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Thermal cracking of hydrocarbon to ethylene etc. - using water with hydrogen and/or methane to increase yield and reduce coking (HUT 28.5.81)

机译:将碳氢化合物热裂解为乙烯等-使用含氢和/或甲烷的水提高收率并减少焦化(HUT 28.5.81)

摘要

In the thermal cracking of hydrocarbons to ethylene and other prods., the diluent is water with hydrogen and/or methane. The wt. ratio diluent/hydrocarbon is 0.25-0.50 for gaseous feedstocks and 0.5-1.2 for liq. feedstocks, and the wt. ratio (H2 and/or H2 equiv. of CH4)/hydrocarbon is 0.0025-0.0195. Pref. the wt. ratio H2/hydrocarbon is 0.004-0.01. The ethylene and propylene yields are higher than with water as the only diluent, the effects being greater if ethane and propane prod. are recycled for cracking either in a separate furnace or mixed with the hydrocarbon feed. The raffinates from C4, C5 and pyrolysis gasoline streams may also be recycled. The H2 may be added as the CH4 rich H2 stream sepd. from the cracker.
机译:在碳氢化合物热裂解为乙烯和其他产品时,稀释剂是具有氢和/或甲烷的水。重量气态原料的稀释剂/烃的比率为0.25-0.50,液体为0.5-1.2。原料和重量(H 2和/或H 2当量的CH 4)/烃之比为0.0025-0.0195。首选wt。 H2 /烃的比率为0.004-0.01。乙烯和丙烯的收率高于用水作为唯一的稀释剂,如果使用乙烷和丙烷,则收率更高。将其再循环以在单独的炉中裂化或与烃进料混合。来自C4,C5和热解汽油物流的提余液也可以回收。可以将H2作为富CH4的H2流Sepd添加。从饼干。

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