GB1343815A - Method and apparatus for the removal of entrained gases from liquids or from slurries of solids liquids and gases - Google Patents
Method and apparatus for the removal of entrained gases from liquids or from slurries of solids liquids and gasesInfo
- Publication number
- GB1343815A GB1343815A GB1041271*[A GB1041271A GB1343815A GB 1343815 A GB1343815 A GB 1343815A GB 1041271 A GB1041271 A GB 1041271A GB 1343815 A GB1343815 A GB 1343815A
- Authority
- GB
- United Kingdom
- Prior art keywords
- chamber
- tank
- gas
- slurry
- vacuum
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0042—Degasification of liquids modifying the liquid flow
- B01D19/0052—Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused
-
- 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
- Y10S494/00—Imperforate bowl: centrifugal separators
- Y10S494/90—Imperforate bowl: centrifugal separators involving mixture containing one or more gases
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Degasification And Air Bubble Elimination (AREA)
- Treatment Of Sludge (AREA)
Abstract
1343815 Centrifugal separators AUTOMETRICS CO 21 April 1971 [6 May 1970] 10412/71 Heading B2P [Also in Division F2] An apparatus for degassing a liquid or a slurry of suspended solid particles having gas entrained therein comprises a liquid-receiving tank 12, a rotary chamber 62 within the tank with one or more apertures 68 in its periphery for the discharge of degassed liquid or slurry into the tank below the normal liquid level therein, means 76 for introducing the liquid or slurry into the chamber, an outlet in the chamber for separated gas, and vacuum means communicating with the gas outlet to extract the separated gas from the chamber and maintain a vacuum therein. The top of the tank 12 carries a support plate 18 to which is secured a cylindrical extension 22 closed by a top 23 having a central opening 24. The chamber 62 is in the form of a pair of spherical segments, as shown, or of a double cone. The inner and outer walls of the chamber are covered by a coating 63 of elastomer to resist abrasion and the bottom has a clean-out opening 64 closable by a cover 66. The chamber is secured to a tubular member 60 which is screw-threaded to the lower end of a tubular drive shaft 44 supported in bearings 40, 42 in a housing 30 which is secured to the support plate 18 and which has an apertured plate 48 secured to its top. Elastomer ring seals are provided at 46 and 54. The shaft 44 is driven by an electric motor 100 through belt 28 and pulleys 58, 106. A cap 70 extends through the opening 24 in the top 23 and has a central bore 72 in which are threaded a valved inlet pipe 16 and a feed pipe 76 which passes through the tubular shaft 44 and the member 60 and extends into the chamber 62 just above its bottom. The cap 70 has a passage 88 communicating at one end with a vacuum line 90 and at the other end with the annular space 87 within the tubular shaft so that by connecting the line 90 to a vacuum pump the separated, gas can be removed from chamber 62 and a vacuum created therein. Gas-tightness is provided between the space 87 and the ambient atmosphere by a spring-loaded seal 80 (see Division F2) which is lubricated by lubricant supplied through a channel 118 in cap 70. The interior of the tank 12 has radial baffles 92, 94 above and below chamber 62. A horizontal baffle 96 is positioned above the chamber 62 and below the normal liquid level indicated at 98. A pipe 108, 110 is connected to an outlet 14 of the tank and to a chamber 112 which contains instrumentation for measurement of a parameter of the degassed liquid or slurry and which has an overflow 114 which establishes the normal liquid level 98 in the tank. Further level control is provided by an over flow weir 116 in the wall of the tank.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US3494970A | 1970-05-06 | 1970-05-06 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1343815A true GB1343815A (en) | 1974-01-16 |
Family
ID=21879655
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1041271*[A Expired GB1343815A (en) | 1970-05-06 | 1971-04-21 | Method and apparatus for the removal of entrained gases from liquids or from slurries of solids liquids and gases |
Country Status (5)
Country | Link |
---|---|
US (1) | US3768726A (en) |
CA (1) | CA948998A (en) |
DE (1) | DE2120140A1 (en) |
FR (1) | FR2091248A5 (en) |
GB (1) | GB1343815A (en) |
Families Citing this family (29)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3847327A (en) * | 1973-06-04 | 1974-11-12 | Kobe Inc | Centrifugal separator |
US3973930A (en) * | 1973-10-09 | 1976-08-10 | Burgess Harry L | Drilling mud degasser apparatus and method |
DE3008589A1 (en) * | 1980-03-06 | 1981-09-10 | Bayer Ag, 5090 Leverkusen | MECHANICAL FOAM DESTROYER AND METHOD FOR MECHANICAL FOAM DESTROYER |
US4402715A (en) * | 1981-12-23 | 1983-09-06 | Autoclave Engineers, Inc. | Gas/oil separator |
US5387278A (en) * | 1992-07-20 | 1995-02-07 | Grumman Aerospace Corporation | Air-liquid separator assembly and system |
SE514134C2 (en) * | 1999-04-07 | 2001-01-08 | Alfa Laval Ab | Separating device for purifying a liquid from suspended or liquid particles suspended therein which are lighter and / or heavier than the liquid |
SE521578C2 (en) * | 2002-03-21 | 2003-11-11 | Alfa Laval Corp Ab | centrifugal |
US6726743B2 (en) | 2002-06-18 | 2004-04-27 | 3M Innovative Properties Company | Electrostatic deaeration method and apparatus |
US7488448B2 (en) * | 2004-03-01 | 2009-02-10 | Indian Wells Medical, Inc. | Method and apparatus for removal of gas bubbles from blood |
US9614772B1 (en) | 2003-10-20 | 2017-04-04 | F5 Networks, Inc. | System and method for directing network traffic in tunneling applications |
US7210898B2 (en) * | 2004-10-15 | 2007-05-01 | Lloyd Hubbard | Gas removal from a centrifugal pump |
US8418233B1 (en) | 2005-07-29 | 2013-04-09 | F5 Networks, Inc. | Rule based extensible authentication |
US8533308B1 (en) | 2005-08-12 | 2013-09-10 | F5 Networks, Inc. | Network traffic management through protocol-configurable transaction processing |
US8565088B1 (en) | 2006-02-01 | 2013-10-22 | F5 Networks, Inc. | Selectively enabling packet concatenation based on a transaction boundary |
US9106606B1 (en) | 2007-02-05 | 2015-08-11 | F5 Networks, Inc. | Method, intermediate device and computer program code for maintaining persistency |
US7935102B2 (en) * | 2007-12-21 | 2011-05-03 | Indian Wells Medical, Inc | Method and apparatus for prevention of catheter air intake |
US20110067568A1 (en) * | 2008-05-15 | 2011-03-24 | Outotec Oyj | Apparatus and method for mechanical deaeration |
US9832069B1 (en) | 2008-05-30 | 2017-11-28 | F5 Networks, Inc. | Persistence based on server response in an IP multimedia subsystem (IMS) |
US9130846B1 (en) | 2008-08-27 | 2015-09-08 | F5 Networks, Inc. | Exposed control components for customizable load balancing and persistence |
US8366809B2 (en) | 2011-03-14 | 2013-02-05 | Hamilton Sundstrand Corporation | Deaerating method and assembly |
US8444751B2 (en) | 2011-06-17 | 2013-05-21 | Hamilton Sundstrand Corporation | Deaerator and conduit assembly |
CN104040114B (en) | 2012-01-03 | 2017-05-31 | 埃克森美孚上游研究公司 | The method that hydro carbons is produced using solution cavity |
US9920880B2 (en) | 2012-01-16 | 2018-03-20 | Hamilton Sundstrand Corporation | Deaerating assembly |
MY167926A (en) * | 2012-07-27 | 2018-10-03 | Exxonmobil Upstream Res Co | Multiphase separation system cross-reference to related application |
US9371724B2 (en) | 2012-07-27 | 2016-06-21 | Exxonmobil Upstream Research Company | Multiphase separation system |
US9528335B2 (en) * | 2013-05-20 | 2016-12-27 | Halliburton Energy Services, Inc. | Air-driven degasser assembly |
BR112016019671B1 (en) | 2014-03-12 | 2020-01-07 | Exxonmobil Upstream Research Company | Submarine multiphase separation system and method for separating oil, water, and solid particles in a multiphase fluid |
DK179731B1 (en) | 2014-04-29 | 2019-04-26 | Exxonmobil Upstreamresearch Company | Multiphase separation system |
SG11201702668RA (en) | 2014-11-17 | 2017-06-29 | Exxonmobil Upstream Res Co | Liquid collection system |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1056233A (en) * | 1912-06-12 | 1913-03-18 | Lamartine C Trent | Apparatus for separating solids from liquid solutions. |
US2592680A (en) * | 1946-05-14 | 1952-04-15 | American Viscose Corp | Apparatus for removal of gases from liquids |
US2878992A (en) * | 1956-12-28 | 1959-03-24 | Beckman Instruments Inc | Centrifuge apparatus and rotor therefor |
US3012710A (en) * | 1957-10-30 | 1961-12-12 | Westfalia Separator Ag | Centrifugal separator having lining of elastomer material |
GB1027338A (en) * | 1962-04-26 | 1966-04-27 | Cav Ltd | Separators |
US3255958A (en) * | 1962-12-04 | 1966-06-14 | Westfalia Separator Ag | Centrifugal desludging separator |
US3294317A (en) * | 1963-11-27 | 1966-12-27 | Ohg E Fonderie A Bosco S P A | Device for opening the discharge opening of a hydroextractor and concurrently locking the extractor |
US3296776A (en) * | 1964-10-30 | 1967-01-10 | Atlantic Refining Co | Apparatus for separating gases from liquids |
US3536254A (en) * | 1968-12-16 | 1970-10-27 | Marathon Oil Co | Fluid separator |
US3616992A (en) * | 1969-06-06 | 1971-11-02 | James S Deacon | Partial vacuum centrifugal separator |
-
1970
- 1970-05-06 US US00034949A patent/US3768726A/en not_active Expired - Lifetime
-
1971
- 1971-04-21 GB GB1041271*[A patent/GB1343815A/en not_active Expired
- 1971-04-24 DE DE19712120140 patent/DE2120140A1/en active Pending
- 1971-04-27 CA CA111,414A patent/CA948998A/en not_active Expired
- 1971-05-05 FR FR7116231A patent/FR2091248A5/fr not_active Expired
Also Published As
Publication number | Publication date |
---|---|
CA948998A (en) | 1974-06-11 |
DE2120140A1 (en) | 1971-11-18 |
FR2091248A5 (en) | 1972-01-14 |
US3768726A (en) | 1973-10-30 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed [section 19, patents act 1949] | ||
PCNP | Patent ceased through non-payment of renewal fee |