Effect of reaction conditions on methanol to gasoline conversion over nanocrystal ZSM-5 zeolite

被引:26
作者
Wan, Zhijian [1 ]
Li, Gang [1 ]
Wang, Chuanfu [1 ]
Yang, Hong [1 ]
Zhang, Dongke [1 ]
机构
[1] Univ Western Australia, Ctr Energy M473, 35 Stirling Highway, Crawley, WA 6009, Australia
基金
澳大利亚研究理事会;
关键词
Catalyst deactivation; Coke formation; Methanol to gasoline; Nanocrystal ZSM-5 zeolite; Reaction conditions; COKE FORMATION; CATALYTIC CONVERSION; TO-HYDROCARBONS; MFI ZEOLITES; PERFORMANCE; DEACTIVATION; H-ZSM-5; OLEFINS; RATIO; SIZE;
D O I
10.1016/j.cattod.2018.01.017
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
A nanocrystal ZSM-5 zeolite comprising uniform single crystal particles of similar to 100 nm in size was synthesised and characterised using XRD, ICP-AES, SEM, TEM, solid state MAS NMR and nitrogen physisorption techniques. The catalytic performance was tested in methanol to gasoline (MTG) conversion with a particular focus on the effect of reaction conditions, namely, temperature from 300 to 450 degrees C, pressure from 0.1 to 2.0 MPa and WHSV from 1 to 4h(-1). Temperature showed a significant impact. At temperatures <= 350 degrees C, methanol conversion did not complete while the catalyst was deactivated more rapidly. Increasing temperature to above 375 degrees C saw complete methanol conversion and durable catalyst activity. Further increasing the reaction temperature to above 400 degrees C reduced gasoline yield. Pressure mainly affected the product selectivity; a higher pressure led to a lower C-1-C-4 selectivity but enhanced durene formation. Further increasing pressure also favoured coke formation, leading to faster loss of catalyst activity. Likewise, increasing WHSV reduced C-1-C-4 selectivity but promoted the formation of durene and coke, resulting in a rapid deactivation of the catalyst. The optimal reaction conditions for this nanocrystal ZSM-5 catalyst in MTG were found to be 375 degrees C, 1.0 MPa and WHSV of 2h(-1).
引用
收藏
页码:107 / 113
页数:7
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