WO2011159189A1 - Procédé d'extraction de liquide non gazeux en nappe - Google Patents
Procédé d'extraction de liquide non gazeux en nappe Download PDFInfo
- Publication number
- WO2011159189A1 WO2011159189A1 PCT/RU2011/000156 RU2011000156W WO2011159189A1 WO 2011159189 A1 WO2011159189 A1 WO 2011159189A1 RU 2011000156 W RU2011000156 W RU 2011000156W WO 2011159189 A1 WO2011159189 A1 WO 2011159189A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- liquid
- pumps
- pump
- fluid
- well
- Prior art date
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04F—PUMPING OF FLUID BY DIRECT CONTACT OF ANOTHER FLUID OR BY USING INERTIA OF FLUID TO BE PUMPED; SIPHONS
- F04F1/00—Pumps using positively or negatively pressurised fluid medium acting directly on the liquid to be pumped
- F04F1/06—Pumps using positively or negatively pressurised fluid medium acting directly on the liquid to be pumped the fluid medium acting on the surface of the liquid to be pumped
- F04F1/08—Pumps using positively or negatively pressurised fluid medium acting directly on the liquid to be pumped the fluid medium acting on the surface of the liquid to be pumped specially adapted for raising liquids from great depths, e.g. in wells
Definitions
- the method for producing reservoir non-carbonated fluid relates to the field of water production, and can be used to produce produced water and other non-carbonated fluids from deep wells.
- IPC F04F 1/04, F24J 2/42 in which, when the compressor is turned on, air enters through a pipeline through a pipe filled with liquid through an inlet valve from the natural pressure of the thickness of the oil layer, or using a vacuum pump, and creates pressure on liquid, which through the gap between the end surface of the nozzle and the bottom, overcoming the resistance of the outlet valve, enters a special container, which, as a certain amount is filled with liquid, automatically rotates, turning off the compressor, and pours the liquid into the tank at a certain speed corresponding to the inflow of liquid from the cylinder working volume through the inlet valve, and after the liquid has passed from the tank, the latter returns to its original position to receive the next cycle of fluid, closing one valve, turning off the vacuum pump, and simultaneously opens another valve and turns on the compressor, and the process repeats.
- the method does not provide sufficient performance due to the cyclical fluid supply, due to the presence of only one working cylinder. If, when the compressor is turned on, the filling of the cylinder capacity with the liquid has stopped and the liquid level has not yet reached a certain level, and the compressor is working, air is flowing instead of the liquid, it is necessary to balance the container using a counterweight until it returns to its original position, although after such adjustment the pump will not working with the full volume of liquid filling its cylinder.
- the liquid supply to the surface is intermittent, due to the alternation in the GHSN of the processes of absorption and pushing to the surface, which affects the performance of the method.
- the performance of the submersible electric pump is higher than the performance of the main gearbox, this leads to increased wear of the first.
- the pump is poorly suited for fluid production with a high content of solids.
- the objective of the proposed technical solution is to create a reliable and easily integrated into the existing system for producing water from wells, an easy-to-use and electrically safe method (supply voltage of a downhole pump 24 Volts), which allows producing non-carbonated liquid with mechanical impurities from small and large depths, and from wells with a small debit, including.
- the problem is solved due to the method of producing non-carbonated formation fluid by installing on the basis of borehole replacement pumps, including raising the liquid by pumps, while a continuous flow of fluid is created by alternating the cycles of receiving and displacing the working chambers of interchangeable two-chamber borehole replacement pumps connected by pipelines of the produced fluid and of discharging the spent gas and power cable; for this, the pressure in the sealed annulus is increased, by which the static liquid level in it is reduced to a level lower than the placement of the lower stage of the downhole substitution pump, and due to the difference in the increased pressure in the annulus of the well, with the pressure in the exhaust pipe connected to the atmosphere, and from one of the working chambers of the pump of the lower stage of the installation, liquid is received, and all pumps are displaced from the other chamber through the pipeline of the produced liquid to the upper pumps Upenu create due to receipt therein of pressurized gas from the annulus, W 201
- Fig. 1 is a diagram of the installation on the basis of borehole displacement pumps with a single-stage lifting of fluid
- Fig. 2 is a diagram of the installation based on borehole displacement pumps in a multi-stage lifting
- Fig.3 is a schematic diagram of a borehole displacement pump
- Fig.4 is a diagram of the carrier W
- FIGS. 5, 6 and 7 - the operating procedure of downhole displacement pumps.
- Figure 1, 2, 3, 4, 5, 6 and 7 show: casing pipe 1 of the well, perforations of the casing 2, produced fluid 3, well pump 4, bearing pipe 5 for exhaust and associated gases, pipe 6 lifting the produced fluid, receiving pipe 7, the intermediate cable 8, the plug 9 of the lower power connector of the lower stage pump, the casing flange 10, the bearing flange 11 of the downhole pump, the gasket 12, the supporting pipe 13, the produced fluid pipe 14, the compressed gas pipe 15 a, a compressor 16 for supplying compressed gas, an electrical cabinet 17, an outlet pipe 18 of the compressor, a compressed gas pipe 19, an electrical connector 20, an electrical connector 21, a main pipe 22, a central pipe 23, an electric air distributor 24, a suction pipe 25, a discharge pipe 26 , lower electrical connector 27, upper electrical connector 28, filter nozzle 29, well pump power cable 30, compressor power cable 31, power line 32, compressor inlet 33, electric intermediate wire 34, compressed air supply valve 35, sleeve 36, support rod 37 of the intake pipe, breather 38, control section 39 of the well pump, main section 40 of the well pump, valve section 41 of
- the method of producing reservoir non-carbonated liquid is as follows.
- FIG. 1 is a diagram of a one-stage liquid rise of Fig. 2 is a diagram of a multi-stage fluid lifting
- FIG. 3 is a schematic diagram of a well submersible pump
- FIG. 4 is a schematic diagram of a bearing flange of a well pump
- FIGS. 5, 6 and 7 are an operating procedure of well submersible pumps.
- n H / h
- n is the number of installation steps
- h is the step with which borehole replacement pumps are mounted (5-50 m.).
- a bearing flange 11 When installing the installation on the basis of borehole replacement pumps for producing non-carbonated liquid, to a hermetically mounted casing pipe 1 on the flange 10, a bearing flange 11, with nozzles hermetically assembled on it: a carrier 13, produced fluid 14, compressed gas 15, and electrical connectors 20 and 21, connected by an intermediate wire 34, are fastened by a supporting pipe 5, one or more stages, one below the other in the form of a string of borehole displacement pumps 4.
- the pump of the lower stage of the installation is located in the well below the static liquid level by 5-25 m.
- the receiving pipe 7 with the filter nozzle 29 is connected by a supporting rod 37 with a sleeve 36 to the lower end of the central pipe 23 of the well replacement pump 4, with a sleeve 36 tightly closed the lower end of the Central pipe 23;
- the length of the receiving pipe can be any, and depends only on how deep the liquid must be lifted;
- the downhole displacement pump is lowered to the required depth, while the carrier pipe 5 is hermetically connected to the carrier pipe 13, hermetically assembled on the carrier flange 11.
- the pipeline of produced fluid 6 is connected to the pipe of produced fluid 14, which is also hermetically assembled on the carrier flange 11.
- Power cable 8 is connected to the connector 20 located on the bearing flange 11.
- the bearing flange 11 is mounted on the flange of the casing 10, and to ensure tightness, a gasket 12 is installed between them and tightened with bolts (in the drawing e shown).
- the compressed gas pipe 15 is connected to a valve 35 mounted on the outlet pipe 18 of the compressor 16 by means of a pipe 19, and the pipe of the produced fluid 14 is connected to the main pipe 22.
- the power cable of the downhole pump 30, connected to the electrical cabinet 17 at one end, is connected to the connector 21, located on the carrier flange 11, and connected to the connector 20 by means of an intermediate wire 34, hermetically sealed into it.
- the compressor 16 is connected to an electrical cabinet 17, which in turn is connected to the power line 32.
- the bearing flange of the installation on the basis of borehole displacement pumps at a single-stage or multi-stage lifting of non-carbonated liquid is structurally no different (Fig. 4) and is an assembly unit consisting of a flange 11 and nozzles hermetically assembled on it: a carrier 13, which is tightly connected to the carrier pipe of the well pump and is designed to hold it, at the same time serves to discharge the exhaust gas, produced fluid 14, used to pump the produced fluid from the well to the surface, compressed gas 15, used to supply compressed gas to the shutter bnoe space well.
- On the flange are also electrical connectors 20 and 21, which are interconnected by an intermediate wire 34.
- valve 35 Before turning on the mounted installation, in the annulus of the well create an increased pressure of atmospheric air, (Fig.1 and 2). To do this, turn on compressor 16, valve 35 must be open. At this point, increased air pressure is created in the annulus, under which the static level of the liquid in the well decreases, and the downhole substitution pump 4 of the lower stage is higher than the liquid level. In this case, the air entering one of the working chambers of the borehole replacement pump (Fig.
- the reed switch 53 gives a signal via wire 65 to control unit 70, which generates a command and transmits it via wire 63 to switch the air distributor 24.
- compressed air starts to flow from the chamber 43 from annular space through the breather 38 through the channel 71 and 69 and displace the fluid into the pipe 6 through the seat 49, the discharge valve 57 and the channel 59.
- compressed air is removed from the chamber 42 into the exhaust gas pipe 5 through channels 68 and 67 through Mon self-distributor 24, as a result of lowering the pressure, the fluid enters the chamber under pressure through the seat 48, valve 54 and through the receiving channel 58 from the intake pipe 7.
- the float valve 47 closes the seat 49, preventing compressed air from leaking.
- the float valve 46 floating up, closes the seat 50, at the same time closing the reed switch 52, as a result of which the air distributor 24 switches.
- compressed air enters the chamber 42 and displaces the liquid through the seat 48 and valve 56 into the discharge channel 59 and then into the pipe 6.
- the downhole displacement pump creates a continuous liquid flow in the pipeline 6 until the power supply to the installation is turned off.
- a well replacement pump for any stage in the production of non-carbonated liquid by a multi-stage installation is designed to receive fluid from the next lower and rise to the next upper one, and they begin to work only when it fills one of the working chambers, and until that moment they are in standby mode.
- the principle of operation of all borehole pumps for plant replacement in single-stage and multi-stage fluid lifting is the same.
- the technical effect is the creation of a reliable and easily integrated into the existing system for producing water from wells, an easy-to-use and electrically safe method that allows producing non-carbonated liquid with mechanical impurities from shallow and deep depths, and from wells with a small debit, including through the method the production of still non-carbonated fluid by an installation based on borehole displacement pumps, including raising the fluid by pumps, while creating a continuous flow of fluid by alternating cycles of EMA and displacing working chambers interchangeable dual chamber substitution downhole pump connected by pipelines extracted liquid outlet of the exhaust gas and the power cable; for this, the pressure in the sealed annulus is increased, by which the static liquid level in it is reduced to a level lower than the placement of the lower stage of the downhole substitution pump, and due to the difference in the increased pressure in the annulus of the well, with the pressure in the exhaust pipe connected to the atmosphere, and from one of the working chambers of the pump of the lower stage of the installation, liquid is received, and all pumps are displaced from the other chamber through the pipeline of the produced liquid
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Jet Pumps And Other Pumps (AREA)
Abstract
L'invention concerne un procédé d'extraction de liquide non gazeux en nappe, procédé qui peut être utilisé pour extraire des puits profonds de l'eau en nappe et d'autres liquides non gazeux. Le procédé consiste à faire le remonter le liquide par des pompes. Pour cela, on crée un courant continu de liquide en alternant des cycles d'admission et d'évacuation des chambres de travail de pompes de substitution à deux chambres interchangeables pour le forage de puits qui sont raccordées par des conduites destinées au liquide extrait en vue de refouler le gaz d'échappement, et par un câble d'alimentation électrique. A cette fin, on augmente la pression dans l'espace annulaire du tubage de puits hermétiquement fermé, dans lequel le niveau statique du liquide est réduit à un niveau inférieur à celui auquel se trouve l'étage inférieur de la pompe de substitution pour le forage de puits du fait de la différence de l'augmentation de pression dans l'espace annulaire du tubage de puits, de la pression dans la conduite de renvoi du gaz d'échappement qui débouche dans l'atmosphère, et dans l'une des chambres de travail de la pompe à l'étage inférieur de l'installation. Puis s'effectue l'admission du liquide, mais qui est ensuite refoulé, depuis une autre chambre de toutes les pompes le long de la conduite destinée au liquide extrait, vers des pompes dans les étages supérieurs sous l'effet du passage du gaz comprimé provenant de l'espace annulaire du tubage de puits. L'admission du liquide par les chambres de travail des pompes situées dans le haut est conditionnée par le refoulement du liquide des chambres de travail situées en contrebas des pompes.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
RU2010124183/06A RU2424448C1 (ru) | 2010-06-16 | 2010-06-16 | Способ добычи пластовой негазированной жидкости |
RU2010124183 | 2010-06-16 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2011159189A1 true WO2011159189A1 (fr) | 2011-12-22 |
Family
ID=44752609
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/RU2011/000156 WO2011159189A1 (fr) | 2010-06-16 | 2011-03-14 | Procédé d'extraction de liquide non gazeux en nappe |
Country Status (2)
Country | Link |
---|---|
RU (1) | RU2424448C1 (fr) |
WO (1) | WO2011159189A1 (fr) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA2938934C (fr) * | 2014-02-17 | 2019-04-16 | Baker Hughes Incorporated | Pompe a tige de verrouillage anti-gaz magnetique |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6435838B1 (en) * | 1998-06-11 | 2002-08-20 | John E. Marvel | Fluid well pump |
AU2004200667A1 (en) * | 2003-02-20 | 2004-09-09 | Jones, James Stephen | Pump |
RU2293886C2 (ru) * | 2005-02-07 | 2007-02-20 | Василий Алексеевич Горлов | Насос |
RU2325553C1 (ru) * | 2006-11-07 | 2008-05-27 | Общество с ограниченной ответственностью "Пермское конструкторско-технологическое бюро технического проектирования и организации производства" | Способ и устройство для подъема жидкостей из скважин |
RU90859U1 (ru) * | 2009-10-08 | 2010-01-20 | Анатолий Михайлович Данч | Система многоступенчатого подъема жидкостей из буровых скважин |
-
2010
- 2010-06-16 RU RU2010124183/06A patent/RU2424448C1/ru not_active IP Right Cessation
-
2011
- 2011-03-14 WO PCT/RU2011/000156 patent/WO2011159189A1/fr active Application Filing
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6435838B1 (en) * | 1998-06-11 | 2002-08-20 | John E. Marvel | Fluid well pump |
AU2004200667A1 (en) * | 2003-02-20 | 2004-09-09 | Jones, James Stephen | Pump |
RU2293886C2 (ru) * | 2005-02-07 | 2007-02-20 | Василий Алексеевич Горлов | Насос |
RU2325553C1 (ru) * | 2006-11-07 | 2008-05-27 | Общество с ограниченной ответственностью "Пермское конструкторско-технологическое бюро технического проектирования и организации производства" | Способ и устройство для подъема жидкостей из скважин |
RU90859U1 (ru) * | 2009-10-08 | 2010-01-20 | Анатолий Михайлович Данч | Система многоступенчатого подъема жидкостей из буровых скважин |
Also Published As
Publication number | Publication date |
---|---|
RU2424448C1 (ru) | 2011-07-20 |
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