Tetralin hydrocracking over a commercial catalyst NiMo/HY was carried out to study temperature effect on product distribution in a laboratory-scale fixed-bed reactor. Based on the experimental results
a reaction network for tetralin hydrocracking was proposed
which contained 12 reactions with different types such as hydrogenation
isomerization
dehydrogenation
ring opening and dealkylation. Thermodynamic equilibrium calculations provided equilibrium constants for all reactions in the network
equilibrium yields of different products as well as yield variations with temperature
pressure and molar ratio of H2 to tetralin. Thermodynamic calculation of product yield changes with operating conditions was generally in agreement with those of experiments
demonstrating that the reaction network depicted well for tetralin hydrocracking over NiMo/HY catalyst system.
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Related Author
Xingchuan YANG
Genlei WEI
Li XU
Guoji LIU
LIU Qihong
CHEN Fengyang
LYU Qinghui
LI Jiafeng
Related Institution
School of Chemical Engineering, Zhengzhou University
State Key Laboratory of Complex Nonferrous Metal Resources Clean Utilization, School of Metallurgical and Energy Engineering, Kunming University of Science and Technology
State Key Laboratory of Advanced Metallurgy for Non-ferrous Metals, Kunming Metallurgical Research Institute Co., Ltd.
School of Energy and Power Engineering, Lanzhou University of Technology
School of Aerospace Engineering, Guizhou University of Science and Technology