NO20092002L - Emulsjonsbehandlingsanordning - Google Patents

Emulsjonsbehandlingsanordning

Info

Publication number
NO20092002L
NO20092002L NO20092002A NO20092002A NO20092002L NO 20092002 L NO20092002 L NO 20092002L NO 20092002 A NO20092002 A NO 20092002A NO 20092002 A NO20092002 A NO 20092002A NO 20092002 L NO20092002 L NO 20092002L
Authority
NO
Norway
Prior art keywords
emulsion
outlet
stable emulsion
stable
inlet
Prior art date
Application number
NO20092002A
Other languages
Norwegian (no)
Inventor
Donald R Smuin
Louis D'souza
J Stewart Mulvey
Original Assignee
Aker Process Systems As
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 Aker Process Systems As filed Critical Aker Process Systems As
Priority to NO20092002A priority Critical patent/NO20092002L/en
Priority to PCT/NO2010/000180 priority patent/WO2010134822A1/en
Publication of NO20092002L publication Critical patent/NO20092002L/en

Links

Classifications

    • 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
    • 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
    • B01D17/04—Breaking emulsions
    • B01D17/042—Breaking emulsions by changing the temperature
    • 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
    • B01D17/04—Breaking emulsions
    • B01D17/045—Breaking emulsions with coalescers
    • 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
    • B01D17/04—Breaking emulsions
    • B01D17/048—Breaking emulsions by changing the state of aggregation
    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C11/00—Separation by high-voltage electrical fields, not provided for in other groups of this subclass
    • 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
    • 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
    • C10G33/06—Dewatering or demulsification of hydrocarbon oils with mechanical means, e.g. by filtration

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

En emulsjonsbehandlingsanordningfor separering av en emulsjon av emulsifiserte produserte vanndråper og olje innbefatter en i hovedsaken horisontal og avlang beholder (10) utformet og anordnet for langsgående strømning av emulsjon gjennom den, og innbefattende et emulsjonsinnløp (12), et oljeutløp (22), et vannutløp (24) og minst ett koaliseringselement (18) anordnet i beholderen (10), og et utløp for en stabil emulsjon (R) som danner seg i området ved en grenseflate (I) mellom emulsjon (E) og vann (W) når anordningen er i bruk. Utløpet for den stabile emulsjonen er gjennom en fluidledning (30) forbundet med en separatorbeholder (34; 32) som har et innløp og videre innbefatter et oljeutløp (36), et vannutløp (38) og midler (26; 28; 32) for bryting av den stabile emulsjonen (R). Midlene for bryting av den stabile emulsjonen kan innbefatte et elektrostatisk element (26), et oppvarmingselement (28) eller en elektrostatisk koaliseringsinnretning (32).An emulsion treatment device for separating an emulsion from emulsified produced water droplets and oil includes a substantially horizontal and elongated container (10) formed and arranged for longitudinal flow of emulsion through it, including an emulsion inlet (12), an oil outlet (22), (24) and at least one coalescing element (18) provided in the container (10), and an outlet for a stable emulsion (R) forming in the region at an interface (I) between emulsion (E) and water (W) when the device is in use. The outlet for the stable emulsion is connected through a fluid line (30) to a separator vessel (34; 32) having an inlet and further comprising an oil outlet (36), a water outlet (38) and means (26; 28; 32) for refraction. of the stable emulsion (R). The means for breaking the stable emulsion may include an electrostatic element (26), a heating element (28) or an electrostatic coalescing device (32).

NO20092002A 2009-05-22 2009-05-22 Emulsjonsbehandlingsanordning NO20092002L (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
NO20092002A NO20092002L (en) 2009-05-22 2009-05-22 Emulsjonsbehandlingsanordning
PCT/NO2010/000180 WO2010134822A1 (en) 2009-05-22 2010-05-14 Method and apparatus for breaking a stable emulsion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NO20092002A NO20092002L (en) 2009-05-22 2009-05-22 Emulsjonsbehandlingsanordning

Publications (1)

Publication Number Publication Date
NO20092002L true NO20092002L (en) 2010-11-23

Family

ID=42556637

Family Applications (1)

Application Number Title Priority Date Filing Date
NO20092002A NO20092002L (en) 2009-05-22 2009-05-22 Emulsjonsbehandlingsanordning

Country Status (2)

Country Link
NO (1) NO20092002L (en)
WO (1) WO2010134822A1 (en)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8981174B2 (en) 2013-04-30 2015-03-17 Pall Corporation Methods and systems for processing crude oil using cross-flow filtration
CN103437749B (en) * 2013-08-14 2016-01-20 张彦忠 A kind of combustion heater for Oil-gas Separation
US20150152340A1 (en) * 2013-12-03 2015-06-04 Exxonmobil Research And Engineering Company Desalter emulsion separation by emulsion recycle
RU2541544C1 (en) * 2013-12-26 2015-02-20 Закрытое акционерное общество "Теплосервис" Method of purifying liquid
RU2547750C1 (en) * 2014-01-31 2015-04-10 Федеральное автономное учреждение "25 Государственный научно-исследовательский институт химмотологии Министерства обороны Российской Федерации" Method of technical oil purification
GB2528858A (en) * 2014-07-31 2016-02-10 David Andrew Kitson Fluid separator
US20180334621A1 (en) * 2017-05-22 2018-11-22 Saudi Arabian Oil Company Crude hydrocarbon fluids demulsification system
US10513663B2 (en) * 2018-01-09 2019-12-24 Saudi Arabian Oil Company Gas oil separation plant systems and methods for rag layer treatment
US11034893B2 (en) 2018-01-09 2021-06-15 Saudi Arabian Oil Company Desalting plant systems and methods for enhanced tight emulsion crude oil treatment
RU2761441C1 (en) * 2020-12-30 2021-12-08 Акционерное Общество "Атомэнергопроект" Coolant flow filtration system of the sump tank of the emergency core cooling system
US12049594B2 (en) 2022-02-28 2024-07-30 Saudi Arabian Oil Company Natural material for separating oil-in-water emulsions

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3574085A (en) * 1969-04-07 1971-04-06 Petrolite Corp Electric treater for emulsions
US3905891A (en) * 1974-02-19 1975-09-16 Combustion Eng Electric treater
WO1992019348A1 (en) * 1991-05-02 1992-11-12 Conoco Specialty Products Inc. Oil/water separation system
GB0419994D0 (en) * 2004-09-09 2004-10-13 Kvaerner Process Systems As Method and apparatus for improving the performance of a separator

Also Published As

Publication number Publication date
WO2010134822A1 (en) 2010-11-25

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Legal Events

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