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Method of extraction in continuously operating liquid phase extraction apparatus

机译:在连续操作的液相萃取装置中的萃取方法

摘要

892,783. Liquid phase extraction. ALLMANNA SVENSKA ELEKTRISKA A.B. April 14, 1960 [April 15, 1959], No. 13304/60. Class 46. The extraction apparatus comprises a pulsed column 1. The lighter organic phase introduced at 3 is homogeneous and the transition zone consequently lies at the lower end 2 of the column 1, the heavy phase being introduced at 4. The outflow of the light phase occurs at 5 while the heavy phase leaves mainly at 6. The outflow of the heavy phase may, for example, take place with the help of a pulsing means 9 which is connected to the lower end of the column via a conduit 10. In this case a non- return valve 11 prevents the reflux and the regulation of the flow is carried out with the help of the valve 12, the liquid outflow taking place at 13. A pump can be used for this purpose. A cleaning circuit is connected to the lower end of the column at 14 which is in that plane at which the interface 15 is intended to be, and consists of a filter unit 16 and a level regulating device 17, the object of which is also to distribute the two liquid phases which are led through the filter unit. The device 17 consists of a cylindrical vessel 18 with a riser 19 for the lighter phase and a riser 20 for the heavier phase. The risers are provided with outlets 21 and 22, respectively, which are adjustable vertically. The outlets 21 and 22 are set at such a level that the phases reach the outlet level when the transition zone 15 in the column is at the level of the connection 14 of the branch conduit 23. At the level at which the branch conduit is connected, the column is provided with a guiding screen 24 which conducts the impurities from the transition zone towards the branch conduit. Fig. 2 shows another embodiment of the regulating device 25. Outlets 21 and 22 are at the liquid level reached when the transition zone 15 is at the level of the branch conduit 23. A guiding screen 24 directs the impurities from the transition zone to the branch conduit. Another similar cleaning device is illustrated in Fig. 2 (not shown).
机译:892,783。液相萃取。 ALLMANNA SVENSKA ELEKTRISKA A.B. 1960年4月14日[1959年4月15日],编号13304/60。 46类。萃取设备包括一个脉冲塔1。在3处引入的较轻有机相是均质的,因此过渡区位于塔1的下端2处,重相在4处引入。相发生在5,重相主要在6离开。重相的流出可以例如通过脉冲装置9进行,该脉冲装置通过导管10连接到塔的下端。在这种情况下,止回阀11防止回流,并借助阀12进行流量调节,液体流出发生在13。为此可以使用泵。清洁回路连接到塔柱的下端,在该处位于接口15所处的那个平面上,并由一个过滤器单元16和一个液位调节装置17组成,其目的也在于此。分配被引导通过过滤器单元的两个液相。装置17包括圆柱形容器18,其具有用于较轻阶段的立管19和用于较重阶段的立管20。立管分别设有出口21和22,其可垂直调节。出口21和22被设置在这样的水平,即当塔中的过渡区15在分支导管23的连接14的水平时,相达到出口水平。该塔设有导向筛24,该筛将杂质从过渡区流向分支导管。图2示出了调节装置25的另一实施例。当过渡区15处于分支导管23的高度时,出口21和22处于所达到的液位。导向筛24将杂质从过渡区引导至底部。分支导管。在图2中示出了另一种类似的清洁装置(未示出)。

著录项

  • 公开/公告号GB892783A

    专利类型

  • 公开/公告日1962-03-28

    原文格式PDF

  • 申请/专利权人 ALLMANNA SVENSKA ELEKTRISKA AKTIEBOLAGET;

    申请/专利号GB19600013304

  • 发明设计人

    申请日1960-04-14

  • 分类号B01D11/04;

  • 国家 GB

  • 入库时间 2022-08-23 17:38:57

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