GB734459A - Method of and apparatus for the breaking down of froth - Google Patents

Method of and apparatus for the breaking down of froth

Info

Publication number
GB734459A
GB734459A GB16880/53A GB1688053A GB734459A GB 734459 A GB734459 A GB 734459A GB 16880/53 A GB16880/53 A GB 16880/53A GB 1688053 A GB1688053 A GB 1688053A GB 734459 A GB734459 A GB 734459A
Authority
GB
United Kingdom
Prior art keywords
froth
gas
vortex
vessel
outlet
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
GB16880/53A
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.)
Stamicarbon BV
Original Assignee
Stamicarbon BV
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 Stamicarbon BV filed Critical Stamicarbon BV
Publication of GB734459A publication Critical patent/GB734459A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C13SUGAR INDUSTRY
    • C13BPRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B25/00Evaporators or boiling pans specially adapted for sugar juices; Evaporating or boiling sugar juices
    • C13B25/02Details, e.g. for preventing foaming or for catching juice
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01JMANUFACTURE OF DAIRY PRODUCTS
    • A01J11/00Apparatus for treating milk
    • A01J11/02Appliances for preventing or destroying foam
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01BBOILING; BOILING APPARATUS ; EVAPORATION; EVAPORATION APPARATUS
    • B01B1/00Boiling; Boiling apparatus for physical or chemical purposes ; Evaporation in general
    • B01B1/02Preventing foaming
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D19/00Degasification of liquids
    • B01D19/02Foam dispersion or prevention
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/10Mixing by creating a vortex flow, e.g. by tangential introduction of flow components
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05BPHOSPHATIC FERTILISERS
    • C05B1/00Superphosphates, i.e. fertilisers produced by reacting rock or bone phosphates with sulfuric or phosphoric acid in such amounts and concentrations as to yield solid products directly
    • C05B1/10Apparatus for the manufacture of superphosphates
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S261/00Gas and liquid contact apparatus
    • Y10S261/54Venturi scrubbers

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Biochemistry (AREA)
  • Animal Husbandry (AREA)
  • Environmental Sciences (AREA)
  • Degasification And Air Bubble Elimination (AREA)

Abstract

may be used. The gas is supplied at low pressure to the chamber and the resultant depression at the core of the vortex aspirates froth from a container 1. The liquid and gas discharged through the outlet 8 are collected in a radially symmetrical vessel 10 where the separation continues. Liquid and gas are discharged from the vessel through outlets 12, 11 respectively. In a modification (Fig. 3, not shown), the rotation chamber is disposed with its outlet uppermost at the bottom of the receiving vessel which has an axial gas outlet at the top and a tangential liquid outlet at the bottom. Suction applied to the outlets of the vessel causes gas to be drawn into the rotation chamber to form the vortex and the depression at the centre of the vortex draws froth into the chamber. In a further modification (Fig. 4, not shown), the rotation chamber and the receiving vessel form a cylindrical unit having a horizontal axis. Before separation the froth may be separated from liquid by the method described in Specification 734,460. A screw conveyer may be used to facilitate the supply of stiff froth to the core of the vortex. Dimensions are given in the Specification.
GB16880/53A 1952-06-19 1953-06-18 Method of and apparatus for the breaking down of froth Expired GB734459A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL170454 1952-06-19

Publications (1)

Publication Number Publication Date
GB734459A true GB734459A (en) 1955-08-03

Family

ID=19750569

Family Applications (1)

Application Number Title Priority Date Filing Date
GB16880/53A Expired GB734459A (en) 1952-06-19 1953-06-18 Method of and apparatus for the breaking down of froth

Country Status (7)

Country Link
US (1) US2813833A (en)
CH (1) CH314629A (en)
DE (1) DE1022189B (en)
ES (1) ES209827A1 (en)
FR (1) FR1084313A (en)
GB (1) GB734459A (en)
NL (1) NL75693C (en)

Families Citing this family (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2838543A (en) * 1957-11-29 1958-06-10 Upjohn Co 6-fluoro steroids and process
DE1168868B (en) * 1958-11-11 1964-04-30 Waldhof Zellstoff Fab Method for breaking foams
DE1083201B (en) * 1958-12-11 1960-06-15 phil Karl Rolf Dietrich Frankfurt/M Dr Cyclone defoamer for nutrient subsrates for growing microorganisms
DE1271677B (en) * 1959-10-08 1968-07-04 Standard Messo Duisburg Device for preventing foam formation in a liquid under vacuum
US3161490A (en) * 1960-11-01 1964-12-15 Edmund F Dudek Gas-liquid separator
US3345803A (en) * 1965-01-07 1967-10-10 Fmc Corp Method and apparatus for degassing viscose
US3420450A (en) * 1965-05-03 1969-01-07 Svenska Cellulosa Ab Nozzle means for breaking foam
US3830041A (en) * 1971-10-20 1974-08-20 Environeering Foam breaker
US4111829A (en) * 1975-07-31 1978-09-05 Societe Nationale Elf Aquitaine (Production) Device for destroying foam
DE3635713A1 (en) * 1986-10-21 1988-04-28 Voith Gmbh J M DEFOAMING PROCESS
NZ226639A (en) * 1987-10-23 1991-04-26 Harrier Gmbh Method and apparatus for producing supersaturated solution of gas in water
DE3900170C2 (en) * 1989-01-05 1994-02-17 Kammerer F Gmbh Method and device for reducing the volume of foam over a liquid in a container
US5015273A (en) * 1990-03-16 1991-05-14 Camco International Inc. Foam breaker and method
FR2661450A1 (en) * 1990-04-30 1991-10-31 Total Petroles Method and device for breaking up foam loaded with debris coming from drilling a well and for recovering the liquid phase from this foam
US5194814A (en) * 1991-05-22 1993-03-16 Tremetrics, Inc. Electrolytic conductivity detector
US7449051B2 (en) * 2005-07-11 2008-11-11 Hewlett-Packard Development Company, L.P. Separation of liquid and gas from froth
CA2724171A1 (en) * 2008-05-15 2009-11-19 Outotec Oyj Apparatus and method for mechanical deaeration
CN109277068B (en) * 2018-11-27 2023-09-22 河钢股份有限公司承德分公司 Reaction device and reaction method for vanadium-chromium co-extraction at normal temperature and normal pressure
EP4382184A1 (en) * 2022-12-06 2024-06-12 Yara International ASA System for breaking a liquid foam and method of operating thereof

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB104183A (en) * 1916-02-16 1918-02-15 Rasmussen & Ernst G M B H Process and Apparatus for Separating Air or Gases from Liquids.
US1440808A (en) * 1920-06-02 1923-01-02 Sullivan Machinery Co Separator
DE541226C (en) * 1925-10-18 1932-01-07 Metallgesellschaft Ag Method and device for evaporating vapor- or gas-releasing liquids
CH136359A (en) * 1927-11-15 1929-11-15 Harald Ledin Sven Method and apparatus for exchanging heat between liquid and gases or vapors, or for cleaning and absorbing gases.
DE615004C (en) * 1933-12-31 1935-06-24 Hartmann A G Maschf Centrifugal dust collector
US2118167A (en) * 1935-12-12 1938-05-24 Micromatic Hone Corp Separator
US2353833A (en) * 1941-07-28 1944-07-18 Garman O Kimmell Separator for treating foamy oil
US2447119A (en) * 1944-06-30 1948-08-17 Harold J Goodyer Device for separating liquid or foreign matter in suspension from fluid under pressure
DE817441C (en) * 1948-10-02 1951-10-18 Chemische Werke Huels G M B H Process and device for defoaming liquids
BE493152A (en) * 1949-01-07
DE855686C (en) * 1949-11-30 1952-11-17 Rosenblads Patenter Ab Device for limiting the foam height of liquids
NL75390C (en) * 1950-10-13 1900-01-01

Also Published As

Publication number Publication date
US2813833A (en) 1957-11-19
NL75693C (en)
DE1022189B (en) 1958-01-09
CH314629A (en) 1956-06-30
ES209827A1 (en) 1953-12-16
FR1084313A (en) 1955-01-18

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