EP0236166B1 - Procédé et installation pour faire circuler des fluides par pompage - Google Patents
Procédé et installation pour faire circuler des fluides par pompage Download PDFInfo
- Publication number
- EP0236166B1 EP0236166B1 EP87400158A EP87400158A EP0236166B1 EP 0236166 B1 EP0236166 B1 EP 0236166B1 EP 87400158 A EP87400158 A EP 87400158A EP 87400158 A EP87400158 A EP 87400158A EP 0236166 B1 EP0236166 B1 EP 0236166B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- pump
- liquid
- turbine
- fluid
- inlet
- Prior art date
- Legal status (The legal status 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 status listed.)
- Expired - Lifetime
Links
- 239000012530 fluid Substances 0.000 title claims description 37
- 238000000034 method Methods 0.000 title claims description 12
- 238000005086 pumping Methods 0.000 title claims description 10
- 238000009434 installation Methods 0.000 title description 7
- 239000007788 liquid Substances 0.000 claims description 37
- 239000007789 gas Substances 0.000 claims description 17
- 239000000203 mixture Substances 0.000 claims description 14
- 239000007791 liquid phase Substances 0.000 claims description 9
- 238000004891 communication Methods 0.000 claims description 5
- 239000007792 gaseous phase Substances 0.000 claims description 5
- 230000005514 two-phase flow Effects 0.000 claims description 3
- 230000000063 preceeding effect Effects 0.000 claims 2
- 235000021183 entrée Nutrition 0.000 description 4
- 239000003921 oil Substances 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 210000004027 cell Anatomy 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D31/00—Pumping liquids and elastic fluids at the same time
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D13/00—Pumping installations or systems
- F04D13/02—Units comprising pumps and their driving means
- F04D13/04—Units comprising pumps and their driving means the pump being fluid driven
Definitions
- the present invention relates to methods and installations for circulating fluids by pumping. More particularly, the invention relates to methods and installations for pumping fluids composed of at least one liquid phase and at least one gaseous phase, the latter making pumping very difficult.
- the ejector thus formed applies an initial pressure increase to the fluid in the well.
- the liquid should therefore leave the turbine while also having a certain pressure.
- the energy of the liquid is not optimally used in the turbine, since part of this energy is necessary for a downstream operation.
- this has the disadvantage that the pump must be designed for a large flow rate and therefore requires a large power .
- the liquid serves as the supply fluid for the turbine of the turbomachine, supplying the energy necessary for the operation of the pump.
- Part of the liquid also serves to decrease the gas content of the fluid and thus make it acceptable so that the mixture of fluid and liquid can be pumped. Since as little expanded turbid liquid is passed through the pump as possible, it requires as little power as possible.
- the liquid is completely expanded in the turbine and neither is it allowed kinetic energy.
- the turbine thus operates under the best conditions.
- the gas content of the fluid is detected and the proportion of the liquid mixed with the fluid is modified as a function of the gas content detected.
- the ratio between the quantity of turbinated liquid entering the mixture and that which is discharged can vary between 0 and 0.5.
- the flow rate of turbinated liquid mixed with the fluid which represents from 0 to 2 parts by volume per 1 part of the fluid, is equal to the flow rate of liquid, separated in the form of a first stream and representing from 25% to 65% of the volume of the mixture, which leaves the pump.
- the invention also relates to a pumping installation comprising a fluid source and a turbomachine comprising a pump, having an inlet and an outlet, and a turbine which is set on the same shaft as the pump and which has an inlet and an outlet, the outlet of the turbine opening into a conduit putting the source in communication with the pump.
- the installation is characterized by a rejection or return duct communicating with the outlet of the turbine and by a device making it possible to regulate the quantities of liquid coming from the outlet of the turbine which go into the rejection or return duct and into the conduit putting the source in communication with the pump.
- the installation comprises a detector of the gas content of the fluid and the device making it possible to adjust the quantities of liquid is controlled by the detector via a control line as a function of the levels detected.
- the installation comprises an apparatus for separating a fluid consisting of a gas phase and a liquid phase into a first stream richer in the liquid phase than the fluid and into a second stream, the apparatus being provided an input which communicates with the output of the pump and two outputs, one of which for the first current communicates with the input of the turbine.
- the pump is such that the curve representing the value of the curvature along the skeleton of the profile of a blade as a function of the curvilinear absence along this skeleton, has a slope whose value gradually increases from the edge of attack towards the trailing edge of the blade, as described in French patent 7,536,774; the pump advantageously has the other characteristics defined in this patent, but the pump can have any other hydraulic specially adapted to two-phase flows.
- Fluid composed of a liquid phase and a gaseous phase comes from a source 1 through a conduit 2.
- a conduit 3 coming from the outlet 4 of a turbine 5 of a turbomachine.
- This machine essentially comprises the turbine having the outlet 4 and an inlet 6 and a pump 7 having an inlet 8 and an outlet 9 and wedged on the same shaft 10 as the turbine 5.
- a detailed description of this turbomachine can be found in French patent 7823250 .
- a device 18 making it possible to adjust the quantities of liquid which go respectively to the conduit 11 and to a rejection conduit 17.
- the device 18 is controlled via a line 20 by a detector 19 which detects the gas contents of the fluid passing through line 2.
- the mixture of fluid and liquid is sent under a pressure of between 10 and 100 bar, via a conduit 11, to the inlet 8 of the pump 7.
- the latter discharges it through the outlet 9 and through a conduit 12 into a separation apparatus 13, where the mixture, optionally after settling or centrifugation of the solid materials, is separated into a first stream going through the conduit 14, with compression in a pump 16 at a pressure between 20 and 250 bar, at the inlet 6 of the turbine 5 and in a second stream discharged through a conduit 15.
- the gas content of the first stream is less than 5% by volume.
- 60 m 3 / h of gas-free oil are sent to the turbine under a pressure of 100 bar.
- the turbomachine rotates at 6000 rpm.
- the pressure relief height in the turbine is 800 m.
- the expanded oil is mixed with 60 m 3 / h of crude oil having a GLR of 10.
- GLR represents the ratio of the volume of gas to the volume of liquid.
- the head of the pump is 150 m. Despite its high GLR, the crude can thus be pumped without difficulty.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Structures Of Non-Positive Displacement Pumps (AREA)
- Jet Pumps And Other Pumps (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8601763A FR2594183A1 (fr) | 1986-02-10 | 1986-02-10 | Procede et installation pour faire circuler des fluides par pompage |
FR8601763 | 1986-02-10 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0236166A1 EP0236166A1 (fr) | 1987-09-09 |
EP0236166B1 true EP0236166B1 (fr) | 1990-10-03 |
Family
ID=9331956
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP87400158A Expired - Lifetime EP0236166B1 (fr) | 1986-02-10 | 1987-01-23 | Procédé et installation pour faire circuler des fluides par pompage |
Country Status (7)
Country | Link |
---|---|
US (1) | US4712984A (no) |
EP (1) | EP0236166B1 (no) |
JP (1) | JPS62191671A (no) |
DE (1) | DE3765271D1 (no) |
ES (1) | ES2018026B3 (no) |
FR (1) | FR2594183A1 (no) |
NO (1) | NO168965C (no) |
Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2215402B (en) * | 1988-02-29 | 1992-06-17 | Shell Int Research | Apparatus for pumping well effluents |
FR2680983B1 (fr) * | 1991-09-10 | 1993-10-29 | Institut Francais Petrole | Dispositif melangeur continu, procede et utilisation dans une installation de pompage d'un fluide de forte viscosite. |
US5323823A (en) * | 1992-12-11 | 1994-06-28 | Roto Zip Tool Corporation | Wood router bit |
US5562405A (en) * | 1994-03-10 | 1996-10-08 | Weir Pumps Limited | Multistage axial flow pumps and compressors |
GB9526369D0 (en) * | 1995-12-22 | 1996-02-21 | Weir Pumps Ltd | Improved multistage pumps and compressors |
FR2748532B1 (fr) * | 1996-05-07 | 1999-07-16 | Inst Francais Du Petrole | Systeme de pompage polyphasique et centrifuge |
FR2748533B1 (fr) * | 1996-05-07 | 1999-07-23 | Inst Francais Du Petrole | Systeme de pompage polyphasique et centrifuge |
US5863188A (en) * | 1996-07-12 | 1999-01-26 | Dosman; James A. | Fluid flow reducer |
BR0103443A (pt) * | 2001-08-21 | 2004-03-09 | Petroleo Brasileiro Sa | Sistema e método de bombeio multifásico |
US20110223039A1 (en) * | 2010-03-15 | 2011-09-15 | General Electric Company | Pump assembly and method |
NO337108B1 (no) * | 2012-08-14 | 2016-01-25 | Aker Subsea As | Flerfase trykkforsterkningspumpe |
US9512700B2 (en) | 2014-11-13 | 2016-12-06 | General Electric Company | Subsea fluid processing system and an associated method thereof |
CN107532470B (zh) * | 2015-04-01 | 2019-10-18 | 沙特阿拉伯石油公司 | 用于油气应用的流体驱动混合系统 |
US10463990B2 (en) | 2015-12-14 | 2019-11-05 | General Electric Company | Multiphase pumping system with recuperative cooling |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US975526A (en) * | 1910-09-15 | 1910-11-15 | Ernest K Hood | Propeller turbine-pump. |
US1842961A (en) * | 1925-11-16 | 1932-01-26 | Anna M C Wechsberg | Locomotive feed water heater |
DE1103687B (de) * | 1959-06-30 | 1961-03-30 | Siemens Ag | Gasturbinen-Anlage |
US3194026A (en) * | 1963-10-24 | 1965-07-13 | Fleur Corp | Power-refrigeration system |
US3420434A (en) * | 1966-12-30 | 1969-01-07 | Judson S Swearingen | Rotary compressors and systems employing same using compressor gas as seal gas |
US3981626A (en) * | 1975-02-06 | 1976-09-21 | Sundstrand Corporation | Down hole pump and method of deep well pumping |
US4035023A (en) * | 1975-07-15 | 1977-07-12 | Freeport Minerals Company | Apparatus and process for hydraulic mining |
US4271664A (en) * | 1977-07-21 | 1981-06-09 | Hydragon Corporation | Turbine engine with exhaust gas recirculation |
FR2417057A1 (fr) * | 1978-02-14 | 1979-09-07 | Inst Francais Du Petrole | Methode et dispositif pour transporter par canalisation un fluide compose essentiellement d'une masse gazeuse |
NO148199C (no) * | 1978-02-24 | 1983-08-24 | Inst Francais Du Petrole | Fremgangsmaate og anordning for transport av et tofasefluid i en roerledning. |
US4233154A (en) * | 1978-12-29 | 1980-11-11 | Kobe, Inc. | Method for treating petroleum well pumping power fluid |
US4292011A (en) * | 1979-08-20 | 1981-09-29 | Kobe, Inc. | Turbo pump gas compressor |
NL8001472A (nl) * | 1980-03-12 | 1981-10-01 | Tno | Installatie voor warmteterugwinning bij verbrandingsmachine met compressor. |
FR2557643B1 (fr) * | 1983-12-30 | 1986-05-09 | Inst Francais Du Petrole | Dispositif d'alimentation d'une pompe de fluide diphasique et installation de production d'hydrocarbures comportant un tel dispositif |
-
1986
- 1986-02-10 FR FR8601763A patent/FR2594183A1/fr active Pending
-
1987
- 1987-01-23 ES ES87400158T patent/ES2018026B3/es not_active Expired - Lifetime
- 1987-01-23 EP EP87400158A patent/EP0236166B1/fr not_active Expired - Lifetime
- 1987-01-23 DE DE8787400158T patent/DE3765271D1/de not_active Expired - Fee Related
- 1987-02-04 US US07/010,686 patent/US4712984A/en not_active Expired - Lifetime
- 1987-02-09 NO NO870493A patent/NO168965C/no unknown
- 1987-02-10 JP JP62027426A patent/JPS62191671A/ja active Pending
Also Published As
Publication number | Publication date |
---|---|
DE3765271D1 (de) | 1990-11-08 |
NO168965C (no) | 1992-04-22 |
NO870493L (no) | 1987-08-11 |
ES2018026B3 (es) | 1991-03-16 |
US4712984A (en) | 1987-12-15 |
FR2594183A1 (fr) | 1987-08-14 |
JPS62191671A (ja) | 1987-08-22 |
NO870493D0 (no) | 1987-02-09 |
NO168965B (no) | 1992-01-13 |
EP0236166A1 (fr) | 1987-09-09 |
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