EA200401602A1 - Устройство и способ (варианты) обработки текучих сред из нефтяных скважин - Google Patents

Устройство и способ (варианты) обработки текучих сред из нефтяных скважин

Info

Publication number
EA200401602A1
EA200401602A1 EA200401602A EA200401602A EA200401602A1 EA 200401602 A1 EA200401602 A1 EA 200401602A1 EA 200401602 A EA200401602 A EA 200401602A EA 200401602 A EA200401602 A EA 200401602A EA 200401602 A1 EA200401602 A1 EA 200401602A1
Authority
EA
Eurasian Patent Office
Prior art keywords
treatment
residual
tank
oil
separation
Prior art date
Application number
EA200401602A
Other languages
English (en)
Other versions
EA006839B1 (ru
Inventor
Ханну Юхани Салокангас
Уэйн Хессе
Original Assignee
Дженойл Инк.
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 Дженойл Инк. filed Critical Дженойл Инк.
Publication of EA006839B1 publication Critical patent/EA006839B1/ru
Publication of EA200401602A1 publication Critical patent/EA200401602A1/ru

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D19/00—Degasification of liquids
    • B01D19/0036—Flash degasification
    • 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
    • B01D17/02—Separation of non-miscible liquids
    • B01D17/0217—Separation of non-miscible liquids by centrifugal force
    • 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
    • E—FIXED CONSTRUCTIONS
    • E21—EARTH OR ROCK DRILLING; MINING
    • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/34—Arrangements for separating materials produced by the well

Landscapes

  • Physics & Mathematics (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Thermal Sciences (AREA)
  • Mining & Mineral Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Geology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Fluid Mechanics (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Cyclones (AREA)

Abstract

В настоящем изобретении предлагается устройство и способ обработки текучих сред из нефтяной скважины с использованием двух резервуаров высокого давления. Первый резервуар содержит гидроциклоны для разделения текучих сред на водную и нефтяную фазы. Нефтяная фаза задерживается в камере верхнего продукта на время обработки, обеспечивающее дальнейшее отделение остаточной водной фазы, которая повторно пропускается через гидроциклоны. Второй резервуар установлен с наклоном, имеет камеру обработки для приема водной фазы из первого резервуара и обеспечивает время обработки для осуществления отделения остаточной нефтяной фазы. Коалесцирующая среда в камере обработки улучшает это отделение. Остаточная нефтяная фаза подается в нагретую камеру очистки вместе с нефтяной фазой из первого резервуара для обработки в течении второго времени обработки с дальнейшим отделением остаточной водной фазы. Очищенные обработанные вода и нефть выходят из второго резервуара отдельными потоками.
EA200401602A 2004-10-22 2004-12-30 Устройство и способ (варианты) обработки текучих сред из нефтяных скважин EA200401602A1 (ru)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US10/970,010 US20060086658A1 (en) 2004-10-22 2004-10-22 Apparatus and method for processing fluids from oil wells

Publications (2)

Publication Number Publication Date
EA006839B1 EA006839B1 (ru) 2006-04-28
EA200401602A1 true EA200401602A1 (ru) 2006-04-28

Family

ID=36202657

Family Applications (1)

Application Number Title Priority Date Filing Date
EA200401602A EA200401602A1 (ru) 2004-10-22 2004-12-30 Устройство и способ (варианты) обработки текучих сред из нефтяных скважин

Country Status (5)

Country Link
US (1) US20060086658A1 (ru)
AR (1) AR051399A1 (ru)
CA (1) CA2585004A1 (ru)
EA (1) EA200401602A1 (ru)
WO (1) WO2006042421A1 (ru)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NO333990B1 (no) * 2011-10-21 2013-11-11 Green Well Technology As Anordning for påfylling og resirkulering av smøreolje eller tetningssolje(grease) i stigerør
CN107152270B (zh) * 2017-07-11 2023-04-21 山西锦联建设科技有限公司 一种全自动回注水（添加剂）系统及其使用方法
US11293240B2 (en) * 2018-09-04 2022-04-05 Enercorp Engineered Solutions Inc. Integrated multi-stage sand separation system
CN112282726A (zh) * 2020-11-02 2021-01-29 中国石油天然气集团有限公司 油田采出液外置式聚结整流装置及处理方法

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2706531A (en) * 1951-10-30 1955-04-19 Sivalls Tanks Inc Gas and multiple liquid separator apparatus
US2783854A (en) * 1954-05-12 1957-03-05 Sivalls Tanks Inc Gas and multiple liquid separator apparatus
US5302294A (en) * 1991-05-02 1994-04-12 Conoco Specialty Products, Inc. Separation system employing degassing separators and hydroglyclones
CA2108297A1 (en) * 1993-10-13 1995-04-14 Wayne William Hesse Oil/water separation process
GB9602631D0 (en) * 1996-02-09 1996-04-10 Vortoil Separation Systems Ltd Hydrocyclone separator
GB9625999D0 (en) * 1996-12-13 1997-01-29 Hesse Wayne W Hydrocyclone
US5837152A (en) * 1997-04-09 1998-11-17 Corlac Inc. Inclined separation tank
US6255324B1 (en) * 1998-11-25 2001-07-03 Ned D. Heindel Amino-and mercurio-substituted 4′,5'-dihydropsoralens and therapeutical uses thereof
GB0011928D0 (en) * 2000-05-17 2000-07-05 Kellogg Brown & Root Inc Separation method and apparatus for stream containing multi-phase liquid mixture and entrained particles
CA2339590C (en) * 2001-03-07 2002-03-12 Cory Hetherington Heated inclined separation pressure vessel

Also Published As

Publication number Publication date
US20060086658A1 (en) 2006-04-27
EA006839B1 (ru) 2006-04-28
AR051399A1 (es) 2007-01-10
WO2006042421A1 (en) 2006-04-27
CA2585004A1 (en) 2006-04-27

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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 AZ BY KZ KG MD TJ TM RU