Analyze standard and process reaction heat with clarity. Enter species data, temperatures, conversion, and losses. Generate results, downloads, visuals, and explanations for confident decisions.
Enter each species on a new line in this format: coefficient, name, ΔHf (kJ/mol), Cp (J/mol·K).
This example uses methane combustion. You can load it directly with the example button, then adjust temperatures, conversion, or loss factors.
| Side | Coefficient | Species | ΔHf (kJ/mol) | Cp (J/mol·K) |
|---|---|---|---|---|
| Reactant | 1 | CH4 | -74.85 | 35.69 |
| Reactant | 2 | O2 | 0.00 | 29.36 |
| Product | 1 | CO2 | -393.51 | 37.11 |
| Product | 2 | H2O(g) | -241.82 | 33.58 |
Standard reaction heat: ΔH°rxn = Σ(νproducts × ΔHf°) − Σ(νreactants × ΔHf°)
Net heat capacity change: ΔCp = Σ(νproducts × Cp) − Σ(νreactants × Cp)
Temperature correction: ΔHT corr = ΔCp × (Tprocess − Tref) ÷ 1000
Process reaction heat: ΔHprocess = ΔH°rxn + ΔHT corr
Reacted extent: nreacted = reaction basis × conversion ÷ 100
Total heat: Qgross = ΔHprocess × nreacted
Net heat after losses: Qnet = Qgross × (1 − loss fraction)
This formulation is useful for quick engineering estimates, teaching examples, and screening calculations. For high-temperature design work, temperature-dependent Cp correlations are better.
It is the enthalpy change for the stoichiometric reaction basis you define. Negative values indicate heat release, while positive values indicate heat input is needed.
The calculator applies Hess’s law. It combines stoichiometric coefficients with standard enthalpies of formation to determine the standard reaction enthalpy from products minus reactants.
Use it when the process temperature differs from the reference temperature and you have reasonable Cp values. It adjusts the reaction heat using a constant heat-capacity approximation.
Conversion scales the reacted extent. If conversion is 80 percent, only 80 percent of the chosen reaction basis contributes to the total heat calculation.
The loss factor reduces the gross heat magnitude by the chosen percentage. It gives a simple estimate of usable released heat or retained required heat after losses.
Yes, as long as your ΔHf and Cp data are consistent with the specified phase. Include the phase in the species name so your records remain clear.
It is best for screening, education, and preliminary engineering checks. Detailed design should use temperature-dependent properties, equilibrium effects, and possibly pressure corrections.
Use one species per line in this order: coefficient, name, ΔHf, Cp. For example: 1,CH4,-74.85,35.69
Important Note: All the Calculators listed in this site are for educational purpose only and we do not guarentee the accuracy of results. Please do consult with other sources as well.