GaBi Solutions

Extension database Ib: Intermediates inorganic

Process nameCountryTypeData source

Aluminium hydroxide from aluminium sulphate
based on stoichiometry ;
single route, at plant ;
2.42 g/cm3, 78.00 g/mol

DEaggts

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

DEaggts

Ammonia (NH3) production mix, 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

EU-28aggts

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

GBp-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

GBaggts

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

GBaggts

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

ITaggts

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

NOaggts

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

FRaggts

Ammonium chloride (Salmiac, Solvay-process)
Solvay process ;
production mix, at plant ;
solid, density: 1,53 g·cm−3, molar mass: 53,49...

DEaggts

Ammonium nitrate
neutralisation of nitric acid wit ammonia ;
production mix, at plant ;
1.73 g/cm3, 80.04 g/mol

EU-28aggts

Ammonium sulphate mix (by-product)
propene ammoxidation ;
production mix, at plant ;
solid, density: 1,77 g·cm−3, molar mass: 132,1...

DEaggts

Calcium hypochlorite
from sodium chloride production ;
production mix, at plant ;
solid, density: 2,35 g·cm−3, molar mass: 142,9...

DEaggts

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

BEaggts

Carbon monoxide (via synthetic gas)
cryogenic separation ;
production mix, at plant ;
density: 1,25 kg·m−3 (0 °C, 1013 mbar), molar ...

FRaggts

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

ITaggts

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

GBaggts

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

FRaggts

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

FRaggts

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

BEaggts

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

FRaggts

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

BRaggts

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

GBaggts

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

ITaggts

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

NLaggts

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

ITaggts

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

BEaggts

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

NOaggts

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

GBaggts

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

ESaggts

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

FRaggts

Hydrogen (cracker)
steam cracker, from naphtha ;
production mix, at plant ;
gaseous, density: 0,0899 kg · m−3, molar mass:...

GBaggts

Hydrogen (cracker)
steam cracker, from naphtha ;
production mix, at plant ;
gaseous, density: 0,0899 kg · m−3, molar mass:...

ITaggts

Hydrogen (cracker)
steam cracker, from natural gas ;
production mix, at plant ;
gaseous, density: 0,0899 kg · m−3, molar mass:...

NOaggts

Hydrogen (steam reforming from heavy fuel oil)
Steam reforming - heavy fuel oil ;
production mix, at plant ;
0.0899 kg/m3, 2 g/cm3

FRaggts

Hydrogen (steam reforming from heavy fuel oil)
Steam reforming - heavy fuel oil ;
production mix, at plant ;
0.0899 kg/m3, 2 g/cm3

EU-28aggts

Hydrogen (steam reforming from heavy fuel oil)
Steam reforming - heavy fuel oil ;
production mix, at plant ;
0.0899 kg/m3, 2 g/cm3

GBaggts

Hydrogen (steam reforming from natural gas)
Steam reforming - heavy fuel oil ;
production mix, at plant ;
0.0899 kg/m3, 2 g/cm3

ITaggts

Hydrogen (steam reforming from natural gas)
Steam reforming - natural gas ;
production mix, at plant ;
0.0899 kg/m3, 2 g/cm3

EU-28aggts

Hydrogen (steam reforming from natural gas)
Steam reforming - natural gas ;
production mix, at plant ;
0.0899 kg/m3, 2 g/cm3

GBaggts

Hydrogen (steam reforming from natural gas)
Steam reforming - natural gas ;
production mix, at plant ;
0.0899 kg/m3, 2 g/cm3

FRaggts

Hydrogen cyanide (prussic acid)
technology mix ;
production mix, at plant ;
0.687 g/cm3, 27.03 g/mol

GBaggts

Hydrogen cyanide (prussic acid)
technology mix ;
production mix, at plant ;
0.687 g/cm3, 27.03 g/mol

FRaggts

Hydrogen cyanide (prussic acid)
technology mix ;
production mix, at plant ;
0.687 g/cm3, 27.03 g/mol

BEaggts

Nitric acid (60%)
oxidation of ammonia ;
single route, at plant ;
60%

NLaggts

Nitric acid (60%)
oxidation of ammonia ;
single route, at plant ;
60%

GBaggts

Nitric acid (60%)
oxidation of ammonia ;
single route, at plant ;
60%

ITaggts

Nitric acid (60%)
oxidation of ammonia ;
single route, at plant ;
60%

NOaggts

Nitric acid (60%)
oxidation of ammonia ;
single route, at plant ;
60%

FRaggts

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

ESaggts

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

ATaggts

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

GBaggts

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

BEaggts

Nitrogen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.250 kg/m3, 14.0 g/mol

NOaggts

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

ITaggts

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

FRaggts

Nitrogen (liquid)
via cryogenic air separation ;
production mix, at plant ;
14.0 g/mol

ESaggts

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

ITaggts

Nitrogen (liquid)
via cryogenic air separation ;
production mix, at plant ;
14.0 g/mol

GBaggts

Nitrogen (liquid)
via cryogenic air separation ;
production mix, at plant ;
14.0 g/mol

FRaggts

Nitrogen (liquid)
via cryogenic air separation ;
production mix, at plant ;
14.0 g/mol

BEaggts

Nitrogen (liquid)
via cryogenic air separation ;
production mix, at plant ;
14.0 g/mol

NOaggts

Nitrogen (liquid)
via cryogenic air separation ;
production mix, at plant ;
14.0 g/mol

THaggts

Oxygen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.429 kg/m3, 16.0 g/mol

NOaggts

Oxygen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.429 kg/m3, 16.0 g/mol

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

ITaggts

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

FRaggts

Oxygen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.429 kg/m3, 16.0 g/mol

BEaggts

Oxygen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.429 kg/m3, 16.0 g/mol

CAaggts

Oxygen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.429 kg/m3, 16.0 g/mol

GBaggts

Oxygen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.429 kg/m3, 16.0 g/mol

JPaggts

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

ESaggts

Oxygen (liquid)
via cryogenic air separation ;
production mix, at plant ;
16.0 g/mol

NOaggts

Oxygen (liquid)
via cryogenic air separation ;
production mix, at plant ;
16.0 g/mol

GBaggts

Oxygen (liquid)
via cryogenic air separation ;
production mix, at plant ;
16.0 g/mol

BEaggts

Oxygen (liquid)
via cryogenic air separation ;
production mix, at plant ;
16.0 g/mol

FRaggts

Oxygen (liquid)
via cryogenic air separation ;
production mix, at plant ;
16.0 g/mol

ITaggts

Phosphoric acid (100%) (wet process)
wet process, from raw phosphate and sulphuric acid ;
production mix, at plant ;
100%

DEaggts

Phosphoric acid (75%)
wet process ;
production mix, at plant ;
75%

DEaggts

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

Sodium chloride (rock salt)
mining and processing ;
production mix, at plant ;
2.17 g/cm3, 58.44 g/mol

AUaggts

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%

ITaggts

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%

BEaggts

Sodium hydroxide (caustic soda) mix (100%)
technology mix ;
production mix, at plant ;
100%

GBaggts

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%

NOaggts

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%

ESaggts

Sodium hydroxide (caustic soda) mix (100%)
technology mix ;
production mix, at plant ;
100%

HUaggts

Sodium hydroxide (caustic soda) mix (100%)
technology mix ;
production mix, at plant ;
100%

FRaggts

Sodium hydroxide (caustic soda) mix (100%)
technology mix ;
production mix, at plant ;
100%

NLaggts

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%

BEaggts

Sodium hydroxide mix (50%)
technology mix ;
consumption mix, to consumer ;
50%

ESaggts

Sodium hydroxide mix (50%)
technology mix ;
consumption mix, to consumer ;
50%

FRaggts

Sulphur (elemental) at refinery
from crude oil ;
production mix, at refinery ;
elemental sulphur

GBaggts

Sulphur (elemental) at refinery
from crude oil ;
production mix, at refinery ;
elemental sulphur

NLaggts

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

GBaggts

Sulphuric acid (96%)
oxidation of sulphur ;
production mix, at plant ;
96% concentrated

BEaggts

Sulphuric acid (96%)
oxidation of sulphur ;
production mix, at plant ;
96% concentrated

FRaggts

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 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

ESaggts

Titanium dioxide pigment (chloride process)
chloride process, from rutile ;
single route, at plant ;
4.23 g/cm3, 79.87 g/mol

EU-28aggts

Titanium dioxide pigment (sulphate process)
sulphate process, from rutile ;
single route, at plant ;
4.23 g/cm3, 79.87 g/mol

EU-28aggts

Titanium dioxide pigment (sulphate process)
sulphate process, from rutile ;
single route, at plant ;
4.23 g/cm3, 79.87 g/mol

DEaggts