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The process of the reform of operation

机译:运作改革的过程

摘要

1421339 Catalyst discharge in reforming process U O P INC 13 Dec 1972 [14 Dec 1971] 57421/72 Heading B1F [Also in Divisions C4 and C5] A reforming process comprises (a) charging a hydrogen-hydrocarbon mixture to a reforming reactor containing a moving bed of platinum group metal catalyst particles at reforming conditions, (b) withdrawing a hydrocarbon stream from the reactor and separately withdrawing used catalyst particles from the reactor through a plurality of catalyst transfer conduits to a catalyst collector, (c) continuously charging a hydrogen rich gas, e.g. recycle gas, to the collector to preclude the passage of hydrocarbons from the reactor through the transfer conduits, the hydrogen-rich gas passing through the conduits into the reactor to be withdrawn therefrom in admixture with the hydrocarbon stream, (d) periodically increasing the flow of the hydrogen rich gas to the collector to preclude the passage of catalyst through the conduits, and withdrawing used catalyst from the collector and (e) adding a quantity of active platinum group metal catalyst to the reactor substantially equivalent to the quantity withdrawn from it to maintain a substantially constant catalyst inventary therein, the reactor remaining on stream at reforming conditions during the addition of said active catalyst to it and withdrawal of used catalyst from it. The process may be carried out in a series of side by side vertical reactors through which the catalyst and hydrocarbon pass generally downward, but the hydrocarbon passes laterally through an annular catalyst bed, and the catalyst and hydrocarbon may move cocurrently or countercurrently between reactors.
机译:1421339重整过程中的催化剂排放UOP INC 1972年12月13日[1971年12月14日] 57421/72标题B1F [也在C4和C5分区中]重整过程包括(a)将氢-烃混合物装入包含移动床的重整反应器中重整条件下的铂族金属催化剂颗粒的制备,(b)从反应器中抽出烃物流,并通过多个催化剂转移管道分别从反应器中抽出用过的催化剂颗粒到催化剂收集器,(c)连续充入富氢气体,例如再循环气体进入收集器,以防止烃类从反应器通过传输管道的通过,富氢气体通过管道进入反应器,并与碳氢化合物流混合从反应器中抽出,(d)定期增加流量将富氢气体送入收集器以防止催化剂通过导管,并从收集器中抽出用过的催化剂,以及(e)向反应器中添加与从反应器中取出的量基本相等的活性铂族金属催化剂保持其中的催化剂库存基本恒定,在向其中加入活性催化剂和从中取出用过的催化剂的过程中,反应器在重整条件下保持运转。该方法可以在一系列并排的垂直反应器中进行,催化剂和烃通常向下通过该反应器,但是烃横向地通过环形催化剂床,并且催化剂和烃可以在反应器之间并流或逆流移动。

著录项

  • 公开/公告号BR7208793D0

    专利类型

  • 公开/公告日1973-09-25

    原文格式PDF

  • 申请/专利权人 UNIVERSAL OIL PROD CO;

    申请/专利号BR19720879372

  • 发明设计人 CRENWOOD A;VESELY K;

    申请日1972-12-13

  • 分类号C10G35/08;

  • 国家 BR

  • 入库时间 2022-08-23 07:41:49

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