Acidity effects of Hβ zeolite on olefin alkylation of thiophenic sulfur in gasoline

Olefin alkylation of thiophenic sulfur process was carried out in model gasoline, using Hβ zeolites with different Si/Al2 ratios as catalysts. In particular, the influence of acid properties of Hβ zeolites on its catalytic ability for the thiophene alkylation, xylene alkylation and hexene oligomeriz...

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Published inJournal of natural gas chemistry Vol. 17; no. 1; pp. 45 - 50
Main Authors Zhang, Zekai, Liu, Dong, Zhu, Xiangxue, Yu, Haiwei, Liu, Shenglin, Xu, Longya
Format Journal Article
LanguageEnglish
Published Chengdu Elsevier B.V 01.03.2008
Dalian Institute of Chemical Physics
The Graduate University of Chinese Academy of Science,Beijing 100049,China%Dalian Petrochemical Corporations,CNPC,Dalian 116032,Liaoning,China%State Key Laboratory of Catalysis,Dalian Institute of Chemical Physics,Chinese Academy of Sciences,Dalian 116023,Liaoning,China%State Key Laboratory of Catalysis,Dalian Institute of Chemical Physics,Chinese Academy of Sciences,Dalian 116023,Liaoning,China
Dalian Petrochemical Corporations,CNPC,Dalian 116032,Liaoning,China
State Key Laboratory of Catalysis,Dalian Institute of Chemical Physics,Chinese Academy of Sciences,Dalian 116023,Liaoning,China
The Graduate University of Chinese Academy of Science,Beijing 100049, China
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Summary:Olefin alkylation of thiophenic sulfur process was carried out in model gasoline, using Hβ zeolites with different Si/Al2 ratios as catalysts. In particular, the influence of acid properties of Hβ zeolites on its catalytic ability for the thiophene alkylation, xylene alkylation and hexene oligomerization was investigated. The results showed that the acidity of the Hβ zeolite was increased with the decrease of Si/Al2 ratio, but its catalytic ability was not always increased. In fact, it reached the maximal catalytic ability at Si/Al2 ratio of 66, and under the reaction conditions of 60 ℃, 1.5 MPa, WHSV 3.0 h^-1 and time on stream 2 h. At the ratio, the conversion of thiophene, xylene, and oligomerized hexene were 96.6%, 2.7% and 2.8%, respectively. An optimal Si/Al2 ratio exists for the catalytic performance of Hβ zeolite. By investigating the coke deposition of the used Hβ zeolite catalysts, it has been found that the optimal Si/Al2 ratio is attributed to the combined effect of the carbocation activation capability and the hydrogen transformation capability of the Hβ zeolite catalyst.
Bibliography:desulfurization
acidity
TE6
desulfurization; alkylation; acidity; Hβ; gasoline
21-1484/O4
alkylation

gasoline
ISSN:1003-9953
DOI:10.1016/S1003-9953(08)60024-9