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
Bb. Breman et Aa. Beenackers, 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, Industrial & engineering chemistry research, 35(10), 1996, pp. 3763-3775
Various thermodynamic models were tested concerning their applicabilit
y to predict gas-liquid solubilities, relevant for synthesis gas conve
rsion to methanol, higher alcohols, and hydrocarbons via gas-slurry pr
ocesses. Without any parameter optimization the group contribution equ
ation of state (GCEOS) turns out to be the best model with an average,
relative deviation of 19.0%. Ifa single binary interaction parameter
is optimized for each binary system, the Peng-Robinson equation of sta
te, the regular solutions theory, and the Flory-Staverman model all gi
ve good predictions with average, relative deviations of 4.0, 10.4, an
d 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 (a
verage relative deviations < 2% for all models). The gas-liquid solubi
lities could also be correlated accurately to the temperature (average
relative deviation = 2.1%) by assuming a constant enthalpy of solutio
n (CEOS) model. For particular binary systems the Flory-Staverman mode
l and the CEOS model give also reasonably accurate predictions of the
gas-liquid solubilities by calculating the binary interaction paramete
rs from pure component properties. Such an approach is promising for p
redicting as yet unknown gas-liquid solubilities without the need for
experimental data.