SU969282A1 - Separation apparatus - Google Patents
Separation apparatus Download PDFInfo
- Publication number
- SU969282A1 SU969282A1 SU813268462A SU3268462A SU969282A1 SU 969282 A1 SU969282 A1 SU 969282A1 SU 813268462 A SU813268462 A SU 813268462A SU 3268462 A SU3268462 A SU 3268462A SU 969282 A1 SU969282 A1 SU 969282A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- depulsator
- separation
- pipes
- order
- descending
- Prior art date
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- Filtering Of Dispersed Particles In Gases (AREA)
Description
(54) СЕПАРАЦИОННАЯ, УСТАНОВКА (54) SEPARATION, INSTALLATION
Изобретение относитс к сбору и подготовке продукции скважин на нефт ных месторождени х и может быть использовано дл разделени нефти, газа и воды.The invention relates to the collection and preparation of production wells in oil fields and can be used for the separation of oil, gas and water.
Наиболее близкой по технической сущности и достигаемому результату к пр.едлагаемой вл етс репарационна установка, содержаща депульсатор с восход щим и нисход щим участками, соединенный с технологической емкостью и выносным каплеустановителбм ij.The closest in technical essence and the achieved result to the proposed proposal is a reparation installation, containing a bottom-up and down-line depulsator, connected to the process tank and a remote ij-mounted dropper.
Недостатком сепарационных установок данной конструкции вл етс то, что наклонный восход щий участок депульсаторав процессе работы заполн етс пластовой водой независимо от процентного содержани ее в продукции скважины. Движение нефти и газа на этом участке депульсатора происходит по верхней образующей трубе. Эта форма течени вл етс нежелательной, поскольку четочное движение нефти и газа через слой воды создает гидродинамические услови , способствук цие вторичному диспер гированию трехкомпонентного потока и снижению эффективности разделени The disadvantage of separation plants of this design is that the inclined ascending portion of the depulsator is filled with formation water during the operation, regardless of its percentage in the production of the well. The movement of oil and gas in this area of the depulsator occurs along the upper forming pipe. This form of flow is undesirable because the accurate movement of oil and gas through a layer of water creates hydrodynamic conditions, facilitating the secondary dispersion of the three-component flow and reducing the separation efficiency.
нефти, газа и воды в технологической емкости..oil, gas and water in the process tank ..
Цель изобретени - повышение ка ,чества сепарации и увеличение производительности сепарационных установок ,.The purpose of the invention is to improve the quality, separation quality and increase the productivity of separation plants,.
Указанна цель достигаетс тем, что в сепарационнрй установке, содержащей депульсатор с восход щим This goal is achieved by the fact that in a separation plant containing a bottom-loaded blower
10 и нисход щим участками, соединенный с технологической емкостью и выносным каплеуловителем, депульсатор снабжен водосборником с водоотвод щими патрубками, верхний коts нец которых соединен с нисход щим участком депульсатора, прцчем крайние патрубки присоединены на рассто нии от верха депульсатора, составл ющем 0,3-0,5 от общей высоты депуль20 сатора и водосборника.10 and the downstream sections, connected to the process tank and the remote drip catcher, the depulsator is equipped with a water collector with drainage pipes, the upper end of which is connected to the descending section of the depulsator, the extreme branch pipes are attached at a distance of 0.3% from the top of the depulsator 0.5 of the total height of the depulator20 and the sump.
На чертеже представлена конструкци предлагаемой сепара ционной установки . The drawing shows the structure of the proposed separation plant.
Сёпарационна установка включает Equipment installation includes
25 депульсатор,;состо щий из восход щего 1 и нисход щего 2 наклонных участ .ков, газоотвод щий трубопровод 3, водосборник 4 с водоотвод щими патрубками 5, соединенными с нисхо30 д щим учас.тком 2 депульсатора; тех25 a depulsator; consisting of an upstream 1 and a downward 2 inclined sections; a gas exhaust pipe 3; those
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU813268462A SU969282A1 (en) | 1981-01-09 | 1981-01-09 | Separation apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU813268462A SU969282A1 (en) | 1981-01-09 | 1981-01-09 | Separation apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
SU969282A1 true SU969282A1 (en) | 1982-10-30 |
Family
ID=20950710
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU813268462A SU969282A1 (en) | 1981-01-09 | 1981-01-09 | Separation apparatus |
Country Status (1)
Country | Link |
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SU (1) | SU969282A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4661127A (en) * | 1984-02-02 | 1987-04-28 | Stone & Webster Engineering Limited | Submersible liquid/gas separator apparatus |
US7364661B2 (en) | 2002-03-25 | 2008-04-29 | Shell Oil Company | Method and device for separating a mixture of fluids |
FR2921844A1 (en) * | 2007-10-09 | 2009-04-10 | Saipem S A Sa | HORIZONTAL LIQUID / GAS SEPARATION DEVICE AND SEPARATION METHOD, PARTICULARLY LIQUID AND GAS PHASES OF A GROSS OIL |
-
1981
- 1981-01-09 SU SU813268462A patent/SU969282A1/en active
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4661127A (en) * | 1984-02-02 | 1987-04-28 | Stone & Webster Engineering Limited | Submersible liquid/gas separator apparatus |
US7364661B2 (en) | 2002-03-25 | 2008-04-29 | Shell Oil Company | Method and device for separating a mixture of fluids |
FR2921844A1 (en) * | 2007-10-09 | 2009-04-10 | Saipem S A Sa | HORIZONTAL LIQUID / GAS SEPARATION DEVICE AND SEPARATION METHOD, PARTICULARLY LIQUID AND GAS PHASES OF A GROSS OIL |
WO2009050367A3 (en) * | 2007-10-09 | 2009-08-20 | Saipem Sa | Horizontal liquid/gas separation device and separation method, intended in particular for the liquid and gas phases of crude oil |
US20100212492A1 (en) * | 2007-10-09 | 2010-08-26 | Giorgio Miotto | Horizontal Liquid/Gas Separation Device and Separation Method, Intended in Particular for the Liquid and Gas Phases of Crude Oil |
US8273151B2 (en) | 2007-10-09 | 2012-09-25 | Saipem S.A. | Horizontal liquid/gas separation device, and separation method, in particular for the liquid and gaseous phases of a crude oil |
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