Title of article
Semi-continuous hydrogen production from catalytic methane decomposition using a fluidized-bed reactor
Author/Authors
Shah، نويسنده , , Naresh and Ma، نويسنده , , Shankang and Wang، نويسنده , , Yuguo and Huffman، نويسنده , , Gerald P.، نويسنده ,
Issue Information
روزنامه با شماره پیاپی سال 2007
Pages
5
From page
3315
To page
3319
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 , Carbon nanotubes , Switching mode , Catalytic , Methane decomposition , Fluidized-bed reactor
Journal title
International Journal of Hydrogen Energy
Serial Year
2007
Journal title
International Journal of Hydrogen Energy
Record number
1652923
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