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METHOD OF PRODUCING HIGH-OCTANE GASOLINE OR HIGH-OCTANE GASOLINE AND AROMATIC HYDROCARBONS

机译:制备高辛烷值或高辛烷值的汽油和芳烃的方法

摘要

FIELD: petroleum processing and petrochemical industry. SUBSTANCE: hydrocarbon material containing aliphatic hydrocarbons is brought into contact with zeolite catalyst at elevated temperature and pressure using two reaction zones, in one of them crude gasoline fraction and in the other C2-C4-hydrocarbons being converted into C1-C12-hydrocarbon mixture containing desired product. The two catalytic zones operate simultaneously in two different modes with the same duration, which are alternated in such a way as to ensure continuous conversion of crude gasoline. Mode I: conversion of crude gasoline. Mode II - continuous sequence of following processes: regeneration of catalyst after conversion of crude gasoline, conversion of C2-C4-hydrocarbons, and regeneration of catalyst after conversion of C2-C4-hydrocarbons. In a preferred embodiment of invention, desired product is isolated from mixture of products formed in both reaction zones. At least a part of propane-butane fraction formed from crude gasoline can be used as C2-C4-hydrocarbons. EFFECT: increased yield of liquid products. 23 cl, 1 dwg, 3 tbl
机译:领域:石油加工和石化工业。物质:使用两个反应区,在升高的温度和压力下,使含有脂肪族烃的烃类物质与沸石催化剂接触,其中一个反应区为粗汽油馏分,另一个反应区为C 2 -C 4 -烃转化为含有所需产物的C 1 -C 12 -烃混合物。两个催化区以相同的持续时间以两种不同的模式同时运行,以确保连续转化粗汽油的方式交替进行。模式I:粗汽油的转化。模式II-以下过程的连续顺序:粗汽油转化后催化剂的再生,C 2 -C 4 -烃的转化以及C转化后的催化剂再生 2 -C 4 -碳氢化合物。在本发明的优选实施方案中,从在两个反应区中形成的产物的混合物中分离出期望的产物。由粗汽油形成的丙烷-丁烷馏分的至少一部分可以用作C 2 -C 4 -烃。效果:提高液体产品的产量。 23厘升,1载重吨,3汤匙

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