首页> 外国专利> Alkylation process utilizing HF regenerator stream to a multi- tray isoparaffin stripper

Alkylation process utilizing HF regenerator stream to a multi- tray isoparaffin stripper

机译:利用HF再生器流向多塔板异链烷烃汽提塔的烷基化工艺

摘要

In prior art HF alkylation processes, an HR regenerator overhead vapor stream is processed in various ways including combining it with overhead vapor streams of an isoparaffin stripper or an HF stripper, or condensing, settling, and pumping it in a regenerator overhead system to an HF alkylation reaction zone. In the present HF alkylation system comprising a reaction and settling zone, an acid regeneration zone, and a products fractionation zone including an isoparaffin stripper from which a side- cut recycle stream containing principally isoparaffin is withdrawn, an improvement is made by taking overhead vapor from the regenerator and introducing the vapor directly into the isoparaffin stripper at a locus above that at which the side-cut recycle stream is withdrawn.
机译:在现有技术的HF烷基化方法中,以各种方式处理HR再生器塔顶蒸气流,包括将其与异链烷烃汽提器或HF汽提器的塔顶蒸气流合并,或冷凝,沉降,并将其在再生器塔顶系统中泵送至HF。烷基化反应区。在包括反应和沉降区,酸再生区和包括异链烷烃汽提器的产物分馏区的本HF烷基化系统中,主要从异链烷烃中抽出侧馏分再循环料流的异馏分馏出器,是通过从塔顶馏出的塔顶馏出的蒸气中获得的。再生器,并将蒸汽直接引入异链烷烃汽提塔,其位置高于侧馏分回收料流的排出位置。

著录项

  • 公开/公告号US3956416A

    专利类型

  • 公开/公告日1976-05-11

    原文格式PDF

  • 申请/专利权人 UNIVERSAL OIL PRODUCTS COMPANY;

    申请/专利号US19740533421

  • 发明设计人 BIPIN V. VORA;

    申请日1974-12-16

  • 分类号C07C3/54;

  • 国家 US

  • 入库时间 2022-08-23 01:33:06

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