GB680244A - Improved electrical process for breaking emulsions - Google Patents
Improved electrical process for breaking emulsionsInfo
- Publication number
- GB680244A GB680244A GB5360/50A GB536050A GB680244A GB 680244 A GB680244 A GB 680244A GB 5360/50 A GB5360/50 A GB 5360/50A GB 536050 A GB536050 A GB 536050A GB 680244 A GB680244 A GB 680244A
- Authority
- GB
- United Kingdom
- Prior art keywords
- zone
- line
- emulsion
- oil
- phase
- 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
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G33/00—Dewatering or demulsification of hydrocarbon oils
- C10G33/02—Dewatering or demulsification of hydrocarbon oils with electrical or magnetic means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0208—Separation of non-miscible liquids by sedimentation
- B01D17/0211—Separation of non-miscible liquids by sedimentation with baffles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/06—Separation of liquids from each other by electricity
Abstract
<PICT:0680244/III/1> A process for breaking an emulsion comprises subjecting a stream of the emulsion to an electrical field in an initial zone and passing it to a secondary settling zone wherein demulsified constituents are separated, any unbroken emulsion being also separated and returned to the initial zone. Hydrocarbon oils containing salt may be desalted by forming an aqueous emulsion, which is then broken as above to separate the aqueous phase containing the salt. In Fig. 1 a hydrocarbon oil containing salt is introduced into the apparatus by line 1 and water by line 2, and the mixture is heated to 200 DEG F at 25 lbs. sq. in. pressure. The pressure is reduced to about atmospheric by passing through valve 3, and an emulsion is thus formed; this is passed into zone 10 between electrodes 4. The oil phase formed is passed by line 5 to the top of settling zone 20, and the water phase by line 6 to the bottom of this zone, and both streams flow longitudinally through the zone between baffle elements 7 which are sloped slightly upwardly to permit the aqueous phase to flow back to the bottom of the zone from where it is removed by line 12. The desalted oil is removed by line 11 and an emulsion phase withdrawn from the middle of the zone by line 13 is recycled to line 1 for further treatment in zone 10. In a modification, the separation zone is integral with the electrical zone and is positioned so that any unbroken emulsion tends to circulate back to the electrical zone. The oil and water mixture may be heated to 150 DEG -350 DEG F and maintained at a pressure of 25-200 lbs./sq. in. Demulsification agents such as surface active agents or electrolytes such as sodium hydroxide may be used to assist the breaking of the emulsion, and the voltage employed may be 5,000-35,000 volts.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US680244XA | 1949-04-28 | 1949-04-28 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB680244A true GB680244A (en) | 1952-10-01 |
Family
ID=22079939
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB5360/50A Expired GB680244A (en) | 1949-04-28 | 1950-03-02 | Improved electrical process for breaking emulsions |
Country Status (5)
Country | Link |
---|---|
BE (1) | BE495189A (en) |
DE (1) | DE848199C (en) |
FR (1) | FR1017573A (en) |
GB (1) | GB680244A (en) |
NL (1) | NL75524C (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2775541A (en) * | 1954-01-06 | 1956-12-25 | Karl Alfred | Process for dehydrating of tar |
US2825686A (en) * | 1953-10-29 | 1958-03-04 | Exxon Research Engineering Co | Electrical coalescence process |
GB2145730A (en) * | 1983-08-08 | 1985-04-03 | Elf Aquitaine | Process and apparatus for simultaneously dewatering, desalting and deasphalting a mixture of hydrocarbons |
WO2008107696A2 (en) * | 2007-03-07 | 2008-09-12 | Petroleo Brasileiro S.A. - Petrobras | Method for the microwave treatment of water-in-oil emulsions |
EP2623174A1 (en) * | 2012-02-02 | 2013-08-07 | ACO Severin Ahlmann GmbH & Co. KG | Precipitator |
CN103813842A (en) * | 2011-07-26 | 2014-05-21 | 沙特阿拉伯石油公司 | Dynamic demulsification system for use in a gas-oil separation plant |
CN104419448A (en) * | 2013-08-19 | 2015-03-18 | 中石化洛阳工程有限公司 | Crude oil electric desalting process |
CN108463277A (en) * | 2015-12-22 | 2018-08-28 | 卡梅伦解决方案公司 | Crude oil storage tank with the electrostatic inner member for making crude oil dehydration in the processing system of Floating Production storage and debarkation facilities |
CN111450578A (en) * | 2020-04-03 | 2020-07-28 | 成都理工大学 | Demulsification method of W/O emulsion |
-
0
- BE BE495189D patent/BE495189A/xx unknown
- NL NL75524D patent/NL75524C/xx active
-
1950
- 1950-03-02 GB GB5360/50A patent/GB680244A/en not_active Expired
- 1950-03-15 FR FR1017573D patent/FR1017573A/en not_active Expired
- 1950-09-07 DE DEST2089A patent/DE848199C/en not_active Expired
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2825686A (en) * | 1953-10-29 | 1958-03-04 | Exxon Research Engineering Co | Electrical coalescence process |
US2775541A (en) * | 1954-01-06 | 1956-12-25 | Karl Alfred | Process for dehydrating of tar |
GB2145730A (en) * | 1983-08-08 | 1985-04-03 | Elf Aquitaine | Process and apparatus for simultaneously dewatering, desalting and deasphalting a mixture of hydrocarbons |
WO2008107696A2 (en) * | 2007-03-07 | 2008-09-12 | Petroleo Brasileiro S.A. - Petrobras | Method for the microwave treatment of water-in-oil emulsions |
EP1977806A3 (en) * | 2007-03-07 | 2008-10-22 | Petroleo Brasileiro S.A. Petrobras | Method for the microwave treatment of water-in-oil emulsions |
WO2008107696A3 (en) * | 2007-03-07 | 2008-11-06 | Petroleo Brasileiro Sa | Method for the microwave treatment of water-in-oil emulsions |
CN103813842A (en) * | 2011-07-26 | 2014-05-21 | 沙特阿拉伯石油公司 | Dynamic demulsification system for use in a gas-oil separation plant |
CN103813842B (en) * | 2011-07-26 | 2016-03-23 | 沙特阿拉伯石油公司 | For the dynamic demulsification system of oil-gas separator |
EP2623174A1 (en) * | 2012-02-02 | 2013-08-07 | ACO Severin Ahlmann GmbH & Co. KG | Precipitator |
CN104419448A (en) * | 2013-08-19 | 2015-03-18 | 中石化洛阳工程有限公司 | Crude oil electric desalting process |
CN108463277A (en) * | 2015-12-22 | 2018-08-28 | 卡梅伦解决方案公司 | Crude oil storage tank with the electrostatic inner member for making crude oil dehydration in the processing system of Floating Production storage and debarkation facilities |
CN111450578A (en) * | 2020-04-03 | 2020-07-28 | 成都理工大学 | Demulsification method of W/O emulsion |
Also Published As
Publication number | Publication date |
---|---|
FR1017573A (en) | 1952-12-12 |
DE848199C (en) | 1952-09-01 |
NL75524C (en) | |
BE495189A (en) |
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