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Operation Conditions Optimization of Hydrogen Production by Propane Autothermal Reforming for PEMFC Application

Operation Conditions Optimization of Hydrogen Production by Propane Autothermal Reforming for PEMFC Application

作     者:刘志祥 毛宗强 徐景明 Natascha Hess-Mohr Volkmar M. Schmidt LIU Zhixiang;MAO Zongqiang;XU Jingming;Natascha Hess-Mohr;Volkmar M. Schmidt

作者机构:Institute of Nuclear and New Energy Technology Tsinghua University Beijing 100084 China Institute of Electrochemical Process Engineering Mannheim University of Applied Sciences 68163 Mannheim Germany 

出 版 物:《Chinese Journal of Chemical Engineering》 (中国化学工程学报(英文版))

年 卷 期:2006年第14卷第2期

页      面:259-265页

核心收录:

学科分类:0710[理学-生物学] 0830[工学-环境科学与工程(可授工学、理学、农学学位)] 081705[工学-工业催化] 0817[工学-化学工程与技术] 08[工学] 0703[理学-化学] 

基  金:Supported by the National 973 Program of China on Hydrogen Energy (TG2000026410) and International Cooperation Projecton Hydrogen Energy (2001AA515080) 

主  题:hydrogen production autothermal reforming fuel cell propane 

摘      要:Autothermal reforming (ATR) is one of the leading methods for hydrogen production from hydrocar- bons. Liquefied petroleum gas, with propane as the main component, is a promising fuel for on-board hydrogen producing systems in fuel cell vehicles and for domestic fuel cell power generation devices. In this article, propane ATR process is studied and operation conditions are optimized with PRO/Ⅱ? from SIMSCI for proton exchange membrane fuel cell application. In the ATR system including water gas shift and preferential oxidation, heat in the hot streams and cold streams is controlled to be in balance. Different operation conditions are studied and drawn in contour plots. The region for ATR reforming with the highest efficiency can thus be identified. One operation point was chosen with the following process parameters: feed temperature for the ATR reactor is 425℃, steam to carbon ratio S/C is 2.08, air stoichiometry is 0.256. Thermal efficiency for the integrated system is calculated to be as high as 84.0 % with 38.27 % H2 and 3.2μl·L-1 CO in the product gas.

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