Methanol Usage in Toluene Methylation over Pt Modified ZSM-5 Catalyst: Effects of Total Pressure and Carrier Gas

被引:23
|
作者
Wang, Yiren [1 ]
Liu, Min [1 ]
Zhang, Anfeng [1 ]
Zuo, Yi [1 ]
Ding, Fanshu [1 ]
Chang, Yang [1 ]
Song, Chunshan [1 ,2 ,3 ]
Guo, Xinwen [1 ]
机构
[1] Dalian Univ Technol, PSU DUT Joint Ctr Energy Res, Sch Chem Engn, State Key Lab Fine Chem, Dalian 116024, Peoples R China
[2] Penn State Univ, PSU DUT Joint Ctr Energy Res, EMS Energy Inst, Dept Energy & Mineral Engn, University Pk, PA 16802 USA
[3] Penn State Univ, Dept Chem Engn, University Pk, PA 16802 USA
关键词
SHAPE-SELECTIVITY; ALKYLATION REACTION; ACTIVE-SITES; HZSM-5; ZEOLITES; CONVERSION; DEACTIVATION; BENZENE; XYLENE; TRANSALKYLATION;
D O I
10.1021/acs.iecr.7b00318
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The present study investigates the effects of total pressure and carrier gas on toluene methylation using two modified ZSM-5 based catalysts impregnated with or without platinum. Toluene alkylation with methanol was carried out not only at different reaction pressure under nitrogen or hydrogen but also at different total pressure while the partial pressure of reactants remained constant. The amount of coke formed on the catalysts was less under hydrogen atmosphere. However, the hydrogenation reaction catalyzed by Pt modified catalyst promoted methanol conversion to undesired methane and light hydrocarbons, which in turn decreased the toluene conversion. For both carrier gases, it was found that methanol usage toward undesired by products increased with total pressure. Such a trend suggests that a higher total pressure results in a lower toluene and methanol adsorption complexes formation rate in the ZSM-5 pores, and therefore the toluene hydrogenation reaction and the higher total pressure simultaneously increased the selectivity of methanol converted to light hydrocarbons and methane, which led to the deteriorated catalytic performance of Pt modified catalysts at elevated reaction pressure. conversion decreased. The
引用
收藏
页码:4709 / 4717
页数:9
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