Irreversible reaction
4C5H9NO+27O2gives20CO2+18H2O+2N2
- Direction
- Irreversible
- Processes
- 1
- Stated as
- Fixed conversion
- Heat of reaction
- ΔH = -11,440,716 kJ/kmol (one process)
- 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 |
|---|---|---|---|---|
| C5H9NO | N-Methyl-2-pyrrolidone | 872-50-4 | reactant | -4 |
| O2 | Oxygen | 7782-44-7 | reactant | -27 |
| CO2 | Carbon dioxide | 124-38-9 | product | 20 |
| H2O | Water | 7732-18-5 | product | 18 |
| N2 | Nitrogen | 7727-37-9 | product | 2 |
In the processes
- Acetylene by partial oxidation of natural gas with NMP recovery (6.25 t/h, synthesis-gas co-product)Concept · not reviewed
FB_NMPC5H9NO + 27/4 O2 → 5 CO2 + 9/2 H2O + 1/2 N2- Scale
- Written at 0.25 times the scale
- Stated as
- Fixed conversion
- Element balance
- Balances in every element
- Conversion
- 99.95 % of
NMP(assumed: D-011, ASSUMED; fuel nitrogen to N2 (NOx not estimated)) - Heat of reaction
- ΔH = -2,860,179 kJ/kmol at 298.15 K, as written (calculated: ideal-gas formation enthalpies of materials.yaml (API TDB for NMP), 298.15 K)
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.
D-011, ASSUMED; fuel nitrogen to N2 (NOx not estimated)
For the conversion · cited by Acetylene by partial oxidation of natural gas with NMP recovery (6.25 t/h, synthesis-gas co-product)
ideal-gas formation enthalpies of materials.yaml (API TDB for NMP), 298.15 K
For the heat of reaction · cited by Acetylene by partial oxidation of natural gas with NMP recovery (6.25 t/h, synthesis-gas co-product)