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Hydrocracking processes having an enhanced efficiency of hydrogen utilization

机译:加氢裂化工艺具有更高的氢气利用率

摘要

A hydrocrackate (14) from a hydrocracking zone (10) operating under hydrocracking conditions is separated into vapor phase has a greater concentration of hydrogen than the minimum concentration of hydrogen in the vapor phase in the hydrocraking zone. at least a portion of the separated vapor phase (22) is contacted with the feed side of a polymeric membrane in a permeator (28), the membrane being selective to the permeation of hydrogen as compared to the permeation of methane, and the opposite side of the polymeric membrane is maintained at a pressure sufficiently below the pressure at the feed side of the polymeric membrane to permeate hydrogen to the opposite side of the polymeric membrane and to provide a hydrogen permeate (30) having a concentration of hydrogen greater than the concentration of hydrogen in the separated vapor phase (22) and greater than the concentration of hydrogen feed gas (44, 46). The hydrogen permeate (30) is compressed and recycled to the hydrocracking zone (10).
机译:来自在加氢裂化条件下操作的加氢裂化区(10)的加氢裂化物(14)被分离成具有比加氢裂化区中的气相中的最小氢浓度更高的氢浓度的气相。至少一部分分离的气相(22)在渗透器(28)中与聚合物膜的进料侧接触,与甲烷的渗透相比,该膜对氢的渗透具有选择性,而相反侧将聚合物膜的第二部分保持在足够低于聚合物膜进料侧压力的压力下,以使氢渗透到聚合物膜的另一侧,并提供氢浓度大于该浓度的氢渗透物(30)。在分离的气相(22)中的氢含量大于氢气进料气(44,46)的浓度。渗透氢(30)被压缩并循环到加氢裂化区(10)。

著录项

  • 公开/公告号EP0061259A1

    专利类型

  • 公开/公告日1982-09-29

    原文格式PDF

  • 申请/专利权人 MONSANTO COMPANY;

    申请/专利号EP19820301236

  • 发明设计人 MACLEAN DONALD LEWIS GAGE;

    申请日1982-03-11

  • 分类号C10G49/22;C10G47/00;C01B3/50;

  • 国家 EP

  • 入库时间 2022-08-22 13:05:15

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