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    • 1. 发明授权
    • Butane cracking
    • BUTANE CRACKING
    • US3761538A
    • 1973-09-25
    • US3761538D
    • 1971-02-11
    • CHEM SYSTEMS
    • SUGERMAN GESPINO RSHERWIN M
    • C07C4/04C07C3/30
    • C07C4/04C07C11/04C07C11/06
    • A process for the preparation of ethylene and propylene wherein n-butane is cracked at high pressure in the presence of steam, preferably with ammonia in a reactor containing a solid support, at a temperature of from 550* to 750* C. for a residence time of 0.2 to 15 seconds to convert 40 to 90 percent of the n-butane. The reaction product is cooled and methane separated therefrom at a pressure not greater than that in the cracking reaction. The C4 fraction separated from the reaction product is recycled to the cracking step.
    • 一种制备乙烯和丙烯的方法,其中正丁烷在蒸汽存在下在高压下,优选在含有固体载体的反应器中在氨的存在下在550℃至750℃的温度下裂解 时间为0.2至15秒,将40至90%的正丁烷转化。 将反应产物冷却,并在不高于裂解反应的压力下从其中分离甲烷。 将与反应产物分离的C4馏分循环至裂化步骤。