Synthesis gas production process for natural gas conversion over Ni-La2O3 catalyst

被引：9

作者：

Cho, Wonjun ^{[1
]}

Yu, Hyejin ^{[1
,2
]}

Ahn, Wha-Seung ^{[2
]}

Kim, Seung-Soo ^{[3
]}

机构：

[1] KOGAS, DME Technol Res Ctr, Inchon 406130, South Korea

[2] Inha Univ, Dept Chem Engn, Inchon 402751, South Korea

[3] Kangwon Natl Univ, Dept Chem Engn, Samcheok 245711, Gangwon Do, South Korea

来源：

JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY | 2015年 / 28卷

关键词：

Syngas; Steam-CO2 reforming (SCR); Synthetic fuel reactor; Catalyst; Kinetics; METHANE; CO2; CHALLENGES; REACTOR; COKE;

D O I：

10.1016/j.jiec.2015.02.019

中图分类号：

O6 [化学];

学科分类号：

0703 ;

摘要：

The synthesis gas (syngas) is a mixture of hydrogen and carbon monoxide, which is suitable as a feed gas to produce clean liquid synthetic fuel in natural gas conversion reactor. In order to achieve the efficiency reactor, the syngas composition should match the usage ratio of the reactors. In this work, we investigate the development of synthesis gas production process in the steam-CO2 reforming (SCR) over Ni-La2O3 catalyst supported Ce-ZrO2/Al2O3. And, we developed the kinetics model for SCR used by the profiles of concentration and temperature in the SCR reactor. (C) 2015 The Korean Society of Industrial and Engineering Chemistry. Published by Elsevier B.V. All rights reserved.

引用

页码：229 / 235

页数：7

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