首页 | 本学科首页   官方微博 | 高级检索  
     检索      

C12A7-Mg催化剂水蒸汽重整生物油、石脑油和CH4制氢
引用本文:潘越,王兆祥,阚涛,朱锡峰,李全新.C12A7-Mg催化剂水蒸汽重整生物油、石脑油和CH4制氢[J].化学物理学报(中文版),2006,19(3):190-192.
作者姓名:潘越  王兆祥  阚涛  朱锡峰  李全新
摘    要:

关 键 词:生物油  石脑油  催化水蒸汽重整  氢气

Hydrogen Production by Catalytic Steam Reforming of Bio-oil, Naphtha and CH4 over C12A7-Mg Catalyst
Yue Pan,Zhao-xiang Wang,Tao Kan,Xi-feng Zhu,Quan-xin Li.Hydrogen Production by Catalytic Steam Reforming of Bio-oil, Naphtha and CH4 over C12A7-Mg Catalyst[J].化学物理学报(中文版),2006,19(3):190-192.
Authors:Yue Pan  Zhao-xiang Wang  Tao Kan  Xi-feng Zhu  Quan-xin Li
Institution:{{each article.affiliations aff i}} {{if aff.addressEn && aff.addressEn != ""}} {{if aff.label && aff.label != "" && article.affiliations.length != 1}}{{@ aff.label}}.{{/if}}{{@ aff.addressEn}}{{/if}} {{/each}}
Abstract:Hydrogen production by catalytic steam reforming of the bio-oil, naphtha, and CH4 was investigated over anovel metal-doped catalyst of (Ca24Al28O64)4+¢4O-/Mg (C12A7-Mg). The catalytic steam reforming wasinvestigated from 250 to 850 ±C in the ˉxed-bed continuous °ow reactor. For the reforming of bio-oil, theyield of hydrogen of 80% was obtained at 750 ±C, and the maximum carbon conversion is nearly close to95% under the optimum steam reforming condition. For the reforming of naphtha and CH4, the hydrogenyield and carbon conversion are lower than that of bio-oil at the same temperature. The characteristics ofcatalyst were also investigated by XPS. The catalyst deactivation was mainly caused by the deposition ofcarbon in the catalytic steam reforming process.
Keywords:C12A7-Mg  CH4  C12A7-Mg  Bio-oil  Naphtha  CH4  Catalytic steam reforming  Hydrogen
本文献已被 万方数据 等数据库收录!
点击此处可从《化学物理学报(中文版)》浏览原始摘要信息
点击此处可从《化学物理学报(中文版)》下载免费的PDF全文
设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号