GB734459A - Method of and apparatus for the breaking down of froth - Google Patents
Method of and apparatus for the breaking down of frothInfo
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B25/00—Evaporators or boiling pans specially adapted for sugar juices; Evaporating or boiling sugar juices
- C13B25/02—Details, e.g. for preventing foaming or for catching juice
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01J—MANUFACTURE OF DAIRY PRODUCTS
- A01J11/00—Apparatus for treating milk
- A01J11/02—Appliances for preventing or destroying foam
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01B—BOILING; BOILING APPARATUS ; EVAPORATION; EVAPORATION APPARATUS
- B01B1/00—Boiling; Boiling apparatus for physical or chemical purposes ; Evaporation in general
- B01B1/02—Preventing foaming
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/02—Foam dispersion or prevention
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/10—Mixing by creating a vortex flow, e.g. by tangential introduction of flow components
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05B—PHOSPHATIC FERTILISERS
- C05B1/00—Superphosphates, 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
- C05B1/10—Apparatus for the manufacture of superphosphates
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S261/00—Gas and liquid contact apparatus
- Y10S261/54—Venturi 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.
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)
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)
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 |
-
0
- NL NL75693D patent/NL75693C/xx active
-
1953
- 1953-06-17 CH CH314629D patent/CH314629A/en unknown
- 1953-06-17 ES ES0209827A patent/ES209827A1/en not_active Expired
- 1953-06-17 FR FR1084313D patent/FR1084313A/en not_active Expired
- 1953-06-17 US US362305A patent/US2813833A/en not_active Expired - Lifetime
- 1953-06-18 DE DEST6592A patent/DE1022189B/en active Pending
- 1953-06-18 GB GB16880/53A patent/GB734459A/en not_active Expired
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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