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Effective Coke Removal in Methane to Benzene (MTB) Reaction on Mo/HZSM-5 Catalyst by H2 and H2O Co-addition to Methane

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The catalytic dehydro-aromatization reaction over Mo/HZSM-5 catalyst was drastically stabilized by the co-addition of 5.4% H2 and 1.8% H2O to methane feed at 750 °C, 0.3 MPa and methane space velocity of 3000 mL g−1 h−1, suppressing the coke formation effectively, compared with single hydrogen or steam addition.

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Authors and Affiliations

  1. Catalysis Research Center, Hokkaido University, N-21 W-10, Kita-ku, Sapporo, 001-0021, Japan

    Hongtao Ma, Ryoichi Kojima, Satoshi Kikuchi & Masaru Ichikawa

Authors
  1. Hongtao Ma
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  2. Ryoichi Kojima
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  3. Satoshi Kikuchi
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  4. Masaru Ichikawa
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Correspondence to Masaru Ichikawa.

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Ma, H., Kojima, R., Kikuchi, S. et al. Effective Coke Removal in Methane to Benzene (MTB) Reaction on Mo/HZSM-5 Catalyst by H2 and H2O Co-addition to Methane. Catal Lett 104, 63–66 (2005). https://doi.org/10.1007/s10562-005-7437-y

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  • DOI: https://doi.org/10.1007/s10562-005-7437-y

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