SU968347A1 - Method of preparing and shipping gas - Google Patents
Method of preparing and shipping gas Download PDFInfo
- Publication number
- SU968347A1 SU968347A1 SU802980090A SU2980090A SU968347A1 SU 968347 A1 SU968347 A1 SU 968347A1 SU 802980090 A SU802980090 A SU 802980090A SU 2980090 A SU2980090 A SU 2980090A SU 968347 A1 SU968347 A1 SU 968347A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- gas
- absorbent
- separator
- preparing
- condensate
- Prior art date
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- Gas Separation By Absorption (AREA)
Description
Изобретение относитс к газовой промышленности и может использоватьс в газодобывающей промышленности , в частности при добыче природного газа.The invention relates to the gas industry and can be used in the gas industry, in particular in the extraction of natural gas.
Известен способ подготовки и транспорта газа, включающий его осушку с помощью абсорбентов, компримирование пердд подачей в газосепаратор и последующую подачу в газопровод 1 . There is a method of preparation and transport of gas, including its drying using absorbents, compressing the feed gas to the gas separator and then to the gas pipeline 1.
Недостатком данного способа вл етс его сложность.The disadvantage of this method is its complexity.
Целью изобретени вл етс упрощение способа подготовки и транспорта газа.The aim of the invention is to simplify the method of preparation and transport of gas.
Эта цель достигаетс ;тем, что согласно способу подготовки и транспорта газа, включающему осушку с по мощью абсорбентов,, компримирование пеперед подачей в газосепаратор и последующую подачу в газопровод, компримирование и осушку газа производ т одновременно путем его по- . дачи в газожидкостной эжектор, рабочей жидкостью которого вл етс абсорбент, например диэтйленгликоль. . На чертеже представлена схема реализации способа.This goal is achieved by the fact that according to the method of gas treatment and transportation, which includes drying with absorbents, the compression is carried out before being supplied to the gas separator and the subsequent supply to the gas pipeline, the compression and drying of the gas is carried out simultaneously. The dachas are supplied to a gas-liquid ejector whose working fluid is an absorbent, for example diethylene glycol. . The drawing shows a diagram of the implementation of the method.
Из газовых коллекторов двухфаз .на смесь поступает на прием газожидкостного эжектора 1, куда насосом 2 подаетс и насыщенный абсорбент . В газожидкостном эжектора 1 происходит абсорбци и одновременное компримирование смеси. Нп эжектора 1 уже трехфазна смесь (газ + конденсат -I- абсорбент) поступает в сепаратор 3, где происходит разделение газа, конденсата и абсорбента. From the gas collectors of the two phases, the mixture enters the intake of the gas-liquid ejector 1, where the pump 2 also supplies the saturated absorbent. In the gas-liquid ejector 1, the mixture is absorbed and simultaneously compressed. NP ejector 1 already three-phase mixture (gas + condensate -I- absorbent) enters the separator 3, where the separation of gas, condensate and absorbent.
10 Положение уровн конденсата и абсорбента регулируетс при помощи регул торов 4 и 5, -из сепаратора 3 . отсепарироваиный газ поступает на газосепаратор 6. Здесь происходит 10 The position of the level of the condensate and the absorbent is regulated by means of the regulators 4 and 5, of the separator 3. separation gas enters gas separator 6. Here occurs
15 дополнительна сепараци газа, после- чего он поступает в магистр Ьный газопровод, а отделившийс абсорбент самотеком поступает в сепаратор 3. Из сепаратора 3 излишек ненасыщен20 ного абсорбента через регул тор 5 подаетс в регенерационную установ- . ку 7, .где происходит отделение мельчайших капель конденсата и воды и насыщение абсорбента. Затем насыщенный абсорбент подаетс на газожидкостной эжектор 1, и цикл повтор етс .15 additional gas separation, after which it enters the master gas pipeline, and the separated absorbent flows by gravity into separator 3. From the separator 3, the excess unsaturated absorbent through regulator 5 is fed to the regeneration plant. 7, where the smallest droplets of condensate and water are separated and the absorbent is saturated. Then, a saturated absorbent is supplied to the gas-liquid ejector 1, and the cycle is repeated.
В сепараторе 3 происходит грубое сепарирование конденсата и егоIn separator 3 there is a rough separation of the condensate and its
30 даление при помощи регул тора I30 dan using controller I
н конденсата 4 на дальнейшую обработку . Раствор насыщенного арсорбента из сепаратора 3 поступает на холодильник 8, где охлаждаетс до температуры откачиваемого газа и затем подаетс на прием эжектора л. Благодар использованию в газожидкостном эжекторе в качестве рабочего агента абсорбента, например диэтиленгликол , одновременно с компримированием газа производитс и его осушка, что позвол ет упростить способ подготовки и транспорта газа.n condensate 4 for further processing. A solution of the saturated adsorbent from the separator 3 is fed to the refrigerator 8, where it is cooled to the temperature of the pumped gas and then fed to the intake of the ejector l. Due to the use of an absorbent, such as diethylene glycol, as a working agent in a gas-liquid ejector, simultaneously with the compression of gas, its drying is also carried out, which simplifies the method of gas preparation and transport.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU802980090A SU968347A1 (en) | 1980-06-30 | 1980-06-30 | Method of preparing and shipping gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU802980090A SU968347A1 (en) | 1980-06-30 | 1980-06-30 | Method of preparing and shipping gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU968347A1 true SU968347A1 (en) | 1982-10-23 |
Family
ID=20917025
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU802980090A SU968347A1 (en) | 1980-06-30 | 1980-06-30 | Method of preparing and shipping gas |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU968347A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000077406A2 (en) * | 1999-06-16 | 2000-12-21 | Valery Grigorievich Tsegelsky | Method for compressing a hydrocarbon-containing gaseous medium |
-
1980
- 1980-06-30 SU SU802980090A patent/SU968347A1/en active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000077406A2 (en) * | 1999-06-16 | 2000-12-21 | Valery Grigorievich Tsegelsky | Method for compressing a hydrocarbon-containing gaseous medium |
| WO2000077406A3 (en) * | 1999-06-16 | 2001-03-15 | Valery Grigorievich Tsegelsky | Method for compressing a hydrocarbon-containing gaseous medium |
| US6579069B2 (en) | 1999-06-16 | 2003-06-17 | Valery Grigorievich Tsegelsky | Method of compressing gaseous hydrocarbon-containing medium |
| US6767191B2 (en) | 1999-06-16 | 2004-07-27 | Valery Grigorievich Tsegelsky | Method of compressing gaseous hydrocarbon-containing medium |
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