Autothermal reforming of methane to syngas using co-precipitated Ni-(La2O3)1-x catalyst

Sun Hee Park; Kook Chun; Wang Lai Yoon; Sung Hyun Kim

doi:10.1163/156856708786189429

Autothermal reforming of methane to syngas using co-precipitated Ni-(La₂O₃)_1-x catalyst

Sun Hee Park, Kook Chun, Wang Lai Yoon, Sung Hyun Kim

Research output: Contribution to journal › Article › peer-review

3 Citations (Scopus)

Abstract

Two different catalysts, Ni-(ZrO₂) and Ni-(La₂O ₃)_0.1-(ZrO₂)_0.9, were synthesized to use as catalysts in the autothermal reforming of methane. Ni-(ZrO₂) catalyst without lanthanum prepared in this study has a good initial performance, but as the reactions keep progressing, the activities gradually decrease. In contrast, the activities of Ni-(La₂O₃) _0.1-(ZrO₂)_0.9 catalyst have high thermal stability and coke resistance due to the presence of La. Both methane conversion and hydrogen yield of Ni-(La₂O₃)0.1-(ZrO ₂)_0.9 in non-reduced form are better than reduced form and as good as commercial Ni-based catalyst (ICI 57-4).

Original language	English
Pages (from-to)	781-786
Number of pages	6
Journal	Research on Chemical Intermediates
Volume	34
Issue number	8-9
DOIs	https://doi.org/10.1163/156856708786189429
Publication status	Published - 2008 Oct 1

Bibliographical note

Funding Information:
The authors thank the Korea Institute Energy Research for providing financial support for the study.

Copyright:
Copyright 2009 Elsevier B.V., All rights reserved.

Keywords

Autothermal reforming
Catalyst
Lanthanum
Methane
Reforming

ASJC Scopus subject areas

General Chemistry

Access to Document

10.1163/156856708786189429

Cite this

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title = "Autothermal reforming of methane to syngas using co-precipitated Ni-(La2O3)1-x catalyst",

abstract = "Two different catalysts, Ni-(ZrO2) and Ni-(La2O 3)0.1-(ZrO2)0.9, were synthesized to use as catalysts in the autothermal reforming of methane. Ni-(ZrO2) catalyst without lanthanum prepared in this study has a good initial performance, but as the reactions keep progressing, the activities gradually decrease. In contrast, the activities of Ni-(La2O3) 0.1-(ZrO2)0.9 catalyst have high thermal stability and coke resistance due to the presence of La. Both methane conversion and hydrogen yield of Ni-(La2O3)0.1-(ZrO 2)0.9 in non-reduced form are better than reduced form and as good as commercial Ni-based catalyst (ICI 57-4).",

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