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Hydrocracking of heavy hydrocarbon oils with heavy hydrocarbon recycle

机译:重烃循环利用对重烃油进行加氢裂化

摘要

A heavy hydrocarbon oil, a substantial portion of which boils above 524° C., is subjected to hydrocracking with a fractionated heavy oil recycle stream containing active additive particles. In the process, a slurry feed of (1) fresh heavy hydrocarbon oil feedstock and a heavy hydrocarbon recycle and (2) from about 0.01-4% by weight (based on fresh feedstock) of iron sulphate additive particles having sizes less than 45 . mu.m, is passed upwardly through a confined vertical hydrocracking zone. A mixed effluent is removed from the top of the hydrocracking zone, which is then passed through a hot separator vessel. From the bottom of the separator is withdrawn a liquid heavy hydrocarbon stream comprising heavy hydrocarbons and particles of the iron sulphate additive converted mainly to an iron sulphide phase. This separated liquid heavy hydrocarbon stream is fractionated to obtain a heavy oil which boils above 450° C., containing the additive particles. The fractionated heavy oil containing the additive particles is then recycled to and mixing with the hydrocracking zone feed slurry in an amount up to 40% by weight of the combined feed slurry.
机译:使重质烃油的大部分在高于524°C的条件下沸腾,然后使其与含有活性添加剂颗粒的分馏重油循环物流进行加氢裂化。在该方法中,浆液进料(1)新鲜的重质烃油原料和重质烃再循环和(2)以重量计约0.01-4%(基于新鲜的原料)的尺寸小于45%的硫酸铁添加剂颗粒。微米,向上通过一个狭窄的垂直加氢裂化区。从加氢裂化区的顶部除去混合的流出物,然后将其通过热分离器。从分离器的底部抽出液态重烃料流,其包含重烃和主要转化为硫化铁相的硫酸铁添加剂颗粒。分馏该分离的液态重烃料流以获得沸点在450℃以上的重油,其包含添加剂颗粒。然后将含有添加剂颗粒的分馏重油循环至加氢裂化区进料浆料中并与之混合,其量最高为合并进料浆料的40重量%。

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