Development of heavy oil hydrocracking catalysts using amorphous silica-alumina and zeolites as catalyst supports

被引:171
作者
Ali, MA [1 ]
Tatsumi, T
Masuda, T
机构
[1] KFUPM, Ctr Refining & Petrochem, Res Inst, Dhahran, Saudi Arabia
[2] Yokohama Natl Univ, Fac Engn, Div Mat & Chem Engn, Yokohama, Kanagawa 240, Japan
[3] Japan Petr Energy Ctr, Adv Technol & Res Inst, Adv Catalysts Res Lab, Kanagawa, Japan
关键词
silica-alumina; beta-zeolite; USY-zeolite; hydrocracking; extrudates; Co-impregnation; incipient wetness method; desulfurized VGO; acidity; surface area; catalytic evaluation; fixed bed reaction system;
D O I
10.1016/S0926-860X(02)00121-7
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 [物理化学]; 081704 [应用化学];
摘要
The overall objective of this research work was to prepare hydrocracking catalysts using amorphous silica-alumina (ASA) supports in combination with USY and beta-zeolites. Three supports: namely silica-alumina, USY and beta-zeolites were selected to prepare the extrudates using AP-1 as a binder, while two metal pairs: namely Ni-W and Ni-Mo were loaded on the extrudates through co-impregnation using incipient wetness technique. The catalysts were then calcined at 550 degreesC for 2 h. The catalysts were tested in a fixed-bed flow reaction system for their activity, using desulfurized vacuum gas oil (DS-VGO) as a feedstock. The catalytic evaluation results of the cataiysts showed that beta-zeolite alone and in combination with the ASA used in this study, has a potential as a support for developing heavy oil hydrocracking catalysts. A balance of weak and strong acidities of beta-zeolite provides control cracking, while high surface area and bigger pores of silica-alumina may be useful for producing stable hydrocracking and hydrotreating catalysts. (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:77 / 90
页数:14
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