Volume 42 Issue 03
Mar.  2014
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LI Wei-wei, LI Ke-zhong, KANG Shou-guo, ZHENG Yan, ZHANG Rong, BI Ji-cheng. Heterogeneous reaction kinetics of catalytic coal gasification[J]. Journal of Fuel Chemistry and Technology, 2014, 42(03): 290-296.
Citation: LI Wei-wei, LI Ke-zhong, KANG Shou-guo, ZHENG Yan, ZHANG Rong, BI Ji-cheng. Heterogeneous reaction kinetics of catalytic coal gasification[J]. Journal of Fuel Chemistry and Technology, 2014, 42(03): 290-296.

Heterogeneous reaction kinetics of catalytic coal gasification

  • Received Date: 2013-08-26
  • Rev Recd Date: 2013-10-28
  • Publish Date: 2014-03-31
  • The gasification tests of Shenmu coal char were carried out in a pressured fixed bed reactor to investigate the effect of gasification agents (H2O, CO2, H2), catalyst loading, and partial pressure of hydrogen and carbon monoxide on the carbon conversion and reaction rate. The results show that the heterogeneous reaction rate is in the order of C-H2O >C-CO2>C-H2. H2 and CO inhibit the steam gasification rate to some degrees. The inhibition of CO is much greater than that of H2. The carbon conversion decreases by about 50% with the addition of only 5% CO at 700 ℃. A kinetic model is developed combined Langmuir-Hinshelwood (L-H) with the random pore model, considering the effect of catalyst loading and the partial pressure of gasification product gases. The deviation between predication and experiment value is less than 10%, indicating that the derived kinetic model is appropriate for describing the catalytic coal gasification with steam.
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