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, preferably employing interfacially polymerized membranes

Solvent extraction process involving membrane separation of extract phase and/or intermediate zone phase with pseudo extract/pseudo raffinate recycle, preferably employing interfacially polymerized membranes

机译:溶剂萃取工艺包括采用伪萃取物/伪萃余液循环进行萃取相和/或中间区相的膜分离,优选采用界面聚合膜

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phase which is recycled to the solvent extraction zone, preferably at a point below that at which the side stream was withdrawn.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:通过使萃取相经历膜分离步骤以产生渗透相和水相的步骤,改进了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/芳烃的贫提余液的步骤。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。

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