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;
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 g·mol−1

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: 132,14 g·mol−1

DEaggts

Calcium hypochlorite
from sodium chloride production;
production mix, at plant;
solid, density: 2,35 g·cm−3, molar mass: 142,98 g·mol−1

DEaggts

Carbon monoxide (via synthetic gas)
cryogenic separation;
production mix, at plant;
density: 1,25 kg·m−3 (0 °C, 1013 mbar), molar mass: 28,01 g·mol−1

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: 2 g.cm-3, boiling point: −252 °C

GBaggts

Hydrogen (cracker)
steam cracker, from naphtha;
production mix, at plant;
gaseous, density: 0,0899 kg · m−3, molar mass: 2 g.cm-3, boiling point: −252 °C

ITaggts

Hydrogen (cracker)
steam cracker, from natural gas;
production mix, at plant;
gaseous, density: 0,0899 kg · m−3, molar mass: 2 g.cm-3, boiling point: −252 °C

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

ESaggts

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

GBaggts

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

ITaggts

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

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

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

ITaggts

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

GBaggts

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

CAaggts

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

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%

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%

NOaggts

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%

FRaggts

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

NLaggts

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

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

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