Hydrotreatment of SRC-II heavy distillate was investigated over presulfided CoMo/Al
2O
3 catalyst at 390°C, 10MPa both in H
2 flow and in 5%H
2S/H
2 flow. Elemental analysis, 1H-NMR, FT-IR and column chromatography were used for characterization of pro-duct oils. It was observed that hydrotreatment over presulfided catalyst decreased both nitrogen and sulfur contents. It was also found that gas phase addition of H
2S promoted HDN reaction and inhibited HDS reaction. In order to clarify the promoting effect of H
2S on HDN reaction, product oils were separated into base components by column chromatography and investigated in detail. Hydrotreatment in H
2S/H
2 flow removed 80% of base component of reactant. Compar-ing with the reaction in H
2 flow, removal of strong base was especially promoted in the presence of H
2S/H
2 and removal of very weak base was conversely inhibited. 1H-NMR results of strong base component showed that hydrogen aromaticity of feed markedly decreased in H
2 S/H
2 flow but no difference was observed between Ha in H
2 flow and that in H
2S/H
2 flow. Pro-moting effect of H
2S on HDN reaction was thus ascribed to a improvement of catalytic cracking ability for C-N bond.
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