催化作用
选择性
芳构化
甲醇
沸石
ZSM-5型
粒径
结晶
初湿浸渍
布朗斯特德-洛瑞酸碱理论
Crystal(编程语言)
晶种
化学
路易斯酸
化学工程
锌
材料科学
无机化学
有机化学
单晶
程序设计语言
结晶学
物理化学
工程类
计算机科学
作者
Xianjun Niu,Yang Bai,Yi-En Du,Hongxue Qi,Yong‐Qiang Chen
摘要
ZSM-5 zeolites were hydrothermally synthesized with commercial silica sol, and the crystal size was controlled by adding silicalite-1 seed in the synthetic system. The crystal size of ZSM-5 was affected by the crystallization time of seed, seed content and seed size. ZSM-5 zeolites with controllable particle size in the range of 200–2200 nm could be obtained. The prepared samples with different particle sizes were used for the reaction of methanol conversion to aromatics (MTA). The results suggested that the HZSM-5 catalyst with small crystal size showed much longer catalyst lifetime and higher selectivity for C 5 + hydrocarbons and aromatics, especially C 9 + aromatics in the MTA reaction. Moreover, the introduction of zinc (Zn) into the HZSM-5 zeolites can considerably promote the selectivity to aromatics in the products. Zn modified HZSM-5 zeolites with different Zn loading amounts were prepared by the incipient wetness impregnation method, and the highest aromatics selectivity was obtained when the Zn loading was 1.0%. The improvement of methanol aromatization was ascribed to the synergistic effect of Brønsted acid sites and the newly formed Zn-Lewis acid sites.
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