substance
Oxygen
- Formula
- O2
- CAS
- 7782-44-7
- InChIKey
- MYMOFIZGZYHOMD-UHFFFAOYSA-N
- ChEBI
- CHEBI:15379
Made by
- Cryogenic air separation unit (500 t/d GOX)Co-product, Main productScreening · level Balanced · not reviewed
Used by
- Acetaldehyde by the one-stage Wacker oxidation of ethylene (100 kt/a)FeedstockConcept · not reviewed
- Acetylene by partial oxidation of natural gas with NMP recovery (6.25 t/h, synthesis-gas co-product)FeedstockConcept · not reviewed
- Ethylene glycol by ethylene oxide hydration (glycols-only EO/EG plant, 1200 t/d MEG)FeedstockConcept · not reviewed
- Hydroxylammonium sulfate by catalytic NO hydrogenation (30 kt/a NH2OH, 25 wt% solution)FeedstockConcept · not reviewed
- Bleached softwood kraft pulp with chemical recovery (1000 ADt/d market pulp, concept)FeedstockConcept · not reviewed
- Phosphorus oxychloride from white phosphorus, chlorine and oxygen via PCl3 (4.0 t/h)FeedstockConcept · not reviewed
Emitted by
- Hydrazine hydrate by the peroxide process (PCUK, methyl ethyl ketazine route, 16 kt/a)EmissionConcept · not reviewed
- Thionyl chloride from sulfur, chlorine and SO2 over activated carbon (3.75 t/h)EmissionConcept · not reviewed
Takes part in
- 2C2H2+5O2gives4CO2+2H2OReactant · one process
- 2C2H4+2HCl+3O2gives2CH3Cl+2CO2+2H2OReactant · one process
- 2C2H4+O2gives2C2H4OReactant · Partial oxidation of ethylene to ethylene oxide (silver catalyst) · one process
- 2C2H4+O2gives2C2H4OReactant · Ethylene + Oxygen → Acetaldehyde · one process
- 2C2H6+7O2gives4CO2+6H2OReactant · Combustion of ethane · 4 processes
- 2C4H2+9O2gives8CO2+2H2OReactant · one process
- 2C6H6+15O2gives12CO2+6H2OReactant · one process
- 2C9H12+O2gives2C9H12OReactant · one process
- 2CH2O+O2gives2CO+2H2OReactant · one process
- 2CH4+2NH3+3O2gives2CHN+6H2OReactant · one process
- 2CH4+O2gives2CO+4H2Reactant · one process
- 2CH4O+3O2gives2CO2+4H2OReactant · 2 processes
- 2CH4O+O2gives2CH2O+2H2OReactant · one process
- 2CO+O2gives2CO2Reactant · CO burn-off at the charge surface and in the hood · 8 processes
- 2Na2S+2CO2+3O2gives2Na2CO3+2SO2Reactant · Sulfur release as SO2 to the flue gas · one process
- 2H2+O2in equilibrium with2H2OReactant · Combustion of the oxygen in the chlorine feed with excess hydrogen · one process
- 2H2+O2gives2H2OReactant · 6 processes
- 4NO+3O2+2H2Ogives4HNO3Reactant · 2 processes
- 4NO2+O2+2H2Ogives4HNO3Reactant · one process
- 2H2Ogives2H2+O2Product · Anodic oxygen from back-migrated hydroxide (net water electrolysis) · 2 processes
- 2H2O2gives2H2O+O2Product · Peroxide decomposition · 2 processes
- 2LIG+2NaOH+O2gives2NaOXL+2H2OReactant · Oxidative lignin dissolution in the O2 stage · one process
- 2N2Ogives2N2+O2Product · one process
- 2NaEXT+53O2givesNa2CO3+39CO2+29H2OReactant · Combustion of resin soap · one process
- 2NaISA+12O2givesNa2CO3+11CO2+11H2OReactant · Combustion of sodium isosaccharinate · one process
- 2NaLIG+23O2givesNa2CO3+19CO2+11H2OReactant · Combustion of sodium lignate · one process
- 2NaOXL+22O2givesNa2CO3+19CO2+11H2OReactant · Combustion of oxidised sodium lignate · one process
- 2NH3+2O2givesN2O+3H2OReactant · Ammonia oxidation to nitrous oxide (side reaction) · 3 processes
- 2NO+O2in equilibrium with2NO2Reactant · Oxidation of nitric oxide (oxidation volume and tower gas spaces) · 2 processes
- 2SO2+O2in equilibrium with2SO3Reactant · one process
- 4C5H9NO+27O2gives20CO2+18H2O+2N2Reactant · one process
- 4CHN+5O2gives4CO2+2H2O+2N2Reactant · one process
- 2MnO2+4KOH+O2gives2K2MnO4+2H2OReactant · Oxidation of MnO2 to potassium manganate in KOH with air (roaster) · one process
- 4KMnO4+4KOHgives4K2MnO4+O2+2H2OProduct · Reversion of recycled permanganate to manganate in the hot KOH melt · one process
- 4NH3+3O2gives2N2+6H2OReactant · Ammonia oxidation to nitrogen (side reaction) · 4 processes
- 4NO+4NH3+O2gives4N2+6H2OReactant · one process
- 4NH3+5O2gives4NO+6H2OReactant · Ammonia oxidation to nitric oxide · 3 processes
- C+O2givesCO2Reactant · Coke combustion (lime kiln) · one process
- C2H2O+2O2gives2CO2+H2OReactant · one process
- C2H4+3O2gives2CO2+2H2OReactant · Total combustion of ethylene (side reaction, R-101) · 4 processes
- C2H4+HCl+O2givesC2H3ClO+H2OReactant · one process
- C2H4+O2givesC2H4O2Reactant · one process
- C2H4O2+2O2gives2CO2+2H2OReactant · one process
- C2H6O+3O2gives2CO2+3H2OReactant · one process
- C3H8+5O2gives3CO2+4H2OReactant · Combustion of propane · 3 processes
- C9H12+O2givesC8H8O+CH4OReactant · one process
- C9H12+O2givesC9H12O2Reactant · one process
- CH2O+O2givesCO2+H2OReactant · one process
- CH4+2O2givesCO2+2H2OReactant · Natural gas combustion (calciner) · 10 processes
- EAHQ+O2givesC16H12O2+H2O2Reactant · one process
- N2+2O2gives2NO2Reactant · NOx formation (fuel and thermal, as NO2) · one process
- Na2S+2O2givesNa2SO4Reactant · Oxidation of the sulfide of the white liquor alkali to sulfate · one process
- Na2SO4givesNa2S+2O2Product · Sulfate reduction in the char bed (formal net reaction; the reductant is the char carbon of the combustion reactions) · one process
- 2PCl3+O2gives2POCl3Reactant · Oxidation of PCl3 by the oxygen of the chlorine feed · one process
- 2SiO+O2gives2SiO2Reactant · Oxidation of SiO to silica fume · one process
- S+O2givesSO2Reactant · Oxidation of the coke sulfur to SO2 · 2 processes
Routes compared
All 2 ways to make Oxygen, with filters →
Per 1 t of Oxygen: inventory from each route's LCI dataset, unallocated; footprints per the functional unit of their own LCA.
| Route | Tier, design maturity, review status | Geography, year | Energy | Feedstocks | Key emissions | Footprint | Comparability |
|---|---|---|---|---|---|---|---|
| Cryogenic air separation unit (500 t/d GOX)cryogenic double-column air separation, 500 t/d GOX, pumped liquid products, TSA front endoxygen/gox-30barg-99.5 | flowsheet or hand-writtenDesign maturity: Screening (research)Not independently reviewedDataset review: not stated | generic, 2026 |
|
| none | 66.7 kg CO2-eq33.1 to 133 (95 %)Climate change per 1 t oxygen, gaseous, >= 99.5 mol%, 30 barg |
|
| Cryogenic air separation unit (500 t/d GOX)cryogenic double-column air separation, 500 t/d GOX, pumped liquid products, TSA front endoxygen/lox | flowsheet or hand-writtenDesign maturity: Screening (research)Not independently reviewedDataset review: not stated | generic, 2026 | a co-product of a multi-output dataset (product:GOXP, product:GANP, product:LIN besides it): its share needs the allocation of the LCI database build | no footprint |
| ||
Footprint data: UK Government GHG Conversion Factors for Company Reporting 2026 (flat file) (OGL-3.0); Greenhouse gas emission intensity of electricity generation in Europe (indicator ENER038) (CC BY (version not stated) under the EEA legal notice (https://www.eea.europa.eu/en/legal-notice): re-use, including commercial, with the EEA acknowledged in each copy and the meaning not distorted). Contains public sector information licensed under the Open Government Licence v3.0 (UK Government GHG Conversion Factors for Company Reporting 2026, DESNZ). Source: European Environment Agency (EEA), indicator ENER038 'Greenhouse gas emission intensity of electricity generation in Europe' (2026), https://www.eea.europa.eu/en/analysis/indicators/greenhouse-gas-emission-intensity-of-1, CC BY; values converted from g to kg CO2e per kWh.
How comparability is checked
- Allocation
- same (same allocation method: exergy)
- Background data (impacts)
- not applicable (same background data and boundary behind the impact numbers (only routes with a footprint))
- System boundary
- same (same system boundary of the inventory (the dataset's boundary): gate-to-gate foreground of the plant with its construction)
- Data quality (TfS DQR)
- same (data quality: every route states a TfS DQR, none more than 1 above the best)
- Functional unit
- differs (same functional unit (amount and unit of the reference product): 1 kg, 1 t)
- Reference product (grade, state)
- differs (same reference product: registry grade and state: oxygen/gox-30barg-99.5 (basis mole, component O2, phase gas, pressure 31.0, purity 0.997115, temperature 40.0), oxygen/lox (basis mole, component O2, phase liquid, pressure 1.3, purity 0.998093, temperature -183.0))
- System model
- same (same system model (docs/system-model.md): cutoff)
Market activity in the LCI database: market:oxygen/lox:RER (production-mix, RER), market:oxygen/gox-30barg-99.5:RER (production-mix, RER). Link a consumer of Oxygen to the market rather than to one route.
ISO 14044 requires a critical review (by a panel of interested parties, ISO/TS 14071) of a comparative assertion intended to be disclosed to the public. These routes are listed side by side for screening; a statement that one is better than another needs that review. None of these routes has had such a review.