Liu Li - Dalian Research Institute of Petroleum and Petrochemicals, SINOPEC, Dalian, China
Yang Min - Dalian Research Institute of Petroleum and Petrochemicals, SINOPEC, Dalian, China
Duan Weiyu - Dalian Research Institute of Petroleum and Petrochemicals, SINOPEC, Dalian, China
Sun Jin - Dalian Research Institute of Petroleum and Petrochemicals, SINOPEC, Dalian, China
Yao Yunhai - Dalian Research Institute of Petroleum and Petrochemicals, SINOPEC, Dalian, China
Li Shicai - Dalian Research Institute of Petroleum and Petrochemicals, SINOPEC, Dalian, China
Guo Rong - Dalian Research Institute of Petroleum and Petrochemicals, SINOPEC, Dalian, China

Series of Mo-Co type catalysts were supported on Al۲O۳, Al۲O۳-meso-ZSM-۵-Al۲O۳-typical-ZSM-۵ and tested in the hydrodesulfurization (HDS) of straight-run diesel feedstocks. The materials were characterized by N۲ physisorption, X-ray diffraction, scanning electron microscopy, NH۳ adsorption and temperature-programmed desorption, and Py-adsorbed IR spectra. The dynamics of the main steps in the HDS reaction were calculated, and seven lumped kinetic equations were established containing reaction pathways of hydrogenation (HYD), direct desulfurization (DDS) and alkyl transfer on the catalyst. The Levenberg-Marquardt (LM) algorithm method was used then to solve the resulting differential equations. The results showed that the HDS activity of C۱۲-ZSM۵ was highest because it had large VP and DP, and moderate acid content, which could improve the alkyl transfer activity and the macromolecular sulfide diffusion. By increasing the operating temperatures, the sulfur removal through the alkyl transfer route on C۱۲-ZSM۵ catalyst significantly increased, and the removal of sulfur content through alkyl transfer at ۴۰۰ °C and ۴.۰ MPa or ۶.۰ MPa was ۸۶ or ۸۸%, respectively. Furthermore, the increase of sulfur removal confirmed that the alkyl transfer route was dominant at a deep HDS level at a high operating temperature.

Mo-Co Type Catalyst, ZSM Zeolite, Hydrodesulfurization, Kinetics