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
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Authors
Dates
1999-01-10—Published
1997-01-31—Filed