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Method of recovering phenol from a BPA production facility and the facility for recovering the same

机译:从双酚A生产设备中回收苯酚的方法及其回收设备

摘要

In an embodiment, a method of recovering an unreacted phenol from a bisphenol A production facility comprises reacting an initial phenol and an initial acetone in the presence of a catalyst to produce a bisphenol A stream comprising the unreacted phenol of the initial phenol and a bisphenol A, separating a purge stream comprising the unreacted phenol, and wherein the unreacted phenol is present in the purge stream in an amount of 60 to 90 wt %, based on the total weight of the purge stream; adding the purge stream to a phenol purification section of a phenol production facility; and forming a purified phenol outlet stream in the phenol purification section, wherein the purified phenol outlet stream comprises a total phenol concentration of greater than or equal to 99.5 wt % based on the total weight of the purified phenol outlet stream.
机译:在一个实施方案中,从双酚A生产设施中回收未反应的苯酚的方法包括在催化剂的存在下使初始苯酚和初始丙酮反应以产生包含初始苯酚和双酚A的未反应苯酚的双酚A料流。 ,分离包含未反应的苯酚的吹扫物流,其中基于吹扫物流的总重量,未反应的苯酚以60至90wt%的量存在于吹扫物流中;将吹扫料流加入苯酚生产设备的苯酚纯化段;在苯酚纯化段中形成纯化的苯酚出口物流,其中,基于纯化的苯酚出口物流的总重量,纯化的苯酚出口物流包含的总苯酚浓度大于或等于99.5重量%。

著录项

  • 公开/公告号US10246391B2

    专利类型

  • 公开/公告日2019-04-02

    原文格式PDF

  • 申请/专利权人 SABIC GLOBAL TECHNOLOGIES B.V.;

    申请/专利号US201615757070

  • 申请日2016-11-22

  • 分类号C07C37/00;C07C37/08;C07C37/20;C07C37/68;C07C37/74;C07C37/80;C07C37/84;C07C39/04;C07C39/16;

  • 国家 US

  • 入库时间 2022-08-21 12:11:15

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