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Publication numberUS3704567 A
Publication typeGrant
Publication dateDec 5, 1972
Filing dateDec 9, 1970
Priority dateDec 9, 1970
Publication numberUS 3704567 A, US 3704567A, US-A-3704567, US3704567 A, US3704567A
InventorsEngel Robert F
Original AssigneeShell Oil Co
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Well production method and apparatus
US 3704567 A
Abstract
A multiphase hydrocarbon mixture is produced from each of a plurality of wells. The multiphase mixture is pressurized by a single machine without separating the gas and liquid components. The multiphase mixture is then transported through a conduit to a treating facility where the gas and liquid components are separated for ultimate sale or use.
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Description  (OCR text may contain errors)

[451 Dec. 5, 1972 United States Patent Engel WELL PRODUCTION METHOD AND APPARATUS XX X 64 6 4754 I 5/ 5 5 55 5 J.

[ 2,937,140 5/ 1960 Strnson 3,246,451 4/1966 Glasgow [72] Inventor: Robert F. Engel, New Orleans, La. 3474596 10/1969 F? 3,486,297 12/1969 Elslnga et a1. [73] Assignee: Shell Oil Company, New York, N.Y.

[22] Filed:

Primary Examiner-Reuben Friedman Assistant Examiner-R. W. Burks Dec. 9, 1970 21] Appl. No.: 96,500

Attorney-Harold L. Denkler and Theodore E. Bieber [57] ABSTRACT A multiphase hydrocarbon mixture is produced from .B01d 19/00 each of a plurality of wells. The multiphase mixture is pressurized by a single machine without separating the [52] US. [51] Int. Cl. [58] Field of Search.....

r gas and liquid components. The multiphase mixture is [56] Relerences Cited then transported through a conduit to a treating facili- UNITED STATES PATENTS ty where the gas and liquid components are separated for ultimate sale or use.

2,773,556 12/1956 Meyers et al.l'.....................55/l7S X 2,381,695 8/1945 Sennet....;.............;...........417/3ll X 12 Claims, 2 Drawing Figures LIQUIDS N o B R A C 6 m N D l T A H E R TW R E 'T NI A AC w M m L S D. 'A N A H PATENTED DEC 5 m2 SHEET 1 or 2 Robert F. Engel INV ENT OR PATENTEIIUEB 5 I972 3,704,567

sum a nr 2 204 i ij IZO HANDLING AND TREATING FACILITY GAS WATER HYDROCARBON I96 LIQUIDS Robert FEngel I Fig. 2 INVENTOR WELL PRODUCTION Ma rrron AND APPARATUS BACKGROUNDOFTI-IE INVENTION The term oil well" is used in the industry to connote a well producing predominantly liquid hydrocarbons. This term is somewhat misleading since almost all oil wells produce some gaseous hydrocarbons and, conversely, most gas wells produce some quantity of liquid hydrocarbons. It is a characteristic of oilwells that the tubing string or other production conduit is more or lessfilled with liquid. Even though the formation pressure may be substantiaLthe wellhead pressure of an oil well is characteristically low to moderate. Conversely, gas wells do not characteristically have a column of liquid in the production conduit and the wellhead pressure is accordingly a substantial fraction of the formation pressure.

It is desirable in many produced fluids to a relatively remote facility for treating and/or separating the produced fluids. Since gas wells typically exhibit a substantial wellhead pressure, such wells may be produced into a conduit for transmitting all produced fluids to a treating facility without having tocompress the well fluids. Since oil wells do not typically exhibit a substantial wellhead pressure and since they produce a large proportion of liquid, the wellhead pressure is often insufficient to'move the produced fluids through a single conduit to a remote treating facility. Consequently, oil wells produced in this manner are typically provided with a gas-oil separator adjacent the wellhead with separate conduits being provided for the oil and gas respectively. Pump and/or compressor facilities .are provided adjacent the wellhead to move the produced fluids separately to a treating facility and/or to points of sale or use.

Situations commonly. exist where it would be desirable to transmit produced fluids from a plurality of oil wells to a common treatment facility. One common situation is where a number of oil wells are located in inland waters or near shore where a large onshore treating facility havingthe capacity of treating production from a large number of wells is substantially cheaper than separate treatingfacilities located in the water for each of the wells. Another common situation is where a plurality of oil wells are located offshore producing onto a platform having no treatment facility where a'platform and treating facility is located nearby. Another situation is where a plurality of oil wells are completed underwater or on shore which do not separately produce enough gaseous hydrocarbons to justify separate gas handling facilities.

The prior art has avoided laying separate gas and liquid gathering systems to a plurality of oil wells only by separating the produc d fluids at each wellhead, elevating the pressure of the separate phases and then commingling the separate phases for delivery into a single conduit. While this approach avoids laying separate conduits, it is still quite expensive because of the cost of individual gas compressing and oil pumping equipment.

It will be appreciated by those skilled in the art that the ability to transport low pressure multiphase fluids from a plurality of oil wells through a single conduit without having to separate and then separately pressurize the fluid phases can have many applications.

instances to transport SUMMARY OF THE INVENTION It is an object of this invention to provide a method of producing a low pressure multiphase mixture from a plurality of wells and transporting the mixtures through a single conduit for treatment at a common facility without having to separate and separately pressurize the fluid phases.

- Another object of the invention is to provide a method and apparatus for producing a two phase fluid from a plurality of wells and pressurizing the two phase 1 fluid adjacent the wells where some of the liquid phase material is recycled through the compressor to provide sufficient fluid to lubricate and cool the heat of compression. I I i The method of this invention comprises producing from each of a plurality of wells a multiphase mixture i including liquid and gaseous hydrocarbons; pressurizing the multiphase mixture adjacent the wells; transporting the multiphase mixture through a conduit to a treating facility; and separating the liquid and gaseous components at the treating facility.

The combination of this invention comprises a plurality of wells for producing a low pressure multiphase mixture including liquid and gaseous hydrocarbons; multiphase machine means for receiving the low pressure mixture and elevating the pressure thereof; a treating facility common to the plurality of wells; and conduit means receiving the low pressure multiphase mixture from the wells and delivering the same through the multiphase machine means to the common facility. BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic view of one production arrangement of the. invention illustrating a plurality of wells connected'to a single machine for delivery to a 1 common handling and treating facility; and

FIG. 2 is a schematic view of another arrangement of the invention illustrating a pluralityof wells delivering a low pressure multiphase mixture to separate multiphase machines means for delivery to a common handling and treating facility. I

DESCRIPTION OF THE PREFERRED EMBODIMENTS Referring to FIG. 1, there is illustrated a production system 10 comprising as major components a plurality of wells 12 producing a low pressure multiphase mixture including liquid and gaseous hydrocarbons, means 14 for receiving,initially treating and initially transporting the multiphase mixture, machine means 16 for elevating the pressure of the multiphase mixture, means 18 for transporting the high pressure multiphase mixture and a handling and treating facility 20 for separating the mixture into salable or usable components. It will be seen that the general plan of operation is to pressurize the low pressure multiphase mixture for transport through a conduit to a common treatment facility rather than separating the phases of the mixture, separately compressing the phases and then recombining the phases for transportation purposes.

Each of the wells 12 comprises a production conduit or tubing string 22 having a suitable valve 24 thereon. The wells 12 produce a low pressure multiphase mixture including liquid and gaseous hydrocarbons. The

3 wells 12 may also produce substantial quantities of salt water and/or sand. As will be apparent, the ,components of the initialtreating and transporting means 14 depend in large part on the relative quantity of sand and salt water produced from the wells 12. r

The initial treating and transportingmeans 14'comprises a gatheringsystem 26 collectingthe' produced mixture from each of the wells 12 and delivering it to a desander 28. The desander 28 is particularly desirable to protect the machine 16 if the wells 12 produce a substantial amount of sand. It may be desirable to include the desander 28 as a preventive measure even if the wells 12 do'not produce sand'at the time the system is installed. The desander 28 includes an outlet conduit 30 having a valve 32 therein controlled by a timer 34' or other suitable mechanism. A sand deoiler 36 may be provided to remove oil absorbed on the sand, particularly ifa large quantity of sand is produced by the wells 12. The deoiler 36 includes an outlet conduit 38 having a suitable valve 40 therein for discharging sand from the system 10. The deoiler 36 also includes an oil outlet 42 having a pump 44 therein for delivering oil to .the transporting means 18 as will be more fully apparent hereinafter. I

The initial treating and transporting means 14 also includes a conduit 46 connecting'the desander 28 to a free water knockout 48 which 'may desirably be provided if the wells 12 produce a substantial amount of water. As will be apparent to those skilled in the art, the horsepower expended by the machine 16 to move liquid through the transporting means 18 is relatively small. Consequently, the decision to incorporate the free water knockout 48 in the system 10 depends not only on the total amount of water produced by the wells l2but also the capacity of themachine 16, the transporting means 18 and the handling facility 20. The

The machine 16 includesan outlet 66 which is connected to a conduit 68. If the gas-oil ratio of the wells 12 is below about 1500 cubic feet per barrel, there is sufficient liquid passing through the machine 16 to perform the cooling, sealing and lubricating functionsyln this event, the conduit 68 may be directly connected to the transporting means 18 for delivering the multiphase mixture to the handling facility 20. In the event the gasoil ratio of the wells 12 is higher,.means 70 may be provided for recirculating part of the liquids throughthe machine l6 to provide a sufficient quantity of liquid therefor.

The recirculating means 70 comprises a separator 72 for extracting liquid from the multiphase mixture passing therethrough and includes an oil outlet 74 leading to the connection 58 for delivering liquid into the conduit 62. A suitable control valve 76 is positioned in the oil outlet74 and includes a valve operator 78 controlled through a control line 80 leading to a flow meter 82 in the oil line. 60, and a pressure controller 84 associated with the conduit 62. The flow meter 82 includes an orifice plate 86 or other suitable measuring device to ascertain the quantity of liquid flowing free water knockout 48 is basically a gas-liquid separator having a water outlet conduit 50 anda valve 52 therein controlled by a water level sensor 54- for discharging water from the system 10.

A gas outlet conduit 56 connects the upper end of the free water knockout 48 to a connection. 58. An oil outlet conduit 60 extends from intermediate the free water knockout 48 to the connection 58 to commingle the oil and gas emitting from the free water knockout 48. A conduit 62 extends from the connection 58 to an inlet 64 of the machine 16 for carrying the com mingled fluids thereto.

The machine 16 may be any suitable type multiphase helical-rotor type machine including that shown in U.S. Pat. No. 2,381,695 but is preferably of the type presently available from Ingersoll-Rand Corporation under the tradename H-AXl Compressor. Compressors of this latter type comprise single or multiple compression stages and utilize the liquid phase passing therethrough as a coolant, sealant and lubricant for the internal moving parts. In the normal mode of operation, compressors of this type are used to compress gasses only with the necessary liquid being injected into the compressor inlet, passed through the compressor to perform the desired functions and separated in the outlet stream for reuse. Compressors of this type may be driven by any suitable means,-e.g. .electric motors, turbines, internal combustion engines, diesel engines and the like.

through the oil line 60. The pressure controller 84 includes a control line 88 in communication with the conduit '62. The pressure controller 84 ascertains' if there is sufficient fluid passing throug'hthe machine 16 and if there is an adequate input to prevent the machine 16 from operating without suction fluid.

The recirculating means alleviates two distinct problems. If the wells 12 do not produce sufficient liquid to cool, seal and lubricate'the machine 16, the recirculating means 70 provides additional liquid for these functions. When insufficient liquid is flowing through the oil outlet 60 to cool, seal and lubricate the machine means '16, a signal is generated by the flow meter 82 which is transmitted to the valve operator 78 through the control line 80. The valve 76 is thereupon opened todeliver additional liquid to the conduit 62. The other function of the recirculating means 70 is to keep the machine 16 loaded. When-the pressure at the machine inlet 64 falls below a predetermined value, the machine 16 is starved and will not function properly. The pressure controller 84 senses the pressure at the machine inlet and provides a signal when the inlet pressure falls below the predetermined value. The pressure controller 84 thereupon transmits a signal through the control line to manipulate the valve operator 78 to deliver oil and gas, if required, through the oil outlet 74 into the conduit 62. While the oil outlet 74 is normally below the liquid level in the recirculating means 70, under some load conditions the machine 16 will draw the liquid level down and gas will be circulated through the machine.

The temperature in the outlet stream from the machine means 16 is quite hot and is typically on the order of about 200 F. Without some cooling, it will be apparent that liquids of this temperature do not efficiently cool the machine 16 when circulated therethrough. Accordingly, a heat exchanger 92 is provided in heat exchanging relation with the oiloutlet 74 to depress the temperature of the oil stream passing into the connection 58.

The separator 72 is equipped with a liquid outlet 94 having a valve 96 therein controlled by a liquid level sensor 98. It will be noted that the liquid level sensor 98 is above the oil outlet 74 to provide a liquid reservoir for recirculation at any time. It will also be seen that oil is recirculated through the machine 16 rather than water which will tend to collect in the bottom of the separator 72.

The separator 72 also includes a gas outlet 100 joining the liquid outlet 94 for commingling the fluid phases emitting from the, separator 72. The oil outlet 42 from the sand deoiler 36 also merges with the conduits 94, 100 for delivery to the transporting means 18. A gas line 102 may be connected to the gas outlet 100 to deliver high pressure gas for gas lift purposes and the like to the wells 12.

The transporting means 18 comprises a conduit 104 in fluid receiving relation with the conduits 42, 94, 100 for delivering a multiphase high pressure mixture to the handling facility 20. The conduit 104 is of whatever length necessary to reach the handling facility 20. The handling and treating facility 20 may be of any desired type to separate and/or treat the multiphase mixture for ultimate sale, use or disposition of the fluid com ponents.

. In the operation of the production system 10, a low pressure multiphase fluid mixture is produced from the wells 12 and typically includes oil, gas, water, and sand. The desander 28 removes sand above a predetermined size from the mixture. The mixture then passes into the free water knockout 48 where a large proportion of salt water produced from the wells 12 is discharged from the system 10. Gas and liquid hydrocarbons separately emitting from the free water knockout 48 are recombined at the connection 58 and pass through the conduit 62 into the machine 16. The machine inlet pressure and temperature are typically on the order of about to 200 psig and to 100 F. The mixed fluid stream emittingfrom the machine outlet 66 is typically at about 400 to 1,400 psig and 100 to 300 F.

If insufficient liquid is passing through the oil outlet or if the machine inlet pressure falls below a predetermined value, the valve 76 is opened allowing some of the oil accumulating in the separator to flow past the heat exchanger 92 and into the conduit 62 for recirculation. When the liquid level in the separator 72 rises above the sensor 98, the valve 96 is opened allowing liquid to flow into the conduit 104 for transport to the handling facility 20. Gas from the separator 72 passes through the outlet and is commingled with the liquid stream in the conduit 104.

A comparison of this invention with the typical oil well production plan where the oil and gas are separated, separately pressurized and then commingled for transport through a common conduit to a treating facility reveals that the production system of this invention is substantially cheaper than the prior art approach. The most expensive single item of the prior art approach is the gas compressor which has been omitted entirely. For offshore installations, the construction cost of a production system of this invention is about two-thirds that of the conventional approach.

Referring to FIG. 2, there is illustrated a production system comprising another embodiment of this invention and including as major components a plurality of wells 112 producing a low pressure multiphase mixture including liquid and gaseous hydrocarbons, means 114 for receiving, initially treating and initially transporting the multiphase mixture, machine 116 for elevating the pressure of the multiphase mixture, means 118 for transporting the high pressure multiphase mixture and a handling and treating facility 120 for separating the mixture into salable or usable components. It will be seen that the general plan of operation is to pressurize the low pressure multiphase mixture for transport through a conduit to a common treatment facility rather than separating the phases of the mixture, separately pressurizing the phases and then recombining the phases for transportation purposes.

It will be seen that the production system 110 differs from the system 10 in that each of the wells 112 is provided with machine 16 for elevating the pressure of the multiphase mixture produced thereby. For purposes of brevity, analogous reference characters are used to indicate analogous components of the system 110 and only the differences between the system 10, 110 are described with specificity.

Since individual machines 116 are provided for each of the wells 112, the initial transporting means 114 includes a gathering system 126 leading to only one well. The initial transporting and treating means 114 is not illustrated as including a sand deoiler since the quantity of sand produced by each of the wells 112 is probably insufficient to justify a deoiler. Such devices may be included, of course, if desired.

The liquid carrying capacity of the compressors of the type envisioned for use as the machine 116 is quite high. Consequently, it is unlikely that the wells 112 will each produce more liquid than can be handled by the machine 116. Consequently, the low pressure free water knockout is omitted from the system 110 although such devices may be incorporated if desired.

Since the system 110 is not equipped with a low pressure free water knockout and since it is desirable to measure the liquid flowing toward the machine, the flow meter 182 is a meter to determine the quantity of liquid flowing in the conduit 146. The flow meter 182 is equipped with means for actuating the valve operator 178 when the liquid passing therethrough falls below a predetermined value. In this manner liquid may be recirculated from the separator 172 to ensure adequate sealing, cooling and lubricating of the machine 116.

Where the wells being produced are closely spaced, e.g., offshore wells producing on a platform, the production system 10 is preferred because of the cost savings over the system 110. With widely spaced wells, e.g., underwater completions, the production system 110 is preferred.

It will be seen that there is provided a well production method and apparatus having many applications for present and contemplated situations.

I claim as my invention:

1. The method of producing a plurality of wells comprising the steps of producing from each of the plurality of wells a low pressure multiphase mixture including liquid and gaseous hydrocarbons;

pressurizing the multiphase mixture adjacent the plurality of wells;

transporting themultiphase mixture through a conduit to a treating facility; and separating the liquid and gaseous hydrocarbons at the treating facility.

2. The method of claim 1 wherein the producing step comprises commingling the multiphase mixture from the plurality of wells before the pressurizing step.

3. The method of claim 1 comprising the steps of extracting liquid from the high pressure mixture; and

delivering the extracted liquid into the low pressure multiphase mixture for repressuring.

4. The method of claim 3 further comprising sensing the pressure of the low pressure multiphase mixture; and wherein the delivering step is conducted in response to the pressure of the low pressure multiphase mixture below a predetermined value.

5. The method claim 3 further comprising measuring the liquid in the low pressure multiphase mixture before the pressurizing step; and wherein the delivering step is conducted in response to the flow rate of the liquid below a predetermined value.

6. In combination,

a plurality of wells for producing a low pressure multiphase mixture including liquid and gaseous hydrocarbons;

a machine for receiving the low pressure mixture and elevating the pressure thereof;

a treating facility common to the plurality of wells;

and

conduit means receiving the low pressure multiphase mixture from the wells and delivering the same through the machine to the common facility.

7. The combination of claim 6 further comprising means upstream of the machine for desanding the low pressure multiphase mixture. 8. Thecombination of claim 6 further comprising a free water knockout upstream of the machine.

9. The combination of claim 6 wherein the machine is of the type circulating liquid therethrough for sealing the moving parts and for cooling the machine and further comprising means downstream of the machine for extracting high pressure liquid from the high pressure mixture and delivering the extracted liquid into the suction inlet. 1

10. The combination of claim 9 wherein the extracting and delivering means includes normally closed valve means for controlling delivery of extracted liquid into the suction inlet; and

means responsive to suction inlet pressure below a predetermined value for opening the valve means.

1 l. The combination of claim 10 further comprising a separator in the conduit means upstream of the machine for separating gas and liquid phases in the mixture, the separator having a gas outlet and a liquid outlet; and wherein the extracting and delivering means includes means responsive to liquid flow through the liquid outlet below a predetermined value for opening the valve means.

12. The combination of claim 10 wherein the delivering and extracting means includes means responsive to the amount of liquid flowing toward the machine below a predetermined value for opening the valve means.

Patent Citations
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US2381695 *Mar 11, 1943Aug 7, 1945Laval Steam Turbine CoPumping system
US2773556 *Jan 18, 1955Dec 11, 1956Shell DevApparatus for automatically treating and metering oil field production
US2937140 *Jul 19, 1956May 17, 1960Phillips Petroleum CoTreatment of petroleum well effluents
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Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US5601635 *Oct 25, 1994Feb 11, 1997Spiro Research B.V.Method and apparatus for deaerating a liquid in a substantially closed liquid circulation system
US5900137 *Jun 27, 1996May 4, 1999Homan; Edwin DarylApparatus and method for separating components in well fluids
US5928519 *Nov 3, 1997Jul 27, 1999Homan; Edwin DarylControlling operating pressure in high pressure separator which receives bore hole fluid by controlling the outflow of gas from separator in response to pressure variations within bore hole during under-balanced drilling
US6132494 *Nov 27, 1995Oct 17, 2000Read Group A/SDynamic separation of liquid phase in dehydration step and split into light oil phase and heavy water phase, dynamic separation of the water phase to deoil and produce pure water and reject; gas phase injected into a water injection flow
US6197095 *Feb 16, 1999Mar 6, 2001John C. DitriaFor remote separation operation at deep and ultra deep water depths for processing well fluids and solids prior to transport to surface, or disposal either subsea or to surface
US6299672 *Oct 15, 1999Oct 9, 2001Camco International, Inc.System for separating gas from liquid in production well fluid comprising: separation unit including storage tank; first separation stage to separate gas from liquid; second separation stage; electric submersible pumping system
US6989103 *Oct 10, 2001Jan 24, 2006Schlumberger Technology CorporationFor oil and gas wells; acid neutralization of fluid; adjustment of pH; mixing with surfactant
US7347945 *Apr 26, 2001Mar 25, 2008Schlumberger Technology CorporationHaving gravity separator means whose geometrical separation characteristics can be adjusted during separation; to treat the effluent in the separator regardless of how the volume ratios of the various phases fluctuate as a function of time
US8317904 *Jan 5, 2009Nov 27, 2012Caltec LimitedSand separation system and method
US20110036239 *Jan 5, 2009Feb 17, 2011Mir Mahmood SarsharSand separation system and method
US20120160103 *Sep 1, 2010Jun 28, 2012Aruljothy SuppiahSlug Suppressor Apparatus and Crude Oil Stabilization Assembly and Process Therefor
WO2012030431A1 *Jul 1, 2011Mar 8, 2012General Electric CompanySystem and method for multiphase pump lubrication
Classifications
U.S. Classification95/19, 96/183, 95/247, 96/174
International ClassificationE21B43/00, E21B43/34
Cooperative ClassificationE21B43/00, E21B43/34
European ClassificationE21B43/34, E21B43/00