Performance study of Ni, Co, and Mo catalysts supported on gamma-Al2O3 and HZSM5 in HDS reactions of mixed naphtha

نویسندگانمهدی کریمی بروجنی,عبداله ایران خواه
نشریهInternational Journal of Energy Research
شماره صفحات1
شماره مجلد45
ضریب تاثیر (IF)5.164
نوع مقالهFull Paper
تاریخ انتشار2021-08-30
رتبه نشریهعلمی - پژوهشی
نوع نشریهالکترونیکی
کشور محل چاپایران
نمایه نشریهJCR

چکیده مقاله

Ni/γ-Al2O3, Ni/HZSM5, Co/HZSM5, Mo/HZSM5, and NiMo/γ-Al2O3 catalysts were synthesized by the wetness impregnation technique. Field emission scanning electron microscopy, X-ray diffraction, and nitrogen physisorption methods were used for characterizing the prepared catalysts. The activity of the synthesized catalysts was studied by passing the mixed naphtha and H2 over a fixed bed reactor with sulfiding process prior to HDS reactions at ambient pressure, 285°C, LHSV of 5.8 h−1, and H2/HC volumetric ratio of 94. Ni, Co, and Mo with mass percent of 3.5 wt% were loaded on laboratory-synthesized γ-Al2O3 and purchased HZSM5 supports. For promoted NiMo/γ-Al2O3 catalyst, 3.5 wt% Ni and 17 wt% Mo were impregnated on laboratory synthesized γ-alumina support, similar to the commercial industrial catalyst. Ultimately, the HDS reactions over the synthesized NiMo/γ-Al2O3 decreased the total sulfur content of mixed naphtha from 430 to 25 ppm wt, as a synthesized catalyst with the best reactor performance and acceptable long-term stability.

tags: hydrodesulfurization mixed naphtha NiMo/γ-Al2O3 sulfiding total sulfur content