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- W2350748066 abstract "The coking performance for the catalytic pyrolysis of heavy oil with temperature, weight ratios of catalyst-to-oil and steam-to-oil and residence time, was investigated in a confined fluidized bed reactor on catalyst CEP-1,with a special catalyst of catalytic pyrolysis process (CPP) technology. The coke content on catalyst decreases with the increase of the weight ratios of catalyst-to-oil and steam-to-oil and n(H)/n(C) of the feed, and it increases with the enhancement of reaction temperature and aromaticity of the feed. Coke yield increases with increasing reaction temperature, catalyst-to-oil weight ratio and aromaticity, while decreases with increasing steam-to-oil weight ratio and n(H)/n(C) of the feed. Both coke content and coke yield show minimum as residence time of oil gas prolongs. Both n(H)/n(C) and aromaticity of the feed can well reveal the coking tendency of a feed. On the basis of the experimental research, a correlation model of coke content and coke yield with feed property and reaction conditions was established. The parameters in the model were calculated by least square regression." @default.
- W2350748066 created "2016-06-24" @default.
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- W2350748066 date "2009-01-01" @default.
- W2350748066 modified "2023-09-23" @default.
- W2350748066 title "Influencing Factors of Coking for Heavy Oil Catalytic Pyrolysis" @default.
- W2350748066 hasPublicationYear "2009" @default.
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