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Hydrocarbon dehydrogenation to olefins - using iodine, oxygen and iodide acceptor, in separate dehydrogenation, accepting and iodine regeneration zones

机译:烃脱氢制烯烃-使用碘,氧和碘化物受体,在单独的脱氢,接受和碘再生区中

摘要

Hydrocarbons are converted to mono- and diolefins by dehydrogenation at 450-570 degrees C in presence of I2, O2 and a content acceptor for HI formed in dehydrogenation, HI is accepted at 430-550 degrees C. I2 is regenerated from contact by means of O2 at 450-650 degrees C. Dehydrogenation, accepting and regeneration are separately carried out, in appts. zones joined to one another. Dehydrogenation zone is set between accepting and regeneration zones. 90-30% O2, w.r.t. total quantity, is charged to regeneration step. and 10-70% to dehydrogenation step. Prods. are used as monomers and intermediates in prodn. of synthetic rubber and plastics. Process may be used for prepn. of divinyl from n-butane, and n-butylenes, isobutylene from isobutene, isoprene from isopentane and isoamylenes, styrene from ethylbenzene, vinyl toluene from ethyltoluenes. Each step can take place under optimum conditions. End-prods. yield is increased.
机译:在I2,O2和脱氢中形成的HI的含量受体的存在下,在450-570摄氏度下通过脱氢将烃转化为单烯烃和二烯烃.HI在430-550摄氏度下被接受.I2通过O2在450-650摄氏度下进行。脱氢,接受和再生分别进行。区域彼此相连。脱氢区设置在接受区和再生区之间。氧气90-30%(重量)总数量将计入再生步骤。和10-70%进行脱氢步骤。产品。在产品中用作单体和中间体。合成橡胶和塑料。该过程可用于准备。来自正丁烷的二乙烯基和正丁烯,来自异丁烯的异丁烯,来自异戊烷和异戊烯的异戊二烯,来自乙苯的苯乙烯,来自乙基甲苯的乙烯基甲苯。每个步骤都可以在最佳条件下进行。最终产物。产量增加。

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