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Process using staggered bypassing of reaction zones for increased capacity

机译:使用交错反应区的旁路以提高产能的方法

摘要

The operation of multistage catalytic hydrocarbon conversion system in which hydrocarbons flow serially through at least two reaction zones is improved by using staggered by-passing of a portion of the change to each zone such that the first zone processes only a first portion of the feed and the second zone processes the remaining portion of the feed and at least a portion of the effluent from the first zone. Where three reaction zones are used, processing of the effluent stream from the first reaction zone is split between the second and third reaction zones so that a portion of the charge to each zone always is directed around the zone and processed in the next reaction zone. One portion of the effluent stream is combined with hydrocarbons that bypassed the first reaction zone, and the combined stream is passed to the second reaction zone. The other portion of the first reaction zone effluent stream and at least a portion of the effluent stream of the second reaction zone are passed to the third reaction zone. This invention is applicable to processes where the first and second reaction zones are susceptible to pinning in that this invention decreases the mass flow through the first and second reaction zones while nevertheless maintaining high hydrocarbon conversion capacity.
机译:多段催化烃转化系统的运行方式得到改善,在该方法中,碳氢化合物连续流经至少两个反应区,方法是通过将一部分变化错开地绕过每个区,使第一区仅处理进料的第一部分和第二区域处理进料的剩余部分和第一区域的流出物的至少一部分。在使用三个反应区的情况下,将来自第一反应区的流出物流的处理在第二和第三反应区之间分开,以使进入每个区的一部分装料始终围绕该区引导并在下一个反应区中进行处理。将一部分流出物流与绕过第一反应区的烃合并,然后将合并的物流通入第二反应区。将第一反应区流出物的另一部分和第二反应区流出物的至少一部分通到第三反应区。本发明适用于其中第一和第二反应区易于钉扎的方法,因为本发明降低了通过第一和第二反应区的质量流量,同时仍保持了高的烃转化能力。

著录项

  • 公开/公告号EP1033398A1

    专利类型

  • 公开/公告日2000-09-06

    原文格式PDF

  • 申请/专利权人 UOP LLC;

    申请/专利号EP19990301627

  • 发明设计人 PETERS KENNETH D.;

    申请日1999-03-04

  • 分类号C10G35/12;C10G59/00;C10G65/00;

  • 国家 EP

  • 入库时间 2022-08-22 01:46:57

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