GaBi Solutions

Extension database Ia: Intermediates organic

Process nameCountryTypeData source

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

FRaggts

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

GBaggts

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

EU-28aggts

3-Dimethylaminopropylamine (DMAPA)
Hydrogenation of 3-(Dimethylamino)propionitril (DMAPN);
production mix, at producer;
100% active substance; CAS number: 109-55-7

EU-28aggts

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

BEaggts

Acrylonitrile (AN)
ammoxidation of propene;
production mix, at plant;
liquid, density: 0.81 g/cm3, molar mass: 53.06 g mol−1

NLaggts

Acrylonitrile (AN)
ammoxidation of propene;
production mix, at plant;
liquid, density: 0.81 g/cm3, molar mass: 53.06 g mol−1

ITaggts

Acrylonitrile (AN)
ammoxidation of propene;
production mix, at plant;
liquid, density: 0.81 g/cm3, molar mass: 53.06 g mol−1

GBaggts

Acrylonitrile (AN)
ammoxidation of propene;
production mix, at plant;
liquid, density: 0.81 g/cm3, molar mass: 53.06 g mol−1

DEaggts

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

DEaggts

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

GBaggts

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

FRaggts

AH-salt
HMDA from acrylonitrile;
production mix, at plant;
63 % concentrated

DEaggts

AH-salt
HMDA from adipic acid;
production mix, at plant;
63 % concentrated

GBaggts

AH-salt
HMDA from adipic acid;
production mix, at plant;
63 % concentrated

DEaggts

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

DEaggts

Aminoethylethanolamine (AEEA) Production from MEG and Ammonia
Hydrogenative amination of monoethylene glycol;
production mix, at producer;
100% active substance; CAS number: 111-41-1

EU-28aggts

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

FRaggts

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

BEaggts

Benzene
from pyrolysis fuel;
production mix, at plant;
density: 0,88 g·cm−3, molar mass: 78,11 g·mol−1

ITaggts

Benzene
from pyrolysis fuel;
production mix, at plant;
density: 0,88 g·cm−3, molar mass: 78,11 g·mol−1

GBaggts

Benzene
from pyrolysis fuel;
production mix, at plant;
density: 0,88 g·cm−3, molar mass: 78,11 g·mol−1

FRaggts

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

NLaggts

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

FRaggts

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

DEaggts

Butane
from C4-raffinate;
production mix, at plant;
gaseous, density: 2,71 g·l−1 (0 °C, 1013 hPa), molar mass: 58,12 g·mol−1

DEaggts

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

NOaggts

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

GBaggts

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

EU-28aggts

Caprolactam
from Phenol;
production mix, at plant;
solid, density: 1,02 g·cm−3 (75 °C), molar mass: 113,16 g·mol−1

NLaggts

Caprolactam
from Phenol;
production mix, at plant;
solid, density: 1,02 g·cm−3 (75 °C), molar mass: 113,16 g·mol−1

ITaggts

Chloroacetic acid by catalysed chlorination of acetic acid
Catalyzed chlorination of acetic acid;
production mix, at producer;
100% active substance; CAS number: 79-11-8

EU-28aggts

Cumene (C9H12) (based on benzene from reformate)
alkylation of benzene;
production mix, at plant;
0.862 g/cm3, 120.20 g/mol

THaggts

Cumene (C9H12) (based on benzene from reformate)
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

ESaggts

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

FRaggts

Cyclohexane
catalytic hydration of benzene;
production mix, at plant;
0.7781 g/mL, 84.16 g/mol

GBaggts

Cyclohexane
catalytic hydration of benzene;
production mix, at plant;
0.7781 g/mL, 84.16 g/mol

NLaggts

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

DEaggts

Diethanolamine
Reaction of ethylene oxide with excess of ammonia;
production mix, at producer;
100% active substance, 1.09 g/cm3, 105.14 g/mol

EU-28aggts

Di-isononyl phthalate (DINP)
esterification of phthalic acid;
production mix, at plant;
0.98 g/cm3, 418.62 g/mol

DEaggts

Dimethyl carbonate (DMC)
liquid phase, from methanol and phosgene, by-product dimethyleneoxalate;
production mix, at plant;
90.08 g/mol

DEaggts

Dimethyl terephthalate (DMT)
oxidation of p-xylene;
production mix, at plant;
1.35 g/cm3, 194.19 g/mol

NLaggts

Dimethyl terephthalate (DMT)
oxidation of p-xylene;
production mix, at plant;
1.35 g/cm3, 194.19 g/mol

ITaggts

Dimethyl terephthalate (DMT)
oxidation of p-xylene;
production mix, at plant;
1.35 g/cm3, 194.19 g/mol

FRaggts

Dimethyl terephthalate (DMT)
oxidation of p-xylene;
production mix, at plant;
1.35 g/cm3, 194.19 g/mol

DEaggts

Dimethylamine (Production from Alcohols)
Catalytic amination;
production mix, at producer;
100% active substance; CAS number: 124-40-3

EU-28aggts

Dimethylsulphate (DMS) Production via Ethers and SulphurTrioxide
Production from ethers and sulphur trioxide;
production mix, at producer;
100% active substance; CAS number: 77-78-1

EU-28aggts

Dinitro toluene
nitration of toluene;
production mix, at plant;
solid, molar mass: 182,14 g·mol−1

FRaggts

Dinitro toluene
nitration of toluene;
production mix, at plant;
solid, molar mass: 182,14 g·mol−1

ITaggts

Dinitro toluene
nitration of toluene;
production mix, at plant;
solid, molar mass: 182,14 g·mol−1

DEaggts

Dinitro toluene
nitration of toluene;
production mix, at plant;
solid, molar mass: 182,14 g·mol−1

GBaggts

Dioctyltin oxide (Estimation)
hydrolysis of Dialkyltin halide;
production mix, at producer

EU-28aggts

Epichlorohydrin
via allyl chloride;
production mix, at plant;
liquid, density: 1,18 g·cm−3 (20 °C), molar mass: 92,53 g·mol−1

DEaggts

Ethanol
hydrogenation with nitric acid;
single route, at plant;
96 % concentrated

GBaggts

Ethanol
hydrogenation with nitric acid;
single route, at plant;
96 % concentrated

FRaggts

Ethene (ethylene)
steam cracker;
production mix, at plant;
1.178 kg/m3, 28.05 g/mol

ESaggts

Ethene (ethylene)
steam cracker;
production mix, at plant;
1.178 kg/m3, 28.05 g/mol

FRaggts

Ethyl benzene
liquid phase alkylation;
production mix, at plant;
liquid, density: 0,87 g·cm−3, molar mass: 106,17 g·mol−1

NLaggts

Ethyl benzene
liquid phase alkylation;
production mix, at plant;
0.87 g/cm3, 106.17 g/mol

DEaggts

Ethylamine
from ethanol and ammonia, by-product Diethylamine, Triethylamine (TEA);
production mix, at plant;
gaseous, density: 2,162 g·m−3(0 °C, 1013 mbar), molar mass: 45,08 g·mol−1

DEaggts

Ethylene glycol
from ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

BEaggts

Ethylene glycol
from ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

FRaggts

Ethylene glycol
from ethene and oxygen via ethylene oxide;
production mix, at plant;
1.11 g/cm³, 62 g/mol

GBaggts

Ethylene oxide (EO) via air
oxidation of ethylene with air;
production mix, at plant;
1.93 kg/m3, 44.05 g/mol

FRaggts

Ethylene oxide (EO) via air
oxidation of ethylene with air;
production mix, at plant;
1.93 kg/m3, 44.05 g/mol

NLaggts

Ethylene oxide (EO) via air
oxidation of ethylene with air;
production mix, at plant;
1.93 kg/m3, 44.05 g/mol

BEaggts

Ethylene oxide (EO) via air
oxidation of ethylene with air;
production mix, at plant;
1.93 kg/m3, 44.05 g/mol

GBaggts

Ethylene oxide (EO) via O2/methane
oxidation of ethylene with oxygen;
production mix, at plant;
gaseous, density: 1,93 kg·m−3 (15 °C, 1000 hPa), molar mass: 44,05 g·mol−1

DEaggts

Ethylenediaminetetraacetic acid (EDTA) (estimated)
Cyanomethylation of ethylene diamine;
single route, at plant;
0.86 g/cm3, 292.24 g/mol

EU-28aggts

Formaldehyde (HCHO; 37%)
dehydrogenation of methanol;
production mix, at plant;
37 % concentrated

ITaggts

Formaldehyde (HCHO; 37%)
dehydrogenation of methanol;
production mix, at plant;
37 % concentrated

GBaggts

Formaldehyde (HCHO; 37%)
dehydrogenation of methanol;
production mix, at plant;
37 % concentrated

NLaggts

Formaldehyde (HCHO; 37%)
dehydrogenation of methanol;
production mix, at plant;
37 % concentrated

FRaggts

Formic acid (methane acid, 85%)
from methanol;
production mix, at plant;
liquid, density: 1.220 g/mL, molar mass: 46.03 g mol−1, pKa value: 3.77

DEaggts

Glycerine (from Epichlorohydrine)
via epichlorohydrine;
production mix, at plant;
1.26 g/cm3, 92.09 g/mol

DEaggts

Glycerine (refined) by-product rapeseed methyl ester (RME) (energy allocated)
extraction, refining, transesterification;
single route, at plant;
1.26 g/cm3, 92.09 g/mol

EU-28aggts

Glycerine (refined) by-product rapeseed methyl ester (RME) (energy allocated)
extraction, refining, transesterification;
single route, at plant;
1.26 g/cm3, 92.09 g/mol

DEaggts

Glycerine (refined) by-product rapeseed methyl ester (RME) (price 2014 allocated)
extraction, refining, transesterification;
single route, at plant;
1.26 g/cm3, 92.09 g/mol

DEaggts

Glycerine (refined) by-product rapeseed methyl ester (RME) (price 2014 allocated)
extraction, refining, transesterification;
single route, at plant;
1.26 g/cm3, 92.09 g/mol

EU-28aggts

Glycerine by-product rapeseed methyl ester (RME) (energy allocated)
extraction, refining, transesterification;
single route, at plant;
1.26 g/cm3, 92.09 g/mol

DEaggts

Glycerine by-product rapeseed methyl ester (RME) (energy allocated)
extraction, refining, transesterification;
single route, at plant;
1.26 g/cm3, 92.09 g/mol

EU-28aggts

Glycerine by-product rapeseed methyl ester (RME) (price 2014 allocated)
extraction, refining, transesterification;
single route, at plant;
1.26 g/cm3, 92.09 g/mol

EU-28aggts

Glycerine by-product rapeseed methyl ester (RME) (price 2014 allocated)
extraction, refining, transesterification;
single route, at plant;
1.26 g/cm3, 92.09 g/mol

DEaggts

Hexabromododecane (HBCD, 1,2,5,6,9,10-Hexabromododecane)
reaction of cyclododecatriene and bromine;
single route, at plant;
643.71 g/mol

EU-28aggts

Hexabromododecane (HBCD, 1,2,5,6,9,10-Hexabromododecane)
reaction of cyclododecatriene and bromine;
single route, at plant;
643.71 g/mol

DEaggts

Hexamethylenediamine (HMDA; from adipic acid via adiponitrile)
via adipic acid;
single route, at plant;
0.84 g/mL, 116.20 g/mol

GBaggts

Hexamethylenediamine (HMDA; from butadiene via adiponitrile)
from butadiene via adiponitrile;
single route, at plant;
0.84 g/mL, 116.20 g/mol

FRaggts

Hexamethylenediamine (HMDA; from butadiene via adiponitrile)
from butadiene via adiponitrile;
single route, at plant;
0.84 g/mL, 116.20 g/mol

GBaggts

Hexamethylenediamine (HMDA; from butadiene via adiponitrile)
from butadiene via 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

DEaggts

Isobutane (from n-butane)
via n-butane;
production mix, at plant;
gaseous, density: 2,71 g·l−1 (0 °C, 1013 hPa), molar mass: 58,12 g·mol−1

DEaggts

Isononanoic acid
aldehyde oxidation;
production mix, at plant;
liquid, density: 0.897 - 0.903 g/cm3, molar mass: 158,2 g/mol

DEaggts

Isononanol
single route;
production mix, at plant;
liquid, density: 0,82 g·cm−3, molar mass: 144.25 g/mol

DEaggts

Isopropanol
indirect hydrogenation;
production mix, at plant;
0.78 g/cm3, 60.10 g·/mol

GBaggts

Isopropanol
indirect hydrogenation;
single route, at plant;
0.78 g/cm3, 60.10 g·/mol

FRaggts

Isopropanol
indirect hydrogenation;
single route, at plant;
0.78 g/cm3, 60.10 g·/mol

NLaggts

Isopropanol
indirect hydrogenation;
single route, at plant;
0.78 g/cm3, 60.10 g·/mol

ITaggts

Maleic anhydride
from n-butane;
production mix, at plant;
solid, density: 1.48 g/cm3, molar mass: 98.06 g/mol

GBaggts

Maleic anhydride
via oxidation of xylene;
production mix, at plant;
solid, density: 1.48 g/cm3, molar mass: 98.06 g/mol

DEaggts

Maleic anhydride
from n-butane;
production mix, at plant;
solid, density: 1.48 g/cm3, molar mass: 98.06 g/mol

BEaggts

Maleic anhydride
from n-butane;
production mix, at plant;
solid, density: 1.48 g/cm3, molar mass: 98.06 g/mol

ITaggts

Maleic anhydride
from benzene;
production mix, at plant;
solid, density: 1.48 g/cm3, molar mass: 98.06 g/mol

ITaggts

Methane
purification of natural gas;
single route, at plant;
0.72 kg/m3, 84.16 g/mol

GBaggts

Methane
purification of natural gas;
single route, at plant;
0.72 kg/m3, 84.16 g/mol

FRaggts

Methane
purification of natural gas;
single route, at plant;
0.72 kg/m3, 84.16 g/mol

ESaggts

Methane
purification of natural gas;
single route, at plant;
0.72 kg/m3, 84.16 g/mol

EU-28aggts

Methane
purification of natural gas;
single route, at plant;
0.72 kg/m3, 84.16 g/mol

BEaggts

Methane
purification of natural gas;
single route, at plant;
0.72 kg/m3, 84.16 g/mol

NLaggts

Methane
purification of natural gas;
single route, at plant;
0.72 kg/m3, 84.16 g/mol

ITaggts

Methane
purification of natural gas;
single route, at plant;
0.72 kg/m3, 84.16 g/mol

NOaggts

Methanol from natural gas (integrated technologies)
from natural gas, integrated technology;
production mix, at plant;
0.79 g/cm3, 32.04 g/mol

DEaggts

Methanol mix
technology mix;
consumption mix, to consumer;
0.79 g/cm3, 32.04 g/mol

EU-28aggts

Methyl acetate
esterification of methanol with acetic acid;
single route, at plant;
0.93 g/cm3, 74.08 g/mol

DEaggts

Methyl bromide
by-product tetrabromo bisphenol A;
production mix, at plant;
gaseous, density: 3,97 kg·m−3 (0 °C, 1013 hPa), molar mass: 94,94 g·mol−1

DEaggts

Methyl isobutyl ketone (MIBK)
technology mix;
production mix, at plant;
0.80 g/mL, 100 g/mol

DEaggts

Methylene diisocyanate (MDI)
phosgenation of methylenedianiline;
production mix, at plant;
solid, density: 1,18 g·cm−3, molar mass: 250,26 g·mol−1

FRaggts

Methylene diisocyanate (MDI)
phosgenation of methylenedianiline;
production mix, at plant;
solid, density: 1,18 g·cm−3, molar mass: 250,26 g·mol−1

BEaggts

Methylmethacrylate (MMA, recycling of spent acid)
recycling of spent acid;
production mix, at plant;
0.94 g/cm³, 100.12 g/mol

GBaggts

Methylmethacrylate (MMA, recycling of spent acid)
recycling of spent acid;
production mix, at plant;
0.94 g/cm³, 100.12 g/mol

FRaggts

Methylmethacrylate (MMA, recycling of spent acid)
recycling of spent acid;
production mix, at plant;
0.94 g/cm³, 100.12 g/mol

NLaggts

N,N-Dimethylaminopropyl Acrylamide (DiMAPA), credit butanol
Continuous aminolysis;
production mix, at producer

EU-28aggts

Nitrobenzene
from benzene via nitration;
production mix, at plant;
1.199 g/cm3, 123.06 g/mol

BEaggts

Nitrobenzene
from benzene via nitration;
production mix, at plant;
1.199 g/cm3, 123.06 g/mol

FRaggts

n-Methylpyrolidone (NMP, Butyrolactone via Maleic anhydride)
via maleic anhydride;
production mix, at plant;
liquid, density: 1,03 g·cm−3, molar mass: 99,13 g·mol−1

DEaggts

o-Xylene
from pyrolysis gasoline;
single route, at plant;
0.88 g/ml, 106.17 g/mol

ITaggts

o-Xylene
from pyrolysis gasoline;
single route, at plant;
0.88 g/ml, 106.17 g/mol

FRaggts

o-Xylene
from pyrolysis gasoline;
single route, at plant;
0.88 g/ml, 106.17 g/mol

NLaggts

Phenol
Hock Process, oxidation of cumene;
single route, at plant;
1.07 g/cm3, 94 g/mol

BEaggts

Phenol
Hock Process, oxidation of cumene;
single route, at plant;
1.07 g/cm3, 94 g/mol

FRaggts

Phthalic anhydride
via oxidation of xylene;
production mix, at plant;
1.53 g/cm, 148.12 g/mol

ITaggts

Phthalic anhydride
via oxidation of xylene;
production mix, at plant;
1.53 g/cm, 148.12 g/mol

GBaggts

Phthalic anhydride
via oxidation of xylene;
production mix, at plant;
1.53 g/cm, 148.12 g/mol

NLaggts

Phthalic anhydride
via oxidation of xylene;
production mix, at plant;
1.53 g/cm, 148.12 g/mol

DEaggts

Phthalic anhydride
via oxidation of xylene;
production mix, at plant;
1.53 g/cm, 148.12 g/mol

FRaggts

Production 3-(Dimethylamino)propionitril (DMAPN)
Reaction of Dimethyl amine and acrylonitrile;
production mix, at producer

EU-28p-aggts

Production dimethyl ether from methanol
Catalytic dehydration of methanol;
production mix, at plant;
2.1146 kg/m3, 46.07 g/mol

EU-28aggts

Propene (propylene)
steam cracker;
single route, at plant;
1.91 kg/m3, 42.08 g/mol,

GBaggts

Propylene glycol
via PO-hydrogenation;
single route, at plant;
1.04 g/cm3, 76.10 g/mol

FRaggts

p-Xylene (from reformate)
from reformate;
production mix, at plant;
liquid at room temperature, molar mass: 106,17 g·mol−1, melting point: 13,3 °C

GBaggts

p-Xylene (from reformate)
from reformate;
production mix, at plant;
liquid at room temperature, molar mass: 106,17 g·mol−1, melting point: 13,3 °C

ITaggts

p-Xylene (from reformate)
from reformate;
production mix, at plant;
liquid at room temperature, molar mass: 106,17 g·mol−1, melting point: 13,3 °C

FRaggts

p-Xylene (from reformate)
from reformate;
production mix, at plant;
liquid at room temperature, molar mass: 106,17 g·mol−1, melting point: 13,3 °C

DEaggts

Sodium citrate
neutralization of citric acid with sodium hydroxide;
single route, at plant;
1.7 g/cm3, 258.06 g/mol

DEaggts

Soot (C carrier, from ethyne production)
via SACHSSE-BARTHOLOME process;
production mix, at plant;
solid powder

DEaggts

Styrene
catalytic dehydrogenation of ethylbenzene (EBSM);
production mix, at plant;
liquid, density: 0,91 g·cm−3, molar mass: 104,15 g·mol−1

ITaggts

Styrene
catalytic dehydrogenation of ethylbenzene (EBSM);
production mix, at plant;
liquid, density: 0,91 g·cm−3, molar mass: 104,15 g·mol−1

FRaggts

Styrene
catalytic dehydrogenation of ethylbenzene (EBSM);
production mix, at plant;
liquid, density: 0,91 g·cm−3, molar mass: 104,15 g·mol−1

GBaggts

Styrene
catalytic dehydrogenation of ethylbenzene (EBSM);
production mix, at plant;
liquid, density: 0,91 g·cm−3, molar mass: 104,15 g·mol−1

BEaggts

Tallow fatty acid (C16-C18 fatty acid from tallow)
Hydrolysis and fractionated distillation;
single route, at plant

EU-28aggts

Titanium isopropoxide (estimation)
reaction of titanium tetrachloride and isopropanol;
production mix, at producer

EU-28aggts

Toluene
BTX; from reformate;
production mix, at plant;
density: 0,87 g·cm−3, molar mass: 92,14 g·mol−1

GBaggts

Toluene
BTX; from reformate;
production mix, at plant;
density: 0,87 g·cm−3, molar mass: 92,14 g·mol−1

FRaggts

Toluene
BTX; from reformate;
production mix, at plant;
density: 0,87 g·cm−3, molar mass: 92,14 g·mol−1

EU-28aggts

Toluene
from pyrolysis fuel;
production mix, at plant;
density: 0,87 g·cm−3, molar mass: 92,14 g·mol−1

ITaggts

Toluene
from pyrolysis fuel;
production mix, at plant;
density: 0,87 g·cm−3, molar mass: 92,14 g·mol−1

NLaggts

Toluene diisocyanate (TDI; Phosgenation)
phosgenation of toluenediamine;
production mix, at plant;
liquid, density: 1.214 g/cm3, molar mass: 174.2 g/mol

GBaggts

Toluene diisocyanate (TDI; Phosgenation)
phosgenation of toluenediamine;
production mix, at plant;
liquid, density: 1.214 g/cm3, molar mass: 174.2 g/mol

FRaggts

Triethanolamine (TEA)
from ethylene oxide;
production mix, at plant;
1.12 g/mL, 149.19 g/mol

EU-28aggts

Urea (stamicarbon process)
single route;
production mix, at plant;
solid, density: 1,32 g·cm−3, molar mass: 60,06 g·mol−1

DEaggts

Vinylchloride monomer (VCM)
chlorination of ethylene;
production mix, at plant;
2.86 kg/m3, 62.5 g/mol

GBaggts

Vinylchloride monomer (VCM)
chlorination of ethylene;
production mix, at plant;
2.86 kg/m3, 62.5 g/mol

FRaggts