Irreversible reaction

CO+3H2givesCH4+H2O

Direction
Irreversible
Processes
1
Stated as
Fixed conversion
Element balance
Checked: balances
As the processes state itStoichiometry, conversions, heats of reaction and catalyst windows are taken from each process's files with their provenance. The build checks only that each process's equation balances in every element, from the process's own component formulas; it does not check the numbers. A process's design maturity applies to them.

Species

SpeciesNameCASRoleCoefficient
COCarbon monoxide630-08-0reactant-1
H2Hydrogen1333-74-0reactant-3
CH4Methane74-82-8product1
H2OWater7732-18-5product1

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

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.

  1. 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

A starting template is in the ChemE-as-Code toolkit (Fischer-Tropsch synthesis (lumped, n-octane as the product)): cheme chemistry library fischer_tropsch --add
A starting template is in the ChemE-as-Code toolkit (Methanation (syngas purification, substitute natural gas)): cheme chemistry library methanation --add
A starting template is in the ChemE-as-Code toolkit (Steam methane reforming): cheme chemistry library steam_reforming --add

Templates 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.