Knowledge Management System Of Guangzhou Institute of Energy Conversion, CAS
Numerical simulation and experimental study of hydrogen production from dimethyl ether steam reforming in a micro-reactor | |
Yan, Chang-Feng1,2,3; Ye, Wen1,2; Guo, Chang-Qing1; Huang, Shi-Lin1; Li, Wen-Bo1; Luo, Wei-Min1 | |
2014-10-31 | |
发表期刊 | INTERNATIONAL JOURNAL OF HYDROGEN ENERGY |
卷号 | 39期号:32页码:18642-18649 |
摘要 | To enhance the heat and mass transfer during dimethyl ether (DME) steam reforming, a micro-reactor with catalyst coated on nickel foam support was designed and fabricated. A two-dimensional numerical model with SIMPLE algorithm and finite volume method was used to investigate 1) the fluid flow, 2) the heat transfer and 3) chemical reactions consist of DME hydrolysis, methanol steam reforming, methanol decomposition and water gas shift reactions. Both the numerical and the experimental results showed that the DME conversion in the micro-reactor is higher than that in the fixed bed reactor. The numerical study also showed that the velocity and the temperature distribution were more uniform in the micro-reactor. Wall temperature, porosity and steam/DME ratio have been investigated in order to optimize the process in the micro-reactor. The wall temperature of 270 degrees C and the steam/DME feed ratio of 5 were recommended. Meanwhile the results indicate that a larger porosity will give a higher DME conversion and CO concentration. Copyright (C) 2014, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved. |
文章类型 | Article |
关键词 | Numerical Simulation Hydrogen Production Micro-reactor Dme Steam Reforming |
WOS标题词 | Science & Technology ; Physical Sciences ; Technology |
DOI | 10.1016/j.ijhydene.2014.02.133 |
研究领域[WOS] | Chemistry ; Electrochemistry ; Energy & Fuels |
关键词[WOS] | CATALYTIC COMBUSTION ; OLEFINS PROCESS ; FUEL-CELLS ; METHANOL ; CU/ZNO/AL2O3 ; MODEL ; DME ; MICROREACTOR ; ZSM-5 |
收录类别 | SCI |
语种 | 英语 |
WOS类目 | Chemistry, Physical ; Electrochemistry ; Energy & Fuels |
WOS记录号 | WOS:000345804600053 |
引用统计 | |
文献类型 | 期刊论文 |
条目标识符 | http://ir.giec.ac.cn/handle/344007/10681 |
专题 | 中国科学院广州能源研究所 |
作者单位 | 1.Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou 510640, Guangdong, Peoples R China 2.Univ Chinese Acad Sci, Beijing 100039, Peoples R China 3.Chinese Acad Sci, Key Lab Renewable Energy, Guangzhou 510640, Guangdong, Peoples R China |
第一作者单位 | 中国科学院广州能源研究所 |
推荐引用方式 GB/T 7714 | Yan, Chang-Feng,Ye, Wen,Guo, Chang-Qing,et al. Numerical simulation and experimental study of hydrogen production from dimethyl ether steam reforming in a micro-reactor[J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY,2014,39(32):18642-18649. |
APA | Yan, Chang-Feng,Ye, Wen,Guo, Chang-Qing,Huang, Shi-Lin,Li, Wen-Bo,&Luo, Wei-Min.(2014).Numerical simulation and experimental study of hydrogen production from dimethyl ether steam reforming in a micro-reactor.INTERNATIONAL JOURNAL OF HYDROGEN ENERGY,39(32),18642-18649. |
MLA | Yan, Chang-Feng,et al."Numerical simulation and experimental study of hydrogen production from dimethyl ether steam reforming in a micro-reactor".INTERNATIONAL JOURNAL OF HYDROGEN ENERGY 39.32(2014):18642-18649. |
条目包含的文件 | 条目无相关文件。 |
除非特别说明,本系统中所有内容都受版权保护,并保留所有权利。
修改评论