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通过热等离子体重整由甲烷生产富氢气体。

Production of hydrogen-rich gas from methane by thermal plasma reform.

作者信息

Chun Young N, Kim Seong C

机构信息

BK 21 Team for Hydrogen Production, Department of Environmental Engineering, Chosun University, Gwangju, South Korea.

出版信息

J Air Waste Manag Assoc. 2007 Dec;57(12):1447-51. doi: 10.3155/1047-3289.57.12.1447.

DOI:10.3155/1047-3289.57.12.1447
PMID:18200929
Abstract

This study investigated the reforming characteristics and optimum operating condition of the high-temperature plasma torch (so called plasmatron) for hydrogen-rich gas (syngas) production. At the optimum condition, the composition of produced syngas was 45.4% hydrogen (H2), 6.9% carbon monoxide (CO), 1.5% carbon dioxide (CO2), and 1.1% acetylene (C2H2). The H2/CO ratio was 6.6, hydrogen yield was 78.8%, and the energy conversion rate was 63.6%. To obtain the optimum operating condition, parametric studies were carried out examining the effects of O2/CH4 ratio, steam/CH4 ratio, and Ni catalyst addition in reactor. When the steam/CH4 ratio was 1.23, the production of hydrogen was maximized and the methane conversion rate was 99.7%. The syngas composition was determined to be 50.4% H2, 5.7% CO, 13.8% CO2, and 1.1% C2H2. The H2/CO ratio was 9.7, hydrogen yield was 93.7%, and the energy conversion rate was 78.8%. Hydrogen production with catalyst was effective, compared with no catalyst.

摘要

本研究调查了用于生产富氢气体(合成气)的高温等离子体炬(即等离子管)的重整特性和最佳运行条件。在最佳条件下,所生产合成气的组成为:氢气(H₂)45.4%、一氧化碳(CO)6.9%、二氧化碳(CO₂)1.5%、乙炔(C₂H₂)1.1%。H₂/CO比为6.6,氢气产率为78.8%,能量转换率为63.6%。为了获得最佳运行条件,进行了参数研究,考察了O₂/CH₄比、蒸汽/CH₄比以及在反应器中添加镍催化剂的影响。当蒸汽/CH₄比为1.23时,氢气产量最大化,甲烷转化率为99.7%。合成气组成确定为:H₂ 50.4%、CO 5.7%、CO₂ 13.8%、C₂H₂ 1.1%。H₂/CO比为9.7,氢气产率为93.7%,能量转换率为78.8%。与不使用催化剂相比,使用催化剂制氢效果显著。

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