首页 | 本学科首页   官方微博 | 高级检索  
     


Semi-continuous hydrogen production from catalytic methane decomposition using a fluidized-bed reactor
Authors:Naresh Shah  Shankang MaYuguo Wang  Gerald P. Huffman
Affiliation:University of Kentucky, 533 S. Limestone Street, Suite 107, Lexington, KY 40508, USA
Abstract:Non-oxidative, catalytic decomposition of hydrocarbons is an alternative, one-step process to produce pure hydrogen with no production of carbon oxides or higher hydrocarbons. Carbon produced from the decomposition reaction, in the form of potentially valuable carbon nanotubes, remains anchored to the active catalyst sites in a fixed bed. To facilitate periodical removal of this carbon from the reactor and to make hydrogen production continuous, a fluidized-bed reactor was envisioned. The hypothesis that the tumbling and inter-particle collisions of bed material would efficiently separate nanotubes anchored to the active catalyst sites of the bed particles was tested and shown to be invalid. However, a switching mode reaction system for the semi-continuous production of hydrogen and carbon nanotubes by periodic removal and replenishment of the catalytic bed material has been successfully demonstrated.
Keywords:Hydrogen production   Non-oxidative   Catalytic   Methane decomposition   Carbon nanotubes   Switching mode   Fluidized-bed reactor
本文献已被 ScienceDirect 等数据库收录!
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