Influence of Preparation Method on the Catalytic Activity over AlCl3 Supported Catalyst for Alkylation Reaction of Thiophene and Olefins in Coking Benzene

被引:2
作者
Ma, Lin
Liao, Junjie
Wang, Wenbo
Chang, Jinyu
Fan, Lijun
Chang, Liping
Bao, Weiren [1 ]
机构
[1] Taiyuan Univ Technol, State Key Lab Breeding Base Coal Sci & Technol, Taiyuan 030024, Peoples R China
基金
中国国家自然科学基金;
关键词
Closely Pressurized Loading; AlCl3 Supported Catalyst; Thiophene; Alkylation Reaction; Benzene;
D O I
10.1252/jcej.13we177
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
AlCl3/gamma-Al2O3 and AlCl3/silica gel catalysts were respectively prepared by closely pressurized and atmospheric loading methods, and then used as the catalysts for the alkylation reaction between thiophene and 1-hexene in benzene. The influences of the preparation conditions of AlCl3 supported catalysts on the catalytic activity in the alkylation reaction were investigated. The results show that the catalysts prepared by the closely pressurized loading method present a higher catalytic activity than those by the atmospheric loading method. The ion chromatography, nitrogen adsorption, scanning electron microscope and X-ray diffraction techniques were used to characterize the composition and structure properties of catalysts. Compared with the atmospheric loading method, the closely pressurized loading method could effectively promote the active component amounts and its combined forms on the catalyst surface, and improve the pore structure of the support during the preparing processes. Among all catalysts, Si2H prepared with 2 g of AlCl3 loaded on 10 g of silica gel by the closely pressurized loading method has the best catalytic activity, which should be attributed to the appropriate loading amount and combined forms of AlCl3 in this catalyst, as well as the more suitable pore structure. The thiophene conversion rate of the Si2H catalyst can reach up to about 80% in the model coking benzene system and remains stable in five cycle experiments, where the thiophene concentration is 700 mg/L and the molar ratio of 1-hexene to thiophene is 6:1.
引用
收藏
页码:261 / 266
页数:6
相关论文
共 11 条
[1]   Preparation of supported H3PW12O40•6H2O for thiophenic compounds alkylation in FCC gasoline [J].
Arias, Maria ;
Laurenti, Dorothee ;
Belliere, Virginie ;
Geantet, Christophe ;
Vrinat, Michel ;
Yoshimura, Yuji .
APPLIED CATALYSIS A-GENERAL, 2008, 348 (01) :142-147
[2]   PREPARATION AND CATALYTIC ACTIVITY OF A NEW SOLID ACID CATALYST [J].
DRAGO, RS ;
GETTY, EE .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1988, 110 (10) :3311-3312
[3]  
Jaimes L, 2008, INT J CHEM REACT ENG, V6
[4]  
[柯明 KE Ming], 2006, [化工进展, Chemical Industry and Engineering Progress], V25, P357
[5]   Preparation of AlCl3/silica gel catalyst for simultaneously removing thiophene and olefins from coking benzene by inclosed grafting method [J].
Liao, Junjie ;
Bao, Lei ;
Wang, Wenbo ;
Xie, Yuanyuan ;
Chang, Jinyu ;
Bao, Weiren ;
Chang, Liping .
FUEL PROCESSING TECHNOLOGY, 2014, 117 :38-43
[6]  
[刘磊 Liu Lei], 2007, [石油炼制与化工, Petroleum Processing and Petrochemicals], V38, P30
[7]  
Wang W. B., 2012, CHINESE J CATAL, V33, P181
[8]   A solid acid catalyst at the threshold of superacid strength: NMR, calorimetry, and density functional theory studies of silica-supported aluminum chloride [J].
Xu, T ;
Kob, N ;
Drago, RS ;
Nicholas, JB ;
Haw, JF .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1997, 119 (50) :12231-12239
[9]  
[徐新 XU Xin], 2006, [过程工程学报, The chinese journal of process engineering], V6, P181
[10]   Modification of HP zeolite by fluorine and its influence on olefin alkylation thiophenic sulfur in gasoline [J].
Zhang, Zekai ;
Liu, Shenglin ;
Zhu, Xiangxue ;
Wang, Qingxia ;
Xu, Longya .
FUEL PROCESSING TECHNOLOGY, 2008, 89 (01) :103-110