CO hydrogenation over K-Co-MoSx catalyst to mixed alcohols: A kinetic analysis

Higher alcohol synthesis (HAS) from syngas is one of the most promising approaches to produce fuels and chemicals. Our recent investigation on HAS showed that potassium-promoted cobalt-molybdenum sulfide is an effective catalyst system. In this study, the intrinsic kinetics of the reaction were studied using this catalyst system under realistic conditions. The study revealed the major oxygenated products are linear alcohols up to butanol and methane is the main hydrocarbon. The higher alcohol products (C-3+) followed an Anderson-Schultz-Flory distribution while the catalyst suppressed methanol and ethanol formation. The optimum reaction conditions were estimated to be at temperature of 340 degrees C, pressure of 117 bar, gas hourly space velocity of 27 000 mL g(-1 )h(-1) and H-2/CO molar feed ratio of 1. A kinetic network has been considered and kinetic parameters were estimated by nonlinear regression of the experimental data. The results indicated an increasing apparent activation energy of alcohols with the length of alcohols except for ethanol. The lower apparent activation energy of alcohols compared with hydrocarbon evidenced the efficiency of this catalyst system to facilitate the formation of higher alcohols.

Automated summary

The study found that the major oxygenated products are linear alcohols up to butanol, while methane is the main hydrocarbon. The higher alcohol products followed an Anderson-Schultz-Flory distribution, with the catalyst suppressing methanol and ethanol formation. The optimal reaction conditions were estimated to be at a temperature of 340 degrees C, pressure of 117 bar, gas hourly space velocity of 27,000 mL g(-1)h(-1), and H-2/CO molar feed ratio of 1.