Hybrid catalysts in a double-layered bed reactor for the production of C2-C4 paraffin hydrocarbons

被引：5

作者：

Jo, Seong Bin ^{[1
]}

Kim, Tae Young ^{[2
]}

Lee, Chul Ho ^{[1
]}

Kang, Suk-Hwan ^{[3
]}

Kim, Joon Woo ^{[4
]}

Jeong, Moon ^{[5
]}

Lee, Soo Chool ^{[1
]}

Kim, Jae Chang ^{[2
]}

机构：

[1] Kyungpook Natl Univ, Res Inst Adv Energy Technol, Daegu 41566, South Korea

[2] Kyungpook Natl Univ, Dept Chem Engn, Daegu 41566, South Korea

[3] Inst Adv Engn, Yongin 41718, South Korea

[4] Res Inst Ind Sci & Technol, Pohang 37673, South Korea

[5] Construct Engn Serv Co LTD, Gunpo 15850, South Korea

来源：

CATALYSIS COMMUNICATIONS | 2019年 / 127卷

基金：

新加坡国家研究基金会;

关键词：

Fischer-Tropsch (FT); Cracking; Hybrid catalyst; Double-layered bed reactor; LIGHT-HYDROCARBONS; CO HYDROGENATION; METHANATION; SYNGAS; COBALT;

D O I：

10.1016/j.catcom.2019.05.002

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：

Hybrid catalysts in a double-layered bed reactor were used to produce light C-2-C-4 paraffin hydrocarbons. Combinations of Fischer-Tropsch (FT) and cracking catalysts in a double-layered bed reactor configuration were studied. SAPO-34 and Ni-based cracking catalysts (hybrid catalyst) were used to convert C-5(+) into CH4 and C-2-C-4 paraffin hydrocarbons. Activity tests in the double-layered bed reactor at 10 bar and 300 degrees C and using a H-2/CO feed gas ratio of 3.0 revealed that the hybrid catalyst showed lower C-5(+) and higher CH4 and C-2-C-4 selectivities than the FT catalyst alone. The Ni-based catalyst enabled additional CO conversion and CO2 methanation.

引用

页码：29 / 33

页数：5

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