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Process for simultaneous separation of aromatics from heavy and light hydrocarbon streams

机译:同时从重烃和轻烃物流中分离芳香烃的方法

摘要

A process for the simultaneous separation of aromatics and non- aromatics from a heavy hydrocarbon stream and a light hydrocarbon stream in which process:PP(a) aromatics are extracted in a first extractor from the heavy hydrocarbon stream with the aid of a selective solvent which has a higher boiling point than that of said light hydrocarbon stream,PP(b) selective solvent is removed from the raffinate obtained from said first extractor, to yield heavy non- aromaticsPP(c) aromatics are extracted from the light hydrocarbon stream in a second extractor with the aid of the extract phase obtained from the first extractor,PP(d) selective solvent is removed from the raffinate obtained from said second extractor to yield heavy aromatics and light non-aromaticsPP(e) the extract phase from the second extractor is subjected to extractive distillation,PP(f) the bottom fraction of the extractive distillation is separated by distillation into light aromatics and selective solvent, andPP(g) the selective solvent obtained in step (f) is at least partially recycled to the first extractor.
机译:同时从重烃流和轻烃流中分离芳族化合物和非芳族化合物的方法,其中方法:在第一萃取器中借助辅助设备从重烃流中提取

(a)芳族化合物。在沸点高于所述轻烃物流沸点的选择性溶剂中,从所述第一萃取器得到的萃余液中除去P(P)(b)选择性溶剂,得到重的非芳族化合物在从第一萃取器获得的萃取相的帮助下,在第二萃取器中从轻烃物流中萃取出P>(c)芳族化合物,从所述第二萃取器获得的萃余液中除去

(d)选择性溶剂。提取重质芳烃和轻质非芳族化合物的萃取器(e)将第二个萃取器的萃取相进行萃取蒸馏,分离出萃取蒸馏塔的底部馏分通过蒸馏成轻质芳烃和选择性溶胶将步骤(f)中获得的选择性溶剂至少部分再循环至第一萃取器。

著录项

  • 公开/公告号US4428829A

    专利类型

  • 公开/公告日1984-01-31

    原文格式PDF

  • 申请/专利权人 SHELL OIL COMPANY;

    申请/专利号US19810301493

  • 发明设计人 WALTER C. G. KOSTERS;

    申请日1981-09-14

  • 分类号C10G21/02;C10G21/22;

  • 国家 US

  • 入库时间 2022-08-22 08:39:51

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