Technol. problems of natural gas desulfurization in syngases manufg. plants have been discussed and the results of investigations on the activity of the model Ni-Mo/Al2O3 catalyst in hydrogenation of selected sulfur compds. have been presented. The HDS reaction rate is dependent on a compd. structure. The hydrogenation rate on the Ni-Mo/Al2O3 catalyst for the given sulfur compd. increases in the order: CS2>(CH3)2S>C4H10S>C2H6S2>C4H4S. [on SciFinder(R)]
CITATION STYLE
Antoniak, K., Kowalik, P., Narowski, R., Konkol, M., & Ryczkowski, J. (2011). Investigations on hydrogenation of selected organic sulfur compounds on the Ni-Mo/Al2O3 catalyst in terms of natural gas desulfurization. Annales UMCS, Chemistry, 66(1). https://doi.org/10.2478/v10063-011-0011-0
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