首页> 外国专利> A combined process for the isomerization of c5 - c6 hydrocarbons and pressure swing adsorption stage.

A combined process for the isomerization of c5 - c6 hydrocarbons and pressure swing adsorption stage.

机译:c5-c6烃异构化和变压吸附阶段的组合过程。

摘要

An isomerization zone process is disclosed that combines a deisohexanizer with a PSA separation section to provide a product stream comprising methylbutane and dimethylbutane. The process combines a methylpentane and normal hexane recycle stream, a normal pentane recycle stream and a fresh feedstream to provide a combined feedstream that is charged to an isomerization zone. The effluent from the isomerization zone is stabilized and passed to a deisohexanizer. A sidecut stream carries the methylpentane and normal hexane recycle stream from the deisohexanizer. Hydrocarbons having a higher boiling point than the sidecut stream are withdrawn as a bottoms stream from the deisohexanizer. An overhead carries normal pentane, methylbutane and dimethylbutanes to the PSA separation section. An extract stream is recovered as the normal pentane recycle stream. The raffinate from the PSA provides a high octane isomerate stream comprising mainly methylpentane and dimethylbutanes.
机译:公开了一种异构化区方法,其将脱异己酮与PSA分离段组合以提供包含甲基丁烷和二甲基丁烷的产物流。该方法将甲基戊烷和正己烷再循环料流,正戊烷再循环料流和新鲜进料流合并以提供合并的进料流,其被加入异构化区。来自异构化区的流出物被稳定并传递至脱异己醇。侧馏分馏分流携带来自异异己醇的甲基戊烷和正己烷循环流。将沸点高于侧馏分料流的烃作为塔底料流从脱异己烃中抽出。塔顶馏出物将正戊烷,甲基丁烷和二甲基丁烷带到PSA分离段。提取物流作为常规戊烷循环流回收。来自PSA的提余液提供了主要包含甲基戊烷和二甲基丁烷的高辛烷值异构体物流。

著录项

  • 公开/公告号DE69102249T2

    专利类型

  • 公开/公告日1994-09-15

    原文格式PDF

  • 申请/专利权人 UOP INC US;

    申请/专利号DE1991602249T

  • 发明设计人 ZARCHY ANDREW S US;SYMONIAK MARTIN F US;

    申请日1991-11-29

  • 分类号C07C9/16;C10G67/06;

  • 国家 DE

  • 入库时间 2022-08-22 04:34:46

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