Irreversible reaction
C3H8+3H2Ogives3CO+7H2
- 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
| Species | Name | CAS | Role | Coefficient |
|---|---|---|---|---|
| C3H8 | Propane | 74-98-6 | reactant | -1 |
| H2O | Water | 7732-18-5 | reactant | -3 |
| CO | Carbon monoxide | 630-08-0 | product | 3 |
| H2 | Hydrogen | 1333-74-0 | product | 7 |
Also stated as C3H8 + 3 H2O ⇌ 3 CO + 7 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
C3H8_REFC3H8 + 3 H2O → 3 CO + 7 H2- Stated as
- Fixed conversion
- Element balance
- Balances in every element
- Conversion
- 100 % of
C3H8(given: EP 1586535 A2, para. [0003], as C2H6_REF (D-034)) - Catalyst
- nickel reforming 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.
EP 1586535 A2, para. [0003], as C2H6_REF (D-034)
For the conversion · cited by Ammonia from natural gas (1500 t/d, steam reforming with air-fed secondary reformer, Haber-Bosch loop)