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

DEaggSphera

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

DEaggSphera

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-28aggSphera

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-aggSphera

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

GBaggSphera

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

FRaggSphera

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

ITaggSphera

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

GBaggSphera

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

NOaggSphera

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

DEaggSphera

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

EU-28aggSphera

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

DEaggSphera

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

DEaggSphera

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

BEaggSphera

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

FRaggSphera

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

FRaggSphera

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

ITaggSphera

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

GBaggSphera

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

FRaggSphera

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

GBaggSphera

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

FRaggSphera

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

ITaggSphera

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

BRaggSphera

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

BEaggSphera

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

ESaggSphera

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

NLaggSphera

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

NOaggSphera

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

FRaggSphera

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

BEaggSphera

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

GBaggSphera

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

ITaggSphera

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

GBaggSphera

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

NOaggSphera

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

ITaggSphera

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

EU-28aggSphera

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

FRaggSphera

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

GBaggSphera

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

GBaggSphera

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

ITaggSphera

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

EU-28aggSphera

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

FRaggSphera

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

FRaggSphera

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

GBaggSphera

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

BEaggSphera

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

ITaggSphera

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

NOaggSphera

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

GBaggSphera

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

NLaggSphera

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

FRaggSphera

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

GBaggSphera

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

CZaggSphera

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

HUaggSphera

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

ATaggSphera

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

ESaggSphera

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

THaggSphera

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

ROaggSphera

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

NOaggSphera

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

PLaggSphera

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

ITaggSphera

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

AUaggSphera

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

FRaggSphera

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

SEaggSphera

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

CHaggSphera

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

BEaggSphera

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

THaggSphera

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

BEaggSphera

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

FRaggSphera

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

ITaggSphera

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

GBaggSphera

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

AUaggSphera

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

ESaggSphera

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

NOaggSphera

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

ESaggSphera

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

BEaggSphera

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

ITaggSphera

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

AUaggSphera

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

GBaggSphera

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

TWaggSphera

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

FRaggSphera

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

JPaggSphera

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

NOaggSphera

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

CAaggSphera

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

ITaggSphera

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

SEaggSphera

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

ESaggSphera

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

GBaggSphera

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

BEaggSphera

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

FRaggSphera

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

NOaggSphera

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

DEaggSphera

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

DEaggSphera

Soda (Na2CO3)
Solvay process, from calcium carbonate and sodium chloride ;
production mix, at plant ;
2.53 g/cm3, 105.99 g/mol

JPaggSphera

Soda (Na2CO3)
Solvay process, from calcium carbonate and sodium chloride ;
production mix, at plant ;
2.53 g/cm3, 105.99 g/mol

AUaggSphera

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

AUaggSphera

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

ROaggSphera

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

JPaggSphera

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

PTaggSphera

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

BEaggSphera

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

NLaggSphera

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

CZaggSphera

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

NOaggSphera

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

HUaggSphera

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

ESaggSphera

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

FRaggSphera

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

SEaggSphera

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

PLaggSphera

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

ITaggSphera

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

GBaggSphera

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

ITaggSphera

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

ESaggSphera

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

BEaggSphera

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

JPaggSphera

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

FRaggSphera

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

GBaggSphera

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

NLaggSphera

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

GBaggSphera

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

JPaggSphera

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

ESaggSphera

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

FRaggSphera

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

BEaggSphera

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

AUaggSphera

Sulphuric acid mix (96%)
technology mix ;
consumption mix, to consumer ;
96% aqueous solution, M= 98.079 g/mol

FRaggSphera

Sulphuric acid mix (96%)
technology mix ;
consumption mix, to consumer ;
96% aqueous solution, M= 98.079 g/mol

ESaggSphera

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

EU-28aggSphera

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

DEaggSphera

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

EU-28aggSphera