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Transformation manner of the gas oil which uses the improvement of the gasoline fraction and the further treatment in order to make the yield of the gas oil fraction increase

机译:通过提高汽油馏分和进一步处理以提高粗柴油馏分收率的粗柴油的转化方式

摘要

Process for the adjustment of the relative productions of petrol and gasoil from a petrol cut comprsing 4 - 15 C hydrocarbons to obtain a petrol with an improved octane index and a gasoil fraction with a high cetane index. The process is carried out in the following stages (1) membrane separation, B, of the hydrocarbon charge to obtain a selective separation of most of the linear olefins, cut beta, from the branched chain olefins, cut gamma and comprising petrols of higher octane index than the original charge; (2) (b) oligomerization, C, of the linear olefins, beta cut and in the effluents from the membrane separation; (C) (3) separation by distillation, D and of the effluents from oligomerization to give two cuts; cut delta comprises hydrocarbons of final boiling points lower than 150 - 200 [deg] C, and a cut and comprising hydrocarbons of initial boiling points greater than 150 - 200 [deg] C; (4) (d) hydrogenation, E and of the cut to obtain a gasoil of cetane index of at least 45; (5) (e) dehydrogenation, F, of the cut delta to convert paraffins to olefins and producing a cut mu which is partly recycled to the membrane separation stage.
机译:从包含4-15 C碳氢化合物的汽油馏分中调整汽油和瓦斯油的相对产量的方法,以获得具有改进的辛烷值指数和高十六烷值的瓦斯油馏分的汽油。该方法在以下步骤中进行(1):烃进料的膜分离B,以从支链烯烃,切割的γ和包含高级辛烷的汽油中选择性地分离出大部分直链烯烃,经切割的β。索引比原来收费; (2)(b)直链烯烃的低聚C,β馏分和膜分离后的流出物; (C)(3)通过蒸馏分离D和低聚反应产生的废水,得到两个馏分;馏分包括最终沸点低于150-200℃的烃,并且馏分包括初始沸点高于150-200℃的烃; (4)(d)将馏分E和馏分进行氢化,得到十六烷值指数至少为45的粗柴油; (5)(e)馏分δ的脱氢F以将链烷烃转化为烯烃并产生馏分μ,其部分再循环至膜分离阶段。

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