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Catalytic Conversion of Octanoic Acid over HZSM-5 Catalyst
Abstract:
Catalytic conversion experiment of octanoic acid over HZSM-5 catalyst was carried out in a fixed fluidized bed reactor system. The effects of reaction temperature and catalyst to oil ratio on product distribution were investigated. The results showed that temperature influenced the LCO, gasoline and CO yields obviously. LCO yield decreased while CO yield increased with increasing reaction temperature. Gasoline yield reached maximum at 450 oC. CO is the major oxygenated product, and the yield increased linearly with increasing catalyst to oil ratio..
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60-63
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May 2014
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© 2014 Trans Tech Publications Ltd. All Rights Reserved
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