GaBi Solutions

Data on demand - datasets


The following 2,000+ datasets are directly available on demand, complementing the ~12,500 of the Professional and Extension databases:

 

 

 

Process nameCountryTypeData source

1,1,1-Trichloroethane (methylchloroform)
chlorination of ethane;
production mix, at plant;
1.34 g/cm3, 133.42 g/mol

DEaggts

1,12-Dodecandioic acid (from Cyclododecatriene)
hydrogenation of cyclododecatriene, oxidation of cyclodocecane;
single route, at plant;
1.15 g/cm3, 230.31 g/mol

DEaggts

1,1-Difluoroethane (HFC 152a)
hydrofluorination of vinyl chloride;
single producer, at plant;
3.04 kg/m3 at 0°C, 66.05 g/mol

DEaggts

1,3-bis[3-(dimethylamino)propyl]urea
reaction of urea with N,N-dimethylamino-propylamine;
single route, at plant;
230.35 g/mol

EU-28aggts

1,3-Butadiene
oxidative catalytic dehydrogenation of C4;
production mix, at plant;
2.4982 kg/m3, 54.09 g/mol

NLaggts

1,3-Butadiene
oxidative catalytic dehydrogenation of C4;
production mix, at plant;
2.4982 kg/m3, 54.09 g/mol

ESaggts

1,3-Butadiene
oxidative catalytic dehydrogenation of C4;
production mix, at plant;
2.4982 kg/m3, 54.09 g/mol

CNaggts

1,3-Butadiene
oxidative catalytic dehydrogenation of C4;
production mix, at plant;
2.4982 kg/m3, 54.09 g/mol

JPaggts

1,3-butadiene
oxidative catalytic dehydrogenation of C4;
production mix, at plant;
2.4982 kg/m3, 54.09 g/mol

NOaggts

1,4-Dioxane (Diethylene oxide)
dehydration and ring closure of diethylene glycol;
production mix, at plant;
1.03 g/cm3, 88.11 g/mol

DEaggts

1,6-Hexanediol (estimation)
catalytic hydrogenation of adipic acid;
production mix, at plant;
118.18 g/mol

EU-28aggts

1,6-Hexanediol (estimation)
catalytic hydrogenation of adipic acid;
single producer, at plant;
118.18 g/mol

DEaggts

1-Aminoanthraquinone
from chlorobenzoic acid and xylene;
production mix, at plant;
223.23 g/mol

USaggts

1-Decanol (estmation)
Hydrogenation of decanoic acid, based on palm kernel oil;
production mix, at plant;
0.8297 g/cm3, 158.28 g/mol

EU-28aggts

1-Decene by-product Linear Alphaolefine (LAO) (mass allocation) (estimation)
oligomerization of ethylene, by-product Linear Alphaolefine;
single route, at plant;
0.74 g/cm3, 140.27 g/mol

DEaggts

1-Dodecanol
hydrogenation of dodecanoic acid;
production mix, at plant;
0.83 g/cm3, 186.34 g/mol

DEaggts

1-Dodecanol
hydrogenation of dodecanoic acid;
production mix, at plant;
0.83 g/cm3, 186.34 g/mol

EU-28aggts

2-(Perfluorohexyl)ethyl iodide
radical-catalysed addition of ethylene to perfluorohexyl iodide;
single route, at producer;
474 g/mol

USaggts

2,4-Dimethylbenzaldehyde
reaction of xylene with carbon monoxide;
single producer, at plant;
density 0.962 g/mL at 25 °C, molar mass 134 g/mol

DEaggts

2,4-Dimethylbenzaldehyde
reaction of xylene with carbon monoxide;
single producer, at plant;
density 0.962 g/mL at 25 °C, molar mass 134 g/mol

EU-28aggts

2-Dimethylaminoethanol (DMAE)
reaction of dimethylamine and ethylene oxide;
production mix, at plant;
0.89 g/cm3, 89.14 g/mol

EU-28aggts

2-Ethylhexanol from propylene
Aldolization of butyraldehyde;
production mix, at plant;
0.83 g/cm3, 130.23 g/mol

USaggts

2-Ethylhexanol from propylene
Aldolization of butyraldehyde;
production mix, at plant;
0.83 g/cm3, 130.23 g/mol

DEaggts

2-Ethylhexanol from propylene
Aldolization of butyraldehyde;
production mix, at plant;
0.83 g/cm3, 130.23 g/mol

EU-28aggts

2K-dispersion adhesive
mixing polyurethane, methyl ethyl ketone, water and hardener;
production mix, at plant;
contains 5% hardener

DEaggts

2-keto-L-gulonic acid butyl ester
esterification of 2-keto-L-gulonic acid with butanol;
production mix, at plant;
250 g/mol

USaggts

2-keto-L-gulonic acid butyl ester (97%)
esterification of 2-keto-L-gulonic acid with butanol;
production mix, at plant;
97% concentrated

USaggts

2-keto-L-gulonic acid preparation
bacteria cultivation, fermentation of L- sorbose;
production mix, at plant;
194.14 g/mol

USaggts

2-Octanol by-product sebacic acid - average, 50:50 mix of best case and worst case scenario
technology mix, saponification of castor oil with alkali;
production mix, at producer;
0.819 g/mL at 25 °C, 130.23 g/mol

CNaggts

3-Aminopropyltriethoxylsilane (estimation)
reaction of chloroalkylsilane with ammonia or an organic amino compound;
production mix, at plant;
0.946 g/cm3, 221.37 g/mol

DEaggts

3-Aminopropyltriethoxylsilane (estimation)
reaction of chloroalkylsilane with ammonia or an organic amino compound;
production mix, at plant;
0.946 g/cm3, 221.37 g/mol

EU-28aggts

3-Hydroxy-2-Naphthoic acid
carboxylation of potassium naphtholate;
production mix, at plant;
188.18 g/mol

DEaggts

3-Mercaptopropionic acid (estimation)
reaction of methanthiol (or H2S) with acrylic acid;
single route, at plant;
1.218 g/mL at 25 °C, molar mass 106.14 g/mol

EU-28aggts

4,4'-DCDPS (4,4'-Dichlorodiphenylsulfon) (estimation)
sulfonation of chlorobenzene;
production mix, at plant;
287 g/mol

USaggts

4,4'-DCDPS (4,4'-Dichlorodiphenylsulfon) (estimation)
sulfonation of chlorobenzene;
production mix, at plant;
287 g/mol

DEaggts

4-Hydroxy 4-methyl-2-pentanone
ketone condensation;
single producer, at plant;
density 0.931 g/mL at 25 °C, molar mass 116.16 g/mol

DEaggts

6-Hydroxy-2-Naphthoic acid
carboxylation of potassium naphtholate;
production mix, at plant;
188.18 g/mol

DEaggts

ABS GF 30
injection moulding of acrylonitrile butadiene styrene with glass fibres;
production mix, at plant;
30% glass fibres

DEaggts

Acetic acid by-product Polyvinyl Alcohol (PVAL) from vinyl acetate
hydrolysis of vinyl acetate;
single route, at plant;
1.049 g/cm3, 60.05 g/mol

DEaggts

Acetic acid from methanol (low pressure carbonylation) (Monsanto process)
catalytic reaction of methanol and carbon monoxide;
single route, at plant;
1.05 g/cm3, 605 g/mol

EU-28aggts

Acetoncyanhydrine (ACH) with HCN from acrylonitrile by-product
with HCN from acrylonitrile by-product;
production mix, at plant;
0.93 g/cm3, 85.11 g/mol

DEaggts

Acetone
Hock Process, oxidation of cumene;
single route, at plant;
0.79 g/cm3, 58 g/mol

THaggts

Acetone
Hock Process, oxidation of cumene;
single route, at plant;
0.79 g/cm3, 58 g/mol

JPaggts

Acetone
Hock Process, oxidation of cumene;
single route, at plant;
0.79 g/cm3, 58 g/mol

FRaggts

Acetone
Hock Process, oxidation of cumene;
single route, at plant;
0.79 g/cm3, 58 g/mol

CNaggts

Acetone cyanohydrin (ACH)
with HCN from acrylonitrile by-product;
production mix, at plant;
0.93 g/cm3, 85.11 g/mol

ITaggts

Acetone cyanohydrin (ACH)
with HCN from acrylonitrile by-product;
production mix, at plant;
0.93 g/cm3, 85.11 g/mol

DEaggts

Acetone cyanohydrin (ACH)
with HCN from acrylonitrile by-product;
production mix, at plant;
0.93 g/cm3, 85.11 g/mol

EU-28aggts

Acetonitrile
ammoxidation of propene;
production mix, at plant;
786 mg/mL, 41 g/mol

GBaggts

Acetophenone (Phenyl methyl ketone)
Friedel Crafts Alkylation of benzene;
single route, at plant;
1.03 g/cm3, 120.15 g/mol

DEaggts

Acrylamide (catalytic hydrolysis) (50% solution)
catalytic hydration of acrylonitrile;
single producer, at plant;
1.13 g/cm3, 71.08 g/mol

DEaggts

Acrylamide (enzymatic hydration) (50% solution)
enzymatic hydration of acrylonitrile;
single producer, at plant;
1.13 g/cm3, 71.08 g/mol

DEaggts

Acrylate (emulsion)
emulsion polymerization;
single producer, at plant;
44% solid content

DEaggts

Acrylate (emulsion)
emulsion polymerization;
single route, at plant;
44% solid content

EU-28aggts

Acrylate resin (epoxy functional)
polymerisation;
single route, at plant;
30.000- 100.000 g/mol

EU-28aggts

Acrylate resin (epoxy-functional)
polymerisation;
single route, at plant;
30.000- 100.000 g/mol

DEaggts

Acrylate resin (solvent-systems)
polymerisation;
single route, at plant;
30.000- 100.000 g/mol

DEaggts

Acrylic acid (Propene)
oxidation of propene;
production mix, at plant;
1.05 g/cm3, 72.06 g/mol

NLaggts

Acrylic acid (Propene)
oxidation of propene;
production mix, at plant;
1.05 g/cm3, 72.06 g/mol

THaggts

Acrylic acid (Propene)
oxidation of propene;
production mix, at plant;
1.05 g/cm3, 72.06 g/mol

BEaggts

Acrylic acid (Propene)
oxidation of propene;
production mix, at plant;
1.05 g/cm3, 72.06 g/mol

FRaggts

Acrylic acid (Propene)
oxidation of propene;
production mix, at plant;
1.05 g/cm3, 72.06 g/mol

CNaggts

Acrylic acid (Propene)
oxidation of propene;
production mix, at plant;
1.05 g/cm3, 72.06 g/mol

GBaggts

Acrylonitrile (AN)
propene ammoxidation, by- product ammonium sulphate;
production mix, at plant;
0.81 g/cm3, 53.06 g/mol

BEaggts

Acrylonitrile (AN)
propene ammoxidation, by- product ammonium sulphate;
production mix, at plant;
0.81 g/cm3, 53.06 g/mol

EU-28aggts

Acrylonitrile-Butadiene-Styrene Granulate (ABS)
polymerisation of acrylonitrile, butadiene and styrene;
production mix, at plant;
1.060- 1.080 g/cm3

NLaggts

Acrylonitrile-Butadiene-Styrene Granulate (ABS)
polymerisation of acrylonitrile, butadiene and styrene;
production mix, at plant;
1.060- 1.080 g/cm3

BEaggts

Acrylonitrile-Butadiene-Styrene Granulate (ABS)
polymerisation of acrylonitrile, butadiene and styrene;
production mix, at plant;
1.060- 1.080 g/cm3

DEaggts

Activated carbon
technology mix;
production mix, at plant;
porous carbon structure

JPaggts

Activated carbon
technology mix;
production mix, at plant;
porous carbon structure

EU-28aggts

Activated carbon
technology mix;
production mix, at plant;
porous carbon structure

CNaggts

Adhesive system MDF (35% H2O content)
hydromethylation and condensation reactions of melamine, urea and formaldehyde;
production mix, at plant;
35% H2O content

DEaggts

Adhesive system MUF (35%M i.T., 35% H2O content)
hydromethylation and condensation reactions of melamine, urea and formaldehyde;
production mix, at plant;
35% M i.T., 35% H2O

DEaggts

Adhesive system mUF (36% moisture)
hydromethylation and condensation reactions of urea and formaldehyde;
production mix, at plant;
36% moisture

DEaggts

Adhesive system MUPF (35% H2O content)
hydromethylation and condensation reactions of melamine, urea, phenol and formaldehyde;
single route, at plant;
35% H2O

DEaggts

Adhesive system PF (F/P=1.8; 40% H2O content)
Phenol- formaldehyde condensation in caustic solution;
single producer, at plant;
F/P=1.8; 40% H2O

DEaggts

Adhesive system PF (F/P=1.8; 52% H2O content)
Phenol- formaldehyde condensation in caustic solution;
single producer, at plant;
F/P=1,8; 52% H2O

DEaggts

Adhesive system polyurethane-prepolymer
reaction of methylene diisocyanate and polyether polyol;
production mix, at plant;
50% methylene diisocyanate, 50% polyether polyol

DEaggts

Adhesive system UFm (4% Melamin; 35% H2O content)
hydromethylation and condensation reactions of urea, melamin and formaldehyde;
single route, at plant;
4% Melamin; 35% H2O

DEaggts

Adhesive system Urea Formaldehyde (UF) (35% H2O content)
hydromethylation and condensation reactions of urea and formaldehyde;
single producer, at plant;
35% H2O

DEaggts

Adipic acid
oxidation of cyclohexane;
production mix, at plant;
1.36 g/cm3, 146 g/mol

EU-28aggts

Adiponitrile
via direct hydrocyanation of Butadiene with hydrogen cyanide (prussic acid);
single route, at plant;
0.96 g/cm3, 108.14 g/mol

FRaggts

Air drying (food products)
Air drying of food products using a Fluidized Bed Dryer;
single operation, at producer;
Fluidized Bed Dryer

USp-aggts

Air drying (food products)
Air drying of food products using a Fluidized Bed Dryer;
single operation, at producer;
Fluidized Bed Dryer

EU-28p-aggts

Alcohol ethoxylate (ethoxylation)
base- catalyzed ethoxylation of alcohol;
single route, at plant;
estimation

USaggts

Alcohol ethoxylate (ethoxylation)
base- catalyzed ethoxylation of alcohol;
single route, at plant;
estimation

DEaggts

Alcohol ethoxylate (ethoxylation)
base- catalyzed ethoxylation of alcohol;
single route, at plant;
estimation

EU-28aggts

Alfol Process (in Octanol production)
hydrogenation, ethylation, chain growth, oxidation, hydrolysis;
single route, at plant;
0.83 g/cm3, 130.23 g/mol

USaggts

Aliphatic polyisocyanate prepolymer (IPDI-based)
polyaddition of isophorone diisocyanate and polyol;
production mix, at plant;
80% isocyanates, 20% polyols

DEaggts

Aliphatic polyisocyanate prepolymer (IPDI-based)
polyaddition of isophorone diisocyanate and polyol;
production mix, at plant;
80% isocyanates, 20% polyols

EU-28aggts

Alkali resistent (AR) glass fibres
from mineral components;
single route, at plant;
SiO2 63%, ZrO2 16,5%, Na2O 15 %, CaO 5,5%

DEaggts

Alkali-Xanthate
reaction of sodium hydroxide with alcohol and carbon disulphide;
production mix, at plant;
144 g/mol in when ethanol and sodium hydroxide are the educts

DEaggts

Alkyd resin (LM-system)
condensation of polyols, polybasic acids or fatty acids;
single route, at plant;
LM-system

DEaggts

Alkyd resin (LM-system)
condensation of polyols, polybasic acids or fatty acids;
single producer, at plant;
LM-system

EU-28aggts

Allyl chloride (C3H5Cl)
chlorination of propene;
production mix, at plant;
0.94 g/cm3, 76.53 g/mol

BEaggts

Allyl chloride (C3H5Cl)
chlorination of propene;
production mix, at plant;
0.94 g/cm3, 76.53 g/mol

ESaggts

Allyl chloride (C3H5Cl)
chlorination of propene;
production mix, at plant;
0.94 g/cm3, 76.53 g/mol

NLaggts

AlNiCo magnet (estimation)
metals casting;
single route, at plant;
55% ferrite, 10% aluminium, 15% nickel, 20% cobalt

DEaggts

Alpha pinene (estimation)
turpentine from kraft paper production, distillation of alpha-pinene;
single route, at producer;
0.858 g/cm3, 136.24 g/mol

EU-28p-aggts

Aluminium (paste; H2O content) Hydropor
atomizing AL powder, ball milling;
single producer, at plant;
particle size around 5- 35 microns

DEaggts

Aluminium chloride
dissolving alumina in hydrochloric acid;
single route, at plant;
2.44 g/cm3, 133.34 g/mol

DEaggts

Aluminium chloride (estimation)
chlorination of alumium or alumina;
single route, at plant;
2.44 g/cm3, 133.34 g/mol

EU-28aggts

Aluminium chloride hexahydrate
electrolytic reaction of aluminium and HCl;
single route, at plant;
1.3 g/cm3, 241.43 g/mol

DEaggts

Aluminium diacetate (estimation)
reaction of sodium aluminate and acetic acid;
production mix, at plant;
162.1 g/mol

DEaggts

Aluminium extrusion profile (AlMg0.5Si)
primary production;
production mix, at plant;
Alloy composition: 0.1%Cr, 0.1%Cu, 0.675%Mg, 0.1%Mn, 0.4%Si, 0.1%Ti, 0.1%Zn, 0.35%Fe

DEaggts

Aluminium extrusion profile (AlMg1SiCu)
primary production;
production mix, at plant;
Alloy composition: 0.195%Cr, 0.275%Cu, 1%Mg, 0.15%Mn, 0.6%Si, 0.15%Ti, 0.25%Zn, 0.7%Fe

DEaggts

Aluminium extrusion profile (AlMgSi0,5)
primary production;
production mix, at plant;
Alloy composition: 0,1%Cu, 0,45%Mg, 0,1%Mn, 0,45%Si, 0,1%Ti, 0,15%Zn, 0.2%Fe

DEaggts

Aluminium extrusion profile (AlZn5Mg1Zr)
primary production;
production mix, at plant;
Alloy composition: 0.05%Cu, 1.05%Mg, 0.05%Mn, 0.1%Si, 0.05%Ti, 5%Zn, 0,185%Zr, 0.1%Fe

DEaggts

Aluminium flakes paste (chromated, 65% solids incl. solvents)
wet milling process;
single route, at plant;
chromated, 65% solids

DEaggts

Aluminium flakes paste (chrome-free, 60% solids incl. solvents)
wet milling process;
single route, at plant;
chrome-free, 60% solids

DEaggts

Aluminium fluoride
reaction of bauxite, fluorspar and sulphuric acid;
production mix, at plant;
2.88 g/cm3, 83.98 g/mol

EU-28aggts

Aluminium foil
technology mix of hot/ cold rolling and strip casting, cutting and packaging;
production mix, at plant;
39% offcut, scrap recycling

DEaggts

Aluminium Hydroxide from Bauxite
Bayer process;
consumption mix, at plant;
2.42 g/cm3, 78.00 g/mol

EU-28aggts

Aluminium ingot (AlMgSc) - Sc2O3 estimated with Ru - best case 0,02% Sc (estimation)
primary production;
production mix, at plant;
Alloy composition: 0.2%Cu, 4.8%Mg, 0.3%Si, 0.15%Ti, 0.02%Sc

DEaggts

Aluminium ingot (AlMgSc) - Sc2O3 estimated with Ru - worst case 0,4% Sc (estimation)
primary production;
production mix, at plant;
Alloy composition: 0.2%Cu, 4.8%Mg, 0.3%Si, 0.15%Ti, 0.4%Sc

DEaggts

Aluminium ingot (AlMgSi0,5)
primary production;
production mix, at plant;
Alloy composition:0.05%Cr, 0.1%Cu, 0.6%Mg, 0.1%Mn, 0.6%Si, 0.1%Ti, 0.15%Zn

DEaggts

Aluminium ingot (AlMgSi0,7)
primary production;
production mix, at plant;
Alloy composition:0.6%Cr, 0.1%Cu, 0.9%Mg, 0.1%Mn, 0.6%Si, 0.1%Ti, 0.1%Zn

DEaggts

Aluminium ingot (AlMgSi1)
primary production;
production mix, at plant;
Alloy composition:0.25%Cr, 0.1%Cu, 1.2%Mg, 1%Mn, 1.3%Si, 0.1%Ti, 0.2%Zn

DEaggts

Aluminium ingot (AlMn1Cu)
primary production;
production mix, at plant;
Alloy composition:0.1%Cr, 0.1%Cu, 0.3%Mg, 1.5%Mn, 0.5%Si, 0.1%Ti, 0.2%Zn

DEaggts

Aluminium ingot (AlSi10MnMg)
primary production;
production mix, at plant;
Alloy composition: 0.05%Cu, 0.35%Mg, 0.35%Mn, 10.25%Si, 0.2%Ti, 0.07%Zn, 0.25%Fe

DEaggts

Aluminium ingot (AlSi7Mg0,3)
primary production;
production mix, at plant

DEaggts

Aluminium nitrate (estimation)
reaction of aluminium hydroxide with nitric acid;
single route, at plant;
1.72 g/cm3, 213 g/mol

EU-28aggts

Aluminium oxide (Al2O3 high purity)
Bayer process;
production mix, at plant;
3.94 g/cm3, 101.96 g/mol

DEaggts

Aluminium sheet (AlMg4.5Mn0.4)
primary production;
production mix, at plant;
Alloy composition: Cr 0,1%; Cu 0,15%; Mg 4,5 %; Mn 0,35%; Si 0,2%; Ti 0,1%; Zn 0,25%; Fe 0,35%

DEaggts

Aluminium sheet (AlSi1.2Mg0.4)
primary production;
production mix, at plant;
Alloy composition: Cr 0,1%; Cu 0,2%; Mg 0,775 %; Mn 0,2%; Si 1,25%; Ti 0,15%; Zn 0,2%; Fe 0,5%

DEaggts

Aluminium sheet (AlZn5.5Mg1.5)
primary production;
production mix, at plant;
Alloy composition: Cr 0,05%; Cu 0,25%; Mg 1,5 %; Mn 0,1%; Si 0,25%; Ti 0,1%; Zn 5,5%; Zr 0,13 %; Fe 0,4%

DEaggts

Aluminium sheet (AlZn5.5MgCu)
primary production;
production mix, at plant;
Alloy composition: Cr 0,23%; Cu 1,6%; Mg 2,5 %; Mn 0,3%; Si 0,4%; Ti 0,2%; Zn 5,6%; Zr 0 %; Fe 0,5%

DEaggts

Aluminium silicate (zeolite type A)
from aluminum, silica, desired ions, and sodium hydroxide;
production mix, at plant;
162.05 g/mol

DEaggts

Aluminium sulphate (estimation)
from aluminium hydroxide and sulphuric acid;
single route, at plant;
2.71 g/cm3, 342.15 g/mol

DEaggts

Aluminium sulphate (estimation)
via aluminium hydroxide and sulphuric acid;
single route, at plant;
2.71 g/cm3, 342.15 g/mol

EU-28aggts

Aluminium sulphate (estimation)
via aluminium hydroxide and sulphuric acid;
single route, at plant;
2.71 g/cm3, 342.15 g/mol

USaggts

Aluminium sulphate from aluminium pig (estimation)
via aluminium ingot and sulphuric acid;
single route, at plant;
2.71 g/cm3, 342.15 g/mol

DEaggts

Aluminium Trilactate/Aluminium Lactate
reaction of lactic acid with aluminium hydroxide;
production mix, at plant;
294.19 g/mol

DEp-aggts

Amine adduct emulsion on an aqueous base (estimation)
polymerisation of a bisphenol A resin with a polyamine;
single route, at plant;
55% polymer, 45% water

EU-28aggts

Amine adduct emulsion on an aqueous base (estimation)
polymerisation of a bisphenol A resin with a polyamine;
single route, at plant;
55% polymer, 45% water

DEaggts

Amino trimethylene phosphonic acid, sodium salt (estimation)
reaction of ammonium chloride, formaldehyde and phosphoric acid;
production mix, at plant;
1.33 g/cm3, 299.05 g/mol

EU-28aggts

Amino trimethylene phosphonic acid, sodium salt (estimation)
reaction of ammonium chloride, formaldehyde and phosphoric acid;
production mix, at plant;
1.33 g/cm3, 299.05 g/mol

DEaggts

Ammonia (high purity)
purified with activated carbon;
single route, at plant;
0.7714 kg/m3, 17.03 g/mol

DEaggts

Ammonia (NH3) synthesis with CO2 recovery, by-product carbon dioxide (without allocation)
Haber-Bosch process, from natural gas;
production mix, at plant;
0.7714 kg/m3, 17.03 g/mol

BEp-aggts

Ammonia (NH3) synthesis with CO2 recovery, by-product carbon dioxide (without allocation)
Haber-Bosch process, from natural gas;
production mix, at plant;
0.7714 kg/m3, 17.03 g/mol

JPp-aggts

Ammonia (NH3) with CO2 recovery, by-product carbon dioxide (economic allocation)
Haber-Bosch process, from natural gas;
production mix, at plant;
0.7714 kg/m3, 17.03 g/mol

BEaggts

Ammonia (NH3) with CO2 recovery, by-product carbon dioxide (economic allocation)
Haber-Bosch process, from natural gas;
production mix, at plant;
0.7714 kg/m3, 17.03 g/mol

JPaggts

Ammonia (NH3) with CO2 recovery, by-product carbon dioxide (economic allocation)
Haber-Bosch process, from natural gas;
production mix, at plant;
0.7714 kg/m3, 17.03 g/mol

CNaggts

Ammonia (NH3) with CO2 recovery, by-product carbon dioxide, feedstock coal (economic allocation)
Haber-Bosch process, from coal;
single, at plant;
0.7714 kg/m3, 17.03 g/mol

CNaggts

Ammonia (NH3) with CO2 recovery, by-product carbon dioxide, feedstock coal (without allocation)
Haber-Bosch process, from coal;
single, at plant;
0.7714 kg/m3, 17.03 g/mol

CNp-aggts

Ammonia (NH3) without CO2 recovery (carbon dioxide emissions to air)
Haber-Bosch process, from natural gas;
production mix, at plant;
0.7714 kg/m3, 17.03 g/mol

CNaggts

Ammonia (NH3) without CO2 recovery (carbon dioxide emissions to air)
Haber-Bosch process, from natural gas;
single route, at plant;
0.7714 kg/m3, 17.03 g/mol

BRaggts

Ammonia (NH3) without CO2 recovery (carbon dioxide emissions to air)
Haber-Bosch process, from natural gas;
production mix, at plant;
0.7714 kg/m3, 17.03 g/mol

AUaggts

Ammonia (NH3) without CO2 recovery (carbon dioxide emissions to air)
Haber-Bosch process, from natural gas;
production mix, at plant;
0.7714 kg/m3, 17.03 g/mol

MYaggts

Ammonia (NH3) without CO2 recovery, feedstock coal (carbon dioxide emissions to air)
Haber-Bosch process, from coal;
single, at plant;
0.7714 kg/m3, 17.03 g/mol

CNaggts

Ammonia solution, NH3 (aq.) (estimation)
Haber-Bosch process, from natural gas, diluted solution;
production mix, at plant;
35% concentrated

EU-28aggts

Ammonia water (weight share 25% NH3)
ammonium mixed with water;
production mix, at plant;
weight share 25% NH3

DEaggts

Ammonium chloride (salmiac, Solvay-process)
Solvay process;
single route, at plant;
1.53 g/cm3, 53.49 g/mol

EU-28aggts

Ammonium hydrogen carbonate
reacting ammonia with CO2;
single route, at plant;
1.59 g/cm3, 79.06 g/mol

DEaggts

Ammonium hydrogen carbonate (Ammonium bicarbonate)
reacting ammonia with CO2;
single producer, at plant;
1.59 g/cm3, 79.06 g/mol

EU-28aggts

Ammonium nitrate (ON, BAT, 68% solution)
from nitric acid;
production mix, at plant;
1.73 g/cm3, 80.04 g/mol

AUaggts

Ammonium sulphate (co product Acetone cyanohydrin)
with hydrogen cyanide from acrylonitrile by-product;
single route, at plant;
1.77 g/cm3, 132.14 g/mol

EU-28aggts

Ammonium sulphate by-product acrylonitrile (AN), hydrogen cyanide (mass allocated)
propene ammoxidation, by- product acrylonitrile;
single route, at plant;
1.77 g/cm3, 132.14 g/mol

DEaggts

Ammonium sulphate by-product caprolactam from phenol
from phenol;
single route, at plant;
1.77 g/cm3, 132.14 g/mol

NLaggts

Ammonium sulphate mix (by-product), 50:50
technology mix;
production mix, at plant;
1.77 g/cm3, 132.14 g/mol

EU-28aggts

Ammonium sulphate, by product acrylonitrile, hydrocyanic acid
propene ammoxidation, by- product acrylonitrile;
single route, at plant;
1.77 g/cm3, 132.14 g/mol

DEaggts

Ammoniumpolyphosphate
from urea and phoshoric acid;
production mix, at plant;
1,9 g/cm3, 97.01 g/mol

DEaggts

Anhydrite (CaSO4) (natural)
technology mix (mining and open pit mining);
production mix, at producer;
2.96 g/cm3

DEaggts

Anhydrite (CaSO4) (natural) (EN15804 A1-A3)
technology mix (mining and open pit mining);
production mix, at producer;
2.96 g/cm3

EU-28aggts

Anhydrite (CaSO4) (thermal) (EN15804 A1-A3)
thermal produced anhydrite;
production mix, at plant;
grinded and purified product

EU-28aggts

Aniline (Phenyl amine, Amino benzene)
catalytic hydrogenation of nitrobenzene;
single route, at plant;
1.022 g/cm3, 93.13 g/mol

BRaggts

Aniline (Phenyl amine, Amino benzene)
catalytic hydrogenation of nitrobenzene;
single route, at plant;
1.022 g/cm3, 93.13 g/mol

EU-28aggts

Anthraquinone
via reformate from pyrolysis gas;
single route, at plant;
1.31 g/cm3, 208.22 g/mol

DEaggts

Anthraquinone via naphthalene
via naphthalene;
single route, at plant;
1.31 g/cm3, 208.22 g/mol

DEaggts

Antimony trioxide
primary production, antimony ore mining, roasting;
single route, at plant;
5.2 g/cm3, 291.5 g/mol

EU-28aggts

Application primer (waterproof)
water proof application;
single route, at plant;
application per m2

USaggts

Application primer (waterproof)
water proof application;
single route, at plant;
application per m2

EU-28aggts

Aramide fiber (para aramid)
condensation of para- phenylene diamine and terephthaloyl dichloride;
single route, at plant;
para aramid

DEaggts

Argon (gaseous)
cryogenic air fractionation;
production mix, at plant;
40 g/mol

CNaggts

Aromatics (BTX) at refinery
from crude oil;
production mix, at refinery

NLaggts

Aromatics (BTX) at refinery
from crude oil;
production mix, at refinery

MYaggts

Aromatics (BTX) at refinery
from crude oil;
production mix, at refinery

RUaggts

Ascorbic acid
Reichstein Synthesis, from glucose;
single route, at plant;
1.65 g/cm3, 176.12 g/mol

DEaggts

Asphalt binder (rolling asphalt)
combination of aggregates and bitumen;
production mix, at plant;
170 - 250 kg/m2

DEaggts

Average load of laundry
average washing machine, for domestic textile cleaning;
production mix, at plant;
energy consumption 2.25 kWh/ load, water consumption 23 gal/load

USp-aggts

Average Printed Wiring Board with Power Electronics (DfX-compatible)
production of power electronics on base of FR4 substrate;
single route, at producer;
0,01 sqm

GLOaggts

Average Printed Wiring Board with Signal Electronics (DfX-compatible)
Production of signal electronics on base of FR4 substrate;
single route, at producer;
0,01 sqm

GLOaggts

Average Printed Wiring Board with Signal-Power Electronics (DfX-Compatible)
Production of signal-power electronics on base of FR4 substrate;
single route, at producer;
0,01 sqm

GLOaggts

Azodicarbonamide (propellant)
from hydrazine and urea;
single route, at plant;
1.65 g/cm3, 116.08 g/mol

DEaggts

Bamboo cultivation (80% H2O content)
technology mix;
production mix, at producer;
80% H2O

CNaggts

Barge, 1,500t payload capacity / canal
technology mix, diesel driven, cargo;
consumption mix;
1,500t payload capacity/ canal

GLOu-sots

Barium carbonate via barium sulfide and CO2
reaction of barium sulfide solution with CO2, precipitation of barium carbonate;
single route, at plant;
4.43 g/cm3 at 20°C, 197.34 g/mol

DEaggts

Barium chloride (estimation)
reaction of barium sulphide and hydrochloric acid;
production mix, at plant;
3.86 g/cm3, 208.23 g/mol

DEaggts

Barium hydroxide (estimation)
reaction of barium sulphide and sodium hydroxide;
single route, at plant;
3.74 g/cm3, 171.34 g/mol

EU-28aggts

Barium magnesium aluminate (BAM)
from Al2O3, BaCO3, MgCO3, and Eu2O3;
single route, at plant;
1202 g/mol

GLOaggts

Barium sulphate (BaSO4)
carbothermal reduction of barium sulphate to barium sulphide, reaction with sodium sulphate;
production mix, at plant;
4.5 g/cm3, 233.43 g/mol

USaggts

Barium sulphate (BaSO4)
carbothermal reduction of barium sulphate to barium sulphide, reaction with sodium sulphate;
production mix, at plant;
4.5 g/cm3, 233.43 g/mol

DEaggts

Barium sulphate (BaSO4)
carbothermal reduction of barium sulphate to barium sulphide, reaction with sodium sulphate;
production mix, at plant;
4.5 g/cm3, 233.43 g/mol

EU-28aggts

Barium sulphide (100%)
carbothermal reduction of barium sulphate;
production mix, at plant;
4.25 g/cm3, 169.39 g/mol

DEaggts

Barium zinc stearate (stabiliser, estimation)
production of barium stearate and zinc stearate, mixing;
production mix, at plant;
60% barium stearate, 40% zinc stearate

EU-28aggts

Basalt production (washed)
basalt mining and crushing;
single producer, at plant;
<52% SiO2

EU-28aggts

Basalt production (washed)
basalt mining and crushing;
single producer, at plant;
<52% SiO2

DEaggts

Base oil (group I) (solvent refined)
from crude oil;
production mix, at refinery;
40 MJ/kg net calorific value

EU-28aggts

Base oil (group II) (hydrotreated)
from crude oil;
production mix, at refinery;
40 MJ/kg net calorific value

EU-28aggts

Base oil (group III) (hydrocracked)
from crude oil;
production mix, at refinery;
40 MJ/kg net calorific value

EU-28aggts

Beech log free forest track
forest cultivation, harvesting, wet storage;
production mix, at plant;
660 kg/m3

DEaggts

Beech log free forest track
forest cultivation, harvesting, wet storage;
production mix, at plant;
660 kg/m3

EU-28aggts

Beech log free forest track (20 % H2O content)
forest cultivation, harvesting, wet storage;
production mix, at plant;
25% moisture, 20% H2O content included in wood

EU-28aggts

Beef filet (cattle slaughterhouse) (economic allocation)
slaughterhouse;
single producer, at plant;
boneless beef filet

DEaggts

Bentonite, natural
mining and beneficiation;
production mix, at plant;
composed primarily of smectite minerals

CNaggts

Bentonite, natural
mining and beneficiation;
production mix, at plant;
composed primarily of smectite minerals

RUaggts

Bentonite, natural
mining and beneficiation;
production mix, at plant;
composed primarily of smectite minerals

INaggts

Bentonite, natural
mining and beneficiation;
production mix, at plant;
composed primarily of smectite minerals

EU-28aggts

Bentonite, natural
mining and beneficiation;
production mix, at plant;
composed primarily of smectite minerals

DEaggts

Benzanthrone
from sulphuric acid and anthrone;
single route, at plant;
230.27 g/mol

USaggts

Benzene
from pyrolysis fuel;
production mix, at plant;
0.88 g/cm3, 78 g/mol

ESaggts

Benzene
dealkylation of toluene;
production mix, at plant;
0.88 g/cm3, 78 g/mol

GBaggts

Benzene
dealkylation of toluene;
production mix, at plant;
0.88 g/cm3, 78 g/mol

ITaggts

Benzene
dealkylation of toluene;
production mix, at plant;
0.88 g/cm3, 78 g/mol

FRaggts

Benzene
dealkylation of toluene;
production mix, at plant;
0.88 g/cm3, 78 g/mol

NLaggts

Benzene (from reformate)
from reformate;
production mix, at plant;
0.88 g/cm3, 78 g/mol

GBaggts

Benzene (from reformate)
from reformate;
production mix, at plant;
0.88 g/cm3, 78 g/mol

FRaggts

Benzene (from reformate)
from reformate;
production mix, at plant;
0.88 g/cm3, 78 g/mol

ITaggts

Benzene (from reformate) (estimation)
from reformate;
production mix, at plant;
0.88 g/cm3, 78 g/mol

THaggts

Benzene (from reformate) (estimation)
from reformate;
production mix, at plant;
0.88 g/cm3, 78 g/mol

CNaggts

Benzene by-product ethine (acetylene)
Sachsse Bartholome Process;
single route, at plant;
0.88 g/cm3, 78 g/mol

DEaggts

Benzene mix
technology mix;
production mix, to consumer

USaggts

Benzene mix
technology mix;
production mix, at plant;
0.88 g/cm3, 78 g/mol

GBaggts

Benzene sulfonic acid
sulfonation of benzene;
single route, at plant;
1.32 g/cm3 (47 °C), 158.18 g/mol

DEaggts

Benzene sulfonic acid (estimate)
sulfonation of benzene;
single producer, at plant;
1.32 g/cm3 (47 °C), 158.18 g/mol

USaggts

Benzene sulfonic acid (estimate)
sulfonation of benzene;
single producer, at plant;
1.32 g/cm3 (47 °C), 158.18 g/mol

EU-28aggts

Benzoic acid ester
esterification of hydroxybenzoic acid with ethanol;
production mix, at plant;
166 g/mol

EU-28aggts

Benzotrichloride (estimation)
chlorination of toluene;
production mix, at plant;
1.38 g/cm3, 195.48 g/mol

USaggts

Benzoyl Chloride (estimation)
reaction of benzoyl trichloride with water;
single route, at plant;
1.21 g/cm3, 140.57 g/mol

USaggts

Benzoyl Peroxide
production from benzoyl chloride and hydrogen peroxide;
production mix, at plant;
1.33 g/cm3, 242.23 g/mol

USaggts

Benzyl alcohol
hydrolysis of benzyl chloride;
single route, at plant;
1.04 g/cm3, 108.14 g/mol

EU-28aggts

Benzyl alcohol in waste incineration plant
waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment;
production mix (region specific plants), at plant;
34.6 MJ/kg net calorific value

EU-28p-aggts

Beta pinene (estimation)
turpentine from kraft paper production, distillation of beta-pinene;
single route, at producer;
0.872 g/cm3, 136.24 g·mol−1

EU-28p-aggts

BF slag incl. grinding
BF route;
production mix and grinding, at plant;
assemblage of Ca-Al-Mg silicates

AEaggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR1 (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 0,6 %; P 0,065 %; S 0,045 %; Al 0,01 %

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR160IF (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,01 %; Si 0,3 %; Mn 0,6 %; P 0,06 %; S 0,025 %; Al 0,01 %; Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR180BH (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,06 %; Si 0,5 %; Mn 0,7 %; P 0,06 %; S 0,025 %; Al 0,015 %

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR180IF (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,01 %; Si 0,3 %; Mn 0,7 %; P 0,06 %; S 0,025 %; Al 0,01 %; Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR2 (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,1 %; Si 0,5 %; Mn 0,5 %; P 0,065 %; S 0,045 %; Al 0,01 %

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR210BH (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,08 %; Si 0,5 %; Mn 0,7 %; P 0,85 %; S 0,025 %; Al 0,015 %

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR210IF (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,01 %; Si 0,3 %; Mn 0,9 %; P 0,08 %; S 0,025 %; Al 0,01 %; Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR210LA (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,1 %; Si 0,5 %; Mn 1 %; P 0,08 %; S 0,03 %; Al 0,015 %

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR240BH (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,1 %; Si 0,5 %; Mn 1 %; P 0,1 %; S 0,03 %; Al 0,01 %

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR240IF (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,01 %; Si 0,3 %; Mn 1,6 %; P 0,1 %; S 0,025 %; Al 0,01 %; Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR240LA (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,1 %; Si 0,5 %; Mn 1 %; P 0,03 %; S 0,025 %; Al 0,015 %

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR270LA (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 1 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR290Y490T-DP (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,14 %; Si 0,5 %; Mn 1,8 %; P 0,08 %; S 0,015 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR3 (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,08 %; Si 0,5 %; Mn 0,5 %; P 0,003 %; S 0,003 %; Al 0,01 %; 0,3%Ti

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR300LA (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 1,4 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR330Y590T-DP (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,15 %; Si 0,75 %; Mn 2,5 %; P 0,04 %; S 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR340LA (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 1,5 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR380LA (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 1,6 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR4 (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,06 %; Si 0,5 %; Mn 0,4 %; P 0,025 %; S 0,025 %; Al 0,01 %; 0,3%Ti

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR400Y690T-TR (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,24 %; Si 2 %; Mn 2,2 %; P 0,08 %; S 0,015 %; Cr+Mo 0,6%; Ti+Nb 0,2%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR420LA (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 1,65 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR440Y780T-DP (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,18 %; Si 0,8 %; Mn 2,5 %; P 0,08 %; S 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR450Y780T-TR (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,25 %; Si 2,2 %; Mn 2,5 %; P 0,08 %; S 0,015 %; Cr+Mo 0,6%; Ti+Nb 0,2%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR460LA (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 1,7 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR5 (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,02 %; Si 0,5 %; Mn 0,3 %; P 0,02 %; S 0,02 %; Al 0,01 %; 0,3%Ti

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR570Y780T-CP (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,18 %; Si 1 %; Mn 2,5 %; P 0,08 %; S 0,015 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR590Y980T-DP (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,2 %; Si 1 %; Mn 2,9 %; P 0,08 %; S 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR700Y980T-DP (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,23 %; Si 1 %; Mn 2,9 %; P 0,08 %; S 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR780Y980T-CP (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,23 %; Si 1 %; Mn 2,7 %; P 0,08 %; S 0,015 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR900Y1180T-CP (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,23 %; Si 1 %; Mn 2,9 %; P 0,04 %; S 0,01 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; EG 2-sides; 1 mm; HR660Y760T-CP (VDA)
BF Steel sheet; cold rolled; EG;
production mix, at producer;
C 0,18 %; Si 1 %; Mn 2,52%; P 0,08 %; S 0,015 %; Cr+Mo 1%; Ti+Nb 0,25%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR1 (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 0,6 %; P 0,065 %; S 0,045 %; Al 0,01 %

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR160IF (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,01 %; Si 0,3 %; Mn 0,6 %; P 0,06 %; S 0,025 %; Al 0,01 %; Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR180BH (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,06 %; Si 0,5 %; Mn 0,7 %; P 0,06 %; S 0,025 %; Al 0,015 %

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR180IF (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,01 %; Si 0,3 %; Mn 0,7 %; P 0,06 %; S 0,025 %; Al 0,01 %; Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR2 (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,1 %; Si 0,5 %; Mn 0,5 %; P 0,065 %; S 0,045 %; Al 0,01 %

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR210BH (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,08 %; Si 0,5 %; Mn 0,7 %; P 0,85 %; S 0,025 %; Al 0,015 %

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR210IF (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,01 %; Si 0,3 %; Mn 0,9 %; P 0,08 %; S 0,025 %; Al 0,01 %; Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR210LA (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,1 %; Si 0,5 %; Mn 1 %; P 0,08 %; S 0,03 %; Al 0,015 %

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR240BH (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,1 %; Si 0,5 %; Mn 1 %; P 0,1 %; S 0,03 %; Al 0,01 %

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR240IF (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,01 %; Si 0,3 %; Mn 1,6 %; P 0,1 %; S 0,025 %; Al 0,01 %; Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR240LA (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,1 %; Si 0,5 %; Mn 1 %; P 0,03 %; S 0,025 %; Al 0,015 %

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR270LA (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 1 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR290Y490T-DP (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,14 %; Si 0,5 %; Mn 1,8 %; P 0,08 %; S 0,015 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR3 (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,08 %; Si 0,5 %; Mn 0,5 %; P 0,003 %; S 0,003 %; Al 0,01 %; 0,3%Ti

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR300LA (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 1,4 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR330Y590T-DP (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,15 %; Si 0,75 %; Mn 2,5 %; P 0,04 %; S 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR340LA (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 1,5 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR380LA (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 1,6 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR4 (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,06 %; Si 0,5 %; Mn 0,4 %; P 0,025 %; S 0,025 %; Al 0,01 %; 0,3%Ti

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR400Y690T-TR (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,24 %; Si 2 %; Mn 2,2 %; P 0,08 %; S 0,015 %; Cr+Mo 0,6%; Ti+Nb 0,2%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR420LA (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 1,65 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR440Y780T-DP (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,18 %; Si 0,8 %; Mn 2,5 %; P 0,08 %; S 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR450Y780T-TR (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,25 %; Si 2,2 %; Mn 2,5 %; P 0,08 %; S 0,015 %; Cr+Mo 0,6%; Ti+Nb 0,2%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR460LA (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 1,7 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR5 (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,02 %; Si 0,5 %; Mn 0,3 %; P 0,02 %; S 0,02 %; Al 0,01 %; 0,3%Ti

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR500LA (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,12 %; Si 0,6 %; Mn 1,7 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR570Y780T-CP (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,18 %; Si 1 %; Mn 2,5 %; P 0,08 %; S 0,015 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR590Y980T-DP (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,2 %; Si 1 %; Mn 2,9 %; P 0,08 %; S 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR700Y980T-DP (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,23 %; Si 1 %; Mn 2,9 %; P 0,08 %; S 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR780Y980T-CP (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,23 %; Si 1 %; Mn 2,7 %; P 0,08 %; S 0,015 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR900Y1180T-CP (VDA)
BF Steel sheet; cold rolled; HDG;
production mix, at producer;
C 0,23 %; Si 1 %; Mn 2,9 %; P 0,04 %; S 0,01 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR1 (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 0,6 %; P 0,065 %; S 0,045 %; Al 0,01 %

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR160IF (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,01 %; Si 0,3 %; Mn 0,6 %; P 0,06 %; S 0,025 %; Al 0,01 %; Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR180BH (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,06 %; Si 0,5 %; Mn 0,7 %; P 0,06 %; S 0,025 %; Al 0,015 %

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR180IF (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,01 %; Si 0,3 %; Mn 0,7 %; P 0,06 %; S 0,025 %; Al 0,01 %; Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR2 (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,1 %; Si 0,5 %; Mn 0,5 %; P 0,065 %; S 0,045 %; Al 0,01 %

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR210BH (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,08 %; Si 0,5 %; Mn 0,7 %; P 0,85 %; S 0,025 %; Al 0,015 %

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR210IF (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,01 %; Si 0,3 %; Mn 0,9 %; P 0,08 %; S 0,025 %; Al 0,01 %; Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR210LA (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,1 %; Si 0,5 %; Mn 1 %; P 0,08 %; S 0,03 %; Al 0,015 %

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR240BH (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,1 %; Si 0,5 %; Mn 1 %; P 0,1 %; S 0,03 %; Al 0,01 %

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR240IF (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,01 %; Si 0,3 %; Mn 1,6 %; P 0,1 %; S 0,025 %; Al 0,01 %; Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR240LA (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,1 %; Si 0,5 %; Mn 1 %; P 0,03 %; S 0,025 %; Al 0,015 %

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR270LA (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 1 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR290Y490T-DP (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,14 %; Si 0,5 %; Mn 1,8 %; P 0,08 %; S 0,015 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR3 (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,08 %; Si 0,5 %; Mn 0,5 %; P 0,003 %; S 0,003 %; Al 0,01 %; 0,3%Ti

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR300LA (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 1,4 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR330Y590T-DP (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,15 %; Si 0,75 %; Mn 2,5 %; P 0,04 %; S 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR340LA (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 1,5 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR380LA (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 1,6 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR4 (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,06 %; Si 0,5 %; Mn 0,4 %; P 0,025 %; S 0,025 %; Al 0,01 %; 0,3%Ti

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR400Y690T-TR (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,24 %; Si 2 %; Mn 2,2 %; P 0,08 %; S 0,015 %; Cr+Mo 0,6%; Ti+Nb 0,2%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR420LA (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 1,65 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR440Y780T-DP (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,18 %; Si 0,8 %; Mn 2,5 %; P 0,08 %; S 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR450Y780T-TR (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,25 %; Si 2,2 %; Mn 2,5 %; P 0,08 %; S 0,015 %; Cr+Mo 0,6%; Ti+Nb 0,2%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR460LA (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,12 %; Si 0,5 %; Mn 1,7 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR5 (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,02 %; Si 0,5 %; Mn 0,3 %; P 0,02 %; S 0,02 %; Al 0,01 %; 0,3%Ti

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR500LA (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,12 %; Si 0,6 %; Mn 1,7 %; P 0,03 %; S 0,025 %; Al 0,015 %, Nb 0,09 %

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR570Y780T-CP (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,18 %; Si 1 %; Mn 2,5 %; P 0,08 %; S 0,015 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR590Y980T-DP (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,2 %; Si 1 %; Mn 2,9 %; P 0,08 %; S 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR700Y980T-DP (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,23 %; Si 1 %; Mn 2,9 %; P 0,08 %; S 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR780Y980T-CP (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,23 %; Si 1 %; Mn 2,7 %; P 0,08 %; S 0,015 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; CR900Y1180T-CP (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,23 %; Si 1 %; Mn 2,9 %; P 0,04 %; S 0,01 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005%

DEp-aggts

BF Steel sheet; cold rolled; uncoated; 1 mm; HR660Y760T-CP (VDA)
BF Steel sheet; cold rolled; uncoated;
production mix, at producer;
C 0,18 %; Si 1 %; Mn 2,52%; P 0,08 %; S 0,015 %; Cr+Mo 1%; Ti+Nb 0,25%; B 0,005

DEp-aggts

Biaxial oriented PA film (BOPA PA6)
polyamide 6 extrusion and stretching;
single route, at plant;
32 MJ/kg net calorific value

DEaggts

Biaxial oriented PET film (BOPET)
PET extrusion and stretching;
single route, at plant;
192.17 g/mol per repeating unit

DEaggts

Biaxial oriented polypropylene film (BOPP)
polypropylene extrusion and stretching;
single producer, at plant;
44 MJ/kg net calorific value

DEaggts

Biaxial oriented polypropylene film (BOPP)
polypropylene extrusion and stretching;
single producer, at plant;
44 MJ/kg net calorific value

USaggts

Biaxial oriented Polystyrene film (BOPS)
polystyrene extrusion and stretching;
single route, at plant;
40 MJ/kg net calorific value

DEaggts

Bicomponent fiber (PET/PA)
spinning of polyethylene terephthalate, polyamide and epoxy resin;
production mix, at plant;
85% PET, 15% PA

DEaggts

Biodiesel based on rape seed methyl ester (RME)
from rape seeds;
production mix, at plant;
78% total carbon content, 74% biogenic carbon content, 37 MJ/kg net calorific value

EU-28aggts

Bioethanol (from corn)
from corn;
production mix, at plant;
55% carbon content, 26.8 MJ net calorific value

EU-28aggts

Bioethanol from corn, at plant
from corn;
production mix, at plant;
55% carbon content, 26.8 MJ net calorific value

USaggts

Bioethanol from sugar beet, at plant
from sugar beet;
production mix, at plant;
52% carbon content, 26.8 MJ net calorific value

EU-28aggts

Bioethanol from sugar beet, at plant
from sugar beet;
single route, at plant;
0.79 g/cm3, 46.07 g/mol

DEaggts

Bioethanol from sugar cane (no slash and burn) (estimation)
from sugar cane;
single route, at plant;
0.79 g/cm3, 46.07 g/mol

BRaggts

Bioethanol from sugar cane, at plant
from sugar cane;
production mix, at plant;
52% carbon content, 26.8 MJ net calorific value

BRaggts

Bioethanol from wheat (DDGS internal energy)
from wheat;
single route, at plant;
0.79 g/cm3, 46.07 g/mol

EU-28aggts

Bioethanol from wheat, at plant
transport, conditioning and fermentation of wheat;
single route, at plant;
55% carbon content, 26.8 MJ net calorific value

EU-28aggts

Bioethanol from wheat, at plant
transport, conditioning and fermentation of wheat;
single route, at plant;
55% carbon content, 26.8 MJ net calorific value

USaggts

Biogas for bioenergy
technology mix;
consumption mix, to consumer

GBaggts

Biogas for bioenergy
technology mix;
consumption mix, to consumer

DEaggts

Biogas for bioenergy
technology mix;
consumption mix, to consumer

NLaggts

Biogas from cattle liquid manure
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
59% methane content, 36 Mj/m3 net calorific value

DEp-aggts

Biogas from cattle paunch contents
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
59% methane content, 36 Mj/m3 net calorific value

DEp-aggts

Biogas from cattle solid manure
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
59% methane content, 36 Mj/m3 net calorific value

DEp-aggts

Biogas from flotate sludge
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
59% methane content, 36 Mj/m3 net calorific value

DEp-aggts

Biogas from kitchen residues
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
59% methane content, 36 Mj/m3 net calorific value

DEp-aggts

Biogas from Maize for bioenergy
technology mix / Anaerobic fermentation of maize silage from whole plants to biogas via wet fermentation prosess;
production mix, at producer, gate to gate;
Biogas net calorific value is 15MJ/kg (~30% (mass) methane content)

DEp-aggts

Biogas from municipal organic waste
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
59% methane content, 36 Mj/m3 net calorific value

DEp-aggts

Biogas from organic waste mix
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
59% methane content, 36 Mj/m3 net calorific value

DEp-aggts

Biogas from pig liquid manure
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
59% methane content, 36 Mj/m3 net calorific value

DEp-aggts

Biogas from poultry solid manure
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
59% methane content, 36 Mj/m3 net calorific value

DEp-aggts

Biogas from sugar beet leaves
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
59% methane content, 36 Mj/m3 net calorific value

DEp-aggts

Biomass (solid) for bioenergy
technology mix;
consumption mix, to consumer

BRaggts

Biomass (solid) for bioenergy
technology mix;
consumption mix, to consumer

NLaggts

Biomass (solid) for bioenergy
technology mix;
consumption mix, to consumer

GBaggts

Biomass (solid) for bioenergy
technology mix;
consumption mix, to consumer

CAaggts

Biomass (solid) for bioenergy
technology mix;
consumption mix, to consumer

HUaggts

Biomass (solid) for bioenergy
technology mix;
consumption mix, to consumer

DKaggts

Biomass (solid) for bioenergy
technology mix;
consumption mix, to consumer

USaggts

Biomass (solid) for bioenergy
technology mix;
consumption mix, to consumer

PTaggts

Biomass (solid) for bioenergy
technology mix;
consumption mix, to consumer

THaggts

Biomass (solid) for bioenergy
technology mix;
consumption mix, to consumer

FIaggts

Biomass (solid) for bioenergy
technology mix;
consumption mix, to consumer

DEaggts

Biomass (solid) for bioenergy
technology mix;
consumption mix, to consumer

SEaggts

Biomass (solid) for bioenergy
technology mix;
consumption mix, to consumer

NZaggts

Biomass Power Plant - CHP (lumber, 12% moisture)
cogeneration electricity and heat, technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28p-aggts

Biomethane from cattle liquid manure
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
97,8% methane

DEp-aggts

Biomethane from cattle paunch contents
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
97,8% methane

DEp-aggts

Biomethane from cattle solid manure
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
97,8% methane

DEp-aggts

Biomethane from flotate sludge
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
97,8% methane

DEp-aggts

Biomethane from glycerine -80% RED value (16,76 g GHG/MJ)
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
97,8% methane

DEp-aggts

Biomethane from hop vine chips -80% RED value (16,76 g GHG/MJ)
technology mix/ anaerobic fermentation of hop vine to biogas via wet fermentation;
production mix, at plant;
97,8% methane

DEp-aggts

Biomethane from kitchen residues
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
97,8% methane

DEp-aggts

Biomethane from municipal organic waste
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
97,8% methane

DEp-aggts

Biomethane from organic waste mix
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
97,8% methane

DEp-aggts

Biomethane from pig liquid manure
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
97,8% methane

DEp-aggts

Biomethane from pig solid manure
technology mix / anaerobic fermentation of organic wastes to biomethane via wet fermentation prosess;
production mix, at plant;
1MJ of biomethane

DEp-aggts

Biomethane from pig solid manure -80% RED value (16,76 GHG/MJ)
technology mix / anaerobic fermentation of organic wastes to biomethane via wet fermentation prosess;
production mix, at plant;
1MJ of biomethane

DEp-aggts

Biomethane from poultry solid manure
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
97,8% methane

DEp-aggts

Biomethane from poultry solid manure -80% RED value (16,76 g GHG/MJ)
technology mix/ anaerobic fermentation of poultry organic matter to biogas via wet fermentation;
production mix, at plant;
97,8% methane

DEp-aggts

Biomethane from sugar beet leaves
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
97,8% methane

DEp-aggts

Biomethane from sugar beet pellets -80% RED value (16,76 g GHG/MJ)
technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation;
production mix, at plant;
97,8% methane

DEp-aggts

Bisphenol A
technology mix;
production mix, at plant;
solid, density: 1,2 g·cm−3, molar mass: 228,28 g·mol−1

EU-28aggts

Bitumen at refinery
from crude oil;
production mix, at refinery

NLaggts

Bitumen at refinery
from crude oil;
production mix, at refinery

RUaggts

Bitumen at refinery
from crude oil;
production mix, at refinery

MYaggts

Blast Furnace slag
iron production, blast furnace route, by- product slag, grinded;
single route, at plant;
2800- 4000 kg/m³

INaggts

Blood from pig, unprocessed, from slaughterhouse (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

EU-28aggts

Blood meal from cattle (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

USaggts

Blood meal from cattle (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

BRaggts

Blood meal from cattle (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

NZaggts

Blood meal from pig (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

BRaggts

Blood meal from pig (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

USaggts

Blood meal from pig (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

EU-28aggts

Blood meal from pig (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

NZaggts

Blood meal from poultry (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

NZaggts

Blood meal from poultry (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

BRaggts

Blood meal from poultry (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

USaggts

Blood meal from poultry (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

ZAaggts

Boiler ash from hard coal power plant
from hard coal power plant;
production mix, at power plant;
grain size ca. 13 mm

EU-28aggts

Boiler ash from hard coal power plant
from hard coal power plant;
production mix, at power plant;
grain size ca. 13 mm

DEaggts

Boneless pork, from pig slaughterhouse (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

BRaggts

Boneless pork, from pig slaughterhouse (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

NZaggts

Boneless pork, from pig slaughterhouse (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

USaggts

Boneless pork, from pig slaughterhouse (economic allocation) - open input pig raising
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

NZp-aggts

Boneless pork, from pig slaughterhouse (economic allocation) - open input pig raising
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

BRp-aggts

Boneless pork, from pig slaughterhouse (economic allocation) - open input pig raising
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

USp-aggts

Boneless pork, from slaughterhouse (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

EU-28aggts

Borax (dehydrated)
via dehydration;
production mix, at plant;
201.37 g/mol

DEaggts

Borax (dehydrated)
via dehydration;
production mix, at plant;
201.37 g/mol

EU-28aggts

Borax pentahydrate
via colemanite;
production mix, at plant;
291 g/mol

DEaggts

Borax pentahydrate
via colemanite;
production mix, at plant;
291 g/mol

EU-28aggts

Boric acid (estimation)
reaction of borax pentahydrate and sulfuric acid;
single route, at plant;
1.44 g/cm3, 61.83 g/mol

EU-28aggts

Boric acid (estimation)
reaction of borax pentahydrate and sulfuric acid;
single route, at plant;
1.44 g/cm3, 61.83 g/mol

DEaggts

Boric acid by-product sodium sulfate (estimation)
reaction of borax pentahydrate and sulfuric acid;
single route, at plant;
1.44 g/cm3, 61.83 g/mol

USaggts

Brass die-casting (CuZn20)
die casting, from copper and zinc, primary production;
single route, at plant;
80% copper, 20% zinc

DEp-aggts

Bromine (from sea water) estimation
from sea water;
single route, at plant;
3.10 g/cm3, 79.90 g/cm3

GBaggts

Bunker oil at refinery
from crude oil;
production mix, at refinery;
3.5 wt.% sulphur

MYaggts

Bunker oil at refinery
from crude oil;
production mix, at refinery;
3.5 wt.% sulphur

RUaggts

Bunker oil at refinery
from crude oil;
production mix, at refinery;
3.5 wt.% sulphur

NLaggts

Butane at refinery
from crude oil;
production mix, at refinery

RUaggts

Butane at refinery
from crude oil;
production mix, at refinery

NLaggts

Butane at refinery
from crude oil;
production mix, at refinery

MYaggts

Butane diamine ( Tetramethylenediamine TMDA) (estimation)
reaction of acrylonitrile, hydrogen cyanide and hydrogen;
single route, at plant;
0.88 g/cm3, 88.15 g/mol

CNaggts

Butane diamine (Tetramethylenediamine TMDA)
reaction of acrylonitrile, hydrogen cyanide and hydrogen;
single route, at plant;
0.88 g/cm3, 88.15 g/mol

DEaggts

Butanediol from propylene oxide (PO chlorohydrine)
from propylene oxide;
single route, at plant;
1.02 g/cm3, 90.12 g/mol

USaggts

Butanediol from propylene oxide (PO oxirane)
from propylene oxide;
single route, at plant;
1.02 g/cm3, 90.12 g/mol

USaggts

Butanol (n-butanol) from propylene
Oxo synthesis, from propylene with rhodium catalyst;
production mix, at producer;
0.81 g/cm3, 74.12 g/mol

EU-28aggts

Butanol (n-butanol) from propylene
Oxo synthesis, from propylene with rhodium catalyst;
production mix, at producer;
0.81 g/cm3, 74.12 g/mol

DEaggts

Butyl Acetate
Fischer esterification;
production mix, at plant;
0.88 g/cm3, 116.16 g/mol

USaggts

Butyl acetate
Fischer esterification;
production mix, at plant;
0.88 g/cm3, 116.16 g/mol

EU-28aggts

Butyl acetate
Fischer esterification;
production mix, at plant;
0.88 g/cm3, 116.16 g/mol

DEaggts

Butyl acrylate
esterification of acrylic acid and butanol;
single producer, at plant;
density 0,90 g·cm−3, molar mass 128,17 g·mol−1

EU-28aggts

Butyl acrylate
esterification of acrylic acid and butanol;
single producer, at plant;
density 0,90 g·cm−3, molar mass 128,17 g·mol−1

DEaggts

Butyldiglycol
ethoxylation of butanol;
production mix, at plant;
liquid, density: 0,95 g·cm−3, molar mass: 162,23 g·mol−1

DEaggts

Butyldiglycol acetate (estimation)
from butyldiglycol and butyl acetate;
single route, at plant;
0.98 gcm-3 at 20°C, 104.27 g/mol

DEaggts

Butylene at refinery
from crude oil;
production mix, at refinery

RUaggts

Butylene at refinery
from crude oil;
production mix, at refinery

MYaggts

Butylene at refinery
from crude oil;
production mix, at refinery

NLaggts

Butyraldehyde
Oxo process, by-product butanol from propylene with rhodium catalyst;
production mix, at plant;
0.80 g/cm3, 72.11 g/mol

DEaggts

Butyraldehyde
Oxo process, by-product butanol from propylene with rhodium catalyst;
production mix, at plant;
0.80 g/cm3, 72.11 g/mol

EU-28aggts

Butyraldehyde by-product butanol from propylene
Oxo process, by-product butanol from propylene with rhodium catalyst;
production mix, at plant;
0.80 g/cm3, 72.11 g/mol

CNaggts

Butyraldehyde by-product butanol from propylene
Oxo process, by-product butanol from propylene with rhodium catalyst;
production mix, at plant;
0.80 g/cm3, 72.11 g/mol

USaggts

Butyric acid anhydride
liquid- phase oxidation of butyraldehyde;
single route, at plant;
0.967 g/cm3, molar mass 158.19 g/mol

DEaggts

C10-Methylester including transesterification and fractionation
Crude coconut oil processing, transesterification and fractionation;
single producer, at plant;
C10 methyl ester fraction

MYaggts

C12-Methylester including transesterification and fractionation
Palm kernel oil processing, transesterification and fractionation;
single producer, at plant;
C12 methyl ester fraction

MYaggts

C4 cut (butadiene)
steam cracker;
production mix, at plant;
45.3 MJ net calorific value

FRaggts

C4 cut (butadiene) (estimation)
steam cracker;
production mix, at plant;
45.3 MJ net calorific value

JPaggts

C4 cut (butadiene) (estimation)
steam cracker;
production mix, at plant;
45.3 MJ net calorific value

ESaggts

C4 cut (butadiene) (estimation)
steam cracker;
production mix, at plant;
45.3 MJ net calorific value

CNaggts

C4 cut from FCC at refinery
from crude oil;
production mix, at refinery

DEaggts

C-6 fluorinated acrylic copolymer
Esterification of 2-(Perfluorohexyl)ethanol by acrylic acid;
single route, at producer;
MW=418.15 g/mol

USaggts

Cable 10-core data ribbon 28AWG PE (25 g/m) 12.7x0.9
technology mix;
production mix, at plant;
tinned Cu wire, PE insulation, unshielded

GLOaggts

Cable 10-core data ribbon 28AWG PVC (25 g/m) 12.7x0.9
technology mix;
production mix, at plant;
tinned Cu wire, PVC insulation, unshielded

GLOaggts

Cable 1-core power 18AWG mPPE (10 g/m) D1.7
technology mix;
production mix, at plant;
tinned Cu wire, mPPE insulation

GLOaggts

Cable 1-core power 18AWG PE (16 g/m) D2.8
technology mix;
production mix, at plant;
tinned Cu wire, PE insulation

GLOaggts

Cable 1-core power 18AWG PTFE (13 g/m) D1.7
technology mix;
production mix, at plant;
tinned Cu wire, PTFE insulation

GLOaggts

Cable Ethernet Cat-6 PE/PVC (66 g/m) D6.4
technology mix;
production mix, at plant;
bare Cu wire, PE insulation, PVC jacket, unshielded

GLOaggts

Cable HDMI v1.0-1.3 28AWG PE/PVC (80 g/m) D7.3
technology mix;
production mix, at plant;
tinned Cu wire, PE insulation, PVC jacket, shielded

GLOaggts

Cadmium acetate (estimation)
reaction of cadmium oxide with acetic acid;
single route, at plant;
2.34 g/cm3, 230.50 g/mol

USaggts

Calcined kaolin powder (Al2O3 * SiO2)
calcination in rotary furnace;
single route, at plant;
162.06 g/mol

DEaggts

Calcined petroleum coke
calcination;
single route, at plant;
95 to 99 wt% carbon content

CNaggts

Calcium chloride (by-product epichlorohydrine, hydrochloric acid)
from Epichlorhydrin synthesis, by-product epichlorohydrine, hydrochloric acid;
single route, at plant;
110.98 g/mol

DEaggts

Calcium chloride, by-product epichlorohydrine, hydrochloric acid
from Epichlorhydrin synthesis, by-product epichlorohydrine, hydrochloric acid;
single route, at plant;
110.98 g/mol

USaggts

Calcium chloride, by-product hydrochloric acid (100%) by-product epichlorohydrine
via allyl chloride;
single route, at plant;
2.15 g/cm3, 110.98 g/mol

EU-28aggts

Calcium diformate
reaction of finelime and formaldehyde;
single route, at plant;
stoichiometrical estimation, density 2,02 g·cm−3, molar mass 130,11 g·mol−1

DEaggts

Calcium diformate (estimation)
reaction of finelime and formaldehyde;
single route, at plant;
stoichiometrical estimation, density 2,02 g·cm−3, molar mass 130,11 g·mol−1

EU-28aggts

Calcium sulfoaluminate cement
from alumina, gypsum and limestone via furnace process;
single route, at producer;
CSA cement requires kiln temperatures of around 1250°C (2250°F)

USaggts

Canola (rapeseed) meal (economic allocation)
canola cultivation, transport, rape processing, pressing and extraction;
single route, at plant;
49% dry carbon, 7% water content

USaggts

Carbon dioxide by-product ethylene oxide (EO) from air
oxidation of ethylene with air;
single route, at plant;
1.98 kg/m3, 44.01 g/mol

GBaggts

Carbon dioxide by-product ethylene oxide (EO) from air
oxidation of ethylene with air;
single route, at plant;
1.98 kg/m3, 44.01 g/mol

BEaggts

Carbon dioxide by-product ethylene oxide (EO) from air
oxidation of ethylene with air;
single route, at plant;
1.98 kg/m3, 44.01 g/mol

FRaggts

Carbon dioxide by-product ethylene oxide (EO) from air
oxidation of ethylene with air;
single route, at plant;
1.98 kg/m3, 44.01 g/mol

NLaggts

Carbon dioxide by-product ethylene oxide (EO) from air
oxidation of ethylene with air;
single route, at plant;
1.98 kg/m3, 44.01 g/mol

DEaggts

Carbon dioxide by-product ethylene oxide (EO) via O2/methane
oxidation of ethylene with oxygen;
single route, at plant;
1.98 kg/m3, 44.01 g/mol

DEaggts

Carbon dioxide highly pure
dewatering, trace removal;
single route, at plant;
1,98 kg/m3, 44 g/mol

DEaggts

Carbon fiber yarn (CF; from PAN; intermediate strength)
spinning, stabilizing, carbonizing, surface treatment, sizing;
single producer, at plant;
from PAN, intermediate strengths 42 million psi tensile modulus (estimation)

DEaggts

Carbon monoxide (via synthesis gas)
gasification of natural gas, cryogenic separation of carbon monoxide and hydrogen;
single route, at plant;
1.25 kg/m3, 28.01 g/mol

NLaggts

Cargo hauled by freight diesel train (indirect)
diesel driven, cargo;
consumption mix;
average train, gross tonne weight 1000t, 726t payload capacity

EU-28aggts

Cargo hauled by freight electric train (indirect)
electricity driven, cargo;
consumption mix;
average train, gross tonne weight 1000t, 726t payload capacity

EU-28aggts

Cargo hauled by truck trailer, 22 t payload [tkm]
diesel driven, cargo;
consumption mix;
Euro 4, 28 - 34t gross weight, 22t payload capacity

EU-28aggts

Cargo hauled by truck trailer, 22 t payload [tkm] (direct)
diesel driven, cargo;
consumption mix;
Euro 4, 28 - 34t gross weight, 22t payload capacity

EU-28aggts

Cargo hauled by truck trailer, 22 t payload [tkm] (indirect)
diesel driven, cargo;
consumption mix;
Euro 4, 28 - 34t gross weight, 22t payload capacity

EU-28aggts

Cargo hauled by truck, 11.4 t payload [tkm]
diesel driven, cargo;
consumption mix;
Euro 4, 14 - 20t gross weight, 11,4t payload capacity

EU-28aggts

Cargo hauled by truck, 11.4 t payload [tkm] (direct)
diesel driven, cargo;
consumption mix;
Euro 4, 14 - 20t gross weight, 11,4t payload capacity

EU-28aggts

Cargo hauled by truck, 11.4 t payload [tkm] (indirect)
diesel driven, cargo;
consumption mix;
Euro 4, 14 - 20t gross weight, 11,4t payload capacity

EU-28aggts

Cargo hauled by truck, 17.3 t payload [tkm]
diesel driven, cargo;
consumption mix;
Euro 4, 20 - 26t gross weight, 17,3t payload capacity

EU-28aggts

Cargo hauled by truck, 17.3 t payload [tkm] (direct)
diesel driven, cargo;
consumption mix;
Euro 4, 20 - 26t gross weight, 17,3t payload capacity

EU-28aggts

Cargo hauled by truck, 17.3 t payload [tkm] (indirect)
diesel driven, cargo;
consumption mix;
Euro 4, 20 - 26t gross weight, 17,3t payload capacity

EU-28aggts

Cargo hauled by truck, 22 t payload [tkm]
diesel driven, cargo;
consumption mix;
Euro 4, 28 - 32t gross weight, 22t payload capacity

EU-28aggts

Cargo hauled by truck, 22 t payload [tkm] (direct)
diesel driven, cargo;
consumption mix;
Euro 4, 28 - 32t gross weight, 22t payload capacity

EU-28aggts

Cargo hauled by truck, 22 t payload [tkm] (indirect)
diesel driven, cargo;
consumption mix;
Euro 4, 28 - 32t gross weight, 22t payload capacity

EU-28aggts

Cargo hauled by truck, 24.7 t payload [tkm]
diesel driven, cargo;
consumption mix;
Euro 4, more than 32t gross weight, 24,7t payload capacity

EU-28aggts

Cargo hauled by truck, 24.7 t payload [tkm] (direct)
diesel driven, cargo;
consumption mix;
Euro 4, more than 32t gross weight, 24,7t payload capacity

EU-28aggts

Cargo hauled by truck, 24.7 t payload [tkm] (indirect)
diesel driven, cargo;
consumption mix;
Euro 4, more than 32t gross weight, 24,7t payload capacity

EU-28aggts

Cargo hauled by truck, 3.3 t payload [tkm]
diesel driven, cargo;
consumption mix;
Euro 4, up to 7,5t gross weight, 3,3t payload capacity

EU-28aggts

Cargo hauled by truck, 3.3 t payload [tkm] (direct)
diesel driven, cargo;
consumption mix;
Euro 4, up to 7,5t gross weight, 3,3t payload capacity

EU-28aggts

Cargo hauled by truck, 3.3 t payload [tkm] (indirect)
diesel driven, cargo;
consumption mix;
Euro 4, up to 7,5t gross weight, 3,3t payload capacity

EU-28aggts

Cargo hauled by truck, 5 t payload [tkm]
diesel driven, cargo;
consumption mix;
Euro 4, 7,5 t - 12t gross weight, 5t payload capacity

EU-28aggts

Cargo hauled by truck, 5 t payload [tkm] (direct)
diesel driven, cargo;
consumption mix;
Euro 4, 7,5 t - 12t gross weight, 5t payload capacity

EU-28aggts

Cargo hauled by truck, 5 t payload [tkm] (indirect)
diesel driven, cargo;
consumption mix;
Euro 4, 7,5 t - 12t gross weight, 5t payload capacity

EU-28aggts

Cargo hauled by truck, 9.3 t payload [tkm]
diesel driven, cargo;
consumption mix;
Euro 4, 12-14t gross weight, 9,3t payload capacity

EU-28aggts

Cargo hauled by truck, 9.3 t payload [tkm] (direct)
diesel driven, cargo;
consumption mix;
Euro 4, 12-14t gross weight, 9,3t payload capacity

EU-28aggts

Cargo hauled by truck, 9.3 t payload [tkm] (indirect)
diesel driven, cargo;
consumption mix;
Euro 4, 12-14t gross weight, 9,3t payload capacity

EU-28aggts

Casein glue (PVAC dispersion)
polymerization of vinyl acetate, PVAC dispersion in water;
single route, at plant;
50% FKA

DEaggts

Cashew nut shell liquid (mass allocation)
Cashew cultivation, sun drying, transport, cleaning and soaking, roasting;
single route, at plant;
70% anacardic acids, 18% cardol, 5% cardanol; 76,5 wt.% biogenic carbon content

INaggts

Cassava dry chips (mechanical chopping and sun drying)
mechanical chopping and sun-drying;
single route, at producer;
10% H2O

THaggts

Castor oil (average)
castor oil pressing;
single route, at plant;
72,5% carbon content

INaggts

Cattle hide, fresh, from slaughterhouse (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

BRaggts

Cattle hide, fresh, from slaughterhouse (economic allocation) - open input cattle raising
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

BRp-aggts

Cattle hide, fresh, from slaughterhouse (economic allocation) - open input cattle raising
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

DEp-aggts

Cellulose
based on timber spruce;
production mix, at plant;
1.5 g/cm3

USaggts

Cellulose (estimation, based on US foreground system)
based on timber spruce;
production mix, at plant;
estimation

DEaggts

Cellulose acetate butyrate (estimation)
viscose process;
single producer, at plant;
estimation

DEaggts

Cement (CEM III/B) Blastfurnance Cement
technology mix;
production mix, at plant;
CEM III B, 25% clinker, 75% BF slag

DEaggts

Cement (CEM III/C) Blastfurnance Cement
technology mix;
production mix, at plant;
CEM III C, 10% clinker, 90% BF slag

DEaggts

Cement average grinding - open input cement clinker
materials grinding at grinding plant;
single route at plant;
3000 kg/m3

DEp-aggts

Ceramic (Passive components)
including slurry preparation, shaping and burning;
single route, at plant;
Al2O3, silica sand, MnO2 mixture

GLOaggts

Cerium oxide mix
Rare earth element mining and processing;
single producer, at plant;
85% China (Inner Mongolia Bayun Obo), 15% USA (Mountain Pass, California), monazite and bastnaesite ores

GLOaggts

Chlorinated Paraffins (estimation)
reaction of paraffins with chlorine;
production mix, at plant;
1.10- 1.26 g/cm3

DEaggts

Chlorinated Polyethylene (estimation)
reaction of polyethylene with chlorine;
production mix, at plant;
1.27- 1.37 g/cm3

DEaggts

Chlorine acetic acid (estimation)
chlorination of acetic acid;
single route, at plant;
1.58 g/cm3, 94.50 g·mol−1

USaggts

Chlorine dioxide (1% ClO, 99% H2O; chlorate based process; SVP-LITE) (estimation)
reduction of sodium chlorate with methanol;
single route, at plant;
2.76 kg/m3, 67.45 g/mol

EU-28aggts

Chlorine from chlorine-alkali-electrolysis (amalgam)
chlorine alkali electrolysis, amalgam;
single route, at plant;
3.2 g/l, 70.9 g/mol

INaggts

Chlorine from chlorine-alkali-electrolysis (amalgam)
chlorine alkali electrolysis, amalgam;
single route, at plant;
3.2 g/l, 70.9 g/mol

EU-28aggts

Chlorine from chlorine-alkali-electrolysis (amalgam)
chlorine alkali electrolysis, amalgam;
single route, at plant;
3.2 g/l, 70.9 g/mol

BEaggts

Chlorine from chlorine-alkali-electrolysis (amalgam)
chlorine alkali electrolysis, amalgam;
single route, at plant;
3.2 g/l, 70.9 g/mol

ESaggts

Chlorine from chlorine-alkali-electrolysis (diaphragm)
chlorine alkali electrolysis, diaphragm;
single route, at plant;
3.2 g/l, 70.9 g/mol

AUaggts

Chlorine from chlorine-alkali-electrolysis (diaphragm)
chlorine alkali electrolysis, diaphragm;
single route, at plant;
3.2 g/l, 70.9 g/mol

NOaggts

Chlorine from chlorine-alkali-electrolysis (diaphragm)
chlorine alkali electrolysis, diaphragm;
single route, at plant;
3.2 g/l, 70.9 g/mol

EU-28aggts

Chlorine from chlorine-alkali-electrolysis (diaphragm)
chlorine alkali electrolysis, diaphragm;
single route, at plant;
3.2 g/l, 70.9 g/mol

CNaggts

Chlorine from chlorine-alkali-electrolysis (membrane)
chlorine alkali electrolysis, membrane;
single route, at plant;
3.2 g/l, 70.9 g/mol

ESaggts

Chlorine from chlorine-alkali-electrolysis (membrane)
chlorine alkali electrolysis, membrane;
single route, at plant;
3.2 g/l, 70.9 g/mol

AUaggts

Chlorine from chlorine-alkali-electrolysis (membrane)
chlorine alkali electrolysis, membrane;
single route, at plant;
3.2 g/l, 70.9 g/mol

INaggts

Chlorine from chlorine-alkali-electrolysis (membrane)
chlorine alkali electrolysis, membrane;
single route, at plant;
3.2 g/l, 70.9 g/mol

JPaggts

Chlorine from chlorine-alkali-electrolysis (membrane)
chlorine alkali electrolysis, membrane;
single route, at plant;
3.2 g/l, 70.9 g/mol

PTaggts

Chlorine from chlorine-alkali-electrolysis (membrane)
chlorine alkali electrolysis, membrane;
single route, at plant;
3.2 g/l, 70.9 g/mol

NLaggts

Chlorine from chlorine-alkali-electrolysis (membrane)
chlorine alkali electrolysis, membrane;
single route, at plant;
3.2 g/l, 70.9 g/mol

NOaggts

Chlorine from chlorine-alkali-electrolysis (membrane) (open input energy, mass allocation)
from chlorine-alkali electrolysis (membrane);
single route, at plant;
3.2 g/l, 70.9 g/mol

EU-28p-aggts

Chlorine mix
technology mix;
production mix, at plant;
3.2 kg/m3, 70.9 g/mol

AUaggts

Chlorine mix
technology mix;
production mix, at plant;
3.2 kg/m3, 70.9 g/mol

JPaggts

Chlorine mix
technology mix;
production mix, at plant;
3.2 kg/m3, 70.9 g/mol

PLaggts

Chlorine mix
technology mix;
production mix, at plant;
3.2 kg/m3, 70.9 g/mol

SEaggts

Chlorine mix
technology mix;
production mix, at plant;
3.2 kg/m3, 70.9 g/mol

PTaggts

Chlorine mix
technology mix;
production mix, at plant;
3.2 kg/m3, 70.9 g/mol

EU-28aggts

Chlorine mix
technology mix;
production mix, at plant;
3.2 kg/m3, 70.9 g/mol

CZaggts

Chlorine mix
technology mix;
production mix, at plant;
3.2 g/l, 70.9 g/mol

INaggts

Chlorine mix
technology mix;
production mix, at plant;
3.2 kg/m3, 70.9 g/mol

HUaggts

Chlorine mix
technology mix;
production mix, at plant;
3.2 kg/m3, 70.9 g/mol

ROaggts

Chloroacetic acid (estimation)
chlorination of acetic acid;
single route, at plant;
1.58 g/cm3, 94.50 g·mol−1

DEaggts

Chloroacetyl chloride from chlorine acetyl acid
reaction of chloroacetic acid with phosgene;
single route, at plant;
1.42 g/cm3, 112.94 g/mol

DEaggts

Chloroacetylic acid from acetic acid
chlorination of acetic acid;
single route, at plant;
1.58 g/cm3, 94.50 g·mol−1

DEaggts

Chlorobenzene (by product chlorobenzene, hydrochloric acid)
chlorination of benzene;
production mix, at plant;
1.11 g/cm3, 112.56 g/mol

DEaggts

Chlorobenzene (by product chlorobenzene, hydrochloric acid)
chlorination of benzene;
production mix, at plant;
1.11 g/cm3, 112.56 g/mol

EU-28aggts

Chlorobenzene (by product chlorobenzene, hydrochloric acid)
chlorination of benzene;
production mix, at plant;
1.11 g/cm3, 112.56 g/mol

JPaggts

Chlorobenzotrifluoride (p-)
from chlorotoluene, chlorine and hydrogen fluoride;
production mix, at plant;
180.55 g/mol

DEaggts

Chlorodifluoroethane (HCFC 142b) by-product Dichloro-1-fluoroethane (HCFC 141b)
reaction of trichloroethane with hydrofluoric acid;
production mix, at plant;
1.25 g/cm3, 116.94 g/mol

DEaggts

Chlorodifluoromethane (R22, HCFC-22)
reaction of trichloromethane with hydrogen fluoride;
production mix, at plant;
3.94 kg/m3, 86.47 g/mol

GBaggts

Chlorodifluoromethane (R22, HCFC-22)
reaction of trichloromethane with hydrogen fluoride;
production mix, at plant;
3.94 kg/m3, 86.47 g/mol

DEaggts

Chlorodifluoromethane (R22, HCFC-22)
reaction of trichloromethane with hydrogen fluoride;
production mix, at plant;
3.94 kg/m3, 86.47 g/mol

NLaggts

Chlorodifluoromethane (R22, HCFC-22)
reaction of trichloromethane with hydrogen fluoride;
production mix, at plant;
3.94 kg/m3, 86.47 g/mol

ITaggts

Chlorodifluoromethane (R22, HCFC-22) (estimation)
reaction of trichloromethane with hydrogen fluoride;
single route, at plant;
3.94 kg/m3, 86.47 g/mol

JPaggts

Chloroprene (from butadiene via chlorination)
from butadiene via chlorination;
single route, at plant;
0.96 g/cm3, 88,54 g/mol

USaggts

Chloroprene (from butadiene via chlorination)
from butadiene via chlorination;
single route, at plant;
0.96 g/cm3, 88,54 g/mol

EU-28aggts

Chromated copper arsenate
from chromic acid, copper sulphate and an arsenic compound;
single route, at plant;
consits of 34% arsenic compound

USaggts

Chromic acid
from sodium dichromate;
production mix, at plant;
1.20 g/cm3, 118 g/mol

DEaggts

Chromic acid anodizing
anodizing aluminium in chromic acid solution;
single producer, at plant;
1 sqm coated

DEp-aggts

Citric acid (from starch)
Enzymatic production of glucose, fermentation with aspergillus niger into citric acid;
single producer, at plant;
1.665 g/cm3 anhydrous, 1.5g/cm3 monohydrate, 192.124 g/mol anhydrous, 210.14 g/mol monohydrate

EU-28aggts

Clay (self-extraction) (average)
Clay extraction;
single producer, at plant;
17% moisture

DEaggts

Clay extracted from clay pit (23.7% moisture)
technology mix;
production mix, at plant;
23.7% moisture

EU-28aggts

Clay extracted from clay pit (23.7% moisture)
technology mix;
production mix, at plant;
23.7% moisture

ATaggts

Clay production
Clay extraction, mechanical processing and storage;
production mix, at plant;
60% H2O content

EU-28aggts

Clay production
Clay extraction, mechanical processing and storage;
production mix, at plant;
60% H2O content

UAaggts

Clay production
Clay extraction, mechanical processing and storage;
production mix, at plant;
60% H2O content

BRaggts

Clay production
Clay extraction, mechanical processing and storage;
production mix, at plant;
60% H2O content

DEaggts

Clay production
Clay extraction, mechanical processing and storage;
production mix, at plant;
60% H2O content

CNaggts

Clay production (estimation)
Clay extraction, mechanical processing and storage;
production mix, at plant;
60% H2O content

INaggts

Clay production (refractory)
open pit mining;
single producer, at plant;
crude clay

DEaggts

Clay production mix
Clay extraction, mechanical processing and storage;
production mix, at plant;
60% H2O content

DEaggts

Cobalt chloride hexahydrate (estimation)
concentrating a HCl solution with CoO;
single route, at producer

DEaggts

Cobalt hydroxide based on cobalt (Ni/Co route) from thinkstep
electrolysis of sulphate;
production mix, at plant;
3.59 g/cm3, 92.95 g/mol

DEaggts

Cobalt hydroxide based on cobalt mix from Cobalt Development Institute (CDI)
electrolysis of sulphate;
production mix, at plant;
3.59 g/cm3, 92.95 g/mol

DEaggts

Cobalt mix (Ni/Co and Cu/Co route)
Nickel cobalt route, pyrometallurgical process and Copper cobalt route, hydrometallurgical process;
production mix, at plant;
8.90 g/cm3, 58.93 g/mol

GLOaggts

Cobalt mix (only Cu/Co route)
Copper cobalt route, hydrometallurgical process;
production mix, at plant;
8.90 g/cm3, 58.93 g/mol

GLOaggts

Cobalt mix (only Ni/Co route)
Nickel cobalt route, pyrometallurgical process;
production mix, at plant;
8.90 g/cm3, 58.93 g/mol

GLOaggts

Cobalt, Nickel cobalt route only
Nickel cobalt route, pyrometallurgical process;
single route, at plant;
8.90 g/cm3, 58.93 g/mol, ferromagnetic

AUaggts

Coconut cultivation
technology mix;
production mix, at field border;
48% H2O

PHp-aggts

Coking coal mix
technology mix;
consumption mix, at border of producing country;
29 MJ/kg net calorific value

GLOaggts

Colophony (rosin)
from tapped CN living pine, via gum rosin;
single route, at plant;
gum rosin

EU-28aggts

Colophony (rosin)
from tapped CN living pine, via gum rosin;
production mix, at plant;
gum rosin

CNaggts

Colophony (rosin) from distilled and esterified tall oil resin
from distilled and esterified tall oil resin;
production mix, at plant;
gum rosin

FRaggts

Colophony (rosin, refined) from CN pine gum rosin
from tapped CN living pine, via gum rosin;
production mix, at plant;
gum rosin

USaggts

Colophony (rosin, refined) from US pine stump
from US pine stump;
consumption mix, at plant;
gum rosin

USaggts

Colophony / tall oil resin (estimation from paper production)
separation from black liquor, depitching, fatty acid distillation;
single route, at plant;
gum rosin

USaggts

Colophony/tall oil resin (estimation from paper production)
Kraft pulping, tall oil occurs as by-product;
single route, at plant;
composition: fatty acids about 42 to 55 %, resin acids about 33 to 47 %, sterines

SEaggts

Compressed air 1.5 bar (low power consumption)
1.5 bar, high efficiency;
consumption mix, at plant;
low electricity consumption

GLOu-sots

Compressed air 2 to 20 bar (high power consumption)
2 to 20 bar, low efficiency;
consumption mix, at plant;
high electricity consumption

GLOu-sots

Compressed air 2 to 20 bar (low power consumption)
2 to 20 bar, high efficiency;
consumption mix, at plant;
low electricity consumption

GLOu-sots

Compressed air 3.5 bar (low power consumption)
3.5 bar, high efficiency;
consumption mix, at plant;
low electricity consumption

GLOu-sots

Compressed natural gas (CNG)
technology mix of screw-type and piston compressors;
production mix, at plant;
compression to 250 bar

EU-28aggts

Compressed natural gas (CNG) supplied and combusted [CNG input in kg]
Combustion of 1kg fuel input;
single route, at plant;
eta 1

EU-28aggts

Compressed natural gas (CNG) supplied and combusted [CNG input in kg] (direct)
Combustion of 1kg fuel input;
single route, at plant;
eta 1, scope 1 (direct GHG emissions)

EU-28aggts

Compressed natural gas (CNG) supplied and combusted [CNG input in kg] (indirect)
Combustion of 1kg fuel input;
single route, at plant;
eta 1, scope 3 (indirect GHG emissions)

EU-28aggts

Compressed natural gas (CNG) supplied and combusted [th. energy output in MJ, 85% eta]
Combustion based on 1 MJ fuel input, eta 85%, thermal energy output 0,85 MJ;
single route, at plant;
eta 0,85

EU-28aggts

Compressed natural gas (CNG) supplied and combusted [th. energy output in MJ, 85% eta] (direct)
Combustion based on 1 MJ fuel input, eta 85%, thermal energy output 0,85 MJ;
single route, at plant;
eta 0,85, scope 1 (direct GHG emissions)

EU-28aggts

Compressed natural gas (CNG) supplied and combusted [th. energy output in MJ, 85% eta] (indirect)
Combustion based on 1 MJ fuel input, eta 85%, thermal energy output 0,85 MJ;
single route, at plant;
eta 0,85, scope 3 (indirect GHG emissions)

EU-28aggts

Concrete liquefier (ferrochrome-lignine sulfonate)
technology mix;
production mix, at plant;
Ferrochrome-lignine sulfonate

EU-28aggts

Condensed skim milk
thermal evaporation using steam heat;
production mix, at producer;
65% H2O

USp-aggts

Connector audio TRS 2.5mm plug (2.0g) (gold-plated)
technology mix;
production mix, at producer;
2.5mm plug (2.0g) (gold-plated)

GLOaggts

Connector audio TRS 2.5mm plug (2.0g) (silver-plated)
technology mix;
production mix, at producer;
2.5mm plug (2.0g) (silver-plated)

GLOaggts

Connector audio TRS 2.5mm socket (500mg) (gold-plated)
technology mix;
production mix, at producer;
2.5mm socket (500mg) (gold-plated)

GLOaggts

Connector audio TRS 2.5mm socket (500mg) (silver-plated)
technology mix;
production mix, at producer;
2.5mm socket (500mg) (silver-plated)

GLOaggts

Connector audio TRS 3.5mm plug (3.0g) (gold-plated)
technology mix;
production mix, at producer;
3.5mm plug (3.0g) (gold-plated)

GLOaggts

Connector audio TRS 3.5mm plug (3.0g) (nickel-plated)
technology mix;
production mix, at producer;
3.5mm plug (3.0g) (nickel-plated)

GLOaggts

Connector audio TRS 3.5mm socket (800mg) (gold-plated)
technology mix;
production mix, at producer;
3.5mm socket (800mg) (gold-plated)

GLOaggts

Connector audio TRS 3.5mm socket (800mg) (silver-plated)
technology mix;
production mix, at producer;
3.5mm socket (800mg) (silver-plated)

GLOaggts

Connector China type I (38,7 g, 3 pins)
technology mix;
production mix, at producer;
38,7 g, 3 pins

GLOaggts

Connector Cinch female (15 g, 1 pin)
technology mix;
production mix, at producer;
15 g, 1 pin

GLOaggts

Connector Cinch female (15 g, 1 pin, gold plated)
technology mix;
production mix, at producer;
15 g, 1 pin, gold plated

GLOaggts

Connector Cinch male (4,1 g, 1 pin)
technology mix;
production mix, at producer;
4,1 g, 1 pin

GLOaggts

Connector Cinch male (4,1 g, 1 pin, gold plated)
technology mix;
production mix, at producer;
4,1 g, 1 pin, gold plated

GLOaggts

Connector DC power female (2 g, 1 pin)
technology mix;
production mix, at producer;
2 g, 1 pin

GLOaggts

Connector DC power male (2,9 g, 1 pin)
technology mix;
production mix, at producer;
2,9 g, 1 pin

GLOaggts

Connector D-Sub (20,4 g, 15 pins, gold plated)
technology mix;
production mix, at producer;
20,4 g, 15 pins, gold plated

GLOaggts

Connector D-Sub (21,1 g, 9 pins, gold plated)
technology mix;
production mix, at producer;
21,1 g, 9 pins, gold plated

GLOaggts

Connector D-sub DE-15 (VGA) 15-pin plug (20.4g) (gold-plated)
technology mix;
production mix, at producer;
D-sub DE-15 (VGA) 15-pin plug (20.4g) (gold-plated)

GLOaggts

Connector D-sub DE-15 (VGA) 15-pin socket (8.4g) (gold-plated)
technology mix;
production mix, at producer;
D-sub DE-15 (VGA) 15-pin socket (8.4g) (gold-plated)

GLOaggts

Connector D-sub DE-9 (RS-232/serial) 9-pin plug (17.7g) (gold-plated)
technology mix;
production mix, at producer;
D-sub DE-9 (RS-232/serial) 9-pin plug (17.7g) (gold-plated)

GLOaggts

Connector D-sub DE-9 (RS-232/serial) 9-pin socket (7.2g) (gold-plated)
technology mix;
production mix, at producer;
D-sub DE-9 (RS-232/serial) 9-pin socket (7.2g) (gold-plated)

GLOaggts

Connector HDMI type A (7,9 g, 19 pins, gold plated)
technology mix;
production mix, at producer;
7,9 g, 19 pins, gold plated

GLOaggts

Connector HDMI type D (2,7 g, 19 pins, gold plated)
technology mix;
production mix, at producer;
2,7 g, 19 pins, gold plated

GLOaggts

Connector HDMI Type-A 19-pin plug (7.8g) (gold-plated)
technology mix;
production mix, at producer;
HDMI Type-A 19-pin plug (7.8g) (gold-plated)

GLOaggts

Connector HDMI Type-A 19-pin socket (2.0g) (gold-plated)
technology mix;
production mix, at producer;
HDMI Type-A 19-pin socket (2.0g) (gold-plated)

GLOaggts

Connector HDMI Type-D 19-pin plug (2.7g) (gold-plated)
technology mix;
production mix, at producer;
HDMI Type-D 19-pin plug (2.7g) (gold-plated)

GLOaggts

Connector IC single-row (2 g, 10 pins)
technology mix;
production mix, at producer;
2 g, 10 pins

GLOaggts

Connector IC single-row (2 g, 10 pins, gold plated)
technology mix;
production mix, at producer;
2 g, 10 pins, gold plated

GLOaggts

Connector IDC socket (5 g, 40 pins, gold plated)
technology mix;
production mix, at producer;
5 g, 40 pins, gold plated

GLOaggts

Connector IEC-60320-C13 female (28,5 g, 3 pins)
technology mix;
production mix, at producer;
28,5 g, 3 pins

GLOaggts

Connector IEC-60320-C14 male (9,1 g, 3 pins)
technology mix;
production mix, at producer;
9,1 g, 3 pins

GLOaggts

Connector IEC-60320-C5 female (16,8 g, 3 pins)
technology mix;
production mix, at producer;
16,8 g, 3 pins

GLOaggts

Connector IEC-60320-C6 male (5,5 g, 3 pins)
technology mix;
production mix, at producer;
5,5 g, 3 pins

GLOaggts

Connector IEC-60320-C7 female (5,5 g, 2 pins)
technology mix;
production mix, at producer;
5,5 g, 2 pins

GLOaggts

Connector IEC-60320-C8 male (5 g, 2 pins)
technology mix;
production mix, at producer;
5,5 g, 2 pins

GLOaggts

Connector Industries 230 V (120 g, 3 pins)
technology mix;
production mix, at producer;
120 g, 3 pins

GLOaggts

Connector Industries 400 V (180 g, 5 pins)
technology mix;
production mix, at producer;
180 g, 5 pins

GLOaggts

Connector NEMA type A (19,2 g, 2 pins)
technology mix;
production mix, at producer;
19,2 g, 2 pins

GLOaggts

Connector NEMA type B (27,7 g, 3 pins)
technology mix;
production mix, at producer;
27,7 g, 3 pins

GLOaggts

Connector PATA
production of brass pin with gold and nickel coating, production of plastic housing;
production mix, at plant;
4 pins

GLOaggts

Connector PCI (2,6 g, 72 pins, gold plated)
technology mix;
production mix, at producer;
2,6 g, 72 pins, gold plated

GLOaggts

Connector power AC mains China Type-I 3-pin plug (38.7g)
technology mix;
production mix, at producer;
China Type-I 3-pin plug (38.7g)

GLOaggts

Connector power AC mains Euro/Schuko Type-C CEE 7/16 2-pin plug (15g)
technology mix;
production mix, at producer;
Euro/Schuko Type-C CEE 7/16 2-pin plug (15g)

GLOaggts

Connector power AC mains Euro/Schuko Type-C CEE 7/7 3-pin plug (39.9g)
technology mix;
production mix, at producer;
Euro/Schuko Type-C CEE 7/7 3-pin plug (39.9g)

GLOaggts

Connector power AC mains industrial 230V 3-pin plug (120g)
technology mix;
production mix, at producer;
industrial 230V 3-pin plug (120g)

GLOaggts

Connector power AC mains industrial 400V 5-pin plug (180g)
technology mix;
production mix, at producer;
industrial 400V 5-pin plug (180g)

GLOaggts

Connector power AC mains NEMA Type-A 2-pin plug (19.2g)
technology mix;
production mix, at producer;
NEMA Type-A 2-pin plug (19.2g)

GLOaggts

Connector power AC mains NEMA Type-B 3-pin plug (27.7g)
technology mix;
production mix, at producer;
NEMA Type-B 3-pin plug (27.7g)

GLOaggts

Connector power AC mains UK Type-G 3-pin plug (46.5g)
technology mix;
production mix, at producer;
UK Type-G 3-pin plug (46.5g)

GLOaggts

Connector power DC circular plug (2.9g)
technology mix;
production mix, at producer;
DC circular plug (2.9g)

GLOaggts

Connector power DC circular socket (2g)
technology mix;
production mix, at producer;
DC circular socket (2g)

GLOaggts

Connector power IEC-60320-C13 3-pin plug (28.5g)
technology mix;
production mix, at producer;
IEC-60320-C13 3-pin plug (28.5g)

GLOaggts

Connector power IEC-60320-C14 3-pin socket (10g)
technology mix;
production mix, at producer;
IEC-60320-C14 3-pin socket (10g)

GLOaggts

Connector power IEC-60320-C5 3-pin plug (17.2g)
technology mix;
production mix, at producer;
IEC-60320-C5 3-pin plug (17.2g)

GLOaggts

Connector power IEC-60320-C6 3-pin socket (5.5g)
technology mix;
production mix, at producer;
IEC-60320-C6 3-pin socket (5.5g)

GLOaggts

Connector power IEC-60320-C7 2-pin plug (5.5g)
technology mix;
production mix, at producer;
IEC-60320-C7 2-pin plug (5.5g)

GLOaggts

Connector power IEC-60320-C8 2-pin socket (5.0g)
technology mix;
production mix, at producer;
IEC-60320-C8 2-pin socket (5.0g)

GLOaggts

Connector RCA/Cinch plug (4.1g) (gold-plated)
technology mix;
production mix, at producer;
plug (4.1g) (gold-plated)

GLOaggts

Connector RCA/Cinch plug (4.1g) (silver-plated)
technology mix;
production mix, at producer;
plug (4.1g) (silver-plated)

GLOaggts

Connector RCA/Cinch socket (2.9g) (gold-plated)
technology mix;
production mix, at producer;
socket (2.9g) (gold-plated)

GLOaggts

Connector RCA/Cinch socket (2.9g) (silver-plated)
technology mix;
production mix, at producer;
socket (2.9g) (silver-plated)

GLOaggts

Connector RJ 45 (5,4 g, 8 pins, gold plated)
technology mix;
production mix, at producer;
5,4 g, 8 pins, gold plated

GLOaggts

Connector RJ45/8P8C ethernet 8-pin plug (2.4g) (gold-plated)
technology mix;
production mix, at producer;
RJ45/8P8C ethernet 8-pin plug (2.4g) (gold-plated)

GLOaggts

Connector RJ45/8P8C ethernet 8-pin socket (2.5g) (gold-plated)
technology mix;
production mix, at producer;
RJ45/8P8C ethernet 8-pin socket (2.5g) (gold-plated)

GLOaggts

Connector RJ45/8P8C ethernet EMI/RFI shielded 8-pin plug (5.5g) (gold-plated)
technology mix;
production mix, at producer;
RJ45/8P8C ethernet EMI/RFI shielded 8-pin plug (5.5g) (gold-plated)

GLOaggts

Connector RJ45/8P8C ethernet EMI/RFI shielded 8-pin socket (3.6g) (gold-plated)
technology mix;
production mix, at producer;
RJ45/8P8C ethernet EMI/RFI shielded 8-pin socket (3.6g) (gold-plated)

GLOaggts

Connector S-ATA (2 g, 7 pins, gold plated)
technology mix;
production mix, at producer;
2 g, 7 pins, gold plated

GLOaggts

Connector SATA 7 + 15 (22-pin) plug (1.4g) (gold-plated)
technology mix;
production mix, at producer;
SATA 7 + 15 (22-pin) plug (1.4g) (gold-plated)

GLOaggts

Connector Schuko CEE 7/7 (39,9 g, 3 pins)
technology mix;
production mix, at producer;
39,9 g, 3 pins

GLOaggts

Connector Steck Klemme Leiste (3 g, 2 pins)
technology mix;
production mix, at producer;
3 g, 2 pins

GLOaggts

Connector Steck Rck Einpress Male (4,2 g, 55 pins, gold plated)
technology mix;
production mix, at producer

GLOaggts

Connector TRS 2,5 female (10 g, 1 pin)
technology mix;
production mix, at producer;
10 g, 1 pin

GLOaggts

Connector TRS 2,5 female (10 g, 1 pin, gold plated)
technology mix;
production mix, at producer;
10 g, 1 pin, gold plated

GLOaggts

Connector TRS 2,5 male (2 g, 1 pin, gold plated)
technology mix;
production mix, at producer;
2 g, 1 pin, gold plated

GLOaggts

Connector TRS 2,5 male 2 g, 1 pin)
technology mix;
production mix, at producer;
2 g, 1 pin

GLOaggts

Connector TRS 3,5 female (15 g, 1 pin)
technology mix;
production mix, at producer;
15 g, 1 pin

GLOaggts

Connector TRS 3,5 female (15 g, 1 pin, gold plated)
technology mix;
production mix, at producer;
15 g, 1 pin, gold plated

GLOaggts

Connector TRS 3,5 male (2,4 g, 1 pin)
technology mix;
production mix, at producer;
2,4 g, 1 pin

GLOaggts

Connector TRS 3,5 male (2,4 g, 1 pin, gold plated)
technology mix;
production mix, at producer;
2,4 g, 1 pin, gold plated

GLOaggts

Connector TRS 6,35 female (30 g, 1 pin)
technology mix;
production mix, at producer;
30 g, 1 pin

GLOaggts

Connector TRS 6,35 male (20 g, 1 pin)
technology mix;
production mix, at producer;
20 g, 1 pin

GLOaggts

Connector TRS 6,35 male (20 g, 1 pin, gold plated)
technology mix;
production mix, at producer;
20 g, 1 pin, gold plated

GLOaggts

Connector UK type G (46,5 g, 3 pins)
technology mix;
production mix, at producer;
46,5 g, 3 pins

GLOaggts

Connector USB micro (2,5 g, 4 pins, gold plated)
technology mix;
production mix, at producer;
2,5 g, 4 pins, gold plated

GLOaggts

Connector USB micro Type-B 5-pin plug (2.5g) (gold-plated)
technology mix;
production mix, at producer;
USB micro Type-B 5-pin plug (2.5g) (gold-plated)

GLOaggts

Connector USB mini (2,8 g, 4 pins, gold plated)
technology mix;
production mix, at producer;
2,8 g, 4 pins, gold plated

GLOaggts

Connector USB mini 5-pin socket (760mg) (gold-plated)
technology mix;
production mix, at producer;
USB mini 5-pin socket (760mg) (gold-plated)

GLOaggts

Connector USB mini Type-B 5-pin plug (1.1g) (gold-plated)
technology mix;
production mix, at producer;
USB mini Type-B 5-pin plug (1.1g) (gold-plated)

GLOaggts

Connector USB type A (1,6 g, 4 pins, gold plated)
technology mix;
production mix, at producer;
1,6 g, 4 pins, gold plated

GLOaggts

Connector USB type B (8,1 g, 4 pins, gold plated)
technology mix;
production mix, at producer;
8,1 g, 4 pins, gold plated

GLOaggts

Connector USB Type-A 4-pin socket (2.1g) (gold-plated)
technology mix;
production mix, at producer;
USB Type-A 4-pin socket (2.1g) (gold-plated)

GLOaggts

Connector USB Type-B 4-pin plug (10.2g) (gold-plated)
technology mix;
production mix, at producer;
USB Type-B 4-pin plug (10.2g) (gold-plated)

GLOaggts

Connector USB Type-B 4-pin socket (2.8g) (gold-plated)
technology mix;
production mix, at producer;
USB Type-B 4-pin socket (2.8g) (gold-plated)

GLOaggts

Connector wire-to-board IDC 2.54mm-pitch 2x10 (20-pin) cable-mounted socket (3.3g) (gold-plated)
technology mix;
production mix, at producer;
wire-to-board IDC 2.54mm-pitch 2x10 (20-pin) cable-mounted socket (3.3g) (gold-plated)

GLOaggts

Connector wire-to-board IDC 2.54mm-pitch 2x10 (20-pin) cable-mounted socket (3.3g) (tin-plated)
technology mix;
production mix, at producer;
wire-to-board IDC 2.54mm-pitch 2x10 (20-pin) cable-mounted socket (3.3g) (tin-plated)

GLOaggts

Connector wire-to-board pin-header 2.54mm-pitch 2x10 (20-pin) (1.3g) (gold-plated)
technology mix;
production mix, at producer;
wire-to-board pin-header 2.54mm-pitch 2x10 (20-pin) (1.3g) (gold-plated)

GLOaggts

Connector wire-to-board pin-header 2.54mm-pitch 2x10 (20-pin) (1.3g) (tin-plated)
technology mix;
production mix, at producer;
wire-to-board pin-header 2.54mm-pitch 2x10 (20-pin) (1.3g) (tin-plated)

GLOaggts

Copper chloride catalyst (estimation)
direct combination of copper and chlorine;
single route, at plant;
3.39 g/cm3, 134.45 g/mol

DEaggts

Copper chloride catalyst (estimation)
direct combination of copper and chlorine;
single route, at plant;
3.39 g/cm3, 134.45 g/mol

JPaggts

Copper phthalocyanine
phthalic anhydride- urea process;
single route, at plant;
1.62 g/cm3, 576.07 g/mol

JPaggts

Copper phthalocyanine (estimation)
phthalic anhydride- urea process;
single route, at plant;
1.62 g/cm3, 576.07 g/mol

DEaggts

Copper sulphate as by-product from copper route
mining, benefication, roasting, CuSO4 production;
production mix, at plant;
3.60 g/cm3, 159.61 g/mol

USaggts

Copper sulphate as by-product from copper route
mining, benefication, roasting, CuSO4 production;
production mix, at plant;
3.60 g/cm3, 159.61 g/mol

CAaggts

Copper wire (0.06 mm)
wire drawing;
single route, at plant;
0.06mm

DEaggts

Copper wire (0.06 mm)
wire drawing;
single route, at plant;
0.06mm

EU-28aggts

Copper wire (0.6 mm)
wire drawing;
single route, at plant;
0.6mm

EU-28aggts

Cork broken
Cork treatment, cork breaking;
single route, at plant;
120–240 kg/m3

DEaggts

Cork flour
Cork washing and grinding;
production mix, at plant;
grain size ~0,0001mm

DEaggts

Cork flour (EN15804 A1-A3)
Cork washing and grinding;
production mix, at plant;
grain size ~0,0001mm

EU-28aggts

Cork veneer
Cork treatment;
single route, at plant;
120–240 kg/m3

DEaggts

Corrugated board 2015, 84,5% recycled fiber, for use in cut-off EoL
technology mix;
production mix, at producer;
15,5% primary fibre, 84,5% recycled fibre

EU-28p-aggts/FEFCO

Cotton fibre (conventional)
cotton ginning;
single route, at plant;
length of fibers 0.5 inch to 2 inches,1.54–1.56 g/cm³

USaggts

Cotton fibre (organic)
cotton ginning;
single route, at plant;
length of fibers 0.5 inch to 2 inches,1.54–1.56 g/cm³

USaggts

Cottonseed meal
cotton cultivation, seed harvesting, pressing, extraction, refining;
single producer, at plant;
press cake from cotton oil pressing

USaggts

Cresol (p-cresol)
sulfonation of toluene;
single route, at plant;
1.05 g/cm3, 108.14 g/mol

DEaggts

Crude coconut oil
harvest, pressing and extraction;
single route, at plant;
80% carbon content

MYaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.3 MJ/kg net calorific value

IRaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.5 MJ/kg net calorific value

EU-28aggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.5 MJ/kg net calorific value

SAaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.1 MJ/kg net calorific value

ECaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.5 MJ/kg net calorific value

MYaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
43.0 MJ/kg net calorific value

MAaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.2 MJ/kg net calorific value

BAaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
41.3 MJ/kg net calorific value

MXaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.2 MJ/kg net calorific value

HRaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.2 MJ/kg net calorific value

US-CAaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.4 MJ/kg net calorific value

OMaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.2 MJ/kg net calorific value

DKaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
43.5 MJ/kg net calorific value

DZaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.3 MJ/kg net calorific value

IQaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.2 MJ/kg net calorific value

RUaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
41.3 MJ/kg net calorific value

IDaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.2 MJ/kg net calorific value

KZaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
43.4 MJ/kg net calorific value

CHaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
43.4 MJ/kg net calorific value

QAaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.7 MJ/kg net calorific value

ALaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.3 MJ/kg net calorific value

LKaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.2 MJ/kg net calorific value

RSaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.5 MJ/kg net calorific value

ARaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.4 MJ/kg net calorific value

KWaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.3 MJ/kg net calorific value

PHaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.1 MJ/kg net calorific value

COaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.8 MJ/kg net calorific value

NGaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.5 MJ/kg net calorific value

CLaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.2 MJ/kg net calorific value

AZaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.2 MJ/kg net calorific value

CZaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.2 MJ/kg net calorific value

TMaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.6 MJ/kg net calorific value

SGaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
43.1 MJ/kg net calorific value

AEaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.5 MJ/kg net calorific value

PEaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.2 MJ/kg net calorific value

UZaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.5 MJ/kg net calorific value

EGaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.6 MJ/kg net calorific value

KRaggts

Crude oil mix
technology mix of conventional and unconventional (oil sands, in-situ) production;
consumption mix, to consumer;
42.1 MJ/kg net calorific value

BGaggts

Cumene (isopropylbenzene) (C9H12)
alkylation of benzene;
production mix, at plant;
0.862 g/cm3, 120.20 g/mol

CNaggts

Cumene (isopropylbenzene) (C9H12)
alkylation of benzene;
production mix, at plant;
0.862 g/cm3, 120.20 g/mol

RUaggts

Cumene (isopropylbenzene) (C9H12)
alkylation of benzene;
production mix, at plant;
0.862 g/cm3, 120.20 g/mol

SGaggts

Cumene (isopropylbenzene) (C9H12)
alkylation of benzene;
production mix, at plant;
0.862 g/cm3, 120.20 g/mol

THaggts

Cumene (isopropylbenzene) (C9H12)
alkylation of benzene;
production mix, at plant;
0.862 g/cm3, 120.20 g/mol

KRaggts

Cumene (isopropylbenzene) (C9H12)
alkylation of benzene;
production mix, at plant;
0.862 g/cm3, 120.20 g/mol

JPaggts

Cumene (isopropylbenzene) (C9H12)
alkylation of benzene;
production mix, at plant;
0.862 g/cm3, 120.20 g/mol

TWaggts

Cumene (isopropylbenzene) (C9H12)
alkylation of benzene;
production mix, at plant;
0.862 g/cm3, 120.20 g/mol

SAaggts

Cupric carbonate basic by-product sodium sulphate (estimation)
reaction of copper sulphate and sodium carbonate;
production mix, at plant;
4 g/cm3, 221 g/mol

EU-28aggts

Cyanogen Chloride (via chlorination of hydrocyanic acid)
chlorination of hydrocyanic acid;
single route, at plant;
61.47 g/mol

DEaggts

Cyanuric acid
pyrolysis of urea;
production mix, at plant;
2.5 g/cm3, 129.07 g/mol

DEaggts

Cyanuric chloride (via trimerization of cyanogen chloride)
via trimerization of cyanogen chloride;
single route, at plant;
1.32 g/cm3, 184.40 g/mol

DEaggts

Cyclododecatriene (CDT, 1,5,9-Cyclododecatriene)
cyclotrimerization of butadiene;
production mix, at plant;
0.89 g/cm3, 162.28 g/mol

DEaggts

Cyclododecatriene by-products 1,5-Cyclooctadiene, 4-Vinylcyclohexene
cyclotrimerization of butadiene;
single route, at plant;
0.89 g/cm3, 162.28 g/mol

DEaggts

Cyclohexanone
from cyclohexane;
production mix, at plant;
0.95 g/cm3, 98.15 g/mol

DEaggts

DDGS (from ethanol from corn)
Corn dry mill process;
single producer, at plant;
26.5% CP

USaggts

Decabromodiphenyl ethane (estimation)
reaction of diphenyl ethane with bromine;
single route, at plant;
971.22 g/mol

DEaggts

Decanoic acid (capric acid) from palm kernel oil (incl. LUC as fossil CO2) (estimate)
Enzymatic hydrolysis of palm oil, separation of capric acid;
single producer, at plant;
density: 0.893 g/cm3, molar mass: 172.26 g mol−1

EU-28aggts

Degreasing agent (aluminium)
mixture of soda, tensides, isononanol and water;
production mix, at plant;
estimation, degreaser

DEaggts

Deionised water (estimation)
via ion exchange;
single route, at plant;
1 kg/l, 18 g/mol

MYaggts

Deionised water (estimation)
via ion exchange;
single route, at plant;
1 kg/l, 18 g/mol

INaggts

Deionised water (estimation)
via ion exchange;
single route, at plant;
1 kg/l, 18 g/mol

THaggts

Deionised water (reverse-osmosis/electrical-deionisation)
technology mix, reverse-osmosis/electrical-deionisation;
production mix, at plant;
1000 kg/m3, 18 g/mol

CNaggts

Desalinated sea water (reverse osmosis with energy recovery)
reverse osmosis with energy recovery;
single route, at plant;
1000 kg/m3, 18 g/mol

DEaggts

Desalinated sea water (reverse osmosis without energy recovery)
reverse osmosis without energy recovery;
single route, at plant;
1000 kg/m3, 18 g/mol

DEaggts

Desalinated sea water (Vaporisation, MSF-Plant)
vaporisation, multi- stage- flash plant;
single route, at plant;
1000 kg/m3, 18 g/mol

DEaggts

Desalinated sea water technology mix (Abu Dhabi)
technology mix, multi stage flash and reverse osmosis;
production mix, at plant;
1000 kg/m3, 18 g/mol

AEaggts

Diammonium phosphate granular fertilizer (DAP)
reaction of ammonia and phosphoric acid;
single producer, at plant;
density 1.619 g/cm3, molar mass 132.07 g/mol

DEaggts

Dibenzanthrone
alkaline fusion of benzanthrone;
production mix, at plant;
1.53 g/cm3, 456.49 g/mol

USaggts

Dichloromethane
chlorination of methyl chloride;
production mix, at plant;
1.33 g/cm3, 84.93 g/mol

EU-28aggts

Dichloromethane (estimation)
chlorination of methyl chloride;
production mix, at plant;
1.33 g/cm3, 84.93 g/mol

USaggts

Dichloropropene by-product allyl chloride (C3H5Cl)
chlorination of propene;
single route, at plant;
1.16 g/cm3, 112.98 g/mol

DEaggts

Dichlorotetrafluoroethane (R114) (estimation)
from perchloroethylene, hydrogen fluoride and chlorine;
production mix, at plant;
1.46 g/cm3, 170.92 g/mol

DEaggts

Dichlorpropane by-product epichlorohydrin, hydrochloric acid
chlorination of propene;
single route, at plant;
1.16 g/cm3, 112.98 g/mol

DEaggts

Dicumyl peroxide (stoichiometric estimation)
via cumyl hydroperoxide;
single route, at plant;
1.02 g/cm3, 270.37 g/mol

EU-28aggts

Diesel at refinery
from crude oil;
production mix, at refinery;
10 ppm sulphur

NLaggts

Diesel at refinery
from crude oil;
production mix, at refinery;
10 ppm sulphur

AUaggts

Diesel at refinery
from crude oil;
production mix, at refinery;
10 ppm sulphur

GBaggts

Diesel at refinery
from crude oil;
production mix, at refinery;
350 ppm sulphur

INaggts

Diesel at refinery
from crude oil;
production mix, at refinery;
10 ppm sulphur

EU-28aggts

Diesel at refinery
from crude oil;
production mix, at refinery;
50 ppm sulphur

MYaggts

Diesel at refinery
from crude oil;
production mix, at refinery;
800 ppm sulphur

CNaggts

Diesel at refinery
from crude oil;
production mix, at refinery;
500 ppm sulphur

BRaggts

Diesel at refinery
from crude oil;
production mix, at refinery;
10 ppm sulphur

JPaggts

Diesel at refinery
from crude oil;
production mix, at refinery;
10 ppm sulphur

DEaggts

Diesel at refinery
from crude oil;
production mix, at refinery;
15 ppm sulphur

USaggts

Diesel at refinery
from crude oil;
production mix, at refinery;
10 ppm sulphur

FRaggts

Diesel at refinery Western Australia
from crude oil;
production mix, at refinery;
10 ppm sulphur

AUaggts

Diesel combustion forest engines
diesel- driven forest engine;
single operation, at work station;
1 kg diesel combusted

GLOu-sots

Diesel combustion in construction machine
diesel driven

GLOu-sots

Diesel fuel supplied and combusted in diesel generator
technology mix regarding firing and flue gas cleaning;
production mix, at diesel generator

EU-28aggts

Diesel fuel supplied and combusted in diesel generator (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28aggts

Diesel fuel supplied and combusted in diesel generator (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28aggts

Diesel generator mechanical
diesel engine;
single operation, at work station;
>500 kW

GLOu-sots

Diesel mix at refinery
from crude oil and bio components;
production mix, at refinery;
10 ppm sulphur, 3.30 wt.% bio components

NLaggts

Diesel mix at refinery
from crude oil and bio components;
production mix, at refinery;
350 ppm sulphur, 0.00 wt.% bio components

RUaggts

Diesel mix at refinery
from crude oil and bio components;
production mix, at refinery;
50 ppm sulphur, 7.42 wt.% bio components

MYaggts

Diesel mix at refinery
from crude oil and bio components;
production mix, at refinery;
10 ppm sulphur, 9.2 wt.% bio components

FRaggts

Diesel mix at refinery Western Australia
from crude oil and bio components;
production mix, at refinery;
10 ppm sulphur, 1.26 wt.% bio components

AUaggts

Diethanolamine (DEA)
Reaction of ethylene oxide with excess of ammonia;
production mix, at producer;
100% active substance, 1.09 g/cm3, 105.14 g/mol

DEaggts

Diethyl carbonate (DEC)
phosgenation of ethanol;
single producer, at plant;
0.975 g/cm3, 118.13 g/mol

DEaggts

Diethyl ether
from ethylene;
production mix, at plant;
by-product ethanol (96%)

DEaggts

Diethyl ether (estimation)
from ethylene;
production mix, at plant;
by-product ethanol (96%)

CNaggts

Diethylamine (by-product Ethylamine, triethylamine (TEA)
from ethanol and ammonia, by-product Ethylamine, Triethylamine;
production mix, at plant;
0.70 g/cm3, 73.14 g/mol

DEaggts

Diethylaniline (2,6) from aniline
reraction of ethene and aniline;
single route, at plant;
0.93 g/cm3, 149.24 g/mol

DEaggts

Diethyldithiocarbamate
from diethyl amine, sodium hydroxide and carbon disulphide;
production mix, at plant;
1.1 g/cm3, 171.26 g/mol

DEaggts

Diethylene glycol by-product ethylene glycol from ethene and oxygen via EO
from ethene and oxygen;
single route, at plant;
1.12 g/m³, 106 g/mol

EU-28aggts

Diethylene glycol by-product ethylene glycol from ethene and oxygen via EO (estimation)
from ethene and oxygen;
single route, at plant;
1.12 g/m³, 106 g/mol

SAaggts

Dihydromyrcenol in waste incineration plant
waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment;
production mix (region specific plants), at plant;
28% of the energy output is electricity, 72% is steam

EU-28p-aggts

Di-iso-butyl Aluminium Hydride (DiBaH)
hydration and butylation of aluminium;
production mix, at plant;
0.79 g/cm3, 142.22 g/mol

DEaggts

Dimethyl succinate (estimation)
cataltytic hydrogenation of maleic acid and the esterification of succinic acid with methanol;
single route, at plant;
1.117 g/mL, 146.14 g/mol

DEaggts

Dimethyl sulfoxide (from Dimethylsulfide)
catalytic oxidation of dimethyl sulfide with oxygen;
single router, at plant;
1.10 g/cm3, 78.13 g/mol

DEaggts

Dimethylamine
reaction of methanol and ammonia;
production mix, at plant;
0.67 g/cm3, 45.08 g/mol

DEaggts

Dimethylamine
reaction of methanol and ammonia;
production mix, at plant;
0.67 g/cm3, 45.08 g/mol

USaggts

Dimethyldichlorosilane
Rochow-Müller-process;
single route, at plant;
1.06 g/cm3, 129.06 g/mol

EU-28aggts

Dimethyldichlorosilane
Rochow-Müller-process;
single route, at plant;
1.06 g/cm3, 129.06 g/mol

USaggts

Dimethylformamide (DMF) (estimation)
catalyzed reaction of dimethylamine and carbon monoxide;
single route, at plant;
0.948 g/cm3, 73.09 g/mol

DEaggts

Dimethyloxalate
oxidative carbonylation of methanol;
single route, at plant;
1.15 g/cm3, 118.09 g/mol

DEaggts

Dimethylsulphidetoluene diamine (DMTDA) (estimation)
reaction of toluene diamine with an organic disulphide;
production mix, at plant;
1.21 g/cm3, 214.36 g/mol

DEaggts

Di-n-butene via Octol Process
industry mix, from n-butene;
single route, at plant;
0.62 g/cm3, 56.11 g/mol

USaggts

Dinitromethane, potassium salt
from 1,2,4-triazol-5-on, nitric acid (96%) and sulphuric acid (96%);
single route, at plant;
144 g/mol

EU-28aggts

Dioctylphthalate/di-(2-ethylhexyl) phthalate (DOTP, DEHP) from esterification of phthalic anhydride
esterification of phthalic anhydride and octanol;
single route, at plant;
0,98 g/cm3, 390.56 g/mol

USaggts

Dioxothiolane (Sulfolan)
from butadiene, via sulfolene;
production mix, at plant;
1.26 g/cm3, 120.17 g/mol

DEaggts

Diphenyl (via benzene from toluene dealkylation)
Byproduct of benzene process from toluene dealkylation;
production mix, at plant;
1.04 g/cm3, 154.21 g/mol

DEaggts

Diphenyloxide (estimation)
non-catalytic process for the production of diphenyloxid and phenylphenol;
production mix, at plant;
170.21 g/mol

EU-28aggts

Dipropylene glycol
from propylene oxide, by product propylene glycol;
production mix, at plant;
1.02 g/cm3, 134.17 g/mol

DEaggts

Dipropyleneglycol dibenzoate plast
production from dipropylene glycol and methyl benzoate;
production mix, at plant;
342.39 g/mol

EU-28aggts

Distance travelled by biodiesel (B100) car >2 l
biodiesel driven, Euro 4, passenger car;
consumption mix;
engine size more than 2l

EU-28aggts

Distance travelled by biodiesel (B100) car >2 l (direct)
biodiesel driven, Euro 4, passenger car;
consumption mix;
engine size more than 2l

EU-28aggts

Distance travelled by biodiesel (B100) car >2 l (indirect)
biodiesel driven, Euro 4, passenger car;
consumption mix;
engine size more than 2l

EU-28aggts

Distance travelled by biodiesel (B100) car 1,4-2 l
biodiesel driven, Euro 4, passenger car;
consumption mix;
engine size 1,4-2l

EU-28aggts

Distance travelled by biodiesel (B100) car 1,4-2 l (direct)
biodiesel driven, Euro 4, passenger car;
consumption mix;
engine size 1,4-2l

EU-28aggts

Distance travelled by biodiesel (B100) car 1,4-2 l (indirect)
biodiesel driven, Euro 4, passenger car;
consumption mix;
engine size 1,4-2l

EU-28aggts

Distance travelled by compressed natural gas (CNG) car 1.3 l
CNG driven, Euro 4, passenger car;
consumption mix;
engine size 1,3l

EU-28aggts

Distance travelled by compressed natural gas (CNG) car 1.3 l (direct)
CNG driven, Euro 4, passenger car;
consumption mix;
engine size 1,3l

EU-28aggts

Distance travelled by compressed natural gas (CNG) car 1.3 l (indirect)
CNG driven, Euro 4, passenger car;
consumption mix;
engine size 1,3l

EU-28aggts

Distance travelled by compressed natural gas (CNG) car 1.6 l
CNG driven, Euro 4, passenger car;
consumption mix;
engine size 1,6l

EU-28aggts

Distance travelled by compressed natural gas (CNG) car 1.6 l (direct)
CNG driven, Euro 4, passenger car;
consumption mix;
engine size 1,6l

EU-28aggts

Distance travelled by compressed natural gas (CNG) car 1.6 l (indirect)
CNG driven, Euro 4, passenger car;
consumption mix;
engine size 1,6l

EU-28aggts

Distance travelled by compressed natural gas (CNG) car 1.9 l
CNG driven, Euro 4, passenger car;
consumption mix;
engine size 1,9l

EU-28aggts

Distance travelled by compressed natural gas (CNG) car 1.9 l (direct)
CNG driven, Euro 4, passenger car;
consumption mix;
engine size 1,9l

EU-28aggts

Distance travelled by compressed natural gas (CNG) car 1.9 l (indirect)
CNG driven, Euro 4, passenger car;
consumption mix;
engine size 1,9l

EU-28aggts

Distance travelled by diesel car >2 l
diesel driven, Euro 4, passenger car;
consumption mix;
engine size more than 2l

EU-28aggts

Distance travelled by diesel car >2 l (direct)
diesel driven, Euro 4, passenger car;
consumption mix;
engine size more than 2l

EU-28aggts

Distance travelled by diesel car >2 l (indirect)
diesel driven, Euro 4, passenger car;
consumption mix;
engine size more than 2l

EU-28aggts

Distance travelled by diesel car 1,4-2 l
diesel driven, Euro 4, passenger car;
consumption mix;
engine size 1,4-2l

EU-28aggts

Distance travelled by diesel car 1,4-2 l (direct)
diesel driven, Euro 4, passenger car;
consumption mix;
engine size 1,4-2l

EU-28aggts

Distance travelled by diesel car 1,4-2 l (indirect)
diesel driven, Euro 4, passenger car;
consumption mix;
engine size 1,4-2l

EU-28aggts

Distance travelled by gasoline car <1,4 l
gasoline driven, Euro 4, passenger car;
consumption mix;
engine size up to 1,4l

EU-28aggts

Distance travelled by gasoline car <1,4 l (direct)
gasoline driven, Euro 4, passenger car;
consumption mix;
engine size up to 1,4l

EU-28aggts

Distance travelled by gasoline car <1,4 l (indirect)
gasoline driven, Euro 4, passenger car;
consumption mix;
engine size up to 1,4l

EU-28aggts

Distance travelled by gasoline car >2 l
gasoline driven, Euro 4, passenger car;
consumption mix;
engine size more than 2l

EU-28aggts

Distance travelled by gasoline car >2 l (direct)
gasoline driven, Euro 4, passenger car;
consumption mix;
engine size more than 2l

EU-28aggts

Distance travelled by gasoline car >2 l (indirect)
gasoline driven, Euro 4, passenger car;
consumption mix;
engine size more than 2l

EU-28aggts

Distance travelled by gasoline car 1,4-2 l
gasoline driven, Euro 4, passenger car;
consumption mix;
engine size 1,4-2l

EU-28aggts

Distance travelled by gasoline car 1,4-2 l (direct)
gasoline driven, Euro 4, passenger car;
consumption mix;
engine size 1,4-2l

EU-28aggts

Distance travelled by gasoline car 1,4-2 l (indirect)
gasoline driven, Euro 4, passenger car;
consumption mix;
engine size 1,4-2l

EU-28aggts

Distance travelled by IC/ EC train (indirect)
electricity driven, passenger train;
consumption mix;
IC/EC train

DEaggts

Distance travelled by ICE train <200 kmh (indirect)
electricity driven, passenger train;
consumption mix;
ICE train <200 kmh

DEaggts

Distance travelled by ICE train >200 kmh (indirect)
electricity driven, passenger train;
consumption mix;
ICE train >200 kmh

DEaggts

Distance travelled by liquified petroleum gas (LPG) car <1,4 l
LPG driven, Euro 4, passenger car;
consumption mix;
engine size up to 1,4l

EU-28aggts

Distance travelled by liquified petroleum gas (LPG) car <1,4 l (direct)
LPG driven, Euro 4, passenger car;
consumption mix;
engine size up to 1,4l

EU-28aggts

Distance travelled by liquified petroleum gas (LPG) car <1,4 l (indirect)
LPG driven, Euro 4, passenger car;
consumption mix;
engine size up to 1,4l

EU-28aggts

Distance travelled by liquified petroleum gas (LPG) car 1,4-2,0 l
LPG driven, Euro 4, passenger car;
consumption mix;
engine size 1,4-2l

EU-28aggts

Distance travelled by liquified petroleum gas (LPG) car 1,4-2,0 l (direct)
LPG driven, Euro 4, passenger car;
consumption mix;
engine size 1,4-2l

EU-28aggts

Distance travelled by liquified petroleum gas (LPG) car 1,4-2,0 l (indirect)
LPG driven, Euro 4, passenger car;
consumption mix;
engine size 1,4-2l

EU-28aggts

Distance travelled by plane (1000 km) (indirect)
technology mix, kerosene driven, passenger plane;
production mix, at plant;
1000 km

EU-28aggts

Distance travelled by plane (250 km) (indirect)
technology mix, kerosene driven, passenger plane;
production mix, at plant;
250 km

EU-28aggts

Distance travelled by plane (500 km) (indirect)
technology mix, kerosene driven, passenger plane;
production mix, at plant;
500 km

EU-28aggts

Distance travelled by plane (5000 km) (indirect)
technology mix, kerosene driven, passenger plane;
production mix, at plant;
5000 km

EU-28aggts

Distance travelled by public bus (indirect)
diesel driven, passenger bus;
consumption mix;
Euro 4, 14 - 20t gross weight, 11,4t payload capacity

DEaggts

Distance travelled by RE/ RB/ IRE train (indirect)
electricity driven, passenger train;
consumption mix;
RE/ RB/ IRE train

DEaggts

Distance travelled by truck trailer, 22 t payload [km]
diesel driven, cargo;
consumption mix;
Euro 4, 28 - 34t gross weight, 22t payload capacity

EU-28aggts

Distance travelled by truck trailer, 22 t payload [km] (direct)
diesel driven, cargo;
consumption mix;
Euro 4, 28 - 34t gross weight, 22t payload capacity

EU-28aggts

Distance travelled by truck trailer, 22 t payload [km] (indirect)
diesel driven, cargo;
consumption mix;
Euro 4, 28 - 34t gross weight, 22t payload capacity

EU-28aggts

Distance travelled by truck, 11.4 t payload [km]
diesel driven, cargo;
consumption mix;
Euro 4, 14 - 20t gross weight, 11,4t payload capacity

EU-28aggts

Distance travelled by truck, 11.4 t payload [km] (direct)
diesel driven, cargo;
consumption mix;
Euro 4, 14 - 20t gross weight, 11,4t payload capacity

EU-28aggts

Distance travelled by truck, 11.4 t payload [km] (indirect)
diesel driven, cargo;
consumption mix;
Euro 4, 14 - 20t gross weight, 11,4t payload capacity

EU-28aggts

Distance travelled by truck, 17.3 t payload [km]
diesel driven, cargo;
consumption mix;
Euro 4, 20 - 26t gross weight, 17,3t payload capacity

EU-28aggts

Distance travelled by truck, 17.3 t payload [km] (direct)
diesel driven, cargo;
consumption mix;
Euro 4, 20 - 26t gross weight, 17,3t payload capacity

EU-28aggts

Distance travelled by truck, 17.3 t payload [km] (indirect)
diesel driven, cargo;
consumption mix;
Euro 4, 20 - 26t gross weight, 17,3t payload capacity

EU-28aggts

Distance travelled by truck, 22 t payload [km]
diesel driven, cargo;
consumption mix;
Euro 4, 28 - 32t gross weight, 22t payload capacity

EU-28aggts

Distance travelled by truck, 22 t payload [km] (direct)
diesel driven, cargo;
consumption mix;
Euro 4, 28 - 32t gross weight, 22t payload capacity

EU-28aggts

Distance travelled by truck, 22 t payload [km] (indirect)
diesel driven, cargo;
consumption mix;
Euro 4, 28 - 32t gross weight, 22t payload capacity

EU-28aggts

Distance travelled by truck, 24.7 t payload [km]
diesel driven, cargo;
consumption mix;
Euro 4, more than 32t gross weight, 24,7t payload capacity

EU-28aggts

Distance travelled by truck, 24.7 t payload [km] (direct)
diesel driven, cargo;
consumption mix;
Euro 4, more than 32t gross weight, 24,7t payload capacity

EU-28aggts

Distance travelled by truck, 24.7 t payload [km] (indirect)
diesel driven, cargo;
consumption mix;
Euro 4, more than 32t gross weight, 24,7t payload capacity

EU-28aggts

Distance travelled by truck, 3.3 t payload [km]
diesel driven, cargo;
consumption mix;
Euro 4, up to 7,5t gross weight, 3,3t payload capacity

EU-28aggts

Distance travelled by truck, 3.3 t payload [km] (direct)
diesel driven, cargo;
consumption mix;
Euro 4, up to 7,5t gross weight, 3,3t payload capacity

EU-28aggts

Distance travelled by truck, 3.3 t payload [km] (indirect)
diesel driven, cargo;
consumption mix;
Euro 4, up to 7,5t gross weight, 3,3t payload capacity

EU-28aggts

Distance travelled by truck, 5 t payload [km]
diesel driven, cargo;
consumption mix;
Euro 4, 7,5 t - 12t gross weight, 5t payload capacity

EU-28aggts

Distance travelled by truck, 5 t payload [km] (direct)
diesel driven, cargo;
consumption mix;
Euro 4, 7,5 t - 12t gross weight, 5t payload capacity

EU-28aggts

Distance travelled by truck, 5 t payload [km] (indirect)
diesel driven, cargo;
consumption mix;
Euro 4, 7,5 t - 12t gross weight, 5t payload capacity

EU-28aggts

Distance travelled by truck, 9.3 t payload [km]
diesel driven, cargo;
consumption mix;
Euro 4, 12-14t gross weight, 9,3t payload capacity

EU-28aggts

Distance travelled by truck, 9.3 t payload [km] (direct)
diesel driven, cargo;
consumption mix;
Euro 4, 12-14t gross weight, 9,3t payload capacity

EU-28aggts

Distance travelled by truck, 9.3 t payload [km] (indirect)
diesel driven, cargo;
consumption mix;
Euro 4, 12-14t gross weight, 9,3t payload capacity

EU-28aggts

Distance travelled by urban railway (indirect)
electricity driven, passenger train;
consumption mix;
passenger train urban

DEaggts

District cooling (estimation)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

EGaggts

District cooling (estimation)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

PKaggts

District cooling (estimation)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

MAaggts

District cooling (estimation)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

UAaggts

District cooling (estimation)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

VNaggts

District cooling (estimation)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

IDaggts

District cooling (estimation)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

RSaggts

District cooling (estimation)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

KZaggts

District cooling (estimation)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

TRaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

NOaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

GRaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

NLaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

IDaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

MAaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

CHaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

EGaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

FIaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

LUaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

USaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

SEaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

VNaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

BEaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

HUaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

CZaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

UAaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

SGaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

TRaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

PTaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

RSaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

MXaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

MYaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

PLaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

PKaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

CAaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

ATaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

FRaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

ESaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

DEaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

KZaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

AEaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

GBaggts

District cooling (estimation) (direct)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

JPaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

JPaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

KZaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

CAaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

SEaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

NOaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

DEaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

CHaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

TRaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

VNaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

AEaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

EGaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

BEaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

MYaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

NLaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

PLaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

ATaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

FRaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

IDaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

LUaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

PTaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

SGaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

HUaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

RSaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

USaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

GBaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

PKaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

UAaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

ESaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

CZaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

GRaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

MXaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

MAaggts

District cooling (estimation) (indirect)
pumping cold water, electricity needed for powering pumps;
production mix, at plant;
COP 3,7 (0.27kWh electricity for 1kWh cooling)

FIaggts

District heating mix
technology mix;
production mix, at plant;
10.7 % energy loss during transmission

DEaggts

District heating mix
technology mix;
production mix, at plant;
10.7 % energy loss during transmission

CNaggts

Dolomite (ground)
dolomite mining and milling;
single route, at plant;
2.90 g/cm3

DEaggts

Dolomite calcination (derived from lime calcination)
Decarboxylation process by burning mined dolomite;
production mix, at plant;
2.90 g/cm3

DEaggts

Dolomite calcination (derived from lime calcination)
Decarboxylation process by burning mined dolomite;
production mix, at plant;
2.90 g/cm3

EU-28aggts

Dolomite calcination (derived from lime calcination)
Decarboxylation process by burning mined dolomite;
production mix, at plant;
2.90 g/cm3

USaggts

Domestic waste (wood, natural finish) on landfill
landfill including landfill gas utilisation and leachate treatment and without collection, transport and pre-treatment;
production mix (region specific sites), at landfill site;
wood, natural finish

EU-28p-aggts

Dragon seed (lat. Lallemantia iberica) dried (9% H2O content)
Dragon seed cultivation (seeding technique, fertilizing, using pesticides), harvesting, drying;
single route, at field border;
9% H2O (maximum moisture for storage)

DEaggts

Dried quartz sand (grain size 0/2)
technology mix;
production mix, at plant;
grain size 0/2

EU-28aggts

Dried starch (Polyglucose) from corn (economic allocation)
corn cultivation and harvesting, wet milling process;
single producer, at plant;
dried corn starch

EU-28aggts

Drum drying (average)
Drum drying;
single operation, at producer;
Drying product on a drum dryer

EU-28p-aggts

Drum drying (average)
Drum drying;
single operation, at producer;
Drying product on a drum dryer

USp-aggts

Dry haricot beans (14% H2O)
bean cultivation and harvest;
production mix, at field border;
14 % H2O

USaggts

Dyes
mixture of aniline and 2,4-dimethylbenzaldehyde;
single producer, at plant;
50% aniline, 50% dimethylbenzaldehyde

DEaggts

Dysprosium (price allocated)
primary production, ore mining and processing, electrolysis;
production mix, at plant;
8.56 g/cm3, 162.50 g/mol

CNaggts

Dysprosium Production (mass allocated)
mining and processing, primary production;
production mix, at plant;
8.54 g/cm3, 162.50 g/cm3

CNaggts

Electricity from biogas
AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
1kV - 60kV

RSaggts

Electricity from biogas (direct)
AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
1kV - 60kV

DEaggts

Electricity from biogas (indirect)
AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
1kV - 60kV

DEaggts

Electricity from biomass (solid)
AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
1kV - 60kV

CLaggts

Electricity from biomass (solid) (direct)
AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
1kV - 60kV

DEaggts

Electricity from biomass (solid) (indirect)
AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
1kV - 60kV

DEaggts

Electricity from diesel fuel (diesel generator)
technology mix regarding firing and flue gas cleaning;
production mix, at power plant

EU-28aggts

Electricity from diesel fuel (diesel generator) (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at power plant

EU-28aggts

Electricity from diesel fuel (diesel generator) (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at power plant

EU-28aggts

Electricity from hard coal
AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
1kV - 60kV

CLaggts

Electricity from hydro power (direct)
AC, technology mix of run-off-river, storage and pump storage;
production mix, at power plant;
1kV - 60kV

DEaggts

Electricity from hydro power (indirect)
AC, technology mix of run-off-river, storage and pump storage;
production mix, at power plant;
1kV - 60kV

DEaggts

Electricity from light fuel oil (LFO)
AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
1kV - 60kV

DEaggts

Electricity from light fuel oil (LFO)
AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
1kV - 60kV

FRaggts

Electricity from natural gas
AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
1kV - 60kV

USp-aggts

Electricity from natural gas (direct)
AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
1kV - 60kV

DEaggts

Electricity from natural gas (indirect)
AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
1kV - 60kV

DEaggts

Electricity from natural gas via CHP (without supply)
AC, combined heat and power generation (CHP), technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
1kV - 60kV

USp-aggts

Electricity from natural gas via direct (without supply)
AC, direct combustion, technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
1kV - 60kV

USp-aggts

Electricity from photovoltaic
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at plant;
1kV - 60kV

PHaggts

Electricity from photovoltaic
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at plant;
1kV - 60kV

ISaggts

Electricity from photovoltaic
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at plant;
1kV - 60kV

IDaggts

Electricity from photovoltaic
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at producer;
1kV - 60kV

UAaggts

Electricity from photovoltaic
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at plant;
1kV - 60kV

NOaggts

Electricity from photovoltaic
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at producer;
1kV - 60kV

EGaggts

Electricity from photovoltaic
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at plant;
1kV - 60kV

PKaggts

Electricity from photovoltaic
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at plant;
1kV - 60kV

THaggts

Electricity from photovoltaic
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at plant;
1kV - 60kV

KEaggts

Electricity from photovoltaic
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at plant;
1kV - 60kV

MXaggts

Electricity from photovoltaic
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at plant;
1kV - 60kV

KRaggts

Electricity from photovoltaic
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at plant;
1kV - 60kV

MKaggts

Electricity from photovoltaic
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at plant;
1kV - 60kV

SGaggts

Electricity from photovoltaic
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at plant;
1kV - 60kV

TWaggts

Electricity from photovoltaic
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at plant;
1kV - 60kV

HRaggts

Electricity from photovoltaic
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at plant;
1kV - 60kV

LKaggts

Electricity from photovoltaic
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at plant;
1kV - 60kV

GLOaggts

Electricity from photovoltaic
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at plant;
1kV - 60kV

ILaggts

Electricity from photovoltaic (indirect)
AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline;
production mix, at plant;
1kV - 60kV

DEaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

NGaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

RSaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

LKaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

HKaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

SAaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

BAaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

AEaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

DZaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

PYaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

SGaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

PKaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

OMaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

VNaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

PHaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

IQaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

KWaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

MAaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

KZaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

EGaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

QAaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

KEaggts

Electricity grid mix
AC, technology mix;
consumption mix, to consumer;
<1kV

ILaggts

Electricity grid mix - Central
AC, technology mix;
consumption mix, to consumer;
<1kV

CNaggts

Electricity grid mix - Central - 1kV-60kV
AC, technology mix;
consumption mix, to consumer;
1kV - 60kV

CNaggts

Electricity grid mix - East
AC, technology mix;
consumption mix, to consumer;
<1kV

CNaggts

Electricity grid mix - East - 1kV-60kV
AC, technology mix;
consumption mix, to consumer;
1kV - 60kV

CNaggts

Electricity grid mix - North
AC, technology mix;
consumption mix, to consumer;
<1kV

CNaggts

Electricity grid mix - North 1kV-60kV
AC, technology mix;
consumption mix, to consumer;
1kV - 60kV

CNaggts

Electricity grid mix - Northeast
AC, technology mix;
consumption mix, to consumer;
<1kV

CNaggts

Electricity grid mix - Northeast - 1kV-60kV
AC, technology mix;
consumption mix, to consumer;
1kV - 60kV

CNaggts

Electricity grid mix - Northwest
AC, technology mix;
consumption mix, to consumer;
<1kV

CNaggts

Electricity grid mix - Northwest - 1kV-60kV
AC, technology mix;
consumption mix, to consumer;
1kV - 60kV

CNaggts

Electricity grid mix - South
AC, technology mix;
consumption mix, to consumer;
<1kV

CNaggts

Electricity grid mix - South - 1kV-60kV
AC, technology mix;
consumption mix, to consumer;
1kV - 60kV

CNaggts

Electricity grid mix (average power plants) 1kV-60kV
AC, technology mix;
consumption mix, to consumer;
1kV - 60kV

EU-28aggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, at consumer;
<1kV

KZaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, at consumer;
<1kV

LKaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, to consumer;
<1kV

ZAaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, at consumer;
<1kV

HRaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, to consumer;
<1kV

HKaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, at consumer;
<1kV

PKaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, at consumer;
<1kV

VEaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, at consumer;
<1kV

IQaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, to consumer;
<1kV

SGaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, at consumer;
<1kV

MKaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, at consumer;
<1kV

RSaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, to consumer;
<1kV

PHaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, at consumer;
<1kV

NGaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, at consumer;
<1kV

KWaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, at consumer;
<1kV

QAaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, at consumer;
<1kV

KEaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, at consumer;
<1kV

SAaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, at consumer;
<1kV

OMaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, at consumer;
<1kV

ILaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, at consumer;
<1kV

PYaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, at consumer;
<1kV

EGaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, to consumer;
<1kV

BAaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, at consumer;
<1kV

DZaggts

Electricity grid mix (direct)
AC, technology mix;
consumption mix, to consumer;
<1kV

MAaggts

Electricity grid mix (direct) (eGRID)
AC, technology mix;
consumption mix, at consumer;
<1kV

USaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, at consumer;
<1kV

RSaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, at consumer;
<1kV

DZaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, at consumer;
<1kV

PYaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, at consumer;
<1kV

ILaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, at consumer;
<1kV

KEaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, to consumer;
<1kV

HKaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, at consumer;
<1kV

VEaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, at consumer;
<1kV

SAaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, to consumer;
<1kV

BAaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, at consumer;
<1kV

IQaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, at consumer;
<1kV

PKaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, at consumer;
<1kV

KZaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, to consumer;
<1kV

PHaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, at consumer;
<1kV

QAaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, at consumer;
<1kV

MKaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, at consumer;
<1kV

KWaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, at consumer;
<1kV

LKaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, at consumer;
<1kV

OMaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, at consumer;
<1kV

NGaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, at consumer;
<1kV

EGaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, at consumer;
<1kV

HRaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, to consumer;
<1kV

SGaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, to consumer;
<1kV

ZAaggts

Electricity grid mix (indirect)
AC, technology mix;
consumption mix, to consumer;
<1kV

MAaggts

Electricity grid mix (indirect) (eGRID)
AC, technology mix;
consumption mix, at consumer;
<1kV

USaggts

Electricity grid mix 1kV-60kV
AC, technology mix;
consumption mix, to consumer;
1kV - 60kV

AEaggts

Electrode
baking petrol coke, pitch and hard coal tar;
production mix, at plant;
>99% carbon

NOaggts

Electrode
baking petrol coke, pitch and hard coal tar;
production mix, at plant;
>99% carbon

ZAaggts

Electrolytic copper secondary (input heavy copper scrap 95-98% Cu)
copper scrap smelting and refining;
single route, at plant;
8.92 g/cm³, 63.55 g/mol

EU-28p-aggts

Electrolytic copper secondary (input light copper scrap 90% Cu)
copper scrap smelting and refining;
single route, at plant;
8.92 g/cm³, 63.55 g/mol

EU-28p-aggts

Electrolytic manganese dioxide (EMD, MnO2) using selenium
from manganese ore;
production mix, at plant;
5.03 g/cm3, 86.94 g/mol

CNaggts

Electrolytic manganese dioxide (EMD, MnO2) using SO2
from manganese ore;
production mix, at plant;
5.03 g/cm3, 86.94 g/mol

CNaggts

Electrolytic manganese dioxide (EMD, MnO2) using SO2
mining, crushing, calcination, electrolysis, oxidation;
production mix, at plant;
5.03 g/cm3, 86.94 g/mol

ZAaggts

EPDM waste in waste incineration plant (inclu credit)
waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment;
production mix (region specific plants), at plant;
43,0 MJ/kg net calorific value

DEp-aggts

Epichlorohydrin (by product calcium chloride, hydrochloric acid)
via allyl chloride;
single route, at plant;
1.18 g/cm3, 92.52 g/mol

BEaggts

Epichlorohydrin (by product calcium chloride, hydrochloric acid)
via allyl chloride;
single route, at plant;
1.18 g/cm3, 92.52 g/mol

NLaggts

Epichlorohydrin by-product calcium chloride, hydrochloric acid (estimation)
via allyl chloride;
single route, at plant;
1.18 g/cm3, 92.52 g/mol

EU-28aggts

Epichlorohydrin by-product dichlorpropane, hydrochloric acid
chlorination of propene;
single route, at plant;
1.18 g/cm3, 92.52 g/mol

DEaggts

Epichlorohydrin from refined glycerine
refined glycerine hydrochlorination to epichlorohydrin;
single route, at plant;
1.18 g/cm3, 92.52 g/mol

USaggts

Epoxidation of soybean oil (ESBO) - open input soy bean (estimation)
catalytic epoxidation;
production mix, at plant;
0.994 g/cm3

EU-28p-aggts

Epoxidized Methyl Soyate by-prod Glycerine (C mass allocated - estimation)
by-product glycerine, soy oil production, refining, transesterification;
production mix, at plant;
70,9% carbon content (67,15% bio)

EU-28aggts

Epoxised soybean oil (ESBO) (estimation)
epoxydising soy bean oil;
single route, at plant;
0.994 g/cm3

EU-28aggts

Epoxy Resin (EP)
from Bisphenol A and epichlorohydrin;
production mix, at plant;
approx. 1.15 g/cm3

ESaggts

Epoxy Resin (EP)
from Bisphenol A and epichlorohydrin;
production mix, at plant;
approx. 1.15 g/cm3

NLaggts

Epoxy Resin (EP)
from Bisphenol A and epichlorohydrin;
production mix, at plant;
approx. 1.15 g/cm3

ITaggts

EPS-Foam (expanded polystyrene foam (PS 12)) incl. flame retardant (estimation)
styrene polymerization, foaming;
production mix, at plant;
PS 12, including flame retardant

USaggts

Ethane
refinery gas separation;
single route, at plant;
1.36 g/l, 30.07 g/mol

DEaggts

Ethane
refinery gas separation;
single route, at plant;
1.36 g/l, 30.07 g/mol

USaggts

Ethanol (96%) (catalytic hydrogenation with phosphoric acid)
catalytic hydrogenation with phosphoric acid;
single route, at plant;
96 % concentrated

DEaggts

Ethene (ethylene)
steam cracker;
production mix, at plant;
1.178 kg/m3, 28.05 g/mol

JPaggts

Ethene (Ethylene)
steam cracker;
production mix, at plant;
1.178 kg/m3, 28.05 g/mol

MYaggts

Ethene (ethylene)
steam cracker;
production mix, at plant;
1.178 kg/m3, 28.05 g/mol

INaggts

Ethene (ethylene)
steam cracker;
production mix, at plant;
1.178 kg/m3, 28.05 g/mol

AUaggts

Ethene (ethylene) (estimation)
steam cracker;
production mix, at plant;
1.178 kg/m3, 28.05 g/mol

CNaggts

Ethene (ethylene) (estimation)
steam cracker;
production mix, at plant;
1.178 kg/m3, 28.05 g/mol

SAaggts

Ethene (ethylene) (estimation)
steam cracker;
production mix, at plant;
1.178 kg/m3, 28.05 g/mol

BEaggts

Ethene (Ethylene) (Oxi)
steam cracker;
production mix, at plant;
1.178 kg/m3, 28.05 g/mol

USaggts

Ethine (acetylene)
Sachsse-Bartholome process;
production mix, at plant;
1.18 g/l, 26.04 g/mol

GBaggts

Ethine (acetylene)
Sachsse-Bartholome process;
production mix, at plant;
1.18 g/l, 26.04 g/mol

EU-28aggts

Ethyl acetate by-product polyvinyl butyral (PVB)
reaction of butyric aldehyde with polyvinyl alcohol, by product polyvinyl butyral;
single route, at plant;
0.897 g/cm³, 88.11 g/mol

NLaggts

Ethyl benzene
liquid phase alkylation;
production mix, at plant;
0.87 g/cm3, 106.17 g/mol

EU-28aggts

Ethyl benzene
liquid phase alkylation;
production mix, at plant;
0.87 g/cm3, 106.17 g/mol

ESaggts

Ethyl carbonate
reaction of ethylene oxide and carbon dioxide;
production mix, at plant;
1.32 g/cm3, 88.06 g/mol

DEaggts

Ethylbenzene (liquid phase alkylation) (estimation)
liquid phase alkylation;
production mix, at plant;
0.87 g/cm, 106.17 g/mol

ITaggts

Ethylbenzene (liquid phase alkylation) (estimation)
liquid phase alkylation;
production mix, at plant;
0.87 g/cm, 106.17 g/mol

BEaggts

Ethylbenzene/Styrene in waste incineration plant
waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment;
production mix (region specific plants), at plant;
39,1 MJ/kg net calorific value

EU-28p-aggts

Ethylen Propylen Dien Elastomer (EPDM)
suspension polymerisation;
production mix, at plant;
Synthetic rubber

USaggts

Ethylene (Ethene) from ethanol (biobased from Brazilian sugar cane
dehydration of biobased ethanol;
production mix, at plant;
1.18 kg/m3, 28.05 g/mol

USaggts

Ethylene (Ethene) from ethanol (biobased from Brazilian sugar cane)
dehydration of biobased ethanol;
production mix, at plant;
1.18 kg/m3, 28.05 g/mol

EU-28aggts

Ethylene (Ethene) from ethanol (biobased from Brazilian sugar cane)
dehydration of biobased ethanol;
production mix, at plant;
1.18 kg/m3, 28.05 g/mol

DEaggts

Ethylene (Ethene) from ethanol (biobased from corn)
dehydration of biobased ethanol;
production mix, at plant;
1.18 kg/m3, 28.05 g/mol

USaggts

Ethylene (Ethene) from ethanol (biobased from corn)
dehydration of biobased ethanol;
production mix, at plant;
1.18 kg/m3, 28.05 g/mol

DEaggts

Ethylene (Ethene) from ethanol (biobased from sugar beet)
dehydration of biobased ethanol;
production mix, at plant;
1.18 kg/m3, 28.05 g/mol

DEaggts

Ethylene (Ethene) from ethanol (biobased from sugar beet)
dehydration of biobased ethanol;
production mix, at plant;
1.18 kg/m3, 28.05 g/mol

EU-28aggts

Ethylene (Ethene) from ethanol (biobased from US corn)
dehydration of biobased ethanol;
production mix, at plant;
1.18 kg/m3, 28.05 g/mol

EU-28aggts

Ethylene (Ethene) from ethanol (biobased from wheat)
dehydration of biobased ethanol;
production mix, at plant;
1.18 kg/m3, 28.05 g/mol

EU-28aggts

Ethylene (Ethene) from ethanol (biobased from wheat)
dehydration of biobased ethanol;
production mix, at plant;
1.18 kg/m3, 28.05 g/mol

USaggts

Ethylene (Ethene) from ethanol (biobased from wheat)
dehydration of biobased ethanol;
production mix, at plant;
1.18 kg/m3, 28.05 g/mol

DEaggts

Ethylene (Ethene) via dehydration of ethanol
dehydration of ethanol;
production mix, at plant;
1.18 kg/m3, 28.05 g/mol

EU-28aggts

Ethylene (Ethene) via dehydration of ethanol
dehydration of ethanol;
production mix, at plant;
1.18 kg/m3, 28.05 g/mol

USaggts

Ethylene bis(stearamide), EBS (stoichiometric estimation)
reaction of ethylene diamine with stearic acid;
production mix, at plant;
0.99–1.01 g/cm3, 593.04 g/mol

DEaggts

Ethylene carbonate
via carbon dioxide and ethylene oxide;
production mix, at plant;
1.32 g/cm3, 88.06 g/mol

DEaggts

Ethylene carbonate (CO2 from EO)
via carbon dioxide and ethylene oxide;
single route, at plant;
1.32 g/cm3, 88.06 g/mol

JPaggts

Ethylene chlorohydrin (estimation)
reaction of ethylene with chlorine and water;
single route, at plant;
1.20 g/cm3, 80.51 g/mol

DEaggts

Ethylene dichloride (EDC) (estimation)
from ethene and chlorine;
production mix, at plant;
1.25 g/cm3, 98.95 g/mol

EU-28aggts

Ethylene dichloride (EDC) (estimation)
from ethene and chlorine;
production mix, at plant;
1.25 g/cm3, 98.95 g/mol

GBaggts

Ethylene dichloride (EDC) (estimation)
from ethene and chlorine;
production mix, at plant;
1.25 g/cm3, 98.95 g/mol

DEaggts

Ethylene glycol butyl ether
via ethylene oxide with butyl alcohol;
production mix, at plant;
0.90 g/cm3, 118.18 g/mol

EU-28aggts

Ethylene glycol butyl ether
via ethylene oxide with butyl alcohol;
production mix, at plant;
0.90 g/cm3, 118.18 g/mol

DEaggts

Ethylene glycol butyl ether (butoxyethanol)
via ethylene oxide with butyl alcohol;
production mix, at plant;
0.90 g/cm3, 118.18 g/mol

USaggts

Ethylene glycol from Ethene (biobased from sugar beet) and oxygen via EO
from biobased ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

DEaggts

Ethylene glycol from Ethene (biobased from sugar beet) and oxygen via EO
from biobased ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

EU-28aggts

Ethylene glycol from Ethene (biobased from sugar cane) and oxygen via EO
from biobased ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

EU-28aggts

Ethylene glycol from Ethene (biobased from sugar cane) and oxygen via EO
from biobased ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

USaggts

Ethylene glycol from Ethene (biobased from sugar cane) and oxygen via EO
from biobased ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

DEaggts

Ethylene glycol from Ethene (biobased from US corn) and oxygen via EO
from biobased ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

DEaggts

Ethylene glycol from Ethene (biobased from US corn) and oxygen via EO
from biobased ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

USaggts

Ethylene glycol from Ethene (biobased from wheat) and oxygen via EO
from biobased ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

USaggts

Ethylene glycol from Ethene (biobased from wheat) and oxygen via EO
from biobased ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

DEaggts

Ethylene glycol from Ethene (biobased from wheat) and oxygen via EO
from biobased ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

EU-28aggts

Ethylene glycol from ethene and oxygen via EO
from ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

CNaggts

Ethylene glycol from ethene and oxygen via EO
from ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

DEaggts

Ethylene glycol from ethene and oxygen via EO
from ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

AUaggts

Ethylene glycol from Ethene and oxygen via EO (biobased from corn)
from biobased ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

EU-28aggts

Ethylene glycol from ethene and oxygen via EO (biobased from sugar cane)
oxidation of ethene with oxygen and water;
production mix, at plant;
1.11 g/cm³, 62 g/mol

EU-28aggts

Ethylene glycol from ethene and oxygen via EO (estimation)
from ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

MYaggts

Ethylene glycol from ethylene oxide
from ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

DEaggts

Ethylene Methacrylic Acid Ionomer (EMAA) (high pressure autoclave)
copolymerization of of ethylene and methacrylic acid;
single producer, at plant

DEaggts

Ethylene Methyl Acrylate (EMA)
copolymerization of ethene and methacrylate;
production mix, at plant;
0.94 g/cm3

DEaggts

Ethylene Norbornen copolymer (COC, Cyclic olefine copolymers)
copolymerization of ethylene and norbornene;
single producer, at plant;
density 1.02 g/cm³, solid

DEaggts

Ethylene oxide (EO) by-product carbon dioxide from air
purified, oxidation of ethylene with air;
production mix, at plant;
0.882 g/mL, 44 g/mol

EU-28aggts

Ethylene oxide (EO) by-product ethylene glycol via O2/methane
oxidation of ethylene with oxygen;
production mix, at plant;
1.93 kg/m3, 44.05 g/mol

EU-28aggts

Ethylene oxide (EO) via air
oxidation of ethylene with air;
production mix, at plant;
1.93 kg/m3, 44.05 g/mol

ESaggts

Ethylene propylene dien elastomer (EPDM) (biobased from BR sugar cane)
copolymerisation of ethylene (biobased) and propylene;
single route, at plant;
ethylene content around 45% to 85%

EU-28aggts

Ethylene Propylene Diene Elastomer (EPDM)
copolymerization of ethylene and propylene;
production mix, at plant;
0.90 to >2.00 g/cm3

EU-28aggts

Ethylene propylene diene elastomer extrusion profile (EPDM)
polymerization of ethylene and propylene, crosslinking, extrusion;
single route, at plant;
0.90 to >2.00 g/cm3

DEaggts

Ethylene propylene diene elastomer extrusion profile (EPDM)
polymerization of ethylene and propylene, crosslinking, extrusion;
single route, at plant;
0.90 to >2.00 g/cm3

EU-28aggts

Ethylene tetrafluoroethylene granulate (ETFE)
copolymerization reaction of tetrafluoroethylene and ethylene;
production mix, at plant;
100.02 g/mol per repeating unit

DEaggts

Ethylene vinyl acetate copolymer (72% ethylene, 28% vinyl acetate)
co- polymerization of ethylene and vinyl acetate;
production mix, at plant;
without additives, 72% ethylene, 28% vinyl acetate

DEaggts

Ethylene vinyl alcohol copolymer (EVOH)
hydrolysis of ethylene–vinyl acetate copolymer;
single route, at plant;
72 g/mol per repeating unit

DEaggts

Ethyleneamines (EDA, DETA, TETA, TEPA, PEHA)
reaction of ethylene dichloride and ammonia;
single route, at plant;
EDA, DETA, TETA, TEPA, PEHA

EU-28aggts

Ethyleneamines (EDA, DETA, TETA, TEPA, PEHA)
reaction of ethylene dichloride and ammonia;
single route, at plant;
EDA, DETA, TETA, TEPA, PEHA

DEaggts

Ethyleneamines (EDA, DETA, TETA, TEPA, PEHA)
reaction of ethylene dichloride and ammonia;
single route, at plant;
EDA, DETA, TETA, TEPA, PEHA

USaggts

Ethyleneamines (EDA, DETA, TETA, TEPA, PEHA)
reaction of ethylene dichloride and ammonia;
single route, at plant;
EDA, DETA, TETA, TEPA, PEHA

GBaggts

Ethylenediaminetetraacetic acid (EDTA) (estimated)
Cyanomethylation of ethylene diamine;
single route, at plant;
0.86 g/cm3, 292.24 g/mol

DEaggts

Ethylene-t-Butylether (ETBE) from C4
reaction of isobutene;
single route, at plant;
0.74 g/cm3, 102.18 g/mol

DEaggts

Ethylene-t-Butylether (ETBE) from C4 (biobased from wheat)
reaction of biobased ethanol and isobutene;
single route, at plant;
0.74 g/cm3, 102.18 g/mol

DEaggts

Eucalyptus plantation (30% H2O content) perennial
cultivation, harvesting, air- drying;
single route, at producer;
30% H2O content

BRaggts

Expanded Polystryrol/polypropylene foam packing (estimation)
plasticising and mixing foam;
single route, at plant;
70% polystyrene, 30% polypropylene

EU-28aggts

Explosives (ANFO)
production, explosion;
single route, to consumer;
blasting agent, explosive; 0.8g/cm3

EU-28aggts

Facade panel (12mm) on landfill
landfill including leachate treatment and without collection, transport and pre-treatment;
production mix (region specific sites), at landfill site;
C 68.8 kg, H 6.2 kg, O 12.3 kg, Si 0.5 kg, inert 912.2 kg

EU-28p-aggts

Facade panel (20mm) on landfill
landfill including leachate treatment and without collection, transport and pre-treatment;
production mix (region specific sites), at landfill site;
C 79.3 kg, H 7.0 kg, O 14.1 kg, inert 899.6 kg

EU-28p-aggts

Fan HDD (120X25mm, PWM)
technology mix;
production mix, at plant;
120X25mm, PWM

DEaggts

Fan PSU (78X25mm, not PWM)
technology mix;
production mix, at plant;
78X25mm, not PWM

DEaggts

Fatty acid monosaturated from rape oil (by-product other fatty acids)
enzymatic hydrolysis and distillation;
single route, at plant;
37.65 MJ/kg net calorific value

DEaggts

Feather meal from poultry (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

BRaggts

Feather meal from poultry (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

ZAaggts

Feather meal from poultry (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

NZaggts

Feather meal from poultry (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

USaggts

Feldspar
Open-pit mining;
Single route, at plant;
Al2O3*SiO2*Na2O

USaggts

Ferric chloride
direct chlorination of iron scrap;
single route, at plant;
estimation, including chlorine recuperation

EU-28aggts

Ferric chloride (estimation)
direct chlorination of iron scrap;
single route, at plant;
estimation, including chlorine recuperation

DEaggts

Ferric oxide (FeO) via Fe2O3
via iron oxide;
production mix, at plant;
5.75 g/cm3, 71.85 g/mol

EU-28aggts

Ferric oxide mix (FeO)
technology mix (via iron and via iron(3) oxide);
production mix, at plant;
5.75 g/cm3, 71.85 g/mol

EU-28aggts

Ferrite (MnZn ferrite)
shape forming and sintering;
single route, at plant;
70% ferrite, 17% manganous oxide, 13% zinc

ESaggts

Ferro Chrome High Carbon
Primary production, ore mining and beneficiation;
production mix, at plant;
60 % chrome, high carbon ~ 6%

GLOaggts

Ferro Chrome Low Carbon
Primary production, ore mining and processing;
production mix, at plant;
60 % chrome, low carbon ~ 1%

GLOaggts

Ferromolybdenum mix (Mo 60%)
separation, leaching, roasting;
production mix, at plant;
60 % molybdenum content

GLOaggts

Ferro-phosphorus (incl. sinter)
reaction of apatite with coke and silica in a low shaft electric furnace;
single producer, at plant;
22.5% phosphorous, 7-14% vanadium pentoxide

DEaggts

Ferro-Vanadium
Primary production, ore mining and processing;
production mix, at plant;
80% vanadium content

ZAaggts

Finished leather unpainted, 1 kg - Chromium tanning (Wet Blue) - open input cattle hide
Chromium tanning, after chromium tanning;
production mix, at consumer;
1 kg, average waste water

USp-aggts

Fire proof stones (alumina-rich)
crushing, mixing, burning;
single route, at plant;
alumina-rich

CNaggts

Fire proof stones (alumina-rich)
crushing, mixing, burning;
single route, at plant;
alumina-rich

DEaggts

Fire proof stones (alumina-rich)
crushing, mixing, burning;
single route, at plant;
alumina-rich

UAaggts

Fire proof stones (alumina-rich)
crushing, mixing, burning;
single route, at plant;
alumina-rich

BRaggts

Fire proof stones (alumina-rich) (estimation)
crushing, mixing, burning;
single route, at plant;
alumina-rich

INaggts

Fish meal
fish grinding, steam cooking, mechanical oil extraction, evaporation;
single route, at plant;
20% carbon content, 20 MJ net calorific value

USaggts

Flat glass
Pilkington process, mixing and melting minerals;
production mix, at plant;
2500 kg/m3

DEaggts

Flax cultivation (10% H2O content)
flax cultivation and harvesting;
production mix, at field border;
10% H2O content

FRaggts

Flax seed cultivation (15% H2O content)
flax cultivation and harvesting;
production mix, at field border;
15% H2O content

CAaggts

Fluorine
electrolysis of KF/HFmixtures;
single route, at plant;
1.6965 kg/m3, 37.98 g/mol

DEaggts

Fluorine
electrolysis of KF/HF mixtures;
single route, at plant;
gas form, 1.6965 kg/m3 at STP condistions (0°C and 1 atm), 37.98 g/mol

EU-28aggts

Fluorine (electrolysis hydrogen fluoride)
electrolysis of CaF2/HFmixtures;
single route, at plant;
gas form, 1.6965 kg/m3, 37.98 g/mol

JPaggts

Fluorine graphite
direct fluorination of graphite;
production mix, at plant;
31.01 g/mol

JPaggts

Fluorosilicic acid by-product phosphoric acid (75%)
phosphoric acid wet process;
single route, at plant;
1.46 g/cm3, 144.09 g/mol

DEaggts

Fluorosilicic acid by-product phosphoric acid (75%) (estimation)
phosphoric acid wet process;
single route, at plant;
1.46 g/cm3, 144.09 g/mol

USaggts

Fluorspar (extraction and processing)
extraction and processing;
production mix, at plant;
3.2 g/cm3

MXaggts

Fluorspar (extraction and processing)
extraction and processing;
production mix, at plant;
3.2 g/cm3

DEaggts

Fluorspar (extraction and processing)
extraction and processing;
production mix, at plant;
3.2 g/cm3

USaggts

Fluorspar (extraction and processing)
extraction and processing;
production mix, at plant;
3.2 g/cm3

CNaggts

Fly ash from hard coal power plant
technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
mineral composition

DEaggts

Fly ash from hard coal power plant
technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
mineral composition

GBaggts

Fly ash from hard coal power plant
technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
mineral composition

CNaggts

Fly ash from hard coal power plant
technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
mineral composition

ROaggts

Fly ash from hard coal power plant
technology mix regarding firing and flue gas cleaning;
production mix, at power plant;
mineral composition

EU-28aggts

Foam glass 1 cbm
from mineral raw materials;
production mix, at plant;
1 cbm

EU-28p-aggts

Formaldehyde (HCHO; 37%)
dehydrogenation of methanol;
production mix, at plant;
37 % concentrated

MYaggts

Formaldehyde (HCHO; 37%)
dehydrogenation of methanol;
production mix, at plant;
37 % concentrated

EU-28aggts

Formic acid (methane acid) 85%
from methanol, carbon monoxide and water;
production mix, at plant;
1.220 g/mL, 46.03 g/mol

EU-28aggts

Freeze drying
Freeze drying of food products;
single operation, at producer;
Production of dried food in a batch process

EU-28p-aggts

Freeze drying
Freeze drying of food products;
single operation, at producer;
Production of dried food in a batch process

USp-aggts

Gadolinium oxide
primary production;
production mix, at plant;
RE95%

USaggts

Gallium
technology mix;
production mix, at plant;
5,9 g/cm3

GLOaggts

Gasoline (premium) at refinery
from crude oil;
production mix, at refinery;
150 ppm sulphur

RUaggts

Gasoline (premium) at refinery
from crude oil;
production mix, at refinery;
10 ppm sulphur

JPaggts

Gasoline (premium) at refinery
from crude oil;
production mix, at refinery;
500 ppm sulphur

BRaggts

Gasoline (premium) at refinery
from crude oil;
production mix, at refinery;
800 ppm sulphur

CNaggts

Gasoline (premium) at refinery
from crude oil;
production mix, at refinery;
50 ppm sulphur

MYaggts

Gasoline (premium) at refinery
from crude oil;
production mix, at refinery;
10 ppm sulphur

EU-28aggts

Gasoline (premium) at refinery
from crude oil;
production mix, at refinery;
30 ppm sulphur

USaggts

Gasoline (premium) at refinery
from crude oil;
production mix, at refinery;
10 ppm sulphur

NLaggts

Gasoline (premium) at refinery
from crude oil;
production mix, at refinery;
10 ppm sulphur

FRaggts

Gasoline (premium) at refinery
from crude oil;
production mix, at refinery;
10 ppm sulphur

GBaggts

Gasoline (premium) at refinery
from crude oil;
production mix, at refinery;
10 ppm sulphur

DEaggts

Gasoline (premium) at refinery
from crude oil;
production mix, at refinery;
10 ppm sulphur

AUaggts

Gasoline (premium) at refinery Western Australia
from crude oil;
production mix, at refinery;
50 ppm sulphur

AUaggts

Gasoline (regular) at refinery
from crude oil;
production mix, at refinery;
500 ppm sulphur

BRaggts

Gasoline (regular) at refinery
from crude oil;
production mix, at refinery;
800 ppm sulphur

CNaggts

Gasoline (regular) at refinery
from crude oil;
production mix, at refinery;
150 ppm sulphur

INaggts

Gasoline (regular) at refinery
from crude oil;
production mix, at refinery;
10 ppm sulphur

AUaggts

Gasoline (regular) at refinery
from crude oil;
production mix, at refinery;
150 ppm sulphur

RUaggts

Gasoline (regular) at refinery
from crude oil;
production mix, at refinery;
30 ppm sulphur

USaggts

Gasoline (regular) at refinery
from crude oil;
production mix, at refinery;
10 ppm sulphur

EU-28aggts

Gasoline (regular) at refinery
from crude oil;
production mix, at refinery;
10 ppm sulphur

JPaggts

Gasoline (regular) at refinery Western Australia
from crude oil;
production mix, at refinery;
50 ppm sulphur

AUaggts

Gasoline (Super) supplied and combusted [gasoline input in kg]
Combustion of 1kg fuel input;
single route, at plant

EU-28aggts

Gasoline (Super) supplied and combusted [gasoline input in kg] (direct)
Combustion of 1kg fuel input;
single route, at plant;
Scope 1 (direct GHG emissions)

EU-28aggts

Gasoline (Super) supplied and combusted [gasoline input in kg] (indirect)
Combustion of 1kg fuel input;
single route, at plant;
Scope 3 (indirect GHG emissions)

EU-28aggts

Gasoline (Super) supplied and combusted [th. energy output in MJ, 85% eta]
Combustion based on 1 MJ fuel input, eta 85%, thermal energy output 0,85 MJ;
single route, at plant;
eta 85%

EU-28aggts

Gasoline (Super) supplied and combusted [th. energy output in MJ, 85% eta] (direct)
Combustion based on 1 MJ fuel input, eta 85%, thermal energy output 0,85 MJ;
single route, at plant;
Scope 1 (direct GHG emissions)

EU-28aggts

Gasoline (Super) supplied and combusted [th. energy output in MJ, 85% eta] (indirect)
Combustion based on 1 MJ fuel input, eta 85%, thermal energy output 0,85 MJ;
single route, at plant;
Scope 3 (indirect GHG emissions)

EU-28aggts

Gasoline mix (premium) at refinery
from crude oil and bio components;
production mix, at refinery;
10 ppm sulphur, 10.34 wt.% bio components

FRaggts

Gasoline mix (premium) at refinery
from crude oil and bio components;
production mix, at refinery;
50 ppm sulphur, 0.00 wt.% bio components

MYaggts

Gasoline mix (premium) at refinery
from crude oil and bio components;
production mix, at refinery;
10 ppm sulphur, 5.92 wt.% bio components

NLaggts

Gasoline mix (premium) at refinery
from crude oil and bio components;
production mix, at refinery;
150 ppm sulphur, 0.00 wt.% bio components

RUaggts

Gasoline mix (premium) at refinery Western Australia
from crude oil and bio components;
production mix, at refinery;
50 ppm sulphur, 1.38 wt.% bio components

AUaggts

Gasoline mix (regular) at refinery
from crude oil and bio components;
production mix, at refinery;
150 ppm sulphur, 0.00 wt.% bio components

RUaggts

Gasoline mix (regular) at refinery Western Australia
from crude oil and bio components;
production mix, at refinery;
50 ppm sulphur, 1.38 wt.% bio components

AUaggts

Gelatine from pork skin
slaughtering and processing, pig skin via acid treatment;
single route, at plant;
about 10 % water content

EU-28aggts

Generic television manufacturing (TV 65")
technology mix;
production mix, at producer;
65" Liquid Crystal Display (LCD), Panel Assembly LED TFT, mixed TN-IPS technology, 65" TV Chassis

GLOaggts

Glass fibre fleece (21% UF resin) (estimation)
mixing of glass fiber, UF and PMMA, fleece production;
production mix, at plant;
21% urea formaldehyde resin

DEaggts

Glass fibre mesh
technology mix;
production mix, at plant;
Glass fibre

CNaggts

Glass fibre mesh
technology mix;
production mix, at plant;
Glass fibre

EU-28aggts

Glass fibres
from mineral components;
production mix, at plant;
Borosillicate glass / E-glass

UAaggts

Glass fibres
from mineral components;
production mix, at plant;
Borosillicate glass / E-glass

CNaggts

Glass fibres
from mineral components;
production mix, at plant;
Borosillicate glass / E-glass

EU-28aggts

Glass fleece
from glass fibres and urea- formaldehyde- resin;
production mix, at plant;
82% glass fibres and 18% UF resin

CNaggts

Glass fleece
from glass fibres and urea- formaldehyde- resin;
production mix, at plant;
82% glass fibres and 18% UF resin

UAaggts

Glass fleece (EN15804 A1-A3)
from glass fibres and urea- formaldehyde- resin;
production mix, at plant;
82% glass fibres and 18% UF resin

EU-28aggts

Glucose from Straw (better case) (open elec. and th.E.)
via enzymatic hydrolysis with acid pre-treatment;
single producer, at plant;
DE 20

DEp-aggts

Glucose from Straw (worse case) (open elec. and th.E.)
via enzymatic hydrolysis with acid pre-treatment;
single producer, at plant;
DE 20

DEp-aggts

Glucose syrup from corn, 30 % H2O content
Corn cultivation, grain drying, corn wet mill, glucose syrup production from corn starch slurry, dyring;
single route, at field border;
30% H2O, syrup

USaggts

Glucose syrup from corn, 30 % H2O content
Corn cultivation, grain drying, corn wet mill, glucose syrup production from corn starch slurry, dyring;
single route, at field border;
30% H2O, syrup

EU-28aggts

Glue system
mixing different adhesives;
production mix, at plant;
33% casein glue, 33% phenol resorcin resin, 33% polyurethane

DEaggts

Glycerin by-product rapeseed methyl ester (RME) (economic allocation)
extraction, refining, transesterification;
single route, at plant;
1.26 g/cm3, 92.09 g/mol

NLaggts

Glycerine (from Epichlorohydrine)
via epichlorohydrine;
single route, at plant;
1.26 g/cm3, 92.09 g/mol

BEaggts

Glycerine (from Epichlorohydrine)
via epichlorohydrine;
single route, at plant;
1.26 g/cm3, 92.09 g/mol

NLaggts

Glycerine (from Epichlorohydrine)
via epichlorohydrine;
single route, at plant;
1.26 g/cm3, 92.09 g/mol

ESaggts

Glycerine by-product rapeseed methyl ester (RME) (economic and C mass allocation)
by-product rapeseed methyl ester (RME);
single route, at plant;
1.26 g/cm3, 92.09 g/mol

NLaggts

Glycerine by-product rapeseed methyl ester (RME) (economic and C mass allocation)
by-product rapeseed methyl ester (RME);
single route, at plant;
1.26 g/cm3, 92.09 g/mol

EU-28aggts

Glycerine by-product rapeseed methyl ester (RME) (economic and C mass allocation)
by-product rapeseed methyl ester (RME);
single route, at plant;
1.26 g/cm3, 92.09 g/mol

DEaggts

Glycerine by-product rapeseed methyl ester (RME) (mass allocation)
extraction, refining, transesterification;
single route, at plant;
1.26 g/cm3, 92.09 g/mol

DEaggts

Glycerol ester from balm colophony
esterification of glycerine with retinoic acid;
single route, at plant;
376 g/mol

EU-28aggts

Glycerol ester from balm colophony
esterification of glycerine with retinoic acid;
single route, at plant;
376 g/mol

DEaggts

Glycidylmethacrylate
esterification of methacrylic acid with epichlorohydrin;
single route, at plant;
1.04 g/cm3, 142.15 g/mol

DEp-aggts

Glycidylmethacrylate
esterification of methacrylic acid with epichlorohydrin;
single route, at plant;
1.04 g/cm3, 142.15 g/mol

EU-28aggts

Glycidylmethacrylate
esterification of methacrylic acid with epichlorohydrin;
single route, at plant;
1.04 g/cm3, 142.15 g/mol

DEaggts

Glycidylmethacrylate (estimation)
esterification of methacrylic acid with epichlorohydrin;
single route, at plant;
1.04 g/cm3, 142.15 g/mol

USaggts

Grey cast iron (GGG70) part (chill-mold)
reduction in blast furnace, chill- mold;
single route, at plant;
GGG70

DEp-aggts

Gypsum (CaSO4 alpha hemihydrate from FGD gypsum)
grinded and purified product, via calcination of calcium sulphate dihydrate;
production mix, at plant;
145.15 g/mol

CNaggts

Gypsum (CaSO4 alpha hemihydrate from FGD gypsum)
grinded and purified product, via calcination of calcium sulphate dihydrate;
production mix, at plant;
145.15 g/mol

UAaggts

Gypsum (CaSO4 alpha hemihydrate from FGD gypsum)
grinded and purified product, via calcination of calcium sulphate dihydrate;
production mix, at plant;
145.15 g/mol

BRaggts

Gypsum (CaSO4) highly pure by-product hydrogen fluoride
highly- pure, reaction of fluorspar and sulfuric acid in rotary furnace;
single route, at plant;
2.96 g/cm3, 136.14 g/mol

DEaggts

Gypsum (CaSO4) highly pure by-product hydrogen fluoride (EN15804 A1-A3)
highly- pure, reaction of fluorspar and sulfuric acid in rotary furnace;
single route, at plant;
2.96 g/cm3, 136.14 g/mol

EU-28aggts

Gypsum plaster (CaSO4-Beta-hemihydrate) (from 100% gypsum stone)
gypsum stone extraction, grinding and calcination;
Mandatory:single route, at plant;
145.15 g/mol

DEaggts

Gypsum stone (CaSO4-Dihydrate)
open pit mining;
single route, at plant;
172 g/mol

ESaggts

Gypsum stone (CaSO4-Dihydrate)
underground and open pit mining;
production mix, at plant;
grinded and purified product

CNaggts

Gypsum stone (CaSO4-Dihydrate)
underground and open pit mining;
production mix, at plant;
grinded and purified product

UAaggts

Gypsum stone (CaSO4-Dihydrate)
open pit mining;
single route, at plant;
172 g/mol

MXaggts

Gypsum stone (CaSO4-Dihydrate)
open pit mining;
single route, at plant;
172 g/mol

TRaggts

Gypsum stone (CaSO4-Dihydrate)
underground and open pit mining;
production mix, at plant;
grinded and purified product

BRaggts

Gypsum stone (CaSO4-Dihydrate)
open pit mining;
single route, at plant;
172 g/mol

CAaggts

Gypsum stone (CaSO4-Dihydrate)
open pit mining;
single route, at plant;
172 g/mol

SAaggts

Gypsum stone (CaSO4-Dihydrate)
open pit mining;
single route, at plant;
172 g/mol

JPaggts

Gypsum stone (CaSO4-Dihydrate)
open pit mining;
single route, at plant;
172 g/mol

USaggts

Gypsum stone (CaSO4-Dihydrate) (EN15804 A1-A3))
underground and open pit mining;
production mix, at plant;
grinded and purified product

EU-28aggts

Hard coal supplied and combusted in power plant
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28aggts

Hard coal supplied and combusted in power plant (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28aggts

Hard coal supplied and combusted in power plant (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28aggts

Hard disk drive (HDD), 2.5", 1 platter, 2 sides, 7 mm high
technology mix;
production mix, at producer;
2.5", 1 platter, 2 sides, 7 mm high

GLOaggts

Hard disk drive (HDD), 2.5", 2 platters, 4 sides, 9.5 mm high
technology mix;
production mix, at producer;
2.5", 2 platters, 4 sides, 9.5 mm high

GLOaggts

Hard disk drive (HDD), 2.5", 3 platters, 6 sides, 12.5 mm high
technology mix;
production mix, at producer;
2.5", 3 platters, 6 sides, 12.5 mm high

GLOaggts

Hard disk drive (HDD), 2.5", 4 platters, 8 sides, 15 mm high
technology mix;
production mix, at producer;
2.5", 4 platters, 8 sides, 15 mm high

GLOaggts

Hard disk drive (HDD), 3.5", 1 platter, 1 side, 26 mm high
technology mix;
production mix, at producer;
3.5", 1 platter, 1 side, 26 mm high

GLOaggts

Hard disk drive (HDD), 3.5", 1 platter, 2 sides, 26 mm high
technology mix;
production mix, at producer;
3.5", 1 platter, 2 sides, 26 mm high

GLOaggts

Hard disk drive (HDD), 3.5", 2 platters, 4 sides, 26 mm high
technology mix;
production mix, at producer;
3.5", 2 platters, 4 sides, 26 mm high

GLOaggts

Hard disk drive (HDD), 3.5", 3 platters, 6 sides, 26 mm high
technology mix;
production mix, at producer;
3.5", 3 platters, 6 sides, 26 mm high

GLOaggts

Hard disk drive (HDD), 3.5", 4 platters, 8 sides, 26 mm high
technology mix;
production mix, at producer;
3.5", 4 platters, 8 sides, 26 mm high

GLOaggts

Hard disk drive (HDD), 3.5", 5 platters, 10 sides, 26 mm high
technology mix;
production mix, at producer;
3.5", 5 platters, 10 sides, 26 mm high

GLOaggts

Hardwood log mix
forest cultivation, harvesting, wet storage;
production mix, at plant;
50% timber beech, 50% timber oak

DEaggts

Hazardous waste (non-specific) (C rich, worst case scenario incl. landfill)
incineration, macroencapsulation, vitrification, transport and landfill;
single route, at plant;
rich in C

GLOaggts

Hazardous waste (non-specific) (no C, worst case scenario incl. landfill)
incineration, macroencapsulation, vitrification, transport and landfill;
single route, at plant;
no C

GLOaggts

Heavy Fuel Oil (HFO) supplied and combusted in power plant
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28aggts

Heavy Fuel Oil (HFO) supplied and combusted in power plant (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28aggts

Heavy Fuel Oil (HFO) supplied and combusted in power plant (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28aggts

Heavy fuel oil at refinery (1.0 wt.% S)
from crude oil;
production mix, at refinery;
1 wt.% sulphur

RUaggts

Heavy fuel oil at refinery (1.0 wt.% S)
from crude oil;
production mix, at refinery;
1 wt.% sulphur

NLaggts

Heavy fuel oil at refinery (1.0 wt.% S)
from crude oil;
production mix, at refinery;
1 wt.% sulphur

MYaggts

Heavy fuel oil at refinery (2.5wt.% S)
from crude oil;
production mix, at refinery;
2.5 wt.% sulphur

RUaggts

Heavy fuel oil at refinery (2.5wt.% S)
from crude oil;
production mix, at refinery;
2.5 wt.% sulphur

NLaggts

Heavy fuel oil at refinery (2.5wt.% S)
from crude oil;
production mix, at refinery;
2.5 wt.% sulphur

MYaggts

Helium (liquid)
Collins cycle (compression, precooling and expansion in different stages);
single producer, at plant;
boiling point of He -269°C

DEaggts

Hemp straw cultivation (10% H2O content)
hemp cultivation;
production mix, at field border;
10% H2O content

DEaggts

Hemp straw with catch crop
hemp cultivation with catch crop;
production mix, at field border;
12% H2O content

DEaggts

Hemp with catch crop
hemp cultivation with catch crop;
production mix, at field border;
15% H2O content

DEaggts

Hexabromododecane (HBCD, 1,2,5,6,9,10-Hexabromododecane)
reaction of cyclododecatriene and bromine;
single route, at plant;
643.71 g/mol

CNaggts

Hexabromododecane (HBCD, 1,2,5,6,9,10-Hexabromododecane)
reaction of cyclododecatriene and bromine;
single route, at plant;
643.71 g/mol

USaggts

Hexamethylene diamine (HMDA) from butadiene via dichlorobutene
from butadiene;
single route, at plant;
0.84 g/cm3, 116.20 g/mol

FRaggts

Hexamethylene diamine (HMDA) over adiponitrile
HMDA via hydrogenation of adiponitrile;
single route, at plant;
0.84 g/mL, 116.20 g/mol

FRaggts

Hexamethylene diamine (HMDA) via adipic acid
HMDA via adipic acid;
single route, at plant;
0.84 g/mL, 116.20 g/mol

BEaggts

Hexamethylene diamine (HMDA) via Adiponitrile (from Acrylonitrile)
HMDA via hydrogenation of adiponitrile;
single route, at plant;
0.84 g/mL, 116.20 g/mol

USaggts

Hexamethylene diamine (HMDA) via adiponitrile (from butadiene)
from butadiene;
single route, at plant;
0.84 g/cm3, 116.20 g/mol

USaggts

Hexamethylene diisocyanate (HMDI) by-product HCl
from hexamethylenediamine (HDI) by phosgenation;
single route, at plant;
1.047 g/cm3, 168 g/mol

DEaggts

Hexamethylene diisocyanate (HMDI) by-product HCl
from hexamethylenediamine (HDI) by phosgenation;
single route, at plant;
1.047 g/cm3, 168 g/mol

EU-28aggts

Hexamethylenediamine (HMDA) from Acrylonitrile via Adiponitrile
HMDA via hydrogenation of adiponitrile;
single route, at plant;
0.84 g/cm3, 116.20 g/mol

CNaggts

Hexamethylenediamine (HMDA; from acrylonitrile via adiponitrile)
HMDA via hydrogenation of adiponitrile;
single route, at plant;
0.84 g/mL, 116.20 g/mol

DEaggts

Hexamethylenediamine (HMDA; from acrylonitrile via adiponitrile)
HMDA via hydrogenation of adiponitrile;
single route, at plant;
0.84 g/mL, 116.20 g/mol

EU-28aggts

Hexamethylenediamine (HMDA; from acrylonitrile via adiponitrile)
HMDA via hydrogenation of adiponitrile;
single route, at plant;
0.84 g/mL, 116.20 g/mol

USaggts

Hexamethylenediamine (HMDA; from butadiene via adiponitrile)
from butadiene via adiponitrile;
single route, at plant;
0.84 g/mL, 116.20 g/mol

EU-28aggts

Hexamethylenimin by-product HMDA via adipic acid
by- product HMDA, via adipic acid;
single route, at plant;
0.88 g/cm3, 99.17 g/mol

DEaggts

Hexanediol diglycidyl ether (estimation)
coupling process;
single route, at plant;
230.3 g/mol

EU-28aggts

Hexanediol diglycidyl ether (estimation)
coupling process;
single route, at plant;
230.3 g/mol

DEaggts

High performance film (Polyether ether ketone)
Plastic extruding, melting, casting and mechanical forming;
single route, at plant;
1.32 g/cm3, 290.31 g/mol per repeating unit

DEaggts

High performance film (Polyetherimide)
Plastic extruding, melting, casting and mechanical forming;
single route, at plant;
1.27 g/cm3, 592 g/mol per repeating unit

DEaggts

High performance film (Polyphenylene sulfide)
Plastic extruding, melting, casting and mechanical forming;
single route, at plant;
1.35 g/cm3,110 g/mol per repeating unit

DEaggts

High performance film (polypropylene/polyethylene membrane/foil)
Plastic extruding, melting, casting and mechanical forming;
single route, at plant;
1.08 g/cm3

DEaggts

High performance film (polyvinyl butyral)
Plastic extruding, melting, casting and mechanical forming;
single route, at plant;
1.08 g/cm3

DEaggts

High performance film (PVB, LCP, Polyacrylate, PEEK, PEI, Polyethersulfide)
Plastic extruding, melting, casting and mechanical forming;
single producer, at plant;
PVB, LCP, Polyacrylate, PEEK, PEI, Polyethersulfide

DEp-aggts

Hominy (nixtamal, estimation)
intensive cultivation, conventional nixtamization process;
production mix, at plant;
12% moisture content

USaggts

Hydrazine hydrate/hydrazine
Bayer Ketazine Process;
production mix, at plant;
1.02 g/cm3, 32.05 g/mol

DEaggts

Hydrochloric acid (100%) by-product allyl chloride (C3H5Cl)
reaction of chlorine and propene;
single route, at plant;
100% HCl

EU-28aggts

Hydrochloric acid (100%) by-product allyl chloride (C3H5Cl)
reaction of chlorine and propene;
single route, at plant;
100% HCl

MYaggts

Hydrochloric acid (100%) by-product epichlorohydrine, calcium chloride
from Epichlorhydrin synthesis, by-product epichlorohydrine, calcium chloride;
single route, at plant;
100% HCl

DEaggts

Hydrochloric acid (100%) by-product epichlorohydrine, calcium chloride
from Epichlorhydrin synthesis, by-product epichlorohydrine, calcium chloride;
single route, at plant;
100% HCl

MYaggts

Hydrochloric acid (100%) by-product epichlorohydrine, calcium chloride
from Epichlorhydrin synthesis, by-product epichlorohydrine, calcium chloride;
single route, at plant;
100% HCl

EU-28aggts

Hydrochloric acid (100%) by-product epichlorohydrine, dichloro propane
from Epichlorhydrin synthesis, by-product epichlorohydrine, dichloro propane;
single route, at plant;
100% HCl

MYaggts

Hydrochloric acid (100%) by-product epichlorohydrine, dichloro propane
from Epichlorhydrin synthesis, by-product epichlorohydrine, dichloro propane;
single route, at plant;
100% HCl

DEaggts

Hydrochloric acid (100%) by-product epichlorohydrine, dichloro propane
from Epichlorhydrin synthesis, by-product epichlorohydrine, dichloro propane;
single route, at plant;
100% HCl

EU-28aggts

Hydrochloric acid (32%), by-product Methylene diisocyanate (MDI), methanol
phosgenation of methylenedianiline;
single route, at plant;
32% concentrated

DEaggts

Hydrochloric acid (32%), by-product Methylene diisocyanate (MDI), methanol
phosgenation of methylenedianiline;
single route, at plant;
32% concentrated

BEaggts

Hydrochloric acid (phosgenation) by-product toluene diamine (TDA),toluene diisocyanate
phosgenation of toluene diamine;
single producer, at plant;
32 % concentrated

GBaggts

Hydrochloric acid 100% (primarily from chlorine)
combustion of hydrogen with chlorine;
production mix, at plant;
100% HCl

DEaggts

Hydrochloric acid 100% (primarily from chlorine)
combustion of hydrogen with chlorine;
production mix, at plant;
100% HCl

CNaggts

Hydrochloric acid 100% (primarily from chlorine) (estimation)
combustion of hydrogen with chlorine;
production mix, at plant;
100% HCl

INaggts

Hydrochloric acid 32%
primarily from chlorine;
production mix, at plant;
32 % concentrated

JPaggts

Hydrochloric acid by-product methylene diisocyanate (MDI), methanol
phosgenation of methylenedianiline;
single route, at plant;
32% concentrated

FRaggts

Hydrogen (chlorine-alkali-electrolysis, membrane)
from chlorine-alkali electrolysis (membrane);
single route, at plant;
0.0899 kg/m3, 2 g/cm3

EU-28aggts

Hydrogen (synthesis gas (H2:CO 1:1) over wood gasification)
water gas shift reaction, synthesis gas produced by wood gasificiation;
single route, at plant;
0.0899 kg/m3, 2 g/mol, 120 MJ/kg net calorific value

EU-28aggts

Hydrogen (synthesis gas (H2:CO 2:1) over coal gasification)
water gas shift reaction, synthesis gas produced by coal gasificiation;
single route, at plant;
0.0899 kg/m3, 2 g/mol, 120 MJ/kg net calorific value

EU-28aggts

Hydrogen at refinery
from crude oil;
production mix, at refinery

GBaggts

Hydrogen at refinery
from crude oil;
production mix, at refinery

INaggts

Hydrogen at refinery
from crude oil;
production mix, at refinery

JPaggts

Hydrogen at refinery
from crude oil;
production mix, at refinery

BRaggts

Hydrogen at refinery
from crude oil;
production mix, at refinery

CNaggts

Hydrogen at refinery
from crude oil;
production mix, at refinery

FRaggts

Hydrogen at refinery
from crude oil;
production mix, at refinery

MYaggts

Hydrogen at refinery
from crude oil;
production mix, at refinery

DEaggts

Hydrogen at refinery
from crude oil;
production mix, at refinery

EU-28aggts

Hydrogen at refinery
from crude oil;
production mix, at refinery

NLaggts

Hydrogen at refinery
from crude oil;
production mix, at refinery

AUaggts

Hydrogen at refinery
from crude oil;
production mix, at refinery

RUaggts

Hydrogen cyanide (prussic acid, Andrussow process)
Andrussow process;
production mix, at plant;
0.687 g/cm3, 27.03 g/mol

USaggts

Hydrogen cyanide (prussic acid, BMA process)
BMA process;
single route, at plant;
0.687 g/cm3, 27.03 g/mol

DEaggts

Hydrogen cyanide by-product acrylonitrile (AN), ammonium sulphate
ammoxidation of propene;
single route, at plant;
0.687 g/cm3, 27.03 g/mol

EU-28aggts

Hydrogen cyanide by-product acrylonitrile (AN), ammonium sulphate
ammoxidation of propene;
single route, at plant;
0.687 g/cm3, 27.03 g/mol

DEaggts

Hydrogen cyanide by-product acrylonitrile (AN), ammonium sulphate (price allocated)
ammoxidation of propene;
single route, at plant;
0.687 g/cm3, 27.03 g/mol

USaggts

Hydrogen cyanide by-product acrylonitrile (AN), ammonium sulphate (price allocated)
ammoxidation of propene;
single route, at plant;
0.687 g/cm3, 27.03 g/mol

FRaggts

Hydrogen cyanide by-product acrylonitrile (AN), ammonium sulphate (price allocated)
ammoxidation of propene;
single route, at plant;
0.687 g/cm3, 27.03 g/mol

DEaggts

Hydrogen cyanide by-product acrylonitrile (AN), ammonium sulphate (price allocated)
ammoxidation of propene;
single route, at plant;
0.687 g/cm3, 27.03 g/mol

NLaggts

Hydrogen cyanide by-product acrylonitrile (AN), ammonium sulphate (price allocated)
ammoxidation of propene;
single route, at plant;
0.687 g/cm3, 27.03 g/mol

BEaggts

Hydrogen peroxide aq. (highly pure, 30%)
H2O2 purification by ion exchange resin;
single route, at plant;
1.11 g/cm3, 34.02 g/mol

USaggts

Hydrogen sulphide
reaction of hydrogen and sulphur;
single route, at plant;
1.36 g/l, 34.08 g/mol

EU-28aggts

Hydrolysis resistant coating (estimation)
hydrolysis resistant coating;
single route, at plant;
60 g/m2

EU-28p-aggts

Hydrolysis resistant coating (estimation)
hydrolysis resistant coating;
single route, at plant;
60 g/m2

USp-aggts

Hydrotreated Vegetable oil (HVO) from beef tallow
remdering, tallow processing, transport, pretreatment, hydroprocessing;
single route, at plant;
780 kg/m3, 44 MJ/kg net calorific value

FIaggts

Hydrotreated Vegetable oil (HVO) from beef tallow (tallow production burden free)
tallow processing, transport, pretreatment, hydroprocessing;
single route, at plant;
780 kg/m3, 44 MJ/kg net calorific value

FIaggts

Hydrotreated Vegetable oil (HVO) from palm oil
palm oil processing, transport, pretreatment, hydroprocessing;
single route, at plant;
780 kg/m3, 44 MJ/kg net calorific value

FIaggts

Hydrotreated Vegetable oil (HVO) from rapeseed oil
rapeseed oil processing, transport, pretreatment, hydroprocessing;
single route, at plant;
780 kg/m3, 44 MJ/kg net calorific value

FIaggts

Hydroxybenzoic acid
alkali phenoxide route;
single producer, at plant;
density 1.46 g/cm³, 138.121 g/mol

EU-28aggts

Hydroxybenzoic acid
alkali phenoxide route;
single producer, at plant;
density 1.46 g/cm³, 138.121 g/mol

DEaggts

Hydroxyethylenemethacrylate
reaction of methacrylic acid and ethylene oxide;
single route, at plant;
1.07 g/cm3, 130.14 g/mol

DEaggts

Incineration of Municipal waste (Credited)
waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment;
production mix (region specific plants), at plant;
Municipal waste incineration

DEaggts

Incineration of Municipal waste (Credited)
waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment;
production mix (region specific plants), at plant;
Municipal waste incineration

EU-28aggts

Industrial wood mix (20% H2O content)
Forest cultivation, plantation maintanance;
production mix, at producer (different trees);
Mix of spruce-, beech-, -oak and pinewood, 20% water content, 14.65 MJ/kg net calorific value

EU-28aggts

Iodine pentafluoride (estimation)
direct fluorination of molten iodine;
single route, at producer;
221.89 g/mol, 3.25 g/cm3

USaggts

Ion exchange resin (estimation)
sulfonation of polystyrene;
single route, at plant;
0.801 g/cm3

DEaggts

Ion exchange resin (estimation)
sulfonation of polystyrene;
single route, at plant;
0.801 g/cm3

USaggts

Ionomeres
copolymerization of of ethylene and methacrylic acid;
single route, at plant;
0.95 g/cm3

DEaggts

Iron ore-mix
iron ore mining and processing;
import mix, to consumer;
5.00 g/cm3, 231.53 g/mol

CNaggts

Iron ore-mix
iron ore mining and processing;
import mix, to consumer;
5.00 g/cm3, 231.53 g/mol

JPaggts

Iron ore-mix
iron ore mining and processing;
import mix, to consumer;
5.00 g/cm3, 231.53 g/mol

DEaggts

Iron oxide (Fe2O3)
dissolving iron ore in acid;
single route, at plant;
5.24 g/cm3, 159.70 g/mol

CNaggts

Iron oxide (Fe2O3) from iron ore
dissolving iron ore in acid;
single route, at plant;
5.24 g/cm3, 159.70 g/mol

DEaggts

Iron oxide (ferrite) (Fe2O3)
electrolytical;
single route, at plant;
5.24 g/cm3, 159.70 g/mol

DEaggts

Isobutene by-product methylene-t-butylether (MTBE) of C4 raffinate with n-butene Isomerisation
acid-catalyzed addition of methanol;
production mix, at plant;
0.58 g/cm3, 56.12 g/mol

DEaggts

Isobutylene (Butyl rubber) by dispersion polymerization
dispersion polymerization of isoprene and isobutene;
production mix, at plant;
95- 99 mol-% isobutene and 1–5 mol-% isoprene

USaggts

Isophorone diisocyanate (IPDI)
from acetone;
single route, at plant;
1.06 g/cm3, 222.3 g/mol

EU-28aggts

Isophorone diisocyanate (IPDI)
from acetone;
single route, at plant;
1.06 g/cm3, 222.3 g/mol

DEaggts

Isopropanol
indirect hydrogenation;
single route, at plant;
0.78 g/cm3, 60.10 g·/mol

BEaggts

Jatropha oil
Jatropha cultivation, fruit harvest, transport, processing of seeds, oil extraction;
single route, at plant;
37 MJ net calorific value

INaggts

Kaolin
mining, wet processing, drying and grinding;
single route, at plant;
2.16- 2.68 g/cm3

CNaggts

Kerosene / Jet A1 at refinery
from crude oil;
production mix, at refinery;
400 ppm sulphur

NLaggts

Kerosene / Jet A1 at refinery
from crude oil;
production mix, at refinery;
0.2 wt.% sulphur

MYaggts

Kerosene / Jet A1 at refinery
from crude oil;
production mix, at refinery;
0.2 wt.% sulphur

RUaggts

Kerosene supplied and combusted [gasoline input in kg] (direct)
Combustion of 1kg fuel input;
single route, at plant;
Scope 1 (direct GHG emissions)

EU-28aggts

Kerosene supplied and combusted [gasoline input in kg] (indirect)
Combustion of 1kg fuel input;
single route, at plant;
Scope 3 (indirect GHG emissions)

EU-28aggts

Kerosene supplied and combusted [Kerosene input in kg]
Combustion of 1kg fuel input;
single route, at plant

EU-28aggts

Kerosene supplied and combusted [th. energy output in MJ, 85% eta]
Combustion based on 1 MJ fuel input, eta 85%, thermal energy output 0,85 MJ;
single route, at plant;
eta 85%

EU-28aggts

Kerosene supplied and combusted [th. energy output in MJ, 85% eta] (direct)
Combustion based on 1 MJ fuel input, eta 85%, thermal energy output 0,85 MJ;
single route, at plant;
Scope 1 (direct GHG emissions)

EU-28aggts

Kerosene supplied and combusted [th. energy output in MJ, 85% eta] (indirect)
Combustion based on 1 MJ fuel input, eta 85%, thermal energy output 0,85 MJ;
single route, at plant;
Scope 3 (indirect GHG emissions)

EU-28aggts

Lactic acid (homofermentative)
fermentation of carbohydrates;
single route, at plant;
90.08 g/mol

EU-28aggts

Lactic acid (homofermentative) - open input corn seeds
fermentation of carbohydrates;
single route, at plant;
90.08 g/mol

DEp-aggts

Lactose monohydrate (estimation)
milk pretreatment, processing of curd and whey, ultrafiltration, reverse osmosis filtration, crystallisation, centrifugation, spray drying;
production mix, at plant;
40% carbon content

DEaggts

L-alanine preparation (fermentation) (estimation)
highly concentrated powder, via fermentation, estimation;
single route, at plant;
1.42 g/cm3, 89.09 g/mol

CNp-aggts

Laminated gorilla glass (0.7 x 0.76 x 0.7 mm)
batch meting, glass forming, annealing, chemical tempering and lamination;
single route, at plant;
2.44 g/cm3, functional unit: 5.7 kg/sqm, Gorilla-PVB-Gorilla laminate thickness: 0.7 mm glass x 0.76 mm PVB interlayer x 0.7 mm glass

USaggts

Laminated tempered glass (1.6 x 0.76 x 1.6 mm)
melting and forming, thermal tempering, lamination;
production mix, at plant;
2.5 g/cm3, functional unit: 8.8 kg/sqm, Flat glass-PVB- flat glass laminate thickness: 1.6 mm glass x 0.76 mm PVB interlayer x 1.6 mm glass

EU-28aggts

Landfilling of food waste (according to the WARM model)
treatment of leachate, production of electricity from percentage of landfill gas captured;
production mix (region specific sites), at landfill site;
MSW, Municipal Solid Waste treatment

USp-aggts

Lanthan-Nickel5 (LaNi5, 88% lanthan, 12% nickel)
mixing lanthan and nickel;
consumer mix, to consumer;
88% lanthan, 12% nickel

EU-28aggts

Laughing gas
ammmonium nitrate route;
single route, at plant;
1.85 kg/m3, 44.01 g/mol

DEaggts

Lead battery 12V (estimation)
assembling housing, electrodes and electrolyte;
production mix, at plant;
12V

DEaggts

Lead oxide (Barton Pot, estimation)
Barton Pot Process, oxidation of lead with air;
single route, at plant;
9.53 g/cm3, 223.19 g/mol

EU-28aggts

Lead stearate (stabilizer, estimation)
reaction of stearic acid and lead oxide;
single producer, at plant;
1.4 g/cm3, 774.15 g/mol

EU-28aggts

Leather (unvarnished; 1 sqm/0.88 kg)
estimation of technology for the use in automotive industry;
production mix, at plant;
1 sqm, unvarnished

DEaggts

Leather (unvarnished; 1 sqm/0.88 kg) - open input cattle hide, open energy inputs
estimation of technology for the use in automotive industry;
production mix, at plant;
1 sqm, unvarnished

DEp-aggts

Leather coating (PU)
spray coating of leather with polyurethane polyacrylate dispersion;
single route, at plant;
1 kg of leather coated

EU-28p-aggts

Leather finished painted, 1 kg - Chromium tanning (Wet Blue)
Chromium tanning, finishing and painting;
production mix, at consumer;
1 kg, average waste water

USaggts

Leather finished painted, 1 kg - Chromium tanning (Wet Blue) - open input cattle hide
Chromium tanning, finishing and painting;
production mix, at consumer;
1 kg, average waste water

USp-aggts

Leather finished unpainted, 1 kg - Chromium tanning (Wet Blue)
Chromium tanning, after chromium tanning;
production mix, at consumer;
1 kg, average waste water

USaggts

Leather hang drying (Split leather)
Hang drying;
single route, at plant;
1 kg dried leather

EU-28p-aggts

Leather retanning & finishing (aldehyde tanned; Split leather)
after aldehyde tanning;
single route, at plant;
1 kg, average waste water

EU-28p-aggts

Leather retanning & finishing (chromium tanned; Split leather)
Post-tanning/finishing after chrome tanning, average waste water emissions;
single route, at plant;
1 kg

EU-28p-aggts

Leather vacuum drying - open input wet blue leather
vacuum drying;
single route, at plant;
0.48% H2O for dried hide

EU-28p-aggts

Leather vacuum drying - open input wet blue leather
vacuum drying;
single route, at plant;
0.48% H2O for dried hide

USp-aggts

Leather wet blue (Grain Split, Chromium tanning) - open input cattle hide
Chromium tanning, average waste water treatment emissions;
single route, at plant;
55% water content

EU-28p-aggts

Leather wet white (Grain Split, Aldehyde tanning) - open input cattle hide
Aldehyde tanning, average waste water treatment emissions;
single route, at plant;
55% water content

EU-28p-aggts

Light Fuel Oil (LFO) supplied and combusted in power plant
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28aggts

Light Fuel Oil (LFO) supplied and combusted in power plant (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28aggts

Light Fuel Oil (LFO) supplied and combusted in power plant (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28aggts

Light fuel oil at refinery
from crude oil;
production mix, at refinery;
0.3 wt.% sulphur

RUaggts

Light fuel oil at refinery
from crude oil;
production mix, at refinery;
0.1 wt.% sulphur

NLaggts

Light fuel oil at refinery
from crude oil;
production mix, at refinery;
0.3 wt.% sulphur

MYaggts

Lignite dust
grinding lignite;
production mix, at plant;
21.5 MJ net calorific value

EU-28aggts

Lignite dust
grinding lignite;
production mix, at plant;
21.5 MJ net calorific value

DEaggts

Lignite dust (estimation)
grinding lignite;
production mix, at plant;
21.5 MJ net calorific value

INaggts

Lime (CaO) grinding
grinding;
production mix, at plant;
3.34 g/cm3, 56.08 g/mol

UAaggts

Lime (CaO) grinding
grinding;
production mix, at plant;
3.34 g/cm3, 56.08 g/mol

EU-28aggts

Lime (CaO) grinding
grinding;
production mix, at plant;
3.34 g/cm3, 56.08 g/mol

DEaggts

Lime (CaO) grinding
grinding;
production mix, at plant;
3.34 g/cm3, 56.08 g/mol

CNaggts

Lime (CaO; quicklime lumpy)
from limestone;
production mix, at plant;
3.37 g/cm3, 56.08 g/mol

THaggts

Lime (CaO; quicklime lumpy)
from limestone;
production mix, at plant;
3.37 g/cm3, 56.08 g/mol

NLaggts

Lime (CaO; quicklime lumpy)
from limestone;
production mix, at plant;
3.37 g/cm3, 56.08 g/mol

MYaggts

Lime (CaO; quicklime lumpy)
from limestone;
production mix, at plant;
3.37 g/cm3, 56.08 g/mol

CNaggts

Lime (CaO; quicklime lumpy)
from limestone;
production mix, at plant;
3.37 g/cm3, 56.08 g/mol

UAaggts

Lime (CaO; quicklime lumpy)
from limestone;
production mix, at plant;
3.37 g/cm3, 56.08 g/mol

BRaggts

Lime hydrate (Ca(OH)2) slaking
lime hydrate slaking;
production mix, at plant;
2.24 g/cm3, 74.10 g/mol

DEaggts

Lime hydrate (Ca(OH)2) slaking
lime hydrate slaking;
production mix, at plant;
2.24 g/cm3, 74.10 g/mol

EU-28aggts

Lime hydrate (Ca(OH)2) slaking
lime hydrate slaking;
production mix, at plant;
2.24 g/cm3, 74.10 g/mol

UAaggts

Lime hydrate (Ca(OH)2) slaking
lime hydrate slaking;
production mix, at plant;
2.24 g/cm3, 74.10 g/mol

CNaggts

Lime hydrate (Ca(OH)2) slaking
lime hydrate slaking;
production mix, at plant;
2.24 g/cm3, 74.10 g/mol

BRaggts

Lime hydrate (Ca(OH)2) slaking
lime hydrate slaking;
production mix, at plant;
2.24 g/cm3, 74.10 g/mol

NLaggts

Limestone (CaCO3; washed)
mining and benefication;
production mix, at plant;
2.73 g/cm3, 100.09 g/mol

NLaggts

Limestone (CaCO3; washed)
mining and benefication;
production mix, at plant;
2.73 g/cm3, 100.09 g/mol

BRaggts

Limestone (CaCO3; washed)
mining and benefication;
production mix, at plant;
2.73 g/cm3, 100.09 g/mol

CNaggts

Limestone (CaCO3; washed)
mining and benefication;
production mix, at plant;
2.73 g/cm3, 100.09 g/mol

EU-28aggts

Limestone (CaCO3; washed)
mining and benefication;
production mix, at plant;
2.73 g/cm3, 100.09 g/mol

THaggts

Limestone (CaCO3; washed)
mining and benefication;
production mix, at plant;
2.73 g/cm3, 100.09 g/mol

UAaggts

Limestone (CaCO3; washed)
mining and benefication;
production mix, at plant;
2.73 g/cm3, 100.09 g/mol

AUaggts

Limestone (CaCO3; washed) (estimation)
mining and benefication;
production mix, at plant;
2.73 g/cm3, 100.09 g/mol

RUaggts

Limestone (CaCO3; washed) (estimation)
mining and benefication;
production mix, at plant;
2.73 g/cm3, 100.09 g/mol

GBaggts

Limestone (CaCO3; washed) (estimation)
mining and benefication;
production mix, at plant;
2.73 g/cm3, 100.09 g/mol

INaggts

Limestone flour (0.115mm)
limestone mining and beneficiation;
production mix, at producer;
grain size 0.115mm

DEaggts

Limestone flour (0.115mm)
limestone mining and beneficiation;
production mix, at producer;
grain size 0.115mm

EU-28aggts

Limestone flour (0.12mm)
limestone mining and beneficiation;
production mix, at plant;
grain size 0.12mm

DEaggts

Limestone flour (0.12mm)
limestone mining and beneficiation;
production mix, at producer;
grain size 0.12mm

EU-28aggts

Limestone flour (0.17mm)
limestone mining and beneficiation;
production mix, at plant;
grain size 0.17mm

DEaggts

Limestone flour (0.17mm)
limestone mining and beneficiation;
production mix, at producer;
grain size 0.17mm

EU-28aggts

Limestone flour (0.1mm)
limestone mining and beneficiation;
production mix, at producer;
grain size 0.1mm

EU-28aggts

Limestone flour (0.25mm)
limestone mining and milling;
production mix, at plant;
grain size 0.25mm

CNaggts

Limestone flour (0.25mm)
limestone mining and beneficiation;
production mix, at plant;
grain size 0.25mm

EU-28aggts

Limestone flour (0.25mm)
limestone mining and beneficiation;
production mix, at plant;
grain size 0.25mm

DEaggts

Limestone flour (0.25mm)
limestone mining and beneficiation;
production mix, at plant;
grain size 0.25mm

UAaggts

Limestone flour (0.25mm)
limestone mining and beneficiation;
production mix, at plant;
grain size 0.25mm

BRaggts

Limestone flour (0.25mm) (estimation)
limestone mining and milling;
production mix, at plant;
grain size 0.25mm

INaggts

Limestone flour (0.25mm) (estimation)
limestone mining and milling;
production mix, at plant;
grain size 0.25mm

BRaggts

Limestone flour (0.25mm) (estimation)
limestone mining and beneficiation;
production mix, at plant;
grain size 0.25mm

THaggts

Limestone flour (0.25mm) (estimation)
limestone mining and beneficiation;
production mix, at plant;
grain size 0.25mm

RUaggts

Limestone flour (0.3mm)
limestone mining and beneficiation;
production mix, at plant;
grain size 0.3mm

DEaggts

Limestone flour (0.3mm)
limestone mining and beneficiation;
production mix, at producer;
grain size 0.3mm

EU-28aggts

Limestone flour (0.5mm)
limestone mining and beneficiation;
production mix, at producer;
grain size 0.5mm

EU-28aggts

Limestone flour (0.75mm)
limestone mining and beneficiation;
production mix, at producer;
grain size 0.75mm

EU-28aggts

Limestone flour (0.75mm)
limestone mining and beneficiation;
production mix, at plant;
grain size 0.75mm

DEaggts

Limestone flour (0.7mm)
limestone mining and beneficiation;
production mix, at producer;
grain size 0.7mm

EU-28aggts

Limestone flour (0.7mm)
limestone mining and beneficiation;
production mix, at plant;
grain size 0.7mm

DEaggts

Limestone flour (1.25mm)
limestone mining and beneficiation;
production mix, at producer;
grain size 1.25mm

EU-28aggts

Limestone flour (1.25mm)
limestone mining and beneficiation;
production mix, at plant;
grain size 1.25mm

DEaggts

Limestone flour (1.75mm)
limestone mining and beneficiation;
production mix, at plant;
grain size 1.75mm

DEaggts

Limestone flour (1.75mm)
limestone mining and beneficiation;
production mix, at producer;
grain size 1.75mm

EU-28aggts

Limestone flour (1.82mm)
limestone mining and beneficiation;
production mix, at producer;
grain size 1.82mm

EU-28aggts

Limestone flour (1.82mm)
limestone mining and beneficiation;
production mix, at plant;
grain size 1.82mm

DEaggts

Limestone flour (12µm)
limestone mining and beneficiation;
production mix, at producer;
grain size 12µm

EU-28aggts

Limestone flour (12µm)
limestone mining and beneficiation;
production mix, at plant;
grain size 12µm

DEaggts

Limestone flour (2.15mm)
limestone mining and beneficiation;
production mix, at plant;
grain size 2.15mm

DEaggts

Limestone flour (2.15mm)
limestone mining and beneficiation;
production mix, at producer;
grain size 2.15mm

EU-28aggts

Limestone flour (2.25mm)
limestone mining and beneficiation;
production mix, at producer;
grain size 2.25mm

EU-28aggts

Limestone flour (2.25mm)
limestone mining and beneficiation;
production mix, at plant;
grain size 2.25mm

DEaggts

Limestone flour (25µm)
limestone mining and beneficiation;
production mix, at producer;
grain size 25µm

EU-28aggts

Limestone flour (25µm)
limestone mining and beneficiation;
production mix, at plant;
grain size 25µm

DEaggts

Limestone flour (29µm)
limestone mining and beneficiation;
production mix, at producer;
grain size 29µm

EU-28aggts

Limestone flour (29µm)
limestone mining and beneficiation;
production mix, at plant;
grain size 29µm

DEaggts

Limestone flour (30µm)
limestone mining and beneficiation;
production mix, at plant;
grain size 30µm

DEaggts

Limestone flour (30µm)
limestone mining and beneficiation;
production mix, at producer;
grain size 30µm

EU-28aggts

Limestone flour (46µm)
limestone mining and beneficiation;
production mix, at plant;
grain size 46µm

DEaggts

Limestone flour (46µm)
limestone mining and beneficiation;
production mix, at producer;
grain size 46µm

EU-28aggts

Limestone flour (50µm)
limestone mining and beneficiation;
production mix, at producer;
grain size 50µm

EU-28aggts

Limestone flour (7µm)
limestone mining and beneficiation;
production mix, at producer;
grain size 7µm

EU-28aggts

Limestone flour (7µm)
limestone mining and beneficiation;
production mix, at plant;
grain size 7µm

DEaggts

Limestone flour (CaCO3; dried)
milling and drying;
production mix, at plant;
2.73 g/cm3, 100.09 g/mol

AUaggts

Limestone flour (CaCO3; dried)
milling and drying;
production mix, at plant;
2.73 g/cm3, 100.09 g/mol

UAaggts

Limestone flour (CaCO3; dried)
milling and drying;
production mix, at plant;
2.73 g/cm3, 100.09 g/mol

EU-28aggts

Limestone flour (CaCO3; dried)
milling and drying;
production mix, at plant;
2.73 g/cm3, 100.09 g/mol

BRaggts

Limestone flour (CaCO3; dried)
milling and drying;
production mix, at plant;
2.73 g/cm3, 100.09 g/mol

CNaggts

Limestone flour (CaCO3; dried) (estimation)
milling and drying;
production mix, at plant;
2.73 g/cm3, 100.09 g/mol

INaggts

Liquefied Petroleum Gas (LPG)
from conventional natural gas production;
production mix, at producer

EU-28aggts

Liquefied Petroleum Gas (LPG)
from conventional natural gas production;
production mix, at producer

NLaggts

Liquefied Petroleum Gas (LPG)
from conventional natural gas production;
production mix, at producer

AUaggts

Liquefied Petroleum Gas (LPG)
from conventional natural gas production;
production mix, at producer

ROaggts

Liquefied Petroleum Gas (LPG)
from conventional natural gas production;
production mix, at producer

GBaggts

Liquefied Petroleum Gas (LPG), from conventional natural gas production
from conventional natural gas production;
production mix, at producer

USaggts

Liquefied Petroleum Gas (LPG), from shale gas production
from shale gas production;
production mix, at producer

USaggts

Liquid carbon dioxide
electric- driven compression of gaseous carbon dioxide;
production mix, at plant;
60 bar pressure

USaggts

Liquid Crystal Display (LCD), Panel Assembly LED TFT, mixed TN-IPS technology (mobile phone), in sqm
TN-IPS technology, without LCD controller, without glass overlay;
production mix, at plant;
in sqm

GLOaggts

Liquidcrystalline Polymer with 30% glass fiber (LCP)
acidolysis of 4- hydroxybenzoic acid (HBA) with 6-hydroxy-2- naphthoic acid (HNA);
single producer at plant;
LCP GF 30

DEaggts

Liquidcrystalline polymer without glass fiber (LCP)
acidolysis of 4- hydroxybenzoic acid (HBA) with 6-hydroxy-2- naphthoic acid (HNA);
single producer at plant;
LCP without glass fiber

DEaggts

Lithium carbonate (from brine)
extraction from brine;
production mix, at plant;
2.11 g/cm3, 73.89 g/mol

CLaggts

Lithium carbonate (spodumene route) (with credits)
spodumene route;
production mix, at plant;
2.11 g/cm3, 73.89 g/mol

CNaggts

Lithium Carbonate mix
technology mix;
production mix, at plant;
2.11 g/cm3, 73.89 g/mol

GLOaggts

Lithium carbonate mix (brine)
extraction from brine;
production mix, at plant;
2.11 g/cm3, 73.89 g/mol

GLOaggts

Lithium carbonate mix (spodumene)
spodumene route;
production mix, at plant;
2.11 g/cm3, 73.89 g/mol

GLOaggts

Lithium chloride (from lithium hydroxide)
reaction of hydrogen chloride and lithium carbonate;
single route, at plant;
2.07 g/cm3, 42.39 g/mol

USaggts

Lithium cobalt oxide battery cell (LiCoO2, LCO), 100g cell weight
technology mix of electrode production, stacking, packaging and filling/ sealing;
production mix, at plant;
cell weight 100g, housing weight 10g, capacity 5100 mAh

CNaggts

Lithium cobalt oxide battery cell (LiCoO2, LCO), scaled up to 1 kg
production of battery components, battery assembling;
production mix, at plant;
1 kg, 55.25 Ah capacity

GLOaggts

Lithium Hexafluorophosphate (LiPF6)
reaction of lithium fluoride and phosphorous pentafluoride;
production mix, at plant;
1.5 g/cm3, 151.9 g/mol

JPaggts

Lithium iron phosphate battery cell (LiFePO4), 100g cell weight
technology mix of electrode production, stacking, packaging and filling/ sealing;
production mix, at plant;
cell weight 100g, housing weight 10g, capacity 5800 mAh

CNaggts

Lithium mangan oxide battery cell (LiMn2O4, Spinell), 100g cell weight
technology mix of electrode production, stacking, packaging and filling/ sealing;
production mix, at plant;
cell weight 100g, housing weight 10g, capacity 4220 mAh

CNaggts

Lithium manganese oxide
sintering lithium carbonate and manganous oxide;
production mix, at plant;
2.93 g/cm3

JPaggts

Lithium metal (high Na-concentration)
electrolysis of lithium chloride (LiCl);
single route, at plant;
0.534 g/cm3, 6.94 g/mol

DEaggts

Lithium metal (low Na-concentration)
electrolysis of lithium chloride (LiCl);
single route, at plant;
0.534 g/cm3, 6.94 g/mol

DEaggts

Lithium metal (low Na-concentration)
electrolysis of lithium chloride (LiCl);
single route, at plant;
0.534 g/cm3, 6.94 g/mol

USaggts

Lithium nickel cobalt manganese oxide battery (NMC), 100 kg weight, without housing
technology mix of electrode production, stacking, packaging and filling/ sealing;
production mix, at plant;
cell weight 100 kg, housing weight 6.99 kg, capacity 15 kWh

GLOp-aggts

Lithium nickel cobalt manganese oxide battery cell (NMC), 100g cell weight
technology mix of electrode production, stacking, packaging and filling/ sealing;
production mix, at plant;
cell weight 100g, housing weight 10g, capacity 5980 mAh

CNaggts

Lithium nickel cobalt manganese oxide battery cell (NMC), 40g cell weight
technology mix of electrode production, stacking, packaging and filling/ sealing;
production mix, at plant;
cell weight 40g, housing weight 4g, capacity 2400 mAh

DEaggts

Lithium sulfide from lithium carbonate and hydrogen sulphide (estimation)
from reaction of lithium carbonate with hydrogen sulfide;
single route, at producer;
45.95 g/mol

EU-28aggts

Lithium sulfide from lithium hydroxide (estimation)
from reaction of lithium hydroxide with hydrogen sulfide;
single route, at producer;
45.95 g/mol

JPaggts

Lithium sulfide from lithium hydroxide (estimation)
from reaction of lithium hydroxide with hydrogen sulfide;
single route, at producer;
45.95 g/mol

DEaggts

Lithium sulfide from lithium metal (estimation)
from reaction of lithium metal with sulfur;
single route, at producer;
45.95 g/mol

DEaggts

Lithium sulfide from lithium metal (estimation)
from reaction of lithium metal with sulfur;
single route, at producer;
45.95 g/mol

JPaggts

Lithium sulfide from lithium sulphate and carbon black (estimation)
from reaction of lithium sulphate with carbon black;
single route, at producer;
45.95 g/mol

EU-28aggts

Lithium titanate (Li4Ti5O12)
technology mix, sol gel method and hydrothermal synthesis;
production mix, at plant;
459 g/mol

GLOaggts

Lithium titanate (Li4Ti5O12) from titanium oxichloride and lithium carbonate
Sol gel method, from lithium carbonate and titanium tetrachloride;
Single route, at plant;
459 g/mol

GLOaggts

Lithium titanate (Li4Ti5O12) from titanium(IV) isopropoxide (TTIP)
Hydrothermal synthesis, from lithium ethanolate and titanium isopropoxide;
Single route, at plant;
459 g/mol

GLOaggts

Lubricants at refinery
from crude oil;
production mix, at refinery

RUaggts

Lubricants at refinery
from crude oil;
production mix, at refinery

NLaggts

Magnesium oxide (MgO, calcinate, fillers)
Dolomite preparation, calcination;
single route, at plant;
3.58 g/cm3, 40.30 g/mol

DEaggts

Magnesium oxide (MgO, calcinate, fillers)
Dolomite preparation, calcination;
single route, at plant;
3.58 g/cm3, 40.30 g/mol

EU-28aggts

Magnesium oxide (MgO, fine, filler)
calcining magnesium carbonate;
single route, at plant;
3.58 g/cm3, 40.30 g/mol

DEaggts

Magnesium oxide (MgO, fine, filler)
calcining magnesium carbonate;
single route, at plant;
3.58 g/cm3, 40.30 g/mol

EU-28aggts

Magnesium sulphate (agrarian) (economic allocation)
from carnallitic hard salt;
single route, at plant;
2.66 g/cm3, 120.366 g/mol

EU-28aggts

Magnet Nd-Fe-Dy-B
sintered magnet process;
single route, at plant;
energy density >385 kJ/m³

DEaggts

Magnet Nd-Fe-Dy-B
sintered magnet process;
single route, at plant;
energy density >385 kJ/m³

CNaggts

Maize cultivation, whole plant (72.6% H2O content)
technology mix;
production mix, at field border;
72.6% H2O

DEaggts

Manganese sulphate (estimation)
manganese dissolved in sulphuric acid;
single route, at plant;
3.25 g/cm3, 151.00 g/mol

DEaggts

Manufacturing electric motor (<=10kW)
assembling electric motor;
production mix, at plant;
<=10kW

EU-28aggts

Manufacturing electric motor (101-200kW)
combination of steel, cast iron, copper, aluminium, impregnation resin and insulation material;
production mix, at plant;
101-200kW

EU-28aggts

Manufacturing electric motor (11-100kW)
combination of steel, cast iron, copper, aluminium, impregnation resin and insulation material;
production mix, at plant;
11-100kW

EU-28aggts

Marble (granulation 30 µm)
limestone mining and beneficiation;
production mix, at plant;
grain size 30 µm

DEaggts

Marble (granulation 30 µm)
limestone mining and beneficiation;
production mix, at plant;
grain size 30 µm

CNaggts

Marble (granulation 30 µm)
limestone mining and beneficiation;
production mix, at plant;
grain size 30 µm

UAaggts

Meat and bone meal (MBM) from cattle (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

NZaggts

Meat and bone meal (MBM) from cattle (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

USaggts

Meat and bone meal (MBM) from cattle (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

BRaggts

Meat and bone meal (MBM) from pig (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

BRaggts

Meat and bone meal (MBM) from pig (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

USaggts

Meat and bone meal (MBM) from pig (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

NZaggts

Meat and bone meal (MBM) from pig (economic allocation) (estimation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

RUaggts

Melamin urea formaldehyde (MUF) adhesive system (20% H2O)
hydromethylation and condensation reactions of melamine, urea and formaldehyde;
single route, at plant;
20% H2O

USaggts

Melamine
Stami carbon process;
production mix, at plant;
1.57 g/cm3, 126.12 g/mol

EU-28aggts

Melamine foam
melamine- formaldehyde addition, etherification with alcohol (foaming);
single route, at plant;
14 MJ/ kg net calorific value

DEaggts

Metal Glue (Screw sealing)
components mixing;
single route, at plant;
20% succinic acid dibutyl ester, 70% glycidylmethacrylate, 10% silica sand

EU-28aggts

Methanol from natural gas
from natural gas;
production mix, at plant;
0.79 g/cm3, 32.04 g/mol

ITaggts

Methanol from natural gas
from natural gas;
production mix, at plant;
0.79 g/cm3, 32.04 g/mol

GBaggts

Methanol from natural gas
from natural gas;
production mix, at plant;
0.79 g/cm3, 32.04 g/mol

NLaggts

Methanol from natural gas (combined reforming)
from natural gas, combined reforming;
production mix, at plant;
0.79 g/cm3, 32.04 g/mol

VEaggts

Methanol from natural gas (combined reforming)
from natural gas, combined reforming;
production mix, at plant;
0.79 g/cm3, 32.04 g/mol

SAaggts

Methanol from natural gas (combined reforming)
from natural gas;
production mix, at plant;
0.79 g/cm3, 32.04 g/mol

JPaggts

Methanol from natural gas (combined reforming)
from natural gas, combined reforming;
production mix, at plant;
0.79 g/cm3, 32.04 g/mol

OMaggts

Methanol from natural gas (combined reforming)
from natural gas;
production mix, at plant;
0.79 g/cm3, 32.04 g/mol

NOaggts

Methanol from natural gas (combined reforming)
from natural gas, combined reforming;
production mix, at plant;
0.79 g/cm3, 32.04 g/mol

RUaggts

Methanol from natural gas (combined reforming) estimate
from natural gas, combined reforming;
production mix, at plant;
0.79 g/cm3, 32.04 g/mol

CNaggts

Methanol from natural gas (integrated technology)
from natural gas, integrated technology;
production mix, at plant;
0.79 g/cm3, 32.04 g/mol

MYaggts

Methanthiol (methyl mercaptan)
reaction of methanol and hydrogen sulphide;
production mix, at plant;
2.00 kg/m3, 48.11 g/mol

EU-28aggts

Methionine
from ammonia;
single route, at plant;
149.21 g/mol

BRaggts

Methionine
from ammonia;
single route, at plant;
149.21 g/mol

USaggts

Methoxypropylacetate PGMEA (estimation)
esterification of propylene glycol monomethyl ether with acetic acid;
production mix, at plant;
0.96 g/cm³, 132.2 g/mol

DEaggts

Methyl cellulose
via alkali cellulose;
production mix, at plant;
0.25- 0.7 g/cm3

DEaggts

Methyl isobutyl ketone (MIBK)
from acetone and hydrogen;
single route, at plant;
0.80 g/cm3, 100.16 g/mol

EU-28aggts

Methylamine (by-product di-, trimethylamine)
via methanol and ammonia;
production mix, at plant;
31.06 g/mol

EU-28aggts

Methylamine by-product di-, trimethylamine
via methanol and ammonia;
production mix, at plant;
31.06 g/mol

DEaggts

Methyldiethanolamine (MDEA)
reaction of ethylene oxide and monomethylamine;
production mix, at plant;
1.04 g/cm3, 119.16 g/mol

DEaggts

Milk protein concentrate powder (from skim milk) (MPC 70)
via spray drying;
production mix, at producer;
MPC 70

USaggts

Milk protein concentrate powder (from skim milk) (MPC 70) (4% moisture, 1% fat)
via spray drying;
production mix, at producer;
MPC 70

USaggts

Milk protein concentrate powder (from skim milk) (MPC 70) (fat allocation)
via spray drying;
production mix, at producer;
MPC 70

USaggts

Milk protein concentrate powder 4424 (MPC 70)
via spray drying;
production mix, at producer;
MPC 4424

USaggts

Milk protein concentrate powder 4424 (MPC) (3% moisture, 26.4% fat)
via spray drying;
production mix, at producer;
MPC 4424, 3% moisture, 26.4% fat

USaggts

Molasse from sugar beet
washing, shredding, extraction, sterilization, juice purification and concentration, crystallization;
production mix, at plant;
beet molasses, 20% H2O

EU-28aggts

Molasse from sugar cane
by-product from crystall sugar production;
single route, at plant;
20% H2O

THaggts

Molasse from sugar cane (45% burning)
by-product from crystall sugar production;
single route, at plant;
20% H2O

BRaggts

Molded pulp loose from bagasse integrated plant case (estimation)
pulp blending, molding, drying;
single route, at plant;
energy for the process from bagasse combustion

CNaggts

Molded pulp loose from bagasse stand alone plant case (estimation)
pulp blending, molding, drying;
single route, at plant;
energy for the process from natural gas and electricity grid

CNaggts

Molybdenum
flotation, roasting, reduction;
production mix, at plant;
10.28 g/cm3

GLOaggts

Monocalciumphosphate (MCP; for Feed) (estimation)
from burnt chalk and phosphoric acid;
single route, at plant;
252.05 g/mol

EU-28aggts

Monocalciumphosphate (MCP; for Feed) (estimation)
from burnt chalk and phosphoric acid;
single route, at plant;
252.05 g/mol

GLOaggts

Mozzarella manufacturing
curd production, spinning+ stretching, molding, cooling and salting;
single producer, at plant;
from curd

USaggts

Nafion (estimation)
production from TFE and a sulfonyl fluoride;
production mix, at plant

USaggts

N-Alkyl asparagine aciddiester (estimation)
reaction of succinic acid with ammonia, esterification of the aspartic acid;
production mix, at plant;
192 g/mol for aspartic acid diethyl ester

DEaggts

Naphtha at refinery
from crude oil;
production mix, at refinery

NLaggts

Naphtha at refinery
from crude oil;
production mix, at refinery

RUaggts

Naphtha at refinery
from crude oil;
production mix, at refinery

MYaggts

Naphtha at refinery (estimated)
from crude oil;
production mix, at refinery;
refinery operations are based on US; upstream processes, i.e. crude oil mix, natural gas mix and electricity, are Venezuelan specific

VEaggts

Natural gas (via LNG) from Australia
technology mix;
consumption mix, at consumer;
medium pressure level (< 1 bar)

KWaggts

Natural Gas (via LNG) from Qatar
technology mix;
consumption mix, at consumer;
medium pressure level (< 1 bar)

KWaggts

Natural gas mix
technology mix;
consumption mix, to consumer;
medium pressure level (< 1 bar)

AEaggts

Natural Gas Mix (2030)
technology mix;
consumption mix, to consumer;
medium pressure level (< 1 bar)

EU-28aggts

Natural gas supplied and combusted in gas turbine
technology mix regarding firing and flue gas cleaning;
production mix, at plant

EU-28aggts

Natural gas supplied and combusted in gas turbine (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28aggts

Natural gas supplied and combusted in gas turbine (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28aggts

Natural gas supplied and combusted in power plant
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28aggts

Natural gas supplied and combusted in power plant (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28aggts

Natural gas supplied and combusted in power plant (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28aggts

Natural graphite (estimation)
mining and beneficiation;
production mix, at plant;
2.1- 2.3 g/cm3

GLOaggts

Natural gypsum mix (including imports)
open pit mining;
production mix, at plant;
172 g/mol

USaggts

Natural rubber
latex collecting from rubber tree, rubber processing;
single producer, at plant;
930 kg/m3, 45.2 MJ kg net calorific value

THaggts

Natural soda
trona mining, milling, calcination, purification;
single route, at plant;
2.53 g/cm3, 105.99 g/mol

USaggts

Needle-punched non-woven - open input fibre
spundbonding process;
single route, at plant;
1 kg woven fabric

USp-aggts

Needle-punched non-woven - open input fibre
spundbonding process;
single route, at plant;
1 kg woven fabric

EU-28p-aggts

Neodymium
primary production, ore mining and processing, electrolysis;
production mix, at plant;
7.00 g/cm3, 144.24 g/cm3

CNaggts

Neodymium oxide
primary production;
production mix, at plant;
RE95%

CNaggts

Nepheline Production
Open-pit and underground mining, transport;
import mix, to consumer;
2.55- 2.66 g/cm3

USaggts

Nepheline Production
Open-pit and underground mining, transport;
import mix, to consumer;
2.55- 2.66 g/cm3

NOaggts

Nepheline Production
Open-pit and underground mining, transport;
import mix, to consumer;
2.55- 2.66 g/cm3

DEaggts

Nickel cadmium battery - 0,98 kg, estimation, material composition
average product based on literature review;
production mix, at plant;
1.2V nominal cell voltage

GLOaggts

Nickel hydroxide
electrolysis of sulphate;
production mix, at plant;
4.10 g/cm3, 92.72 g/mol

DEaggts

Nickel nitrate hexahydrate (estimation)
dissolving nickel metal in nitric acid;
production mix, at plant;
2.05 g/cm3, 290.79 g/mol

DEaggts

Nitrile butadiene rubber (NBR) fiber, fiber production estimated with vulcanisation
Emulsion polymerization of acrylonitrile and butadiene, vulcanisation and fibration;
production mix, at plant;
23% acrylonitrile content

DEaggts

Nitrobenzene
from benzene via nitration;
production mix, at plant;
1.199 g/cm3, 123.06 g/mol

EU-28aggts

Nitrogen (gaseous)
via cryogenic air separation;
production mix, at plant;
1.250 kg/m3, 14.0 g/mol

ROaggts

Nitrogen (gaseous)
via cryogenic air separation;
production mix, at plant;
1.250 kg/m3, 14.0 g/mol

INaggts

Nitrogen (gaseous)
via cryogenic air separation;
production mix, at plant;
1.250 kg/m3, 14.0 g/mol

CNaggts

Nitrogen (gaseous)
via cryogenic air separation;
production mix, at plant;
1.250 kg/m3, 14.0 g/mol

AUaggts

Nitrogen (gaseous)
via cryogenic air separation;
production mix, at plant;
1.250 kg/m3, 14.0 g/mol

CZaggts

Nitrogen (gaseous)
via cryogenic air separation;
production mix, at plant;
1.250 kg/m3, 14.0 g/mol

PLaggts

Nitrogen (gaseous)
via cryogenic air separation;
production mix, at plant;
1.250 kg/m3, 14.0 g/mol

THaggts

Nitrogen (gaseous)
via cryogenic air separation;
production mix, at plant;
1.250 kg/m3, 14.0 g/mol

HUaggts

Nitrogen (gaseous)
via cryogenic air separation;
production mix, at plant;
1.250 kg/m3, 14.0 g/mol

CHaggts

Nitrogen (gaseous)
via cryogenic air separation;
production mix, at plant;
1.250 kg/m3, 14.0 g/mol

MYaggts

Nitrogen (gaseous)
via cryogenic air separation;
production mix, at plant;
1.250 kg/m3, 14.0 g/mol

SEaggts

Nitrogen (gaseous)
via cryogenic air separation;
production mix, at plant;
1.250 kg/m3, 14.0 g/mol

JPaggts

Nitrogen (liquid)
via cryogenic air separation;
production mix, at plant;
14.0 g/mol

AUaggts

Nitrogen (liquid)
via cryogenic air separation;
production mix, at plant;
14.0 g/mol

EU-28aggts

Nitrogen (liquid)
via cryogenic air separation;
production mix, at plant;
14.0 g/mol

CNaggts

Nitrogen (liquid)
via cryogenic air separation;
production mix, at plant;
14.0 g/mol

THaggts

n-Methylpyrolidone (NMP, butyrolactone over butandiol)
butyrolactone over butandiol;
single route, at plant;
1.03 g/cm3, 99.13 g/mol

DEaggts

n-Methylpyrolidone mix (NMP)
technology mix, butyrolactone from maleic anhydride and butandiol;
production mix, at producer;
1.03 g/cm3, 99.13 g/mol

DEaggts

Oat cultivation, Fife Scotland (17% H2O content)
technology mix;
production mix, at field border;
17% H2O

GBaggts

Oat cultivation, West Sussex, England (14% H2O content)
technology mix;
production mix, at field border;
14% H2O

GBaggts

ODD Laptop
technology mix;
production mix, at plant;
ODD

GLOaggts

ODD PC
technology mix;
production mix, at plant;
ODD

GLOaggts

Olive oil (virgin)
olive cultivation, two phase extraction;
production mix, at plant;
carbon content 77%

EU-28aggts

Olive oil (virgin)
olive cultivation, two phase extraction;
production mix, at plant;
carbon content 77%

ESaggts

Oxygen (gaseous)
via cryogenic air separation;
production mix, at plant;
1.429 kg/m3, 16.0 g/mol

TWaggts

Oxygen (gaseous)
via cryogenic air separation;
production mix, at plant;
1.429 kg/m3, 16.0 g/mol

AUaggts

Oxygen (gaseous)
via cryogenic air separation;
production mix, at plant;
1.429 kg/m3, 16.0 g/mol

INaggts

Oxygen (gaseous)
via cryogenic air separation;
production mix, at plant;
1.429 kg/m3, 16.0 g/mol

JPaggts

Oxygen (gaseous)
via cryogenic air separation;
production mix, at plant;
1.429 kg/m3, 16.0 g/mol

CNaggts

Oxygen (highly pure, liquid)
via cryogenic air separation, highly pure;
production mix, at plant;
16.0 g/mol

USaggts

Oxygen (liquid)
via cryogenic air separation;
production mix, at plant;
16.0 g/mol

SEaggts

Oxygen (liquid)
via cryogenic air separation;
production mix, at plant;
16.0 g/mol

EU-28aggts

Oxytriazol
from semicarbazide hydrochloride and formic acid;
single route, at plant;
83 g/mol

EU-28aggts

PA 6.6 GF thermal break
transport, extrusion, mixing, injection moulding, thermal break composition;
production mix, at plant;
contains glass fibres

EU-28aggts

PA6.6GF30 injection molding part (estimation)
plastic injection molding;
production mix, at plant;
30% glass fibres

MYaggts

Palladium chloride
reaction of palladium, chlorine and aqua regia;
production mix, at plant;
4.0 g/cm3, 177.3 g/mol

GLOaggts

Patchouli Oil
technology mix;
production mix, at plant

EU-28aggts

PBT in waste incineration plant
waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment;
production mix (region specific plants), at plant;
Municipal waste incineration

DEp-aggts

PBT in waste incineration plant
waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment;
production mix (region specific plants), at plant;
Municipal waste incineration

EU-28p-aggts

PE Non-woven fabric (estimation)
spundbonding process;
single route, at producer;
estimation

DEaggts

Pellet-feed-mix (import mix)
Beneficiation, pelletizing, sintering;
consumer mix, to consumer;
concentrated- ore pellets

DEaggts

Perchloroethylene
via hydrochloric acid recycling;
production mix, at plant;
1.62 g/cm3, 165.82 g/mol

DEaggts

PET fabric (flame laminated) in waste inceneration plant
waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment;
production mix (region specific plants), at plant

DEp-aggts

PET fabric (fleece laminated) in waste inceneration plant
waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment;
production mix (region specific plants), at plant

DEp-aggts

PET fleece (1 sqm)
plastic production, weaving;
single producer, at plant;
1 sqm

DEaggts

PET knitted fabric (knitted backscrim; 1 sqm) - open input PET fiber
knitting;
single route, at plant;
1 sqm

DEp-aggts

Petroleum coke at refinery
from crude oil;
production mix, at refinery;
31 MJ/kg net calorific value

NLaggts

Petroleum coke at refinery
from crude oil;
production mix, at refinery;
31 MJ/kg net calorific value

RUaggts

Petroleum coke at refinery
from crude oil;
production mix, at refinery;
31 MJ/kg net calorific value

MYaggts

Phenol formaldehyde (33% glass beads, 20% glass fibres)
polycondensation of phenol and formaldehyde, mixing with glass and filler;
production mix, at plant;
33% glass beads, 20% glass fibres

EU-28aggts

Phenol formaldehyde (55% glas beads, 10% MD)
polycondensation of phenol and formaldehyde, mixing with glass and filler;
production mix, at plant;
55% glass beads, 10% talcum filler

EU-28aggts

Phenol formaldehyde resin
polycondensation in acidic/ caustic medium, resin drying;
production mix, at plant;
Resol syrup 50% solid

DEaggts

Phenol formaldehyde-resin (Novolac)
polycondensation of phenol and formaldehyde;
production mix, at plant;
incl. wood flake filler (40% wood content)

EU-28aggts

Phosgene (COCl2)
continuous process, via chlorine and carbon monoxide;
single route, at plant;
4.25 g/L at 15 °C, 1.43 g/cm3 at 0 °C, 98.92 g/mol

BEaggts

Phosgene (COCl2)
continuous process, via chlorine and carbon monoxide;
single route, at plant;
4.25 g/L at 15 °C, 1.43 g/cm3 at 0 °C, 98.92 g/mol

DEaggts

Phosgene (COCl2)
continuous process, via chlorine and carbon monoxide;
single route, at plant;
4.25 g/L at 15 °C, 1.43 g/cm3 at 0 °C, 98.92 g/mol

USaggts

Phosphorus ore mining/processing/transport to EU (raw phosphorus)
mining, processing and transportation to Europe;
consumption mix, to consumer;
30% phosphorus pentoxide

CNaggts

Phosphorus ore mining/processing/transport to EU (raw phosphorus)
mining, processing and transportation to Europe;
consumption mix, to consumer;
30% phosphorus pentoxide

RUaggts

Phosphorus oxychloride (POCl3) (estimate)
via phosphorus trichloride;
single route, at plant;
1.65 g/cm3, 153.33 g/mol

DEaggts

Pigment (red)
condensation of an ester with an aromatic amine, aftertreatment with solvent;
single route, at plant;
1.47 g/cm³

DEaggts

Plastic foil (Polyethylene, PE)
Plastic production, extruding and calendering;
production mix, at plant;
gauge of about 0.1 to 0.5 mm

DEaggts

Plastic foil (Polyethylene, PE)
Plastic production, extruding and calendering;
production mix, at plant;
gauge of about 0.1 to 0.5 mm

CNaggts

Plastic granulate secondary (non specific)
from post-consumer plastic waste, via grinding, metal separation, washing, pelletization;
single route, at plant;
nonspecific plastic waste, without metal fraction

DEp-aggts

Plastic granulate secondary (non specific, no metal contamination)
from post-consumer plastic waste, via grinding, metal separation, washing, pelletization;
single route, at consumer;
plastic waste without metal fraction

EU-28p-aggts

Plastic granulate secondary (nonspecific, low burden)
from post-consumer plastic waste, via grinding, metal separation, washing, pelletization;
single route, at plant;
nonspecific plastic waste, low burden

EU-28p-aggts

Plastic granulate secondary (PET)
from PET waste;
production mix, at plant;
82% recycling rate

DEp-aggts

Poly(ethylene-alt-maleic anhydride) / Ethylene-maleic anhydride copolymer
suspension polymerization;
single route, at producer;
estimation, alternating copolymer

DEaggts

Polyacrylamide (anionic) (solid)
copolimerization of acrylic acid and acrylamide;
single route, at plant;
71,08 g·mol−1 per repeating unit

DEaggts

Polyacrylamide (cationic), powder
Solution polymerization, extrusion and granulation;
single route, at plant;
71,08 g·mol−1 per repeating unit

DEaggts

Polyacrylate ink (estimation)
mixing basic chemicals;
single route, at plant;
59% acrylate, 38% dipropylenglycole, 3% benzene

DEaggts

Polyacrylate ink (estimation)
mixing basic chemicals;
single route, at plant;
59% acrylate, 38% dipropylenglycole, 3% benzene

USaggts

Polyacrylate primary dispersion 40%
emulsion polymerization;
single producer, at plant;
dispersion 40%

DEaggts

Polyacrylate primary dispersion 40%
emulsion polymerization;
single producer, at plant;
dispersion 40%

EU-28aggts

Polyacrylic acid (PAA)
polymerization of acrylic acid;
single route, at plant;
1.4 g/cm3

EU-28aggts

Polyacrylic acid (PAA)
polymerization of acrylic acid;
single route, at plant;
1.4 g/cm3

DEaggts

Polyacrylonitrile Fibres (PAN)
Polymerization, dissolving, spinning;
single route, at plant;
PAN without additives, 53 g/mol

DEaggts

Polyalphaolefine over 1-Decen (PAO)
oligomerization and hydogenation of decene;
single producer, at plant

DEaggts

Polyamid (PA) 6 in waste incineration plant (25% inert)
waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment;
production mix (region specific plants), at plant;
25% inert

DEp-aggts

Polyamide (PA) 12 (incl. 20% TiO2) in waste incineration plant
waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment;
production mix (region specific plants), at plant;
Net calorific value 29 MJ/kg

EU-28aggts

Polyamide (PA) 12 (incl. 20% TiO2) in waste incineration plant
waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment;
production mix (region specific plants), at plant;
Net calorific value 29 MJ/kg

EU-28p-aggts

Polyamide (PA) 6.10 granulate secondary (biobased)
from post-consumer biobased plastic waste, via grinding, metal separation, washing, pelletization;
single route, at consumer;
plastic waste without metal fraction

DEp-aggts

Polyamide 6 fibers (PA 6)
spinning of polyamide and epoxy resin;
production mix, at plant

DEaggts

Polyamide 6 Granulate (PA 6)
reaction of caprolactam with water;
production mix, at plant;
1.084 g/cm3, 113 g/mol per repeating unit

CHaggts

Polyamide 6.10 Granulate (PA 6.10) (HMDA via adipic acid, CN sebacic acid (worst case))
HMDA via adipic acid, CN sebaccic acid (worst case);
single route, at consumer;
PA 6.10 granulate

DEaggts

Polyamide 6.10 Granulate (PA 6.10) (HMDA via adiponitrile, CN sebacic acid (best case))
HMDA via adiponitrile, CN sebaccic acid (best case);
single route, at consumer;
estimation

DEaggts

Polyamide 6.6 fibers (PA 6.6) (HMDA over AN)
spinning of polyamide and epoxy resin;
production mix, at plant;
1.13- 1.14 g/cm3

DEaggts

Polyamide 6.6 Granulate (PA 6.10) (HMDA via adipic acid, CN sebacic acid (worst case))
HMDA via adipic acid, CN sebacic acid (worst case);
single route, at producer;
estimation

DEaggts

Polyamide 6.6 Granulate (PA 6.10) (HMDA via adiponitrile, CN sebacic acid (best case))
HMDA via adiponitrile, CN sebacic acid (best case);
single route, at producer;
estimation

DEaggts

Polyamide 6.6 granulate (PA 6.6) (HMDA over AN)
from hexamethylene diamine and adipic acid;
production mix, at plant;
1.14 g/cm3, 226.32 g/mol per repeating unit

EU-28aggts

Polyamide 6.6 granulate (PA 6.6) (HMDA over AN)
from hexamethylene diamine and adipic acid;
production mix, at plant;
1.14 g/cm3, 226.32 g/mol per repeating unit

FRaggts

Polyamide PA 6.6 adhesive
continuous process extrusion;
single route, at plant;
estimation, filler CaCO3

DEaggts

Polybutylene succinate (PBS) (biobased from corn)
technology mix, starch hydrolysis, fermentation, filtration, esterification, polycondensation;
production mix, at producer;
from US corn, water content <0,5 w%

EU-28aggts

Polycarbonate-acrylonitrile-butadiene-styrene compound (80% PC, 20% ABS)
mixing, pelletizing and compounding;
single route, at plant;
80% polycarbonate, 20% acrylonitrile- butadiene- styrene

DEaggts

Polyethylene (PE; 15% H2O content) in waste incineration plant
waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment;
production mix (region specific plants), at plant

EU-28p-aggts

Polyethylene Film (PE-LD) without additives
Polymerisation of ethylene, extruding and calendering;
production mix, at plant;
0.91- 0.96 g/cm3, 28.05 g/mol per repeating unit

EU-28aggts

Polyethylene glycol (PEG)
ring-opening polymerization of ethylene oxide;
single route, at plant;
44 g/mol

DEaggts

Polyethylene glycol (PEG)
ring-opening polymerization of ethylene oxide;
single route, at plant;
44 g/mol

EU-28aggts

Polyethylene high density granulate (HDPE/PE-HD) (biobased from sugar cane)
production of biobased ethylene from bioethanol, polymerisation;
single route, at plant;
0.91- 0.96 g/cm3, 28 g/mol per repeating unit

USaggts

Polyethylene high density granulate (HDPE/PE-HD) (biobased from sugar cane)
from biobased ethylene based on BR sugar cane (45% slash and burn);
production mix, at plant;
0.91- 0.96 g/cm3, 28 g/mol per repeating unit

BRaggts

Polyethylene high density granulate (HDPE/PE-HD) (biobased from wheat)
production of biobased ethylene from bioethanol, polymerisation;
single route, at plant;
0.91- 0.96 g/cm3, 28 g/mol per repeating unit

USaggts

Polyethylene terephthalate (PET) fibres (bottle grade) (biobased)
partially biobased via terephthalic acid and ethylene glycol from biobased ethylene based on sugar cane;
single route, at producer;
Ethylene glycol biobased and terephthalic acid fossil based, PET fibres without additives

EU-28aggts

Polyethylene terephthalate fiber from r-PET
granulation, washing, pelletizing, spinning;
single route, at plant;
r-PET fibre

DEp-aggts

Polyethylene terephthalate granulate (PET via DMT) (partially biobased from sugar cane)
from dimethyl terephthalate and biobased ethylene glycol;
production mix, at plant;
1.38 g/cm3, 192.17 g/mol

EU-28aggts

Polyimide
Polycondensation of maleic anhydride and methylene dianiline;
single route, at plant;
aromatic polyimide

DEaggts

Polylactic acid (PLA) fibers
extruding, spinning, fiber part processing;
single producer, at plant;
melting point: 150-160 °C

DEaggts

Polyphtalamide (PPA)
polycondensation of hexamethylene diamine (HMDA) and terephtalic acid (TPA);
single route, at plant;
estimation

DEaggts

Polypropylene (PP from Cracker)
steam cracker, polymerisation of propene;
production mix, at plant;
0.9- 0.915 g/cm3, 42.08 g/mol per repeating unit

JPaggts

Polypropylene / nitrile butadiene rubber copolymer (PP/NBR, TPE-V)
dynamic vulcanisation;
single route, at plant;
PP/NBR, TPE-V

DEaggts

Polypropylene / styrene-butadiene rubber copolymer (PP/SBR, TPE-V) (dynamic vulcanisation)
dynamic vulcanisation;
single route, at plant;
PP/SBR, TPE-V

DEaggts

Polypropylene Film (PP) without additives
calendering;
single producer, at plant;
without additives

USaggts

Polypropylene granulate (PP)
polymerisation of propene;
production mix, at plant;
0.91 g/cm3, 42.08 g/mol per repeating unit

EU-28aggts

Polystyrene High Impact Granulate (HI-PS)
polymerisation of styrene;
production mix, at plant;
1.05 g/cm3, 104.15 g/mol per repeating unit

BEaggts

Polystyrene High Impact Granulate (HI-PS)
polymerisation of styrene;
production mix, at plant;
1.05 g/cm3, 104.15 g/mol per repeating unit

DEaggts

Polystyrene High Impact Granulate (HI-PS)
polymerisation of styrene;
production mix, at plant;
1.05 g/cm3, 104.15 g/mol per repeating unit

EU-28aggts

Polystyrene High Impact Granulate (HI-PS)
polymerisation of styrene;
production mix, at plant;
1.05 g/cm3, 104.15 g/mol per repeating unit

FRaggts

Polystyrene High Impact Granulate (HI-PS)
polymerisation of styrene;
production mix, at plant;
1.05 g/cm3, 104.15 g/mol per repeating unit

NLaggts

Polystyrene High Impact Granulate (HI-PS)
polymerisation of styrene;
production mix, at plant;
1.05 g/cm3, 104.15 g/mol per repeating unit

GBaggts

Polysulfone (PSU)
Polycondensation of bisphenol A sodium salt with 4,4'-Dichlorosulfonyl diphenylmethane;
single producer, at plant;
PSU

DEaggts

Polytetramethylen Ether Glycol (via Tetrahydroflourethan) (PTMEG)
polymerization of tetrahydrofuran;
single route, at plant;
0.982 g/cm3, molar mass per chain unit 73 g/mol

DEaggts

Polyurethane (PU) semi-rigid (biobased from rapeseed) in waste incineration plant
waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment;
production mix (region specific plants), at plant;
25.5 MJ/kg net calorific value

EU-28p-aggts

Polyurethane (PU, PUR) semi-rigid from rapeseed
technology mix, transesterification, epoxidation, polyaddition;
production mix, at producer;
from rapeseed, semi-rigid

EU-28aggts

Polyvinyl acetate (PVAC) (estimation)
polymerization of vinylacetate;
single producer, at plant;
1170–1200 kg/m3, 86.09 g/mol per repeating unit

DEaggts

Polyvinyl acetate (PVAC) (estimation)
polymerization of vinylacetate;
single producer, at plant;
1170–1200 kg/m3, 1170–1200 kg/m3, 86.09 g/mol per repeating unit

EU-28aggts

Polyvinyl acetate (PVAC) powder (spray dried)
polymerization of vinylacetate, powder via spray drying of PVAC dispersion;
single producer, at plant;
86.09 g/mol per repeating unit

DEaggts

Polyvinyl Alcohol fibers (PVAL) (estimation)
Dry spinning, low draft spinning;
single route, at plant;
PVAL fibers

DEaggts

Polyvinyl butyral (PVB) (estimation)
polymerisation of polyvinyl alcohol;
single route, at plant;
142 g/mol per repeating unit

USaggts

Polyvinyl chloride cable insulation (from S-PVC)
polymerisation of vinyl chloride, cable insulation production;
production mix, at plant;
62 g/mol per repeating unit

DEaggts

Polyvinyl chloride fibers (PVC) (estimation from PET)
spinning of polyvinyl chloride and epoxy resin;
production mix, at plant;
62 g/mol per repeating unit

DEaggts

Polyvinyl chloride granulate (E-PVC) via acetylene/calcium carbide route (coal based)
polymerisation of vinyl chloride via acetylene/calcium carbide route;
single route, at plant;
62 g/mol per repeating unit

CNaggts

Polyvinyl Chloride Granulate (E-PVC), from VCM via ethylene based on 100% natural gas
polymerisation of vinyl chloride via ethylene based on 100% natural gas;
single route, at plant;
62 g/mol per repeating unit

USaggts

Polyvinylidenchlorid (PVDC) Film
polymerization of vinylidene chloride, extruding and calendering;
single producer, at plant;
1.76–1.78 g/cm3, molar mass per chain unit 64.03 g/mol

DEaggts

Polyvinylidene fluoride (PVDF) in waste incineration plant
waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment;
production mix (region specific plants), at plant;
Net calorific value 16.1 MJ/kg

EU-28p-aggts

Poplar (field border) (50% H2O content)
Poplar cultivation, harvesting;
single route, at field border;
50% water content, 7,7 MJ/kg net calorific value

USaggts

Pork fat, from slaughterhouse (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

USaggts

Pork fat, from slaughterhouse (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

EU-28aggts

Potassium carbonate (K2CO3)
reaction of potassium hydroxide and carbon dioxide;
single route, at plant;
2.43 g/cm3, 138.205 g/mol

EU-28aggts

Potassium chloride (agrarian)
potassium chloride mining and processing;
production mix, at plant;
potassium compound content: 60%

EU-28aggts

Potassium hydroxide (KOH)
via electrolysis of potassium chloride;
production mix, at plant;
esitmation, 2.04 g/cm3, 56.11 g/mol

DEaggts

Potassium hydroxide (KOH) (45%)
via electrolysis of potassium chloride;
production mix, at plant;
45% concentrated

DEaggts

Potassium hydroxide (KOH) (48%)
via electrolysis of potassium chloride;
production mix, at plant;
48% concentrated

DEaggts

Potassium hydroxide (KOH) (50%)
via electrolysis of potassium chloride;
single route, at plant;
estimation, 50% concentrated

DEaggts

Potassium hydroxide (KOH) (50%)
via electrolysis of potassium chloride;
production mix, at plant;
50% concentrated

ESaggts

Potassium hydroxide (KOH) (estimation)
via electrolysis of potassium chloride;
production mix, at plant;
2.04 g/cm3, 56.11 g/mol

EU-28aggts

Potassium iodide (estimation)
reaction of potassium hydroxide and iodine, reduction of potassium iodate with coal;
production mix, at plant;
3.13 g/cm3, 166.00 g/mol

DEaggts

Potassium nitrate from potassium chloride and nitric acid (estimation)
reaction of potassium chloride and nitric acid;
single route, at plant;
2.11 g/cm3, 101.10 g/mol

USaggts

Poultry by-products for petfood and mechanically separated poultry - no allocation of co-products
slaughtering (economic allocation) and processing (no allocation);
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

EU-28p-aggts

Poultry by-products for petfood and mechanically separated poultry - no allocation of co-products
slaughtering (economic allocation) and processing (no allocation);
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

USp-aggts

Poultry by-products for petfood, co-product mechanically separated poultry (mass allocation)
slaughtering (economic allocation) and processing (mass allocation);
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

EU-28aggts

Poultry by-products for petfood, co-product mechanically separated poultry (mass allocation)
slaughtering (economic allocation) and processing (mass allocation);
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

USaggts

Poultry by-products meal (PBM) (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

BRaggts

Poultry by-products meal (PBM) (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

EU-28aggts

Poultry by-products meal (PBM) (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

ZAaggts

Poultry by-products meal (PBM) (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

NZaggts

Poultry by-products meal (PBM) (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

USaggts

Poultry fat (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

EU-28aggts

Poultry fat (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

USaggts

Poultry meat, from slaughterhouse (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

BRaggts

Poultry meat, from slaughterhouse (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

NZaggts

Poultry meat, from slaughterhouse (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

ZAaggts

Poultry meat, from slaughterhouse (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

USaggts

Precious metal recycling
recycling of platinum group metals (PGM) from catalytic converter;
single route, at plant

DEp-aggts

Process steam from biomass (solid) 85%
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 85% efficiency

NLp-aggts

Process steam from hard coal 85%
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 85% efficiency

KRaggts

Process steam from hard coal 90%
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 90% efficiency

KRaggts

Process steam from hard coal 95%
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 95% efficiency

KRaggts

Process steam from heavy fuel oil (HFO) 85%
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 85% efficiency

SAaggts

Process steam from heavy fuel oil (HFO) 90%
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 90% efficiency

SAaggts

Process steam from heavy fuel oil (HFO) 95%
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 95% efficiency

SAaggts

Process steam from light fuel oil (LFO) 85%
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 85% efficiency

SAaggts

Process steam from light fuel oil (LFO) 90%
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 90% efficiency

SAaggts

Process steam from light fuel oil (LFO) 95%
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 95% efficiency

SAaggts

Process steam from natural gas 85%
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 85% efficiency

KRaggts

Process steam from natural gas 85%
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 85% efficiency

SAaggts

Process steam from natural gas 85%
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 85% efficiency

MXaggts

Process steam from natural gas 90 %
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 90% efficiency

KRaggts

Process steam from natural gas 90 %
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 90% efficiency

SAaggts

Process steam from natural gas 90%
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 90% efficiency

MXaggts

Process steam from natural gas 90% (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 90% efficiency

BRaggts

Process steam from natural gas 90% (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 90% efficiency

EU-28aggts

Process steam from natural gas 90% (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 90% efficiency

CNaggts

Process steam from natural gas 90% (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 90% efficiency

USaggts

Process steam from natural gas 90% (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 90% efficiency

CNaggts

Process steam from natural gas 90% (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 90% efficiency

EU-28aggts

Process steam from natural gas 90% (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 90% efficiency

USaggts

Process steam from natural gas 90% (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 90% efficiency

BRaggts

Process steam from natural gas 95%
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 95% efficiency

KRaggts

Process steam from natural gas 95%
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 95% efficiency

SAaggts

Process steam from natural gas 95%
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
MJ, 95% efficiency

MXaggts

Propane at refinery
from crude oil;
production mix, at refinery

DEaggts

Propane at refinery
from crude oil;
production mix, at refinery

RUaggts

Propane at refinery
from crude oil;
production mix, at refinery

NLaggts

Propane at refinery
from crude oil;
production mix, at refinery

MYaggts

Propene (propylene)
steam cracker;
single route, at plant;
1.91 kg/m3, 42.08 g/mol,

AUaggts

Propene (propylene)
steam cracker;
single route, at plant;
1.91 kg/m3, 42.08 g/mol,

ESaggts

Propene (propylene)
steam cracker;
single route, at plant;
1.91 kg/m3, 42.08 g/mol,

FRaggts

Propene (propylene)
steam cracker;
single route, at plant;
1.91 kg/m3, 42.08 g/mol,

MYaggts

Propylamine (estimation)
produced via isopropanol with ammonia;
single route, at producer;
59.11 g/mol, Colorless liquid, 719 kg/m3

DEaggts

Propylene at refinery
from crude oil;
production mix, at refinery

NLaggts

Propylene at refinery
from crude oil;
production mix, at refinery

MYaggts

Propylene at refinery
from crude oil;
production mix, at refinery

RUaggts

Propylene carbonate
from propylene oxide and carbon dioxide;
single route, at plant;
1.21 g/cm3, 102.09 g/mol

DEaggts

Propylene carbonate
from propylene oxide and carbon dioxide;
single route, at plant;
1.21 g/cm3, 102.09 g/mol

JPaggts

Propylene dichloride by-product propylene oxide (Chlorohydrin Process with Ca(OH)2)
chlorohydrination, dehydrochlorination, purification;
single route, at plant;
1.16 g/cm3, 112.98 g/mol

DEaggts

Propylene glycol
via PO-hydrogenation;
single route, at plant;
1.04 g/cm3, 76.10 g/mol

EU-28aggts

Propylene glycol monomethyl ether (Methoxypropanol) PGME
base- catalyzed reaction of propylene oxide and methanol;
single producer, at plant;
0.938 g/cm3, 90.121 g/mol.

USaggts

Propylene Oxide (Chlorohydrin Process with Cell Liquor)
purified, from cell liquor neutralisation;
single route, at plant;
0.830 g/cm3, 58 g/mol

EU-28aggts

Propylene oxide (Chlorohydrin process) (alloc. mass no credit Calciumhypochlorite)
purified, chlorohydrin process, from propene, chlorine and lime;
single route, at plant;
0.830 g/cm3, 58 g/mol

DEaggts

Propylene oxide by-product t-butanol (Oxirane process) (mass allocated)
purified, oxirane- process, from isobutane;
single route, at plant;
0.83 g/cm3, 58 g/mol

DEaggts

Propylene Tetramer
UOP catalytic condensation process from propylene;
single route, at plant;
0.77 g/cm3

USaggts

Propylene via ethanol (biobased from BR sugar cane)
biobased ethanol production, dehydration, dimerization, metathesis and isomerization;
single route, at plant;
1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value

DEaggts

Propylene via ethanol (biobased from BR sugar cane)
biobased ethanol production, dehydration, dimerization, metathesis and isomerization;
single route, at plant;
1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value

EU-28aggts

Propylene via ethanol (biobased from BR sugar cane)
biobased ethanol production, dehydration, dimerization, metathesis and isomerization;
single route, at plant;
1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value

USaggts

Propylene via ethanol (biobased from corn)
biobased ethanol production, dehydration, dimerization, metathesis and isomerization;
single route, at plant;
1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value

EU-28aggts

Propylene via ethanol (biobased from DE wheat)
biobased ethanol production, dehydration, dimerization, metathesis and isomerization;
single route, at plant;
1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value

EU-28aggts

Propylene via ethanol (biobased from DE wheat)
biobased ethanol production, dehydration, dimerization, metathesis and isomerization;
single route, at plant;
1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value

DEaggts

Propylene via ethanol (biobased from sugar beet)
biobased ethanol production, dehydration, dimerization, metathesis and isomerization;
single route, at plant;
1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value

EU-28aggts

Propylene via ethanol (biobased from sugar beet)
biobased ethanol production, dehydration, dimerization, metathesis and isomerization;
single route, at plant;
1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value

DEaggts

Propylene via ethanol (biobased from US corn)
biobased ethanol production, dehydration, dimerization, metathesis and isomerization;
single route, at plant;
1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value

USaggts

Propylene via ethanol (biobased from US corn)
biobased ethanol production, dehydration, dimerization, metathesis and isomerization;
single route, at plant;
1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value

DEaggts

Propylene via ethanol (biobased from wheat)
biobased ethanol production, dehydration, dimerization, metathesis and isomerization;
single route, at plant;
1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value

USaggts

Propylenglycolmonomethylether (Methoxypropanol) PGME
base- catalyzed reaction of propylene oxide and methanol;
single route, at plant;
0.938 g/cm3, 90.121 g/mol

DEaggts

PUR dispersion A
Polymerization of isocyanate, mixing with water;
single producer, at plant;
dispersion A

DEaggts

Purified terephthalic acid (PTA)
Amoco process;
production mix, at plant;
1.522 g/cm³, 166.13 g/mol

DEp-aggts

Purified terephthalic acid (PTA)
Amoco process;
production mix, at plant;
1.522 g/cm³, 166.13 g/mol

INaggts

Quartz flour
mining, cleaning, grinding, screening;
production mix, at plant;
2.65 g/cm3

DEaggts

Quartz flour
mining, cleaning, grinding, screening;
production mix, at plant;
2.65 g/cm3

EU-28aggts

R-1234yf production (estimation)
CTFE route;
single route, at plant;
1.1 g/cm3, 114 g/mol

DEaggts

R-1234yf production (estimation, no allocation or credit for co-products)
CTFE route, no allocation or credit for any co product from CFC 113 production step;
single route, at plant;
1.1 g/cm3, 114 g/mol

DEp-aggts

Rapeseed meal (wet mill) (economic allocation)
Preconditioning, pressing, extraction, refining;
single producer, at plant;
rapeseed presscake, 53% carbon content

FRaggts

Rapeseed methylester (RME)
price, C mass allocated;
production mix, at plant;
78% carbon content, 37 MJ/kg net calorific value, by-product Glycerin

DEaggts

Rapeseed oil, crude (economic allocation)
rape cultivation, rapseed meal and oil production;
single producer, at plant;
crude oil

EU-28aggts

Recycled polyethylene terephthalate (PET) plastic
from post-consumer waste, via washing, granulation, pelletization;
single route, at producer;
1.38 g/cm3, 192.17 g/mol

USaggts

Refined palm oil
refining of palm oil;
single route, at plant;
36.3 MJ/kg net calorific value

DEaggts

Refinery gas at refinery
from crude oil;
production mix, at refinery

NLaggts

Refinery gas at refinery
from crude oil;
production mix, at refinery

RUaggts

Refinery gas at refinery
from crude oil;
production mix, at refinery

MYaggts

Residual forest wood (cut off approach) incl transport
collection of residual forest wood (transport);
single route, at producer;
50 km by truck, 400 km by ship

EU-28aggts

Rice bran (dry mill) (estimation)
paddy rice cultivation and processing of rice grain into white rice;
production mix, at plant;
Rice bran (13,3% CP)

MYaggts

Ruthenium
mining, transport, separation: mechanical separation, smelting, magnetic separation, chemical refining;
production mix, at plant;
12.37 g/cm3, 101.07 g/mol

ZAaggts

Sebacic Acid by-product 2-Octanol - best case scenario
Saponification of castor oil with alkali;
single route, at plant;
1.21 g/cm3, 202.25 g/mol

CNaggts

Sebacic Acid by-product 2-Octanol - worst case scenario
Saponification of castor oil with alkali;
single route, at plant;
1.21 g/cm3, 202.25 g/mol

CNaggts

Selenium powder (from copper anode sludge)
Direct oxidation (acid roating) of copper anode sludge containing Ag, Au, Se;
single route, at plant;
78.97 g/mol

DEp-aggts

Selenium powder (from copper anode sludge)
Direct oxidation/ acid roasting of copper anode sludge containing silver, gold, selenium;
single route, at plant;
78.97 g/mol

DEaggts

Semi-boneless pork, from slaughterhouse (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

EU-28aggts

Semicarbazide Hydrochloride
from semicarbacide, hydrochloric acid and methanol;
single route, at plant;
111.53 g/mol

EU-28aggts

Semiconductor manufacturing flash memory 45 nm tech node
technology mix;
production mix, at plant;
flash memory 45 nm tech node

GLOaggts

Semiconductor manufacturing WLP CSP CMOS logic 14 nm tech node
technology mix;
production mix, at plant;
specification according to the process name

GLOaggts

Semiconductor manufacturing WLP CSP CMOS logic 22 nm tech node
technology mix;
production mix, at plant;
specification according to the process name

GLOaggts

Semiconductor manufacturing WLP CSP CMOS logic with on-chip flash memory 130 nm tech node
technology mix;
production mix, at plant;
specification according to the process name

GLOaggts

Semiconductor manufacturing WLP CSP DRAM 57 nm tech node
technology mix;
production mix, at plant;
specification according to the process name

GLOaggts

Semiconductor manufacturing WLP CSP flash memory 45 nm tech node
technology mix;
production mix, at plant;
specification according to the process name

GLOaggts

Silica (pyrogen over silanes) (estimation)
pyrogen over silanes;
single route, at plant;
bulk density 50 –120 g/L

DEaggts

Silica sand (flour)
silica sand grinding;
production mix, at plant;
grain size in the micrometer range

EU-28aggts

Silica sand (flour)
silica sand grinding;
production mix, at plant;
grain size in the micrometer range

CNaggts

Silicic acid (estimation)
acidification of sodium silicate and precipitated;
single route, at plant;
96.11 g/mol

DEaggts

Silicon Nitride Component (hot isostatic press sintering)
hot isostatic press sintering;
single route, at plant;
3.44 g/cm3, 140.28 g/mol

EU-28p-aggts

Silicon Nitride Powder (reaction-bonded)
reaction-bonded;
single route, at plant;
3.44 g/cm3, 140.28 g/mol

EU-28aggts

Silicone fluids (highly viscous) / polydimethylsiloxanes (from organosilanes)
from organosilanes;
single route, at plant;
highly viscous

DEaggts

Silicone fluids (low viscosity)
from organosilane;
production mix, at plant;
low viscous

EU-28aggts

Siloxane (cyclic) (from organosilanes)
from organosilanes;
single route, at plant;
cyclic

DEaggts

Silver nitrate
dissolving silver in hot nitric acid;
production mix, at plant;
4.35 g/cm3, 169.87 g/mol

USaggts

Silver nitrate
dissolving silver in hot nitric acid;
production mix, at plant;
4.35 g/cm3, 169.87 g/mol

EU-28aggts

Silyl terminated prepolymer
copolimerization, reaction with silane;
single producer, at plant;
molar mass of the polymer >4000- 20000g/mol

DEaggts

Skim milk (fat content)
pre-treated, pasteurized, skim milk powder;
production mix, at plant;
low fat content

USaggts

Soda (Na2CO3)
Solvay process, from calcium carbonate and sodium chloride;
production mix, at plant;
2.53 g/cm3, 105.99 g/mol

INaggts

Soda (Na2CO3)
Solvay process, from calcium carbonate and sodium chloride;
production mix, at plant;
2.53 g/cm3, 105.99 g/mol

JPaggts

Soda (Na2CO3)
Solvay process, from calcium carbonate and sodium chloride;
production mix, at plant;
2.53 g/cm3, 105.99 g/mol

AUaggts

Soda (Na2CO3) (estimation)
Solvay process, from calcium carbonate and sodium chloride;
production mix, at plant;
2.53 g/cm3, 105.99 g/mol

CNaggts

Soda (Na2CO3) (estimation)
Solvay process, from calcium carbonate and sodium chloride;
production mix, at plant;
2.53 g/cm3, 105.99 g/mol

THaggts

Soda (Na2CO3) (estimation)
Solvay process, from calcium carbonate and sodium chloride;
production mix, at plant;
2.53 g/cm3, 105.99 g/mol

MYaggts

Sodium chlorate (from sodium chloride)
electrolysis of sodium chloride;
production mix, at factory;
2.54 g/cm3, 106 g/mol

DEaggts

Sodium chloride (rock salt)
mining and processing;
production mix, at plant;
2.17 g/cm3, 58.44 g/mol

AUaggts

Sodium chloride (rock salt)
mining and processing;
production mix, at plant;
2.17 g/cm3, 58.44 g/mol

JPaggts

Sodium chloride (rock salt) (estimation)
mining and processing;
production mix, at plant;
2.165 g/cm3, 58.44 g/mol

INaggts

Sodium chloride (rock salt) (estimation)
mining and processing;
production mix, at plant;
2.17 g/cm3, 58.44 g/mol

RUaggts

Sodium chloride (rock salt) (estimation)
mining and processing;
production mix, at plant;
2.165 g/cm3, 58.44 g/mol

THaggts

Sodium chloride (rock salt) (estimation)
mining and processing;
production mix, at plant;
2.165 g/cm3, 58.44 g/mol

CNaggts

Sodium formate
from sodium hydroxide and carbon monoxide;
single route, at plant;
1.92 g/cm3, 68.01 g/mol

EU-28aggts

Sodium hydroxide (caustic soda) mix (100%)
technology mix;
production mix, at plant;
100%

CZaggts

Sodium hydroxide (caustic soda) mix (100%)
technology mix;
production mix, at plant;
100%

PLaggts

Sodium hydroxide (caustic soda) mix (100%)
technology mix;
production mix, at plant;
100%

ROaggts

Sodium hydroxide (caustic soda) mix (100%)
technology mix;
production mix, at plant;
100%

SEaggts

Sodium hydroxide (caustic soda) mix (100%)
technology mix;
production mix, at plant;
100%

PTaggts

Sodium hydroxide (caustic soda) mix (100%)
technology mix;
production mix, at plant;
100%

JPaggts

Sodium hydroxide (caustic soda) mix (100%)
technology mix;
production mix, at plant;
100%

HUaggts

Sodium hydroxide mix (50%)
technology mix;
consumption mix, to consumer;
50%

JPaggts

Sodium hydroxide mix (50%)
technology mix;
consumption mix, to consumer;
50%

ITaggts

Sodium hydroxide mix (50%)
technology mix;
consumption mix, to consumer;
50%

USaggts

Sodium hydroxide mix (50%)
technology mix;
consumption mix, to consumer;
50%

BEaggts

Sodium hydroxide mix (50%)
technology mix;
consumption mix, to consumer;
50%

EU-28aggts

Sodium hydroxide mix (50%)
technology mix;
consumption mix, to consumer;
50%

ESaggts

Sodium hydroxide mix (50%)
technology mix;
consumption mix, to consumer;
50%

NLaggts

Sodium hydroxide mix (50%)
technology mix;
consumption mix, to consumer;
50%

FRaggts

Sodium metal (incl. protective oil)
Electrolysis of rock salt;
single route, at plant;
0.968 g/cm3, 22.99 g/mol

USaggts

Sodium metal (incl. protective oil)
Electrolysis of rock salt;
single route, at plant;
0.968 g/cm3, 22.99 g/mol

EU-28aggts

Sodium metal (incl. protective oil)
Electrolysis of rock salt;
single route, at plant;
0.968 g/cm3, 22.99 g/mol

FRaggts

Sodium metal (incl. protective oil)
Electrolysis of rock salt;
single route, at plant;
0.968 g/cm3, 22.99 g/mol

DEaggts

Sodium peroxydisulphate
electrolysis of sodium sulphate and sulphuric acid;
production mix, at plant;
2.59 g/cm3, 238.10 g/mol

DEaggts

Sodium peroxydisulphate (estimation)
electrolysis of sodium sulphate and sulphuric acid;
production mix, at plant;
2.59 g/cm3, 238.10 g/mol

USaggts

Sodium thiosulfate (estimation)
reaction of sulphur and sodium sulfite;
single route, at producer

EU-28aggts

Solid-Bleached sulfate (SBS) coated on one side (estimation)
chemical pulp production, paperboard processing and coating;
single route, at plant;
coating is 10% of total mass

CNaggts

Sorghum grains (20% H2O content) (estimation)
technology mix;
production mix, at field border;
20% H2O

BRaggts

Sorghum grains cultivation (20% H2O content)
summer cultivation;
production mix, at field border;
20% H2O content

AUaggts

Sorghum grains cultivation (20% H2O content) (estimation)
technology mix;
production mix, at field edge;
20% H2O

DEaggts

Soy methylester (SME) by-product Glycerine (price, C mas allocated, estimation)
by-product glycerine, soy oil production, refining, transesterification;
production mix, at plant;
78% total carbon content, 74% biogenic carbon content

BRaggts

Soy methylester (SME) by-product Glycerine (price, C mass allocated, estimation)
by-product glycerine, soy oil production, refining, transesterification;
production mix, at plant;
78% total carbon content, 74% biogenic carbon content

EU-28aggts

Soy methylester (SME) by-product Glycerine (price, C mass allocated, estimation)
by-product glycerine, soy oil production, refining, transesterification;
production mix, at plant;
78% total carbon content, 74% biogenic carbon content

USaggts

Soybean cake (meal from wet mill) (estimation)
soybean cultivation and wet mill with solvent extraction;
production mix, at plant;
Soybean meal hexane extracted (48% crude protein)

INaggts

Soybean meal (wet mill) (economic allocation)
soybean cultivation and wet mill with pressing and solvent extraction;
single producer, at plant;
soybean meal hexane extracted (48% CP)

ARaggts

Soybean meals (from wet mill) (estimation)
oil with solvent extraction;
production mix, at plant;
raw oil

RUaggts

Soybean oil
soybean cultivation and wet mill with pressing and solvent extraction, import from US;
single producer, at plant;
77.8% carbon content, 36.6 MJ/kg net calorific value

NZaggts

Soybean oil (from wet mill) (estimation)
oil with solvent extraction;
production mix, at plant;
raw oil

RUaggts

Spring barley grains (14% H2O content; 12% RP) (estimation)
spring barley cultivation and harvesting;
production mix, at field border;
14% H2O, 12% RP

RUaggts

Spring barley grains cultivation (14% H2O content; 12% RP) (estimation)
Spring barley grain cultivation;
production mix, at field border;
14% H2O content

FRaggts

Stainless steel screw
Cold heading, thread rolling;
production mix, at plant;
stainless steel

EU-28p-aggts

Stainless steel sheet (including stamping and bending)
stainless steel sheet production (sheet stamping and folding);
single producer, at plant;
5% loss (stamping)

DEaggts

Starch (Polyglucose)
corn cultivation, wet milling, drying;
single producer, at plant;
dried starch

DEaggts

Starch glue (for paper/cardboard)
wet milling, starch extraction;
single producer, at plant

DEaggts

Starch glue (for paper/cardboard)
wet milling, starch extraction;
single producer, at plant

EU-28aggts

Starter fluorescent lamp socket (DfX)
technology mix;
production mix, at plant;
1 piece

DEaggts

Stearic acid
via hydration of oleic acid from rape oil;
production mix, at plant;
0.94 g/cm3, 284.48 g/mol

DEaggts

Stearic acid
via hydration of oleic acid from rape oil;
production mix, at plant;
0.94 g/cm3, 284.48 g/mol

EU-28aggts

Steel billet (22MnB5) (BOF)
blast furnace route;
single route, at plant;
Crude steel, 22MnB5, alloys: 0.08% Al, 0.30% Cr, 1.40% Mn, 0.40% Si

DEp-aggts

Steel cold rolled coil (22MnB5) (BOF)
blast furnace route;
single route, at plant;
<1,5mm; 22MnB5, alloys: 0,08% Al; 0,30% Cr; 1,40% Mn; 0,40% Si

DEp-aggts

Steel hot rolled coil (22MnB5) (BOF)
blast furnace route;
single route, at plant;
<1,5mm, 22MnB5, alloys: 0,08% Al; 0,30% Cr; 1,40% Mn; 0,40% Si

DEp-aggts

Steel screw (hardened and galvanized)
steel rolling, hardening, galvanizing;
single route, at plant;
carbon steel, hardened and galvanized

DEp-aggts

Steel screw (unalloyed, galvanized)
electrogalvanization;
single route, at plant;
8.4 kg/m2

EU-28p-aggts

Steel sheet (22MnB5) (BOF) (aluminized, double sides)
blast furnace route;
single route, at plant;
0,75mm steel thickness - 25 micrometer Aluminized both sides, 22MnB5, alloys: 0,08% Al; 0,30% Cr; 1,40% Mn; 0,40% Si

DEp-aggts

Stored thermal energy from concentrated solar power
Compact linear fresnel reflector (CLFR) concentrated solar power (CSP) technology and molten salt thermal energy storage (TES);
single route, at plant;
MJ

USaggts

Styrene acrylate
acrylic acid ester production from propene, reaction with styrene;
single route, at producer

EU-28aggts

Styrene acrylate
acrylic acid ester production from propene, reaction with styrene;
single route, at producer

DEaggts

Styrene acrylonitrile (SAN)
copolymerization of styrene and acrylonitrile;
single route, at plant;
1.09 g/cm3

DEaggts

Styrene acrylonitrile (SAN) in waste incineration plant
waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment;
production mix (region specific plants), at plant;
SAN waste

DEp-aggts

Styrene butadiene block copolymer (SBC, TPE-S)
copolymerization of styrene and butadiene;
single route, at plant

DEaggts

Styrene butadiene copolymer (SBC, TPE-S) star block
anionic polymerization;
production mix, at plant;
70% butadiene, 30% styrene

EU-28aggts

Styrene butadiene copolymer (SBS, TPE-S) star block
anionic polymerization;
production mix, at plant;
70% butadiene, 30% styrene

DEaggts

Styrene ethene butene styrene copolymer (SEBS, TPE-S)
copolymerization (ethylene, butylene, styrene);
production mix, at plant;
25 MJ/kg net calorific value

DEaggts

Styrene ethene propene styrene copolymer (SEPS, TPE-S)
polymerization of ethene, propene, styrene...;
production mix, at plant;
25 MJ/kg net calorific value

DEaggts

Styrene isoprene styrene copolymer (SIS, TPE-S) tri block
copolymerization (isoprene, styrene);
production mix, at plant

DEaggts

Styrene maleic anhydride copolymer (SMA)
copolymerization of styrene and maleic anhydride;
production mix, at plant;
1.08 g/cm3

BEaggts

Styrene maleic anhydride copolymer (SMA)
copolymerization of styrene and maleic anhydride;
production mix, at plant;
1.08 g/cm3

GBaggts

Styrene maleic anhydride copolymer (SMA)
copolymerization of styrene and maleic anhydride;
production mix, at plant;
1.08 g/cm3

DEaggts

Styrene maleic anhydride copolymer (SMA)
copolymerization of styrene and maleic anhydride;
production mix, at plant;
1.08 g/cm3

FRaggts

Styrene-butadiene rubber (E-SBR, high styrene content 40%)
Emulsion polymerization of styrene and butadiene;
single producer, at plant;
high styrene content 40%

DEaggts

Styrene-butadiene rubber (E-SBR, low styrene content 23 %)
Emulsion polymerization of styrene and butadiene;
single producer, at plant;
low styrene content 23 %

DEaggts

Styrene-butadiene rubber (SBR) fiber, fiber production with vulcanisation
Emulsion polymerization of styrene and butadiene, vulcanisation and fibration;
production mix, at plant;
styrene content 27%

DEaggts

Styrene-butadiene rubber (S-SBR)
suspension polymerization of styrene and butadiene;
production mix, at plant;
27% styrene content

EU-28aggts

Sugar beet pellets, dried (mass allocation)
washing, shredding, extraction, drying, pelleting;
production mix, at plant;
11% H2O

EU-28aggts

Sugar beet syrup
sugar juice purification, concentration;
single producer, at plant;
sirup

EU-28aggts

Sugar beet, at field (75% H2O content)
Technology mix;
Production mix, at field border;
75% water content

EU-28aggts

Sugar cane perennial (100% slash and burn) (open press cake and vinasse)
Technology mix;
production mix, to consumer;
74% H2O; 100% pre-harvest burning

BRp-aggts

Sugar raw juice (from sugar cane)
washing, shredding, extraction, boiling;
single producer, at plant

EU-28p-aggts

Sugar, at producer (from Brazilian sugar cane)
sugarcane cultivation, juice production, sugar refining;
single producer, at plant;
cane sugar

USaggts

Sulphur (elemental) at refinery
from crude oil;
production mix, at refinery;
elemental sulphur

RUaggts

Sulphur (elemental) at refinery
from crude oil;
production mix, at refinery;
elemental sulphur

MYaggts

Sulphur from natural gas production
desulpurisation of natural gas;
production mix, at plant;
elemental sulphur

NOaggts

Sulphur from natural gas production
desulpurisation of natural gas;
production mix, at plant;
elemental sulphur

SAaggts

Sulphur from natural gas production
desulpurisation of natural gas;
production mix, at plant;
elemental sulphur

RUaggts

Sulphuric acid (37%)
oxidation of sulphur;
production mix, at plant;
37% concentrated

DEaggts

Sulphuric acid (75%)
oxidation of sulphur;
production mix, at plant;
75% concentrated

USaggts

Sulphuric acid (96%)
oxidation of sulphur;
production mix, at plant;
96% concentrated

ESaggts

Sulphuric acid (96%)
oxidation of sulphur;
production mix, at plant;
96% concentrated

JPaggts

Sulphuric acid aq. (96%)
oxidation of sulphur;
production mix, at plant;
96% concentrated

AUaggts

Sulphuric acid aq. (96%) (estimation)
oxidation of sulphur;
production mix, at plant;
96% concentrated

CNaggts

Sulphuric acid aq. (96%) (estimation)
oxidation of sulphur;
production mix, at plant;
96% concentrated

THaggts

Sulphuric acid aq. from natural gas (96%)
oxidation of sulphur;
production mix, at plant;
96% concentrated

EU-28aggts

Sulphuric acid from spent acid plant
from used H2SO4 37%;
single route, at plant;
96% aqueous solution

EU-28p-aggts

Sulphuric acid from spent acid plant
from used H2SO4 37%;
single route, at plant;
96% aqueous solution

FRp-aggts

Sulphuric acid mix (96%)
technology mix;
consumption mix, to consumer;
96% aqueous solution, M= 98.079 g/mol

FRaggts

Sulphuric acid mix (96%)
technology mix;
consumption mix, to consumer;
96% aqueous solution, M= 98.079 g/mol

EU-28aggts

Sulphuric acid mix (96%)
technology mix;
consumption mix, to consumer;
96% aqueous solution, M= 98.079 g/mol

ESaggts

Sun flower (10% H2O content)
Sunflower cultivation and harvesting;
single route, at field;
10% H2O

FRaggts

Sunflower oil (estimation)
wet mill with solvent extraction;
production mix, at plant;
77% carbon content, 25-30% crude protein

DEaggts

Synthetic graphite mix, average electricity use in graphitization (50% CPC, 50% hard coal coke)
from calcined petroleum coke (CPC), from hard coal coke;
single route mix, 50% calcined petroleum coke (CPC), 50% hard coal coke, at plant;
2.1- 2.3 g/cm3

EU-28aggts

Synthetic graphite powder (estimate)
from hard coal;
single route, at plant;
2.1- 2.3 g/cm3

CNaggts

Synthetic graphite via calcined petroleum coke, average electricity use in graphitization
from petroleum coke;
single route, at plant;
2.1- 2.3 g/cm3

DEaggts

Synthetic graphite via calcined petroleum coke, average electricity use in graphitization
from petroleum coke;
single route, at plant;
2.1- 2.3 g/cm3

USaggts

Synthetic graphite via calcined petroleum coke, average electricity use in graphitization
from petroleum coke;
single route, at plant;
2.1- 2.3 g/cm3

CNaggts

Synthetic graphite via hard coal coke, average electricity use in graphitization
from petroleum coke, from hard coal coke;
single route, at plant;
2.1- 2.3 g/cm3

DEaggts

Synthetic leather, dry process, incl DMF
Synthetic leather, dry process;
Single route, at plant;
Non-woven textile input 213 g/m2, final product 282 g/m2

EU-28aggts

Synthetic leather, dry process, incl DMF
Synthetic leather, dry process;
Single route, at plant;
Non-woven textile input 213 g/m2, final product 282 g/m2

USaggts

Synthetic leather, dry process, incl DMF - open input PE-PP fleece
Synthetic leather, dry process;
Single route, at plant;
Non-woven textile input 213 g/m2, final product 282 g/m2

USp-aggts

Synthetic leather, dry process, incl DMF - open input PE-PP fleece
Synthetic leather, dry process;
Single route, at plant;
Non-woven textile input 213 g/m2, final product 282 g/m2

EU-28p-aggts

Synthetic leather, wet + dry process, incl DMF
Synthetic leather, wet process;
Single route, at plant;
Non-woven textile 213g/m2, finished product 395 g/m2

USaggts

Synthetic leather, wet + dry process, incl DMF
Synthetic leather, wet process;
Single route, at plant;
Non-woven textile 213g/m2, finished product 395 g/m2

EU-28aggts

Synthetic leather, wet + dry process, incl DMF - open input PE-PP fleece
Synthetic leather, wet process;
Single route, at plant;
Non-woven textile 213g/m2, finished product 395 g/m2

EU-28p-aggts

Synthetic leather, wet + dry process, incl DMF - open input PE-PP fleece
Synthetic leather, wet process;
Single route, at plant;
Non-woven textile 213g/m2, finished product 395 g/m2

USp-aggts

Synthetic leather, wet process, incl DMF
Synthetic leather, wet process;
Single route, at plant;
Non-woven textile 213g/m2, finished product 326 g/m2

EU-28aggts

Synthetic leather, wet process, incl DMF
Synthetic leather, wet process;
Single route, at plant;
Non-woven textile 213g/m2, finished product 326 g/m2

USaggts

Synthetic leather, wet process, incl DMF - open input PE-PP fleece
Synthetic leather, wet process;
Single route, at plant;
Non-woven textile 213g/m2, finished product 326 g/m2

USp-aggts

Synthetic leather, wet process, incl DMF - open input PE-PP fleece
Synthetic leather, wet process;
Single route, at plant;
Non-woven textile 213g/m2, finished product 326 g/m2

EU-28p-aggts

Talcum (Underground mining, alpine region)
technology mix;
production mix, at plant;
particle size ca.1 micron to 15 microns

EU-28aggts

Tall oil (raw product) (2015) (mass allocation)
tall oil from kraft paper production, thermal energy sold/used externally;
production mix, at plant;
0.32 kg waste paper input per kg tall oil

EU-28p-aggts/FEFCO

Tall oil (refinement from paper manufacturing)
Dehydration, depitching, fractioning (distillation);
production mix, at plant

SEaggts

Tallow (animal feed) (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

BRaggts

Tallow (animal feed) (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

USaggts

Tallow (animal feed) (economic allocation)
slaughtering and processing;
single route, at plant;
product specification (such as energy, protein and carbon content) given in product flow

NZaggts

Tantalum
tantalit mining, solvent extraction, tantalum production;
production mix, at plant;
16.65 g/cm3, 180.95 g/mol

DEaggts

Tap water from groundwater
filtration, disinfection, ion removement etc.;
production mix, at plant;
1000 kg/m3, 18 g/mol

USaggts

Tap water from groundwater
filtration, disinfection, ion removement etc.;
production mix, at plant;
1000 kg/m 3,18 g/mol

CNaggts

Tap water from surface water
flockulation, filtration, disinfection, ion removement etc., from surface water;
production mix, at plant;
1000 kg/m3, 18 g/mol

DEaggts

Tap water from surface water
flockulation, filtration, disinfection, ion removement etc., from surface water;
production mix, at plant;
1000 kg/m3, 18 g/mol

JPaggts

Tap water from surface water
filtration, disinfection, ion removement etc., from surface water;
production mix, at plant;
1000 kg/m 3,18 g/mol

CNaggts

t-butanol by-product propylene oxide
Oxirane process;
production mix, at plant;
0.79 g/cm3, 74.12 g/mol

DEaggts

Tellurium production
pretreatment, roasting, leaching, electrolysis, purification;
production mix, at plant;
6,24 g/cm3, 127.60 g/mol

GLOp-aggts

Tempered glass 4 mm
melting and forming, thermal tempering;
production mix, at plant;
2.5 g/cm3, functional unit:10 kg/sqm, thickness: 4 mm

EU-28aggts

Terophon (anti drumming compound, Teroson)
mixing of water, kaolin, aluminium hydroxide (major components);
production mix, at plant

DEaggts

Tetra isopropyl titanate (stoichiometric)
reaction of titanium tetrachloride with isopropanol;
production mix, at plant;
0.96 g/cm3, 284.22 g/mol

DEaggts

Tetra isopropyl titanate (stoichiometric)
reaction of titanium tetrachloride with isopropanol;
production mix, at plant;
0.96 g/cm3, 284.22 g/mol

EU-28aggts

Tetraacetyl ethylenediamine (TAED)
reaction of ethylene diamine with acetic acid, reaction of DAED with acetic anhydride;
production mix, at plant;
228.25 g/mol

NLaggts

Tetrachloromethane
chlorination of methyl chloride;
single route, at plant;
1.48 g/cm3, 119.38 g/mol

DEaggts

Tetrachlorosilane (silicon tetrachloride)
reacting pure silicon with dichloromethane;
production mix, at plant;
1.8 g/cm3, 169.90 g/mol

DEaggts

Tetrafluoroethane (R134a) (estimation)
from trichloroethylene and hydrogen fluoride;
single route, at plant;
102.03 g/mol

DEaggts

Tetrafluoroethylene
pyrolysis of chlorodifluoromethane;
single route, at plant;
1.52 g/cm3, 100.02 g/mol

NLaggts

Tetrafluoroethylene
pyrolysis of chlorodifluoromethane;
single route, at plant;
1.52 g/cm3, 100.02 g/mol

ITaggts

Tetrafluoroethylene
pyrolysis of chlorodifluoromethane;
single route, at plant;
1.52 g/cm3, 100.02 g/mol

DEaggts

Tetrafluoroethylene
pyrolysis of chlorodifluoromethane;
single route, at plant;
1.52 g/cm3, 100.02 g/mol

GBaggts

Tetrahydrofuran via 1,4-Butanediol
via 1,4- Butanediol;
single route, at plant;
0.8892 g/cm3, 72.11 g/mol

DEaggts

Thermal energy and electricity from biomass (solid) - HDF/MDF
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28p-aggts

Thermal energy and electricity from sugar cane bagasse (51% H2O content)
combustion of bagasse, CHP plant;
single route, at plant;
85% efficiency

GLOp-aggts

Thermal energy from biomass (solid) - HDF/MDF
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EU-28p-aggts

Thermal energy from hard coal
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

MXaggts

Thermal energy from heavy fuel oil (HFO)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

SAaggts

Thermal energy from heavy fuel oil (HFO)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

CYaggts

Thermal energy from heavy fuel oil (HFO)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EEaggts

Thermal energy from heavy fuel oil (HFO)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

CZaggts

Thermal energy from heavy fuel oil (HFO)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

BGaggts

Thermal energy from light fuel oil (LFO)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

CYaggts

Thermal energy from light fuel oil (LFO)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

BGaggts

Thermal energy from light fuel oil (LFO)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

CZaggts

Thermal energy from light fuel oil (LFO)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

SAaggts

Thermal energy from light fuel oil (LFO)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

EEaggts

Thermal energy from natural gas
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

MXaggts

Thermal energy from natural gas
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

KRaggts

Thermal energy from natural gas
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

SAaggts

Thermal energy from natural gas (CHP)
technology mix regarding firing and flue gas cleaning;
production mix, at plant

EU-28aggts

Thermal energy from natural gas (CHP) (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at plant

EU-28aggts

Thermal energy from natural gas (CHP) (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at plant

EU-28aggts

Thermal energy from natural gas (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

DEaggts

Thermal energy from natural gas (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

DKaggts

Thermal energy from natural gas (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

CHaggts

Thermal energy from natural gas (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

NLaggts

Thermal energy from natural gas (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

ESaggts

Thermal energy from natural gas (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

NZaggts

Thermal energy from natural gas (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

GBaggts

Thermal energy from natural gas (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

AUaggts

Thermal energy from natural gas (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

BEaggts

Thermal energy from natural gas (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

EU-28aggts

Thermal energy from natural gas (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

NOaggts

Thermal energy from natural gas (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

ITaggts

Thermal energy from natural gas (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

BRaggts

Thermal energy from natural gas (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

FRaggts

Thermal energy from natural gas (direct)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

USaggts

Thermal energy from natural gas (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

GBaggts

Thermal energy from natural gas (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

NLaggts

Thermal energy from natural gas (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

AUaggts

Thermal energy from natural gas (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

DEaggts

Thermal energy from natural gas (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

FRaggts

Thermal energy from natural gas (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

NZaggts

Thermal energy from natural gas (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

BEaggts

Thermal energy from natural gas (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

USaggts

Thermal energy from natural gas (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

CHaggts

Thermal energy from natural gas (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

NOaggts

Thermal energy from natural gas (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

ITaggts

Thermal energy from natural gas (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

EU-28aggts

Thermal energy from natural gas (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

BRaggts

Thermal energy from natural gas (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

ESaggts

Thermal energy from natural gas (indirect)
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant;
100% efficiency

DKaggts

Thermal Energy from natural gas 100%
technology mix regarding firing and flue gas cleaning;
production mix, at heat plant

CNp-aggts

Thermal energy from natural gas 100% (2011) (domestic production)
technology mix regarding firing and flue gas cleaning;
single route, at heat plant;
100% efficiency

JPaggts

Thermoplastic polyurethane (TPU, TPE-U) adhesive
reaction of methylene diisocyanate and polyether polyol;
production mix, at plant;
66.5% methylene diisocyanate, 33.5% polyether polyol

EU-28aggts

Tile and stone cleaner (estimation)
material composition;
single route, at producer;
75% H2O

DEaggts

Timber pine
saw, lumber;
production mix, at plant;
65% moisture

DEaggts

Tin Bronze (CuSn6)
Fire refining and casting, secondary production;
single route, at plant;
94% copper, 6% tin

EU-28p-aggts

Tin-lead alloy (SnPb37) (estimation)
Combining 63% tin and 37% lead;
single producer, at plant;
SnPb37

GLOaggts

Titanium alloy (Ti6Al4V)
titanium extraction, processing and alloying;
production mix, at plant;
6% aluminium, 4% vanadium

GLOaggts

Titanium Dioxide Pigment (chloride process) (estimation)
chloride process, from rutile;
single route, at plant;
4.23 g/cm3, 79.87 g/mol

MYaggts

Titanium ore extraction and processing
ore extraction and processing;
production mix, at plant;
ilmentite and rutile ores

GLOaggts

Titanium ore extraction and processing, import DE from AU (ilmenite, sand basis)
mining and processing;
single route, at plant;
50% TiO2

DEaggts

Tomato (97% H2O)
tomato cultivation and harvest;
production mix, at field border;
97% H2O

CNaggts

Tribasic lead sulphate (stabilizer, estimation)
reaction of lead oxide and a sulfated component;
production mix, at plant;
990.86 g/mol

EU-28aggts

Tricalcium phosphate
Neutralizing slaked lime with phosphoric acid;
production mix, at plant;
3.14 g/cm3, 310.18 g/mol

USaggts

Tricalcium phosphate preparation (estimation)
Neutralizing slaked lime with phosphoric acid;
production mix, at plant;
3.14 g/cm3, 310.18 g/mol

EU-28aggts

Tricresylphosphate (TCP) (estimation)
via phosphorous oxychloride and phosphorous acid;
production mix, at plant

DEaggts

Triethylendiamine (TEDA)
reaction of ethylene diamine and piperazine;
single route, at plant;
112.18 g/mol

EU-28aggts

Trimellitic anhydride
oxidation of dimethyl benzaldehyde with air;
single route, at plant;
192.13 g/mol

DEaggts

Trimethylamine
reaction of methanol and ammonia;
production mix, at plant;
670 mg/mL, 59.11 g/mol

DEaggts

Trimethylolpropane (by-product sodium formate)
base- catalyzed reaction of butyraldehyde and formaldehyde, sodium hydroxide used as base, by-product sodium formate;
production mix, at plant;
density: 1.084 g/mL, molar mass: 134.17 g/mol

CNaggts

Tripropylene glycol
PO-hydrogenation;
single route, at plant;
1.02 g/mL, 192.25 g/mol

DEaggts

Tris (chloro-ethyl) phosphate
via ethylene oxide and phosphorus oxychloride;
production mix, at plant;
1.39 g/cm3, 285.48 g/mol

DEaggts

Triticale cultivation (15% H2O content) (estimation)
technology mix;
production mix, at field border;
15% H2O

DEaggts

Truck, Euro 4, 12 - 14t gross weight / 9,3t payload capacity (with SCR)
diesel driven, Euro 4, cargo;
consumption mix;
12 - 14t gross weight / 9,3t payload capacity

GLOu-sots

Truck, Euro 4, 14 - 20t gross weight / 11,4t payload capacity (with SCR)
diesel driven, Euro 4, cargo;
consumption mix;
14 - 20t gross weight / 11,4t payload capacity

GLOu-sots

Truck, Euro 4, 20 - 26t gross weight / 17,3t payload capacity (with SCR)
diesel driven, Euro 4, cargo;
consumption mix;
20 - 26t gross weight / 17,3t payload capacity

GLOu-sots

Truck, Euro 4, 26 - 28t gross weight / 18,4t payload capacity (with SCR)
diesel driven, Euro 4, cargo;
consumption mix;
26 - 28t gross weight / 18,4t payload capacity

GLOu-sots

Truck, Euro 4, 28 - 32t gross weight / 22t payload capacity (with SCR)
diesel driven, Euro 4, cargo;
consumption mix;
28 - 32t gross weight / 22t payload capacity

GLOu-sots

Truck, Euro 4, 7,5 t - 12t gross weight / 5t payload capacity (with SCR)
diesel driven, Euro 4, cargo;
consumption mix;
7,5 t - 12t gross weight / 5t payload capacity

GLOu-sots

Truck, Euro 4, more than 32t gross weight / 24,7t payload capacity (with SCR)
diesel driven, Euro 4, cargo;
consumption mix;
more than 32t gross weight / 24,7t payload capacity

GLOu-sots

Truck, Euro 4, up to 7,5t gross weight / 3,3t payload capacity (with SCR)
diesel driven, Euro 4, cargo;
consumption mix;
up to 7,5t gross weight / 3,3t payload capacity

GLOu-sots

Truck-trailer, Euro 4, 28 - 34t gross weight / 22t payload capacity (with SCR)
diesel driven, Euro 4, cargo;
consumption mix;
28 - 34t gross weight / 22t payload capacity

GLOu-sots

Truck-trailer, Euro 4, 34 - 40t gross weight / 27t payload capacity (with SCR)
diesel driven, Euro 4, cargo;
consumption mix;
34 - 40t gross weight / 27t payload capacity

GLOu-sots

Truck-trailer, Euro 4, 50 - 60t gross weight / 40,6t payload capacity
diesel driven, Euro 4, cargo;
consumption mix;
50 - 60t gross weight / 40,6 t payload capacity

GLOu-sots

Truck-trailer, Euro 4, 50 - 60t gross weight / 40,6t payload capacity (with SCR)
diesel driven, Euro 4, cargo;
consumption mix;
50 - 60t gross weight / 40,6 t payload capacity

GLOu-sots

Truck-trailer, Euro 4, up to 28t gross weight / 12,4t payload capacity (with SCR)
diesel driven, Euro 4, cargo;
consumption mix;
up to 28t gross weight / 12,4t payload capacity

GLOu-sots

Truck-trailer, Euro 5, 50 - 60t gross weight / 40,6t payload capacity
diesel driven, Euro 5, cargo;
consumption mix;
50 - 60t gross weight / 40,6t payload capacity

GLOu-sots

Tungsten Carbide Powder (estimation)
reaction of tungsten metal with black carbon;
single route, at plant;
15.63 g/cm3, 195.9 g/mol

CNaggts

Tungsten Metal Powder (estimation)
Mining, concentration, pre-treatment, APT production, calcination, tungsten trioxide reduction;
single route, at plant;
19,3 g/cm3, 183,8 g/mol

CNaggts

Turpentine (2015) (mass allocation)
turpentine from kraft paper production;
single route, at producer;
50% alpha- and beta-pinene content

EU-28p-aggts/FEFCO

Tyres (sedan car)
mixing, preparation, building, vulcanisation;
single route, at producer;
around 10 kg weight per tyre

FRp-aggts

Urea formaldehyde (UF) adhesive system (20% H2O)
hydromethylation and condensation reactions of urea and formaldehyde;
single route, at plant;
20% H20

USaggts

Used passenger car tyre in waste incineration plant (mix)
waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment;
production mix (region specific plants), at plant;
25.8 MJ/kg net calorific values

EU-28p-aggts

Used wood, wood chips (25% H2O content)
harvesting, wood chipping;
single producer, at plant;
25% water content

GLOaggts

Used wood, woodchips abs. dry
harvesting, wood chipping;
single producer, at plant;
abs. dry

DEaggts

Vanadium pentoxide concentrate (V2O5 86%)
sodium metavanadate route;
production mix, at plant;
3.36 g/cm3, 181.88 g/mol

ZAaggts

Vat Dye
via halogenation of dibenzanthrone;
production mix, at plant;
29.9% wt bromine content, 4.1% chlorine content

USaggts

Vegetable tanning (estimation)
vegetable tanning extraction, leather tanning;
single route, at plant;
tanning extract with 8% moisture content

EU-28p-aggts

Vegetable tanning (estimation)
vegetable tanning extraction, leather tanning;
single route, at plant;
tanning extract with 8% moisture content

USp-aggts

Vinylene carbonate (from ethyl carbonate over hydrochlorination)
from ethyl carbonate over hydrochlorination;
single route, at plant;
1.36 g/mL, 86.05 g/mol

JPaggts

Vinylidene dichloride
from 1,1,2-trichloroethane;
production mix, at plant;
1.21 g/cm3, 96.94 g/mol

DEaggts

Vinylidene fluoride (1,1-difluoroethylene from chlorodifluoroethane R-142b)
dehydrochlorination of chlorodifluoroethane;
single route, at plant;
64.03 g/mol

DEaggts

Washing, average
washing of textiles;
single operation, at work station;
1 kg of textiles wahed

GLOu-sots

Water (desalinated; deionised)
via ion exchange;
single route, at plant;
1000 kg/m3, 18 g/mol

CNaggts

Water glass (sodium silicate) (solid)
reaction of sand with soda ash;
single route, at plant;
2.61 g/cm3, 122.06 g/mol

DEaggts

Water proof agent (C6) and application thick layer (estimation)
water proof;
single route, at plant;
C6, thick layer 2.5 g/m2

USp-aggts

Water proof agent (C6) and application thick layer (estimation)
water proof;
single route, at plant;
C6, thick layer 2.5 g/m2

EU-28p-aggts

Water proof agent (C6) and application thin layer (estimation)
water repellancy;
single route, at plant;
C6, thin layer 0.6 g/m2

EU-28p-aggts

Water proof agent (C6) and application thin layer (estimation)
water repellancy;
single route, at plant;
C6, thin layer 0.6 g/m2

USp-aggts

Waterglass (sodium silicate) (37/40 solution)
mixing of sodium carbonate and quartz sand;
single route, at plant;
37/40 solution, silicate water solution

DEaggts

Wax / Paraffins at refinery
from crude oil;
production mix, at refinery

RUaggts

Wax / Paraffins at refinery
from crude oil;
production mix, at refinery

NLaggts

Wheat middlings from wheat mill (economic allocation)
wheat cultivation, milling and screening;
single route, at plant;
16.5% crude protein

USaggts

Wheel loader (newer standard)
diesel- driven wheel loader engine;
single operation, at work station;
1 kg diesel combusted

GLOu-sots

Window glass
melting, blowing, drawing, pressing;
production mix, at plant;
2500 kg/m3

DEaggts

Wine cork (natural)
Cork debarking, washing, drying, stamping;
single route, at plant;
7% moisture, 50% carbon content

DEaggts

Winter rape cultivation (75% H2O content)
technology mix;
production mix, at producer;
at field border;75% H2O

DEaggts

Winter rye grain cultivation (14% H2O content), by-products straw (economic allocation)
technology mix;
production mix, at field border;
14% H2O

DEaggts

Winter wheat (15% H2O content)
winter wheat cultivation;
production mix, at field border;
15% H2O content

AUaggts

Winter wheat cultivation (grain) (14% H2O content) (estimation)
technology mix;
production mix, at field border;
14% H2O

CAaggts

Winter wheat grains (15% H2O content) (estimation)
technology mix;
production mix, at field border;
15% H2O

CAaggts

Winter wheat straw cultivation (15% H2O content)
technology mix;
production mix, at field border;
14% H2O

DEaggts

Wood pellets (9% H2O content)
milling, drying, pelletizing;
single producer, at plant;
9% water content

EU-28aggts

Wood residue mix
milling, drying, pelletizing (depending on kind of wood residue);
production mix, at producer (different kinds of residual wood);
Wood chips, wood pellets, sawdust, 17% H2O, 14.54 MJ/ kg net calorific value

EU-28aggts

Wood soft fibre board
chipping and hot pressing;
single producer, at plant

DEaggts

Wooden pallets (EURO, 40% moisture)
sawing, piling, nailing;
single route, at plant;
40% moisture

EU-28aggts

Xylene mix
from pyrolysis gasoline;
single route, at plant;
0.86- 0.88 g/ml, 106.16 g/mol

DEaggts

Zinc (remelting)
cleaning, melting, refining;
single route, at plant;
7.14 g/cm3, 65.38 g/mol

DEp-aggts

Zinc acetate (anhydrous) (estimation)
reaction of zinc metal and acetic acid;
production mix, at plant;
183.5 g/mol

EU-28aggts

Zinc acetate (anhydrous) (estimation)
reaction of zinc metal and acetic acid;
production mix, at plant;
183.5 g/mol

DEaggts

Zinc ammonium chloride (estimation)
Acid leaching on metallic zinc with ammonia solution;
single route, at producer;
white crystalline solid, 243 g/mol

EU-28aggts

Zinc cast alloy (GD ZnAl4Cu1)
ore mining and beneficiation, two-stage roasting, leaching,  electrolysis and re-melting;
production mix, at plant;
GD ZnAl4Cu1

DEaggts

Zinc die casting
die casting;
single route, at plant;
7.14 g/cm3, 65.38 g/mol

DEaggts

Zinc mix
roasting, leaching, electrowinning;
production mix, at plant;
7.14 g/cm3, 65.41 g/mol

GLOaggts

Zinc oxide (American process)
from zinc concentrate/zinc scrap iron, American process;
single route, at plant;
5.61 g/cm3, 81.38 g/mol

DEaggts

Zinc oxide (technology mix: American and French process)
technology mix: French process (production from electrolytic zinc) and American process (production from zinc concentrate/ zinc scrap iron);
production mix, at plant;
5.61 g/cm3, 81.39 g/mol

GLOaggts

Zinc oxide high-purity (French process)
French process, production from electrolytic zinc;
single route, at plant;
5.61 g/cm3, 81.39 g/mol

DEaggts

Zinc phosphate (estimation)
stoichiometric estimation;
production mix, at plant;
3.99 g/cm3, 386.11 g/mol

DEaggts

Zinc powder
mining and concentrating, roasting and sintering, leaching, electrolysis, powder production;
production mix, at plant;
7.14 g/cm3, 65.38 g/mol

GLOaggts

Zinc sulphate (ZnSO4) (estimation)
reaction of zinc oxide with sulfuric acid;
single route, at plant;
161.47 g/mol, 3.54 g/cm3

DEaggts

Zircon carbonate (ZrCO3)
from zirconium mineral sand;
single route, at plant;
431.68 g/mol

GBaggts