H-type zeolite coated iron-based multiple-functional catalyst for direct synthesis of middle isoparaffins from syngas

被引:47
作者
Bao, Jun [2 ]
Yang, Guohui [1 ]
Okada, Chie [1 ]
Yoneyama, Yoshiharu [1 ]
Tsubaki, Noritatsu [1 ,3 ]
机构
[1] Toyama Univ, Sch Engn, Dept Appl Chem, Toyama 9308555, Japan
[2] Univ Sci & Technol China, Natl Synchrotron Radiat Lab, Hefei 230029, Peoples R China
[3] CREST, JST, Chiyoda Ku, Tokyo 1020075, Japan
关键词
H-ZSM-5; zeolite; Core-shell structure; Isoparaffin synthesis; Spatially confined effect; Shape selectivity; FISCHER-TROPSCH SYNTHESIS; CO-HYDROGENATION; SELECTIVITY; MECHANISM; DESIGN;
D O I
10.1016/j.apcata.2010.12.041
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 ; 081704 ;
摘要
A compact, integral zeolite shell of H-ZSM-5 was directly crystallized on the surface of fused-iron catalyst pellet by a hydrothermal synthesis method. The synthesized catalyst has a core-shell structure without pinholes and cracks. For the reaction of direct synthesis of isoparaffin from syngas, the formation of C10+ hydrocarbons is suppressed completely on this core-shell catalyst, and the middle isoparaffins become the main products. Especially, desirable low methane selectivity is achieved. The core-shell structure of the catalyst provides a tailor-made confined reaction environment with spatially confined effect and shape selectivity, where isoparaffins escaping from outer surface of one core-shell catalyst hardly enter another core-shell catalyst via surface zeolite shell, due to its large steric obstacle, ensuring the elevated isoparaffin selectivity. Furthermore, this type of core-shell catalyst has very high membrane area per unit reactor volume and easy to be prepared, in contrast to the conventional membrane reactor. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:195 / 200
页数:6
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