用于燃料电池的螺旋甲醇制氢燃料处理器的性能评估

Foad Mehri, Majid Taghizadeh
{"title":"用于燃料电池的螺旋甲醇制氢燃料处理器的性能评估","authors":"Foad Mehri,&nbsp;Majid Taghizadeh","doi":"10.1016/S1003-9953(11)60401-5","DOIUrl":null,"url":null,"abstract":"<div><p>A novel design of plate-type microchannel reactor has been developed for fuel cell-grade hydrogen production. Commercial Cu/Zn/Al<sub>2</sub>O<sub>3</sub> was used as catalyst for the reforming reaction, and its effectiveness was evaluated on the mole fraction of products, methanol conversion, hydrogen yield and the amount of carbon monoxide under various operating conditions. Subsequently, 0.5 wt% Ru/Al<sub>2</sub>O<sub>3</sub> as methanation catalyst was prepared by impregnation method and coupled with MSR step to evaluate the capability of methanol processor for CO reduction. Based on the experimental results, the optimum conditions were obtained as feed flow rate of 5 mL/h and temperature of 250°C, leading to a low CO selectivity and high H<sub>2</sub> yield. The designed reformer with catalyst coated layer was compared with the conventional packed bed reformer at the same operating conditions. The constructed fuel processor had a good performance and excellent capability for on-board hydrogen production.</p></div>","PeriodicalId":56116,"journal":{"name":"Journal of Natural Gas Chemistry","volume":"21 5","pages":"Pages 526-533"},"PeriodicalIF":0.0000,"publicationDate":"2012-09-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/S1003-9953(11)60401-5","citationCount":"10","resultStr":"{\"title\":\"Performance assessment of a spiral methanol to hydrogen fuel processor for fuel cell applications\",\"authors\":\"Foad Mehri,&nbsp;Majid Taghizadeh\",\"doi\":\"10.1016/S1003-9953(11)60401-5\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>A novel design of plate-type microchannel reactor has been developed for fuel cell-grade hydrogen production. Commercial Cu/Zn/Al<sub>2</sub>O<sub>3</sub> was used as catalyst for the reforming reaction, and its effectiveness was evaluated on the mole fraction of products, methanol conversion, hydrogen yield and the amount of carbon monoxide under various operating conditions. Subsequently, 0.5 wt% Ru/Al<sub>2</sub>O<sub>3</sub> as methanation catalyst was prepared by impregnation method and coupled with MSR step to evaluate the capability of methanol processor for CO reduction. Based on the experimental results, the optimum conditions were obtained as feed flow rate of 5 mL/h and temperature of 250°C, leading to a low CO selectivity and high H<sub>2</sub> yield. The designed reformer with catalyst coated layer was compared with the conventional packed bed reformer at the same operating conditions. The constructed fuel processor had a good performance and excellent capability for on-board hydrogen production.</p></div>\",\"PeriodicalId\":56116,\"journal\":{\"name\":\"Journal of Natural Gas Chemistry\",\"volume\":\"21 5\",\"pages\":\"Pages 526-533\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"2012-09-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"https://sci-hub-pdf.com/10.1016/S1003-9953(11)60401-5\",\"citationCount\":\"10\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Journal of Natural Gas Chemistry\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S1003995311604015\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Journal of Natural Gas Chemistry","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S1003995311604015","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 10

摘要

研制了一种新型的用于燃料电池级制氢的板型微通道反应器。以商品Cu/Zn/Al2O3为催化剂进行重整反应,并在不同操作条件下对产物的摩尔分数、甲醇转化率、产氢率和一氧化碳量进行了评价。随后,采用浸渍法制备了0.5 wt% Ru/Al2O3作为甲烷化催化剂,并与MSR步骤相结合,考察了甲醇处理机还原CO的能力。实验结果表明,最佳工艺条件为进料流量为5 mL/h,温度为250℃,CO选择性低,H2产率高。在相同的操作条件下,将所设计的催化剂包覆层重整器与常规填料床重整器进行了比较。所构建的燃料处理器具有良好的性能和优良的车载制氢能力。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Performance assessment of a spiral methanol to hydrogen fuel processor for fuel cell applications

A novel design of plate-type microchannel reactor has been developed for fuel cell-grade hydrogen production. Commercial Cu/Zn/Al2O3 was used as catalyst for the reforming reaction, and its effectiveness was evaluated on the mole fraction of products, methanol conversion, hydrogen yield and the amount of carbon monoxide under various operating conditions. Subsequently, 0.5 wt% Ru/Al2O3 as methanation catalyst was prepared by impregnation method and coupled with MSR step to evaluate the capability of methanol processor for CO reduction. Based on the experimental results, the optimum conditions were obtained as feed flow rate of 5 mL/h and temperature of 250°C, leading to a low CO selectivity and high H2 yield. The designed reformer with catalyst coated layer was compared with the conventional packed bed reformer at the same operating conditions. The constructed fuel processor had a good performance and excellent capability for on-board hydrogen production.

求助全文
通过发布文献求助,成功后即可免费获取论文全文。 去求助
来源期刊
Journal of Natural Gas Chemistry
Journal of Natural Gas Chemistry 化学-工程:化工
自引率
0.00%
发文量
0
审稿时长
2 months
×
引用
GB/T 7714-2015
复制
MLA
复制
APA
复制
导出至
BibTeX EndNote RefMan NoteFirst NoteExpress
×
提示
您的信息不完整,为了账户安全,请先补充。
现在去补充
×
提示
您因"违规操作"
具体请查看互助需知
我知道了
×
提示
确定
请完成安全验证×
copy
已复制链接
快去分享给好友吧!
我知道了
右上角分享
点击右上角分享
0
联系我们:info@booksci.cn Book学术提供免费学术资源搜索服务,方便国内外学者检索中英文文献。致力于提供最便捷和优质的服务体验。 Copyright © 2023 布克学术 All rights reserved.
京ICP备2023020795号-1
ghs 京公网安备 11010802042870号
Book学术文献互助
Book学术文献互助群
群 号:481959085
Book学术官方微信