EA200801246A1 - Способ разделения смеси и установка для разделения смеси, содержащей воду, нефть и газ - Google Patents

Способ разделения смеси и установка для разделения смеси, содержащей воду, нефть и газ

Info

Publication number
EA200801246A1
EA200801246A1 EA200801246A EA200801246A EA200801246A1 EA 200801246 A1 EA200801246 A1 EA 200801246A1 EA 200801246 A EA200801246 A EA 200801246A EA 200801246 A EA200801246 A EA 200801246A EA 200801246 A1 EA200801246 A1 EA 200801246A1
Authority
EA
Eurasian Patent Office
Prior art keywords
oil
gas
separation
mixture
phase
Prior art date
Application number
EA200801246A
Other languages
English (en)
Other versions
EA014250B1 (ru
Inventor
Йорн Фолькванг
Original Assignee
М-И Эпкон Ас
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 М-И Эпкон Ас filed Critical М-И Эпкон Ас
Publication of EA200801246A1 publication Critical patent/EA200801246A1/ru
Publication of EA014250B1 publication Critical patent/EA014250B1/ru

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14—Fractional distillation or use of a fractionation or rectification column
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D11/00—Solvent extraction
    • B01D11/04—Solvent extraction of solutions which are liquid
    • B01D11/0446—Juxtaposition of mixers-settlers
    • B01D11/0449—Juxtaposition of mixers-settlers with stationary contacting elements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D11/00—Solvent extraction
    • B01D11/04—Solvent extraction of solutions which are liquid
    • B01D11/0492—Applications, solvents used
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D19/00—Degasification of liquids
    • B01D19/0005—Degasification of liquids with one or more auxiliary substances
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00—Nature of the contaminant
    • C02F2101/30—Organic compounds
    • C02F2101/32—Hydrocarbons, e.g. oil
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/34—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
    • C02F2103/36—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the manufacture of organic compounds
    • C02F2103/365—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the manufacture of organic compounds from petrochemical industry (e.g. refineries)

Abstract

В смесь, которая была отделена от потока, выходящего из нефтяной скважины, и содержит воду, нефть и газ, вводят текучую среду. Смесь, содержащую текучую среду, подают в сепаратор (3), где она разделяется на водную фазу и фазу нефть/текучая среда. Очищенную водную фазу отводят из указанного сепаратора (3) через выходной патрубок для воды. Фазу нефть/текучая среда разделяют на следующей стадии разделения на нефтяную фазу и газовую фазу, из газовой фазы текучую среду извлекают на стадии конденсации и рециркулируют на стадию добавления в смесь. Сепаратор представляет собой сепаратор жидкость-жидкость-газ (3), давление в котором соответствует диапазону от 0,5 до 25 бар, в нем смесь, содержащая указанную текучую среду, разделяется на указанную водную фазу и фазу нефть/газ.
EA200801246A 2005-11-03 2006-11-03 Способ разделения смеси и установка для разделения смеси, содержащей воду, нефть и газ EA014250B1 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP05388094A EP1783101A1 (en) 2005-11-03 2005-11-03 Method and plant for purifying water
PCT/IB2006/054112 WO2007052236A1 (en) 2005-11-03 2006-11-03 A method of separating a mixture, and a plant for separating a mixture comprising water, oil and gas

Publications (2)

Publication Number Publication Date
EA200801246A1 true EA200801246A1 (ru) 2009-02-27
EA014250B1 EA014250B1 (ru) 2010-10-29

Family

ID=36116135

Family Applications (1)

Application Number Title Priority Date Filing Date
EA200801246A EA014250B1 (ru) 2005-11-03 2006-11-03 Способ разделения смеси и установка для разделения смеси, содержащей воду, нефть и газ

Country Status (10)

Country Link
US (1) US8425777B2 (ru)
EP (2) EP1783101A1 (ru)
CN (1) CN101309867B (ru)
AU (1) AU2006310156C1 (ru)
BR (1) BRPI0618266A2 (ru)
CA (1) CA2626762A1 (ru)
EA (1) EA014250B1 (ru)
MY (1) MY145429A (ru)
NO (1) NO20082568L (ru)
WO (1) WO2007052236A1 (ru)

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GB0812400D0 (en) * 2008-07-07 2008-08-13 Mator As Process
US10155180B2 (en) 2009-04-30 2018-12-18 Phyre Technologies, Inc. Contacting systems and methods and uses thereof
FR2947281B1 (fr) * 2009-06-26 2012-11-16 Total Sa Procede de traitement d'hydrocarbures
DK177387B1 (en) * 2010-04-12 2013-03-04 Schlumberger Norge As A flotation unit for purifying water, such as a CFU (Compact Flotation Unit)
US20120073806A1 (en) * 2010-09-21 2012-03-29 Bp Corporation North America Inc. Low cut water sampling device
WO2013156535A1 (en) * 2012-04-17 2013-10-24 Statoil Canada Limited Method of cleaning water to remove hydrocarbon therefrom
GB2501261A (en) * 2012-04-17 2013-10-23 Statoil Canada Ltd A method of cleaning water to remove hydrocarbon
RU2015133455A (ru) * 2013-01-28 2017-03-06 Солекс Уотер Лтд. Способы и системы для извлечения воды
DK3089801T3 (en) * 2013-12-04 2022-10-24 Schlumberger Norge As Compact flotation unit having multiple vanes disposed around a cylinder used for waste collection
TWI656115B (zh) * 2014-01-24 2019-04-11 美商Ｇｔｃ科技美國有限責任公司 用於移除重烴之方法及系統
EP3271548A4 (en) * 2015-03-16 2018-10-24 Seabed Separation AS Method and system for subsea purification of produced water from subsea oil producing installations
CN105344201B (zh) * 2015-11-16 2018-01-30 广东上典环境保护工程有限公司 基于冷凝‑萃取法有机废气回收方法
US10364173B2 (en) 2015-12-07 2019-07-30 Fmc Technologies, Inc. Systems and methods for treating oilfield wastewater
US10301190B2 (en) 2016-03-17 2019-05-28 Cameron Solutions, Inc. Pressure controlled gas flotation
WO2020080951A1 (en) * 2018-10-16 2020-04-23 Aker Solutions As Petroleum processing system
CN110694341B (zh) * 2019-10-10 2021-09-07 唐山三友硅业有限责任公司 含氢硅油水解物处理装置以及处理工艺

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2235639A (en) * 1938-05-10 1941-03-18 Winkler Koch Patent Company Resolution of oil and water emulsions
US2730190A (en) * 1952-02-08 1956-01-10 Union Oil Co Treatment of oil-containing water
DE2153976A1 (de) * 1971-10-29 1973-05-03 Texaco Development Corp Verfahren zum entoelen und entwaessern von raffinerie- und oelschlamm
NL7403883A (nl) * 1974-03-22 1975-09-24 Philips Nv Werkwijze en inrichting voor extraktie bij vloei- stoffen.
US4752399A (en) * 1984-10-29 1988-06-21 Gilley And Associates Method of removing dissolved oil from produced water
US4824555A (en) * 1987-07-09 1989-04-25 The Standard Oil Company Extraction of oil from stable oil-water emulsions
CN2308435Y (zh) * 1996-10-25 1999-02-24 中国科学院生态环境研究中心 油水分离装置
AU738108B2 (en) * 1997-02-28 2001-09-06 Cagniard De La Tour As Process for simultaneous extraction of dispersed and dissolved hydrocarbon contaminants from water
EP1208897A1 (en) 2000-11-21 2002-05-29 Epcon Norge AS Combined degassing and flotation tank
CN2545186Y (zh) * 2002-04-27 2003-04-16 冯运红 过滤式油水分离器

Also Published As

Publication number Publication date
EP1783101A1 (en) 2007-05-09
CN101309867A (zh) 2008-11-19
AU2006310156C1 (en) 2010-11-11
US8425777B2 (en) 2013-04-23
AU2006310156A1 (en) 2007-05-10
US20100006476A1 (en) 2010-01-14
EA014250B1 (ru) 2010-10-29
AU2006310156B2 (en) 2010-08-26
WO2007052236A1 (en) 2007-05-10
BRPI0618266A2 (pt) 2011-08-23
EP1968896A1 (en) 2008-09-17
CN101309867B (zh) 2013-06-19
MY145429A (en) 2012-02-15
CA2626762A1 (en) 2007-05-10
NO20082568L (no) 2008-06-03

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Legal Events

Date Code Title Description
MM4A Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s)

Designated state(s): AM BY KG MD TJ

PC4A Registration of transfer of a eurasian patent by assignment
MM4A Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s)

Designated state(s): AZ KZ TM RU