Monolith loop catalytic membrane reactor for Fischer-Tropsch synthesis

被引:37
作者
Bradford, MCJ [1 ]
Te, M [1 ]
Pollack, A [1 ]
机构
[1] CeraMem Corp, Waltham, MA 02453 USA
关键词
Fischer-Tropsch monolith loop; membrane reactor; natural gas conversion;
D O I
10.1016/j.apcata.2004.12.032
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 monolith loop catalytic membrane reactor (ML-CMR) concept for Fischer-Tropsch synthesis (FTS) was investigated by evaluating the performance of a P/Pt-Co/gamma-Al2O3 catalyst in a prototype, tubular CMR and in a tubular, fixed-bed reactor (FBR). Although experimental data demonstrate that the selectivity to paraffins and the product yield per unit catalyst mass exhibited by the P/Pt-Co/gamma-Al2O3 catalyst in the tubular CMR exceed those observed by the same catalyst in a tubular FBR, simple model calculations indicate that the ML-CMR product yield per unit reactor volume, at its present stage of development, is less than that for state-of-the-art multi-tubular fixed-bed and slurry-bubble column reactors. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:39 / 46
页数:8
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