GB892783A - Method of extraction in continuously operating liquid phase extraction apparatus - Google Patents

Method of extraction in continuously operating liquid phase extraction apparatus

Info

Publication number
GB892783A
GB892783A GB13304/60A GB1330460A GB892783A GB 892783 A GB892783 A GB 892783A GB 13304/60 A GB13304/60 A GB 13304/60A GB 1330460 A GB1330460 A GB 1330460A GB 892783 A GB892783 A GB 892783A
Authority
GB
United Kingdom
Prior art keywords
level
column
phase
transition zone
branch conduit
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB13304/60A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ABB Norden Holding AB
Original Assignee
ASEA AB
Allmanna Svenska Elektriska AB
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by ASEA AB, Allmanna Svenska Elektriska AB filed Critical ASEA AB
Publication of GB892783A publication Critical patent/GB892783A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D11/00Solvent extraction
    • B01D11/04Solvent extraction of solutions which are liquid
    • B01D11/0484Controlling means

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Extraction Or Liquid Replacement (AREA)

Abstract

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).
GB13304/60A 1959-04-15 1960-04-14 Method of extraction in continuously operating liquid phase extraction apparatus Expired GB892783A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SE892783X 1959-04-15

Publications (1)

Publication Number Publication Date
GB892783A true GB892783A (en) 1962-03-28

Family

ID=20377977

Family Applications (1)

Application Number Title Priority Date Filing Date
GB13304/60A Expired GB892783A (en) 1959-04-15 1960-04-14 Method of extraction in continuously operating liquid phase extraction apparatus

Country Status (1)

Country Link
GB (1) GB892783A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2558594C1 (en) * 2014-08-04 2015-08-10 Валерий Павлович Дробаденко Method of conducting mass-transfer processes and apparatus therefor
CN113372999A (en) * 2021-07-27 2021-09-10 河南省商业科学研究所有限责任公司 Peony essential oil extraction device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2558594C1 (en) * 2014-08-04 2015-08-10 Валерий Павлович Дробаденко Method of conducting mass-transfer processes and apparatus therefor
CN113372999A (en) * 2021-07-27 2021-09-10 河南省商业科学研究所有限责任公司 Peony essential oil extraction device
CN113372999B (en) * 2021-07-27 2023-09-01 河南省商业科学研究所有限责任公司 Peony essential oil extraction device

Similar Documents

Publication Publication Date Title
US2706045A (en) Liquid separation
GB1066532A (en) Removal of dross from molten metal
US2394968A (en) Vitamin concentration
GB892783A (en) Method of extraction in continuously operating liquid phase extraction apparatus
GB835511A (en) Varnish conveying apparatus adapted for use in a varnish pouring machine
FR2438677A1 (en) CLOSED LOOP VACUUM FRACTIONATION PROCESS
SE8400068L (en) CONTINUOUS SEPARATION DEVICE AND PROCEDURE FOR SEPARATING EASY AND HEAVY LIQUID COMPONENTS
US3362791A (en) Apparatus for separation of immiscible liquid pairs including remote interface control
GB934570A (en) Electro-erosion machining apparatus
ES355539A1 (en) Method of optimum operating a sedimentation apparatus and a device for carrying out the method
EP0182110A3 (en) Device for the generation of a stable emulsion for use in cleaning and decontamination equipments
GB874927A (en) Fuel filter and water separator unit
US3189531A (en) Distillation column for vacuum and pressure operations
GB976521A (en) Liquid filter
DE2418046A1 (en) DEVICE FOR REGULATING THE LIQUID LEVEL
EP0127405A2 (en) Improved flow control apparatus
GB1511059A (en) Separator apparatus for separating liquids
GB963117A (en) Improvements relating to apparatus for contacting liquids
GB1172616A (en) Apparatus for Separating Liquid Particles from Gas Streams.
GB907499A (en) Improvements in or relating to the separation of immiscible liquids of differing specific gravities
GB1092591A (en) Submersible pumping apparatus
US2729340A (en) Drain and emulsion preserving arrangement for clarifiers
GB549683A (en) Improvements in or relating to extraction apparatus
JPS57184668A (en) Barrel polishing device
GB1021736A (en) An apparatus for separating a mixture into its components