EP0874694B1 - Ensemble separateur a cyclone et procede - Google Patents

Ensemble separateur a cyclone et procede Download PDF

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Publication number
EP0874694B1
EP0874694B1 EP97900336A EP97900336A EP0874694B1 EP 0874694 B1 EP0874694 B1 EP 0874694B1 EP 97900336 A EP97900336 A EP 97900336A EP 97900336 A EP97900336 A EP 97900336A EP 0874694 B1 EP0874694 B1 EP 0874694B1
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EP
European Patent Office
Prior art keywords
manifold
housing
separator
disposed
fluid pump
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.)
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EP97900336A
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German (de)
English (en)
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EP0874694A1 (fr
Inventor
Bill E. Bowers
Gunnar John Hole
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Baker Hughes Ltd
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Baker Hughes Ltd
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Priority claimed from GB9600600A external-priority patent/GB2308995B/en
Priority claimed from US08/613,929 external-priority patent/US6080312A/en
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00—Apparatus in which the axial direction of the vortex is reversed
    • B04C5/24—Multiple arrangement thereof
    • B04C5/28—Multiple arrangement thereof for parallel flow
    • E—FIXED CONSTRUCTIONS
    • E21—EARTH OR ROCK DRILLING; MINING
    • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/34—Arrangements for separating materials produced by the well
    • E21B43/38—Arrangements for separating materials produced by the well in the well
    • E21B43/385—Arrangements for separating materials produced by the well in the well by reinjecting the separated materials into an earth formation in the same well
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00—Apparatus in which the axial direction of the vortex is reversed
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00—Apparatus in which the axial direction of the vortex is reversed
    • B04C5/08—Vortex chamber constructions
    • B04C5/081—Shapes or dimensions

Definitions

  • the present invention relates to an apparatus for the separation of liquids of differing densities in production streams from underground wells. More particularly, the invention relates to an apparatus for use in the borehole of a wall according to the preamble of claim 1 (see WO-A-94/13930).
  • Hydrocyclones are compact, centrifugal separators with no moving parts, which separate liquids in a liquid mixture. Hydrocyolones are widely used in both onshore and offshore oil production in above-ground applications such as bulk water knockout from produced fluids, de-oiling produced water prior to either water reinjection into a formation or water disposal to a disposal site. In these applications a plurality of hydrocyclones are typically mounted within a pressure vessel assembly. Such an assembly resembles a shell-and-tube heat exchanger, in that the hydrocyclones are mounted to tub sheets which are sandwiched between flanges in the pressure vessel.
  • the complete pressure vessel assembly typically has a single inlet for the produced liquid stream, which comprises as for example, a mixture of oil and water and a plurality of outlets for the separated liquid streams.
  • the assembly has an outlet for the "clean water” stream, which is relatively depleted in oil as compared to the production liquids, and an outlet for the "dry oil” stream, which is relatively enriched in oil as compared to the produced liquids.
  • Hydrocyclones as they are employed in oil production and environmental cleanup applications are designed foremost to remove oil from water, that is, to produce a clean water stream with as low a concentration of oil as practicable.
  • the dry oil stream will typically contain about 50 per cent water, by volume, and may contain more than 50 per cent water.
  • Hydrocyclones, in a single-stage configuration cannot produce both a completely water-free oil stream and a completely oil-free water stream; the design performance must be biased towards either the "dry oil” stream or the "clean water” stream.
  • a clean water stream is obtained at the expense of "wet oil”.
  • a dry oil stream is obtained at the expense of oily water.
  • Multi-stage separator assemblies including multiple hydrocyclones arranged in series, such as taught by U.S. Patent No. 4,738,779 can achieve improved separation at the expense of increasing the pressure drop of the liquids moving through the multi-stage assembly.
  • Hydrocyclones are also useful for making a preliminary separation of oil from water in the production liquids produced downhole in an oil well prior to the production liquids being transported to the surface. This is of particular value in high water cut wells, with a high water content, where the production liquids may comprise about 70 per cent, or more, water. Conventionally, this water must be transported above ground, at significant cost and then disposed of, at additional expense. Hydrocyclone assemblies designed for above-ground use however, are not suitable for downhole applications where the assembly must be disposed within the bore hole of an oil well. This is because conventional hydrocyclone assemblies of sufficient capacity exceed the size limitations imposed by the diameter of the well. Further, previous attempts to overcome these problems have resulted in additional complications.
  • PCT International Application WO 94/13930 discloses a downhole separation apparatus in which one or more hydrocyclones are contained within an axially elongate tubular housing, with the inlet of each hydrocyclone extending through the wall of the housing and having an opening external of the housing.
  • the separated dry oil and clean water streams from each hydrocyclone are transported from the housing by a relatively complex system of pipes.
  • This apparatus there must be sufficient clearance between the housing and the adjacent wall of the well casing to provide a flow annulus for transporting the production fluid to the hydrocyclone inlets. This limits the diameter of the hydrocyclone housing for a given size casing, and hence reduces the capacity of the separation apparatus.
  • the internal space within the housing, but outside of the separators and piping, is dry, so that there is a very substantial pressure differential across the walls both of the housing and the piping within the housing. Further, the housing must be tightly sealed against the full well bore pressure. This obviously requires the use of heavy gauge and/or specialty materials for construction of the housing, which results in increased costs for both materials and fabrication, and increases the risk of failure of the assembly.
  • WO 94/13930 discloses placing a pump on the clean water stream to assist in reinjection of the clean water into the formation. This does not address the important problem of transporting the dry oil stream to the surface however.
  • U.S. Pat. No. 5,296,153 discloses pumping the dry oil stream to the surface and the dean water stream to another formation. This further increases the cost and complexity of oil production, exacerbates the problem of locating the equipment within the well bore, and requires pumping the clean water stream, which increases both the capital and operating costs of oil recovery.
  • the present invention overcomes the deficiencies of the prior art.
  • an apparatus for use in the borehole of a well for separating a recovery liquid from the mixed liquids produced from the formation in the well comprising: a tubular housing forming a cylindrical chamber, the chamber being open to the flow of the mixed liquids; a plurality of cyclone separators disposed within the chamber for separating the recovery liquid from the mixed liquids, each separator having an inlet for allowing the mixed liquids in the chamber to flow into each separator, a first outlet for the recovery liquid, and a second outlet for the disposed liquids; a first manifold connected to each of the first outlets for flowing the recovery liquid to the surface of the well; and a second manifold connected to each of the second outlets for removing the disposed liquids; characterised in that each cyclone separator has a head which has the largest cross-sectional area of the separator, the head having a radial clearance with the housing which is smaller than the diameter of the second manifold, the second manifold having a configured portion
  • the separation apparatus preferably includes a pumping unit which pumps production liquids into the chamber.
  • a second pumping unit may also be provided, if necessary, to transport the dry oil stream to the surface.
  • the housing can be provided with a plurality of apertures so that the production fluid enters the housing at a plurality of locations along the length of the tubular housing. In this case, the size of the apertures may be smaller than the size of any of the passages within the housing and separator(s), to avoid a flow blockage of the separator(s) by any solid matter in the production fluid.
  • a plurality of axially spaced separators are disposed in the chamber.
  • the overflow stream will leave the chamber at one end of the housing for transportation of a dry oil stream to the surface, while the underflow stream will leave the chamber at the opposite end of the housing for transportation of a clean water stream for disposal downhole or elsewhere. If all of the overflow outlet pipes discharge through one end of the housing and/or all of the underflow outlet pipes discharge through the opposite end, it will be necessary for a pipe or manifold leading from the overflow outlet of a separator to extend past the separator or separators positioned above it in the chamber, and/or for a pipe or manifold leading from the underflow outlet of a separator to extend past the separator or separators positioned below it in the chamber.
  • the space available for a pipe adjacent to the head of each hydrocyclone separator may be limited, because the head by its nature is the widest part of a hydrocyclone separator.
  • the pipe is formed with a non-circular cross section, which may have substantially the same cross-sectional area as do the adjacent portions of the pipe.
  • the non-circular cross section may be substantially kidney-shaped.
  • FIGS 1A, 1B, and 2A to 2D do not show embodiments of the invention.
  • the present invention is described with respect to several exemplary down hole hydrocyclone separator assemblies for separating the produced liquids from a well into a dry oil stream and a clean water stream, with satisfactory capacity, compactness, and cost, for application to conventional high cut oil wells in oil production or environmental cleanup.
  • FIG. 1A and 1B there is shown a simplified schematic diagram of a hydrocyclone separator assembly comprising a single hydrocyclone.
  • the separator assembly denoted generally by reference numeral 13, preferably comprises a housing 10, a hydrocyclone 2, and an internal chamber 20 defined by the inside diameter of housing 10.
  • upper and lower support plates 3 and 4 respectively, may be provided for supporting the piping and hydrocyclone 2 within chamber 20. If support plates 3 and 4 are used, production openings 11 are provided in support plates 3 and 4 so that internal chamber 20 remains open to the production liquids.
  • An overflow manifold 7 and an underflow manifold 8 extend through chamber 20 and are preferably provided when multiple separator assemblies are disposed in the well. Manifolds 7 and 8 are both firmly affixed to both support plates 3 and 4.
  • Hydrocyclone 2 is preferably of a well known de-oiling configuration such as that described in British Patent Application GB-A-2248198, and has one or more tangential inlets 9 which are open to the interior of the housing 10.
  • An underflow pipe 6 is hydraulically connected to the underflow outlet 19 of the hydrocyclone separator 2, and is hydraulically connected to the underflow manifold 8.
  • an overflow outlet pipe 5 is connected to the overflow outlet 15 of hydrocyclone separator 2, and is connected to the overflow manifold 7.
  • one or more separator assemblies 13 are run into the cased well bore with minimal clearance between the exterior wall of housing 10 and the interior wall of the well casing.
  • Production fluid which has either been pressurized by a pump or is naturally under pressure, floods the internal chamber 20, and enters hydrocyclone separator 2 through separator inlet(s) 9. If support plates 3 and 4 are provided, production fluid floods chamber 20 by flowing through production openings 11. The production fluid is caused to swirl within hydrocyclone 2 by the tangential orientation of inlet(s) 9.
  • hydrocyclone separator 2 the production fluid is separated into a clean water stream which flows to the underflow and a dry oil stream which flows to the overflow as is well known in the art.
  • the clean water stream is enriched in water relative to the production liquid stream, while the dry oil stream is enriched in oil relative to the production stream.
  • underflow from the hydrocyclone separator 2 flows through the underflow outlet pipe 6 to underflow manifold 8, and is preferably transported downhole below assembly 13 for disposal or reinjection into the formation.
  • the dry oil from the overflow outlet 15 flows up through the overflow outlet pipe 5 to overflow manifold 7, and then to the surface where it may be further treated.
  • underflow pipe 6 is preferably connected to a disposal pipe (not shown) below housing 10, whereby manifolds 7 and 8 are no longer necessary.
  • FIG. 2A there is shown a schematic representation of a second preferred embodiment of the separator assembly including a plurality of the separator assemblies 13 shown in Figure 1A.
  • Separator assemblies 13 are disposed between two axially spaced packers, a lower packer 93 and an upper packer 95.
  • Upper packer 95 is optional.
  • Upper packer 95 is used when an upper formation is isolated from the formation having perforations 90; when the disposal liquid, such as water, is to be disposed above the separator assembly; or when it is desirable to prevent the production fluids from perforations 90 from flowing up hole.
  • Two such separator assemblies, top separator assembly 13A and bottom separator 13B are shown, although any number of separator assemblies 13 may be used without departing from the scope of the present invention. It should be appreciated that separator assemblies 13A and 13B are substantially the same as separator assembly 13 described with respect to Figure 1A, and like reference numerals will be used for like parts with the designation A or B for upper and lower assemblies 13A and 13B, respectively.
  • a production pump 31 is provided for pumping the production fluids and an overflow pump 32 is provided for pumping the overflow (dry oil) stream to the surface.
  • Pumps 31 and 32 are driven by drive means such as one or more drive motors 30.
  • pumps 31 and 32 may be electric submersible pumps, progressive cavity pumps, or beam (or rod) pumps, all of which are well known in the art.
  • Many other types and combinations of pumps and drive systems may be successfully used in accordance with the present invention, such as jet pumps and gas lift systems.
  • a range of artificial lift systems may be used in conjunction with the natural reservoir pressure without departing from the scope of the present invention.
  • Pumps 31, 32 and drive motor 30 are preferably disposed above separator assemblies 13A, 13B to simplify connection to a power source (not shown) which supplies electric or hydraulic power to drive motor 30.
  • a power source not shown
  • Other arrangements of pumps 31, 32 and drive motor 30 with respect to separator assemblies 13A and 13B are, of course, possible without departing from the scope of the invention.
  • separator assemblies 13 are thus modular, and the number of such modules used should be determined in practice by the desired overall capacity, available reservoir pressure, and choice and design of pumps.
  • a first or top sub 41 is preferably disposed between drive motor 30 and the separator assembly 13A, as shown in Figure 2A, and hydraulically seals around its periphery to well casing 17.
  • Sub 41 preferably includes a passage 111 for the production fluids being pumped, an overflow passage 71, and a blind bore 81 for receiving one end of underflow manifold 8A to prevent upward passage of the underflow stream.
  • Passage 111 allows the production fluids from the outlet of production pump 31 to flow to separator assembly 13A
  • Overflow passage 71 in sub 41 interconnects the overflow manifold 7A (shown in Figure 1A) of separator assembly 13A to a dry oil conduit means (not shown) extending to the surface through which the dry oil is transported to overflow pump 32.
  • Blind bore 81 of sub 41 hydraulically seals off one end of underflow manifold 8A.
  • a second or connecting sub 42 preferably is disposed between any two of separator assemblies 13, such as separator assemblies 13A and 13B, as shown in Figure 2A for connecting adjacent assemblies.
  • Sub 42 preferably includes a passage 211 for the pumped production fluids, an overflow passage 72, and an underflow passage 82.
  • Passage 211 hydraulically interconnects the two separator assemblies 13A and 13B adjacent to sub 42 for the flow of production fluids.
  • the production fluids may pass freely between internal chambers 20A and 20B of separator assemblies 13A and 13B.
  • Overflow passage 72 hydraulically interconnects the overflow manifolds 7A and 7B of any two separator assemblies 13 adjacent to sub 42, such as top separator assembly 13A and bottom separator assembly 13B.
  • underflow passage 82 hydraulically interconnects the underflow manifolds 8A and 8B of the two separator assemblies 13 adjacent to sub 42.
  • a third or bottom sub 43 preferably is disposed between the bottom separator assembly 13B and lower packer 93.
  • Sub 43 preferably includes underflow passage 83, which terminates at its lowest end in a threaded pipe box 80.
  • Underflow passage 83 hydraulically connects the underflow manifold 8B of the bottom separator assembly 13B to a disposal pipe 84, shown in Figure 2A.
  • production fluids enter the annulus 85 formed between housing 10 and well casing 17 through production perforations 90 in casing 17.
  • the production fluids are drawn into production pump 31 and pumped through production passage 111 of first sub 41 to top separator assembly 13A. Should optional support plates 3A and 4A be used the production fluids flood chamber 20A by passing through production openings 11A. (See Figure 1A).
  • the production fluids also pass through production passage 211 in second sub 42 and, as above, flood the internal chamber 20B of bottom separator assembly 13B below sub 42. In this way, the internal chamber 20 of each of the separator assemblies 13 is flooded with production fluids.
  • the production fluids are separated by the hydrocyclones 2A and 2B, with the overflow streams passing into overflow manifolds 7A and 7B and the underflow streams passing into underflow manifolds 8A and 8B.
  • the overflow manifolds 8A and 8B of the several separator assemblies 13A and 13B form a continuous manifold by virtue of passage 72 through sub 42.
  • the overflow thus flows up through overflow manifolds 7A and 7B, through overflow passage 72 of sub 42, through overflow passage 71 of sub 41, to overflow pump 32, which then pumps the overflow through recovery pipe 74 extending to the surface. In wells with sufficient natural reservoir pressure, overflow pump 32 is not required.
  • the underflow manifolds 7A and 7B of the several separator assemblies 13A and 13B form a continuous manifold by virtue of passage 82 through sub 42.
  • the underflow is prevented, by blind bore 81 in sub 41, from passing up the well.
  • the underflow from all the separator assemblies 13 therefore finally exits via passage 83 in sub 43 and disposal pipe 84, and may then be injected into the formation via injection perforations 96, located in the well casing 17 anywhere below lower packer 93.
  • Figure 2A includes two separator assemblies 13A and 13B, any number of modular separator assemblies 13 may be used.
  • the separator assembly 113 comprises a housing 100 defining an internal chamber 120 which is sealed at an upper end by a first sealing block 102 and at a lower end by a second sealing block 103.
  • the separator assembly may be reversible, in which case first sealing block 102 seals the lower end and second sealing block 103 seals the upper end.
  • a production fluid inlet may be provided to separator assembly 113 in either of two ways.
  • an inlet 161A into the chamber 120 is preferably provided through the appropriate sealing block.
  • the housing 100 is preferably provided with a plurality of apertures, such as holes 161B, or slots (not shown) which allow direct access for the production fluid into the chamber 120.
  • apertures such as holes 161B, or slots (not shown) which allow direct access for the production fluid into the chamber 120.
  • An upper hydrocyclone separator 104 and a lower hydrocyclone separator 105 preferably are arranged in parallel within housing 100.
  • the hydrocyclone separators 104 and 105 have a de-oiling configuration which is well known in the art. Both separators 104 and 105 have one or more tangential inlets 106 which are open to the interior of separators 104 and 105. Although the inlets are illustrated as being in the plane of the section, this is only for clarity and, in practice, the inlets will generally be out of this plane.
  • An underflow pipe 107 is connected to the underflow outlet 115 of the upper hydrocyclone separator 104 and leads down the chamber 120 past the lower separator 105.
  • the first underflow outlet pipe is provided with a non-circular portion 107A which, in plan, may have a substantially kidney-shaped cross section. This cross-sectional configuration ensures that the cross-sectional area of the pipe underflow pipe 107 remains substantially unchanged as the non-circular portion 107A of underflow pipe 107 passes the head of lower separator 105, despite the limited space available adjacent to the head 117 of the second separator 105.
  • non-circular portion 107A is not necessary, so long as the cross-sectional area of underflow pipe 107 is maintained substantially constant. It should also be appreciated that non-circular portion 107A may include a plurality of pipes extending between outlet 115 and the main tubular portion 107B of pipe 107, it being important that the cross-sectional flow area is substantially the same around head 117 as with portion 107A However, multiple pipes are not preferred because they take up more area within housing 100 than non-circular portion 107A.
  • the underflow outlet pipe 107 leads to a manifold 108 which is shown as a part of the second sealing block 103.
  • the underflow outlet 119 of the lower separator 105 is also connected to manifold 108 so that the underflow streams from the two separators 104, 105 are combined prior to passing through second sealing block 103.
  • an overflow outlet pipe 109 leads from the outlet 121 of lower separator 105 past the upper separator 104, and the overflow stream from lower separator 105 combines with the overflow stream from outlet 110 of the upper separator 104 in a manifold (not shown) similar to manifold 108, which then passes through first sealing block 102.
  • head 117 of the separators it is most desirable to maximize the size of the head 117 of the separators within housing 100, or casing 17 if no separate housing is utilized for the separator assembly, to maximize the separation capacity of each separator.
  • the remaining cross-sectional area around head 117 must accommodate not only underflow manifold 107 and overflow manifold 108 but must also leave adequate flow area for the production fluids flowing by head 117 to feed other separators in the assembly.
  • separator assembly 113 (as well as separator assembly 13, Figure 1A) is preferably simplified by the use of many standard pipe sections as are well-known in the art, and hydrocyclones of de-oiling configurations, also well known in the art.
  • the only specialty parts required are the first sealing block 102 and the second sealing block 103, the non-circular pipe section 107A (if necessary), and an adapter 213 provided between the two separators 104, 105 for connecting separator outlets 107, 121 to corresponding pipes.
  • running the separator assembly 113 into a well bore preferably requires only minimal clearance between the walls of housing 100 and the well casing, i.e., only enough clearance to run the assembly through the well casing.
  • the diametrical clearance may be as small as one sixteenth of an inch.
  • No clearance is required for the flow of production fluids, as in the prior art, since chamber 20 is open to the flow of production fluids.
  • Production fluids flood the internal chamber 120 through the alternative production fluid inlets described above.
  • the production fluids in the internal chamber 120 which have been either pressurized by a pump or is naturally under pressure, enters the two separators 104, 105 through respective separator tangential inlets 106, and is caused to swirl by the tangential orientation of inlets 106.
  • the production fluids are separated into a dean water stream which flows to the underflow and a dry oil stream which flows to the overflow.
  • the clean water stream is enriched in water relative to the production fluids
  • the dry oil stream is enriched in oil relative to the production fluids.
  • the underflow from the two separators flows through the second sealing block 103, and may then be transported downhole for disposal or reinjection via outlet 184.
  • the dry oil stream from the overflow flows up through the first sealing block 102 and then to the surface where it may be further treated.
  • a common underflow outlet pipe is preferably progressively larger in cross-sectional area as it extends down the chamber 120 because the underflow outlet streams from further separators join the common underflow outlet pipe substantially increasing the volume of flow.
  • a common overflow outlet pipe is preferably progressively larger in cross-sectional area as it extends up the chamber, because the overflow outlet streams from further separators join the common overflow outlet pipe also increasing the volume of flow.
  • the outside diameter of housing 100 is preferably less than the inside diameter of the well casing by only the clearance necessary to run the assembly 113 into the well.
  • the diametrical clearance may be approximately one-sixteenth of an inch. This maximizes the diameter of the separator assembly and housing, and maximizes the size of separators 104 and 105, thereby maximizing the capacity of the entire separator assembly.
  • assemblies such as assembly 113 having two hydrocyclones in accordance with the embodiment described above have been constructed and tested where the outside diameter of housing 100 is 4.5 inches and the length of housing 100 is about 13 feet. Such an assembly is suitable for use in 5 inch well casing having an inside diameter of 4-9/16 inches. A capacity of up to 4,000 barrels of production fluid per day may be achieved with such a two hydrocyclone assembly.
  • the cross-sectional area of the head of each hydrocyclone 104 and 105 may be one-hart or greater than the cross-sectional area of the housing 100. It is preferable to maximize this ratio to maximize the capacity of the separator assembly.
  • the remaining cross-sectional area of housing 100 is used for manifolds 107, 108 and the flow of production fluids.
  • the separator assembly 313 comprises a tubular housing 300 defining an internal chamber 320 which is sealed at an upper end by a top adapter 310 and at a lower end by a bottom adapter 380.
  • Top adapter 310 and bottom adapter 380 are secured to housing 300 by threaded collars 311 and 321, respectively.
  • Separator assembly 313 may alternatively be reversed, so that adapter 310 is disposed at the lower end and adaptor 380 is disposed at the upper end.
  • a production fluid inlet may be provided in either of two ways. First, if a production fluid pump is provided above the top adapter 310 (such as production pump 31 shown in Figure 2A) or below the bottom adapter 380, an inlet 361A into the chamber 320 is provided through the appropriate adapter, such as shown in adapter 310. On the other hand, if no pump is required, the housing 300 may be provided with a plurality of apertures, such as holes 361B, or slots (not shown), or screened openings (not shown), which allow direct access of the production fluids into the chamber 320. As one skilled in the art will immediately understand, other means of providing the plurality of apertures may be employed without departing from the scope of the invention.
  • the five hydrocyclone separators are preferably arranged in parallel within housing 300.
  • the hydrocyclone separators have a well known de-oiling configuration as is well known in the art.
  • Each of the separators has one or more tangential inlets (not shown, but substantially similar to inlets 106 described above with reference to Figures 3A and 3B) which are open to the interior of the separators.
  • An underflow pipe 360 connects each of the underflow outlets of the hydrocyclone separators 302, 303, and 304, to an underflow manifold 340.
  • an underflow pipe 360A connects the underflow outlet of the top hydrocyclone 301 to underflow manifold 340.
  • Underflow pipe 360A may vary slightly in its cross-sectional configuration from underflow pipes 360 because underflow pipe 360A forms the top inlet of underflow manifold 340.
  • Underflow manifold 340 extends down through the chamber 320 and past the lowest hydrocyclone 305, into bottom adapter 380.
  • the underflow from hydrocyclone 305 also leads to bottom adapter 380, so that the underflow stream from all of the hydrocyclone separators 301 - 305 is combined prior to passing through bottom adapter 380.
  • the underflow from hydrocyclone 305 communicates with the bore 381 of bottom adapter 380, as does underflow manifold 340.
  • the underflow manifold 340 may be provided with a non-circular portion 340A which, in plan, may have a substantially kidney-shaped cross section (See Figure 4E). Although shown as substantially kidney-shaped in cross-section, non-circular portion 340A may have any cross-sectional configuration that ensures that its cross sectional area at the standard circular portion 340B remains substantially unchanged as the non-circular portion 340A of underflow manifold 340 passes the head 117 of separators 302 - 305 despite the limited space available.
  • underflow manifold 340 and overflow manifold 330 shown in Figure 4E adjacent head 117 of a separator may be cast into one piece which includes two flow passages therethrough, one for overflow and another for underflow.
  • a one piece casting further reduces the cross-sectional area required to by-pass head 117 by manifolds 330, 340. If space limitations do not require it, non-circular portion 340A need not be provided.
  • overflow outlet pipes 370 connect the overflow outlet of each of the separators 301 - 305 with overflow manifold assembly 330, similar to manifold 340, which extends through top adapter 310.
  • Underflow manifold assembly 340 is preferably substantially larger in cross-sectional area than that of overflow manifold assembly 330 to accommodate the relatively larger flow rate of the underflow stream.
  • separation apparatus in accordance with the embodiment of Figures 4A - 4E has been successfully used with the cross-sectional area of the underflow manifold assembly 340 being up to four times larger than the cross-sectional area of the overflow manifold assembly 330.
  • those sections 340B of underflow manifold 340 extending between the underflow outlets of adjacent separators may increase in diameter from separator 301 to separator 305 since the largest volume of flow will occur through underflow manifold 340 adjacent the outlet of lowermost separator 305.
  • housing 300 is preferably less than the inside diameter of the well casing by only the clearance necessary to run the assembly into the well, for example a diametrical clearance of one-sixteenth of an inch may be used. This maximizes the diameter of the housing 300 which, in turn, maximizes the size of hydrocyclone separators 301 - 305, thereby maximizing the capacity of the entire separator assembly.
  • the well casing diameter may be measured prior to running the housing into the well, to ensure sufficient clearance is present.
  • housing 300 may comprise the well casing itself, which further increases the diameter of separator assembly 313 and increases capacity.
  • the construction of the separator assembly described above is preferably simplified by the use of standard pipe sections and standard de-oiling hydrocyclones, as described previously.
  • the specialty parts required may include the top adapter 310, bottom adapter 380, the non-circular portions 340A (if necessary) of underflow manifold 340, underflow pipes 360 and 360A, and overflow pipes 370.
  • adapter 211 as described with reference to Figure 3B is not required between adjacent hydrocyclone separators in the assembly configuration of the embodiment described with reference to Figure 4B.
  • separator assembly 313 In use, the installation and operation of separator assembly 313 is as described above with reference to separator assembly 113, which is illustrated in Figures 3A and 3B. Separator assembly 313 is capable of substantially greater capacity than assembly 113.
  • assemblies such as assembly 313 having five standard sized hydrocyclones in accordance with the embodiment described above have been constructed and tested where the diameter of housing 300 is 5.5 inches and the length of housing 300 is about 24 feet. Such an assembly is suitable for use in 7 inch well casing. A capacity of up to 10,000 barrels of production fluid per day can be achieved with such a five hydrocyclone assembly.
  • the ratio of the cross-sectional area of the head of hydrocyclones 301 - 305 to the cross-sectional area of the housing 300 is about 0.3 or greater. This ratio is smaller than 0.5 because standard-sized hydrocyclones were used. It is preferable to maximize this ratio to maximize the capacity of the separator assembly.

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  • Geochemistry & Mineralogy (AREA)
  • Geometry (AREA)
  • Cyclones (AREA)

Claims (26)

  1. Appareil pour être utilisé dans le trou de forage d'un puits pour séparer un liquide de récupération des liquides mélangés produits à partir de la formation dans le puits, l'appareil comprenant : une enveloppe tubulaire formant une chambre cylindrique, la chambre étant ouverte à l'écoulement des liquides mélangés; une pluralité de séparateurs à cyclone placés à l'intérieur de la chambre pour séparer le liquide de récupération des liquides mélangés, chaque séparateur ayant une entrée pour permettre aux liquides mélangés dans la chambre de s'écouler dans chaque séparateur, une première sortie pour le liquide de récupération, et une deuxième sortie pour les liquides rejetés; un premier collecteur raccordé à chacune des premières sorties pour amener le liquide de récupération à la surface du puits; et un deuxième collecteur raccordé à chacune des deuxièmes sorties pour retirer les liquides rejetés; caractérisé en ce que chaque séparateur à cyclone est muni d'une tête ayant la superticie de section la plus grande du séparateur, la tête ayant un écartement radial avec l'enveloppe qui est inférieur au diamètre du deuxième collecteur, le deuxième collecteur ayant une partie configurée placée entre la tête et l'enveloppe qui offre une section transversale non circulaire afin d'éviter l'écoulement limité des liquides rejetés par l'intermédiaire du collecteur entre la tête et l'enveloppe.
  2. Appareil selon la revendication 1, dans lequel la section de passage du deuxième collecteur s'accroít dans le sens d'écoulement des liquides rejetés.
  3. Appareil selon la revendication 1, dans lequel le deuxième collecteur a des sections dimensionnées pour chaque séparateur, la superficie de section des sections dimensionnées s'accroissant dans le sens d'écoulement des liquides rejetés.
  4. Appareil selon la revendication 1, dans lequel la section de passage du premier collecteur est constante.
  5. Appareil selon l'une quelconque des revendications précédentes, dans lequel la superficie de section de la tête est au moins égale à 30 pour cent de la superficie de section de l'enveloppe.
  6. Appareil selon la revendication 5, dans lequel la superficie de section de la tête est au moins égale à 50 pour cent de la superticie de section de l'enveloppe.
  7. Appareil selon l'une quelconque des revendications dans lequel l'enveloppe comprend une paroi tubulaire traversée par une pluralité d'ouvertures.
  8. Appareil selon la revendication 7, dans lequel les ouvertures sont contiguës à la formation.
  9. Appareil selon l'une quelconque des revendications précédentes, dans lequel l'enveloppe tubulaire comprend un cuvelage de puits de pétrole.
  10. Appareil selon l'une quelconque des revendications 1 à 8, dans lequel l'enveloppe tubulaire a un diamètre externe qui est substantiellement égal à la différence entre le diamètre du cuvelage du puits et un écartement de passage pour introduire l'enveloppe à l'intérieur du cuvelage de puits.
  11. Appareil selon la revendication 10, dans lequel l'écartement de passage est inférieur ou égal à un huitième de pouce (environ 3,18 mm).
  12. Appareil selon la revendication 1, dans lequel le deuxième collecteur a une superficie de section d'écoulement substantiellement plus grande que celle du premier collecteur.
  13. Appareil selon la revendication 12, dans lequel le collecteur de fluide d'écoulement inférieur a une superficie de section d'écoulement qui est environ quatre fois plus grande que celle du collecteur de fluide d'écoulement supérieur.
  14. Appareil selon l'une quelconque des revendications précédentes, comprenant en outre une pompe de fluide de production, placée en bas du trou, pour pomper des liquides mélangés dans l'enveloppe.
  15. Appareil selon la revendication 14, comprenant en outre une pompe de fluide de courant supérieur, placée, en utilisation, en bas du trou, pour pomper le liquide de récupération au-dessus du sol; et un moyen de commande de pompe de fluide d'écoulement supérieur pour entraíner la pompe de fluide d'écoulement supérieur.
  16. Appareil selon la revendication 14, dans lequel la pompe de fluide de production est une pompe électrique immersible.
  17. Appareil selon la revendication 14, dans lequel la pompe de fluide de production est une pompe à cavité à action progressive.
  18. Appareil selon la revendication 15, dans lequel la pompe de fluide de production et la pompe de fluide de courant supérieur sont des pompes électriques immersibles.
  19. Appareil selon la revendication 15, dans lequel la pompe de fluide de production et la pompe de fluide de courant supérieur sont des pompes à cavité à action progressive.
  20. Appareil selon la revendication 15, dans lequel la pompe de fluide de production et le moyen de commande de pompe de fluide de production, et la pompe de fluide de courant supérieur et le moyen de commande de pompe de fluide de courant supérieur sont placés au-dessus de l'enveloppe et, en utilisation, en bas du trou à l'intérieur du cuvelage du puits de pétrole.
  21. Appareil selon la revendication 1, dans lequel l'enveloppe tubulaire est dotée d'une pluralité d'ouvertures dans sa paroi périphérique.
  22. Appareil selon l'une quelconque des revendications précédentes, dans lequel la section transversale non circulaire du deuxième collecteur est, en partie, substantiellement réniforme.
  23. Appareil selon la revendication 22, dans lequel la partie tête d'un deuxième ensemble à hydrocyclone chevauche axialement une première partie de queue d'un premier ensemble à hydrocyclone.
  24. Appareil selon l'une quelconque des revendications précédentes, comprenant en outre un joint placé autour du deuxième collecteur; dans lequel le joint s'engage de manière étanche dans un cuvelage doublant le trou de forage.
  25. Appareil selon la revendication 1, comprenant en outre une première pompe placée, en utilisation, dans le trou de forage et raccordée au premier collecteur pour pomper le liquide de récupération à la surface.
  26. Appareil selon la revendication 24, comprenant en outre une deuxième pompe placée, en utilisation, dans le trou de forage et raccordée à une entrée pour liquides mélangés pour pomper les liquides mélangés dans le séparateur.
EP97900336A 1996-01-12 1997-01-13 Ensemble separateur a cyclone et procede Expired - Lifetime EP0874694B1 (fr)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
GB9600600 1996-01-12
GB9600600A GB2308995B (en) 1996-01-12 1996-01-12 Downhole separation apparatus
US613929 1996-03-11
US08/613,929 US6080312A (en) 1996-03-11 1996-03-11 Downhole cyclonic separator assembly
PCT/GB1997/000087 WO1997025150A1 (fr) 1996-01-12 1997-01-13 Ensemble separateur a cyclone et procede

Publications (2)

Publication Number Publication Date
EP0874694A1 EP0874694A1 (fr) 1998-11-04
EP0874694B1 true EP0874694B1 (fr) 1999-09-08

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EP97900336A Expired - Lifetime EP0874694B1 (fr) 1996-01-12 1997-01-13 Ensemble separateur a cyclone et procede

Country Status (5)

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EP (1) EP0874694B1 (fr)
AU (1) AU1392197A (fr)
DE (1) DE69700496D1 (fr)
NO (1) NO312086B1 (fr)
WO (1) WO1997025150A1 (fr)

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US6105671A (en) * 1997-09-23 2000-08-22 Texaco Inc. Method and apparatus for minimizing emulsion formation in a pumped oil well
US6123149A (en) * 1997-09-23 2000-09-26 Texaco Inc. Dual injection and lifting system using an electrical submersible progressive cavity pump and an electrical submersible pump
US6079491A (en) * 1997-08-22 2000-06-27 Texaco Inc. Dual injection and lifting system using a rod driven progressive cavity pump and an electrical submersible progressive cavity pump
US6092599A (en) * 1997-08-22 2000-07-25 Texaco Inc. Downhole oil and water separation system and method
US6092600A (en) * 1997-08-22 2000-07-25 Texaco Inc. Dual injection and lifting system using a rod driven progressive cavity pump and an electrical submersible pump and associate a method
WO1999015755A2 (fr) * 1997-08-22 1999-04-01 Texaco Development Corporation Systeme double d'injection et elevation
NO308426B1 (no) * 1998-07-13 2000-09-11 Read Group As FremgangsmÕte og innretning for produsering av et oljereservoar
GB9816725D0 (en) * 1998-08-01 1998-09-30 Kvaerner Process Systems As Cyclone separator
GB2400575B (en) * 2000-05-09 2004-12-15 Kgd Process Internat Ltd Supporting elements for a cyclone separator assembly
US20050087336A1 (en) 2003-10-24 2005-04-28 Surjaatmadja Jim B. Orbital downhole separator
US7370701B2 (en) 2004-06-30 2008-05-13 Halliburton Energy Services, Inc. Wellbore completion design to naturally separate water and solids from oil and gas
US7429332B2 (en) 2004-06-30 2008-09-30 Halliburton Energy Services, Inc. Separating constituents of a fluid mixture
US7462274B2 (en) 2004-07-01 2008-12-09 Halliburton Energy Services, Inc. Fluid separator with smart surface
US7823635B2 (en) 2004-08-23 2010-11-02 Halliburton Energy Services, Inc. Downhole oil and water separator and method
GB2490346A (en) * 2011-04-27 2012-10-31 Dps Bristol Holdings Ltd Cyclonic separator having a tapered core element
WO2018015777A1 (fr) 2016-07-22 2018-01-25 Total Sa Séparateur gaz-liquide, extracteur d'hydrocarbures et procédé de séparation associé
CN108612515A (zh) * 2018-06-15 2018-10-02 西南石油大学 一种带螺旋稳流锥的海底水合物井下分离装置
CN108915646A (zh) * 2018-09-06 2018-11-30 李龙龙 输气管线多相流排水采气工具

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Also Published As

Publication number Publication date
EP0874694A1 (fr) 1998-11-04
DE69700496D1 (de) 1999-10-14
WO1997025150A1 (fr) 1997-07-17
NO983185L (no) 1998-09-11
AU1392197A (en) 1997-08-01
NO312086B1 (no) 2002-03-18

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