Abstract
With a small amount of H2 (3 ∼ 6%) addition into methane feed, coke formation on 6 wt% Mo catalyst during the methane dehydroaromatization reaction was effectively suppressed and the catalyst stability was increased evidently under the reaction conditions of 1023K, 0.3MPa and 2520 mL g-MFI-1 h-1 of methane space velocity.
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Ma, H., Ohnishi, R. & Ichikawa, M. Highly Stable Performance of Methane Dehydroaromatization on Mo/HZSM-5 Catalyst with a Small Amount of H2 Addition into Methane Feed. Catalysis Letters 89, 143–146 (2003). https://doi.org/10.1023/A:1024796115700
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DOI: https://doi.org/10.1023/A:1024796115700