Thermodynamic models to predict gas-liquid solubilities in the methanol synthesis, the methanol-higher alcohol synthesis, and the Fischer-Tropsch synthesis via gas-slurry processes
- Univ. of Groningen (Netherlands). Dept. of Chemical Engineering
Various thermodynamic models were tested concerning their applicability to predict gas-liquid solubilities, relevant for synthesis gas conversion to methanol, higher alcohols, and hydrocarbons via gas-slurry processes. Without any parameter optimization the group contribution equation of state (GCEOS) turns out to be the best model with an average, relative deviation of 19.0%. If a single binary interaction parameter is optimized for each binary system, the Peng-Robinson equation of state, the regular solutions theory, and the Flory-Staverman model all give good predictions with average, relative deviations 4.0, 10.4, and 10.0%, respectively. As expected, the predictions from these models improve further and agree excellently with the experimental values by optimizing two binary interaction parameters for each binary system (average relative deviations <2% for all models). The gas-liquid solubilities could also be correlated accurately to the temperature (average relative deviation = 2.1%) by assuming a constant enthalpy of solution (CEOS) models. For particular binary systems the Flory-Staverman model and the CEOS model give also reasonably accurate predictions of the gas-liquid solubilities by calculating the binary interaction parameters from pure component properties. Such an approach is promising for predicting as yet unknown gas-liquid solubilities without the need for experimental data.
- OSTI ID:
- 413453
- Journal Information:
- Industrial and Engineering Chemistry Research, Vol. 35, Issue 10; Other Information: PBD: Oct 1996
- Country of Publication:
- United States
- Language:
- English
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