The thermodynamic of isobutane dehydrogenation reaction was deeply investigated using most reliable literature data. Conversion and reaction mixture distribution at equilibrium was computed for various process conditions.
Reaction enthalpy, ∆_R H_T^o , ranges between 122±1.1 and 123±1.2 kJ.mol-1 over the temperature (773.15 to 923.15) K where the equilibrium constant K_T value varies between 0.12±0.03 and 2.6±0.7. The reaction becomes thermodynamically favorable at temperatures higher than 873.15 K.
Primary Language | English |
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Journal Section | Regular Original Research Article |
Authors | |
Publication Date | January 18, 2015 |
Published in Issue | Year 2015 |