• 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