Journal
CATALYSIS LETTERS
Volume 104, Issue 1-2, Pages 63-66Publisher
SPRINGER
DOI: 10.1007/s10562-005-7437-y
Keywords
methane dehydro-aromatization; Mo catalyst; H-2 addition; H2O addition
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The catalytic dehydro-aromatization reaction over Mo/HZSM-5 catalyst was drastically stabilized by the co-addition of 5.4% H-2 and 1.8% H2O to methane feed at 750 degrees 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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