GB995767A - Improvements in and relating to arrangements for contacting liquids - Google Patents

Improvements in and relating to arrangements for contacting liquids

Info

Publication number
GB995767A
GB995767A GB32272/62A GB3227262A GB995767A GB 995767 A GB995767 A GB 995767A GB 32272/62 A GB32272/62 A GB 32272/62A GB 3227262 A GB3227262 A GB 3227262A GB 995767 A GB995767 A GB 995767A
Authority
GB
United Kingdom
Prior art keywords
liquid
column
line
phase liquid
pump
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
GB32272/62A
Inventor
Leslie Clunn
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.)
SPX Flow Technology Crawley Ltd
Original Assignee
APV Corp Ltd
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
Priority to NL296909D priority Critical patent/NL296909A/xx
Application filed by APV Corp Ltd filed Critical APV Corp Ltd
Priority to GB32272/62A priority patent/GB995767A/en
Publication of GB995767A publication Critical patent/GB995767A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/28Moving reactors, e.g. rotary drums
    • B01J19/285Shaking or vibrating reactors; reactions under the influence of low-frequency vibrations or pulsations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D11/00Solvent extraction
    • B01D11/04Solvent extraction of solutions which are liquid
    • B01D11/0426Counter-current multistage extraction towers in a vertical or sloping position
    • B01D11/043Counter-current multistage extraction towers in a vertical or sloping position with stationary contacting elements, sieve plates or loose contacting elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D11/00Solvent extraction
    • B01D11/04Solvent extraction of solutions which are liquid
    • B01D11/0426Counter-current multistage extraction towers in a vertical or sloping position
    • B01D11/0438Counter-current multistage extraction towers in a vertical or sloping position comprising vibrating mechanisms, electromagnetic radiations
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18Stationary reactors having moving elements inside
    • B01J19/185Stationary reactors having moving elements inside of the pulsating type
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00182Controlling or regulating processes controlling the level of reactants in the reactor vessel

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

<PICT:0995767/C1/1> An arrangement for contacting liquids comprises a liquid contacting apparatus and pumping apparatus for producing a pulsed feed of one stream of liquid through the contacting apparatus, the pumping apparatus comprising a continual flow pump means associated with valve means for cyclically varying the flow of liquid through a discharge conduit attached either to the pump means or the contacting apparatus communicating with and supplied with liquid from the pump means, thereby correspondingly varying the pressure in the contacting apparatus to produce pulsations in the flow therethrough. Contact between a dispersed phase liquid supplied through a line 3 and a continuous phase liquid supplied through a line 37 is effected in a column 1, the contact being facilitated by the provision of perforated plates 2 in conjunction with the application of pulsations to the continuous phase liquid. The continuous phase liquid is supplied by a pipe 13 to a reservoir 12, from which a centrifugal or rotary positive displacement pump 11 delivers it via the line 37 to the column 1, near the base of the latter. The continuous phase liquid is discharged near the top of the column 1 via a line 8, while the dispersed phase liquid is discharged from the bottom of the column via a line 31 which delivers it to the reservoir 12, where it separates from the continuous phase liquid into a heavy bottom layer 33, where it is discharged via a line 35. The rates of discharge through the lines 8 and 35 are controlled by valves 21 and 36 which are automatically actuated by liquid level controllers 22 and 34 respectively to maintain constant levels of the two liquids in the reservoir 12. Pulsations are imposed on the liquid flow through the column 1 by means of a rotating valve 32 in the line 31, the frequency of the pulsations being variable by varying the speed of the motor rotating the valve. The amplitude of the pulsations can be varied by adjusting a valve 38 in the line 37 if the pump 11 is of centrifugal type, or by altering the speed of the pump rotor if the pump is of rotary positive-displacement type. The space above the liquid in the column 1 is filled with air or other gas which acts as a buffer for the pulsations. In another embodiment, the dispersed phase liquid is not delivered to the reservoir 12, and separation of it from the continuous phase liquid is effected at the base of the column 1. In this case, the pump 11 takes its supply from the bottom of the reservoir 12, and the rotating valve for producing pulsations in the liquid flow is contained in a by-pass line connected between the pump discharge line and the reservoir 12. In either embodiment, the continuous phase liquid may be the heavier of the two liquids, in which case the lighter liquid is introduced at the base of the column (above the entry point of the continuous phase liquid) and is broken into a fine dispersion which travels up the column, separating into a surface layer and being removed at the top of the column. Specification 995,766 is referred to.
GB32272/62A 1962-08-22 1962-08-22 Improvements in and relating to arrangements for contacting liquids Expired GB995767A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
NL296909D NL296909A (en) 1962-08-22
GB32272/62A GB995767A (en) 1962-08-22 1962-08-22 Improvements in and relating to arrangements for contacting liquids

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB32272/62A GB995767A (en) 1962-08-22 1962-08-22 Improvements in and relating to arrangements for contacting liquids

Publications (1)

Publication Number Publication Date
GB995767A true GB995767A (en) 1965-06-23

Family

ID=10336026

Family Applications (1)

Application Number Title Priority Date Filing Date
GB32272/62A Expired GB995767A (en) 1962-08-22 1962-08-22 Improvements in and relating to arrangements for contacting liquids

Country Status (2)

Country Link
GB (1) GB995767A (en)
NL (1) NL296909A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GR1002882B (en) * 1997-01-23 1998-03-24 . Method and arrangement for induced pulsing flow in trickle bed columns.
EP1095700A1 (en) * 1999-10-29 2001-05-02 Dr. Frische GmbH Process for performing a multiphase reaction of a liquid and a gas phase in countercurrent flow and apparatus therefore
WO2006136850A1 (en) * 2005-06-23 2006-12-28 Nitech Solutions Limited Method and apparatus for fluid-liquid reactions
WO2007058544A1 (en) * 2005-11-17 2007-05-24 Fluens Synthesis As Continiuous flow reactor

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GR1002882B (en) * 1997-01-23 1998-03-24 . Method and arrangement for induced pulsing flow in trickle bed columns.
EP1095700A1 (en) * 1999-10-29 2001-05-02 Dr. Frische GmbH Process for performing a multiphase reaction of a liquid and a gas phase in countercurrent flow and apparatus therefore
US6512131B1 (en) 1999-10-29 2003-01-28 Dr. Frische Gmbh Process for carrying out multi-phase reactions according to the counter current principle of a liquid and gaseous phase and apparatus for carrying out the process
WO2006136850A1 (en) * 2005-06-23 2006-12-28 Nitech Solutions Limited Method and apparatus for fluid-liquid reactions
WO2007058544A1 (en) * 2005-11-17 2007-05-24 Fluens Synthesis As Continiuous flow reactor

Also Published As

Publication number Publication date
NL296909A (en)

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