Irreversible reaction
CO+3H2givesCH4+H2O
- Direction
- Irreversible
- Processes
- 1
- Stated as
- Fixed conversion
- Element balance
- Checked: balances
Species
| Species | Name | CAS | Role | Coefficient |
|---|---|---|---|---|
| CO | Carbon monoxide | 630-08-0 | reactant | -1 |
| H2 | Hydrogen | 1333-74-0 | reactant | -3 |
| CH4 | Methane | 74-82-8 | product | 1 |
| H2O | Water | 7732-18-5 | product | 1 |
Also stated as each of CH4 + H2O ⇌ CO + 3 H2, CH4 + H2O → CO + 3 H2 (reversible and irreversible statements are kept apart).
In the processes
- Ammonia from natural gas (1500 t/d, steam reforming with air-fed secondary reformer, Haber-Bosch loop)Concept · not reviewed
METH_COCO + 3 H2 → CH4 + H2O- Stated as
- Fixed conversion
- Element balance
- Balances in every element
- Conversion
- 100 % of
CO(given: European Commission (2007), BREF Large Volume Inorganic Chemicals - Ammonia, Acids and Fertilisers, section 2.2.3.6, p. 42: residual carbon oxides after the methanator usually below 10 ppmv, below the balance tolerance (D-010, D-034)) - Catalyst
- nickel methanation catalyst
Sources
What the processes cite for this reaction, each source once: for the reaction itself, its conversion, its heat of reaction or its catalyst. As the processes write them; DOIs, US patent numbers and web addresses are linked.
European Commission (2007), BREF Large Volume Inorganic Chemicals - Ammonia, Acids and Fertilisers, section 2.2.3.6, p. 42: residual carbon oxides after the methanator usually below 10 ppmv, below the balance tolerance (D-010, D-034)
For the conversion · cited by Ammonia from natural gas (1500 t/d, steam reforming with air-fed secondary reformer, Haber-Bosch loop)
Starter template
cheme chemistry library fischer_tropsch --addcheme chemistry library methanation --addcheme chemistry library steam_reforming --addTemplates bring the stoichiometry, the components and typical catalysts; most give no conversion or kinetics, and their sources are general references, not this reaction's processes.