首页> 外国专利> SOLVENT EXTRACTION PROCESS INVOLVING MEMBRANE SEPARATION OF EXTRACT PHASE AND/OR INTERMEDIATE ZONE PHASE WITH PSEUDO EXTRACT/PSEUDO RAFFINATE RECYCLE

SOLVENT EXTRACTION PROCESS INVOLVING MEMBRANE SEPARATION OF EXTRACT PHASE AND/OR INTERMEDIATE ZONE PHASE WITH PSEUDO EXTRACT/PSEUDO RAFFINATE RECYCLE

机译:涉及萃取相和/或中间区相的膜分离的溶剂萃取过程,采用伪萃取/伪萃取残液回收

摘要

The solvent extraction of aromatics containing oil using a selective aromatics extraction solvent to produce an aromatics rich extract phase and an oil rich/aromatics lean raffinate is improved by the steps of subjecting the extract phase to a membrane separation step to produce a permeate phase and a retentate phase passing the retentate phase to a settling zone wherein the retentate phase spontaneously separates into two liquid phases, and recycling the upper phase to the extraction zone, either to the feed inlet or to the bottom of the extract reflux zone to thereby increase the raffinate oil recovered from the extraction tower. Alternatively or in addition to the above, a side stream can be taken from an intermediate zone of the extraction zone (e.g. extraction tower) and fed to a membrane separation to produce a solvent rich permeate and an oil rich retentate. The solvent rich permeate is recycled while the oil rich retentate is fed to a settling zone wherein it will spontaneously separate into an oil rich pseudo raffinate upper phase which is recovered and into a solvent rich pseudo extract bottoms phase which is recycled to the solvent extraction zone, preferably at a point below that at which the side stream was withdrawn. The membrane separation zone preferably employs interfacially polymerized membranes under reverse osmosis conditions.
机译:使用选择性芳烃萃取溶剂萃取含芳烃油的溶剂以产生富含芳烃的萃取相和富含油/芳烃的贫萃余液的步骤通过将萃取相进行膜分离步骤以产生渗透物相和溶剂的步骤得到改进。截留相通过截留相进入沉降区,其中截留相自发分离为两个液相,并将上层相再循环至萃取区,送入进料口或萃取物回流区的底部,从而增加萃余液从萃取塔回收的石油。作为上述的替代或补充,可以从萃取区的中间区(例如萃取塔)中取侧流并进料到膜分离器中以产生富溶剂的渗透物和富油的渗余物。将富含溶剂的渗透物再循环,同时将富含油的渗余物进料到沉降区,在那里它将自发地分离成富含油的拟萃余液上部相,将其回收并分离为富含溶剂的拟萃取物残渣相,将其再循环到溶剂萃取区,优选在低于支流流出的点。膜分离区优选在反渗透条件下采用界面聚合的膜。

著录项

  • 公开/公告号CA2054046A1

    专利类型

  • 公开/公告日1992-05-06

    原文格式PDF

  • 申请/专利权人 IMPERIAL OIL;

    申请/专利号CA19912054046

  • 发明设计人 WELMERS ADRIANUS;BLACK LAURA E.;

    申请日1991-10-23

  • 分类号C10G21/00;B01D61/14;B01D71/60;C10G21/28;

  • 国家 CA

  • 入库时间 2022-08-22 05:32:11

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