CN104771941B - A kind of GEOTHERMAL WATER gas-liquid-solid three-phase separator and method - Google Patents
A kind of GEOTHERMAL WATER gas-liquid-solid three-phase separator and method Download PDFInfo
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- CN104771941B CN104771941B CN201510167995.5A CN201510167995A CN104771941B CN 104771941 B CN104771941 B CN 104771941B CN 201510167995 A CN201510167995 A CN 201510167995A CN 104771941 B CN104771941 B CN 104771941B
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- eddy flow
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/10—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/20—Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
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- E—FIXED CONSTRUCTIONS
- E21—EARTH DRILLING; MINING
- E21B—EARTH DRILLING, e.g. DEEP 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
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/10—Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities
Abstract
The present invention relates to a kind of GEOTHERMAL WATER gas-liquid-solid three-phase separator and method.Including upper shell, lower house, Swirling flow sand-removing mechanism, clash into Fen Lin mechanism and separate umbrella mechanism, upper shell and lower house are flexibly connected, lower housing cavity is installed Swirling flow sand-removing mechanism, is clashed into Fen Lin mechanism and separate umbrella mechanism, Swirling flow sand-removing mechanism separates bucket with gas-liquid runner and coordinates, gas-liquid runner separates the lower section of bucket and is provided with shock Fen Lin mechanism and separates umbrella mechanism, and the bottommost at lower house is provided with outlet pipe；The bottom of described Swirling flow sand-removing mechanism is provided with sediment outflow pipe in eddy flow, is drawn outside lower house by eddy flow effluent sand pipe.Provide the benefit that: by Swirling flow sand-removing, clash into and divide pouring, separation three kinds of separating technologies of umbrella to be integrated in this device, compact conformation, reduce occupation area of equipment；The shock Fen Lin mechanism that uses, separate umbrella mechanism and can multistage arrange, increase separating effect；It addition, the design of apparatus of the present invention ingenious utilization guide rail draw-in groove, device inner core can overall be extracted out, conveniently manufactures and maintenance.
Description
Technical field
The present invention relates to a kind of GEOTHERMAL WATER three-phase separating device, particularly to a kind of GEOTHERMAL WATER gas-liquid-solid three-phase separator and method.
Background technology
Along with the development of national economy, the living standard of the people gradually steps up, and the conventional energy resource such as coal, oil is the most in short supply, and has caused a series of environmental problem, promotes the mankind to start the exploitation to new forms of energy.Underground heat, as the green energy resource of a kind of cleaning, has and is prone to exploit, be easy to the advantages such as application and non-environmental-pollution.But, in GEOTHERMAL WATER, the situation containing natural gas is the most, especially relatively conventional in oil gas field region, is the major security risk of Geothermal Exploitation and Utilization, and nationwide there occurs a lot of security incident.Therefore, research is a kind of particularly important for GEOTHERMAL WATER gas-liquid-solid three-phase segregation apparatus.
Existing three phase separation technology is varied, and ultimate principle includes gravitational settling, baffle separation, centrifugal force separate, silk screen separation, ultra-filtration and separation, filler separation etc..But being mostly applied to oil-gas gathering and transportation field, the three phase separation for gassiness GEOTHERMAL WATER does not the most develop device efficient, reliable.
If the three phase separator in oil-gas gathering and transportation field is applied to geothermal water system, can there is following defect: 1, the three phase separator being designed with oil property is applied to geothermal water system, separating effect cannot ensure；2, equipment volume is big, and floor space is big, increases investment；3, maintenance of equipment difficulty.
Summary of the invention
The purpose of the present invention is aiming at the drawbacks described above that prior art exists, it is provided that a kind of GEOTHERMAL WATER gas-liquid-solid three-phase separator and method, in order to reduces occupation area of equipment, reduce construction investment.
nullA kind of GEOTHERMAL WATER gas-liquid-solid three-phase separator that the present invention mentions: include upper shell、Lower house、Swirling flow sand-removing mechanism、Clash into Fen Lin mechanism and separate umbrella mechanism，Described upper shell and lower house are flexibly connected，The top of upper shell is provided with exhaustor，The middle part of upper shell is provided with drop catching net，Described lower housing cavity installs Swirling flow sand-removing mechanism、Clash into Fen Lin mechanism and separate umbrella mechanism，Swirling flow sand-removing mechanism separates bucket with gas-liquid runner and coordinates，Gas-liquid runner separates the bottom of bucket and is provided with baffle liner，Described gas-liquid runner separates the lower section of bucket and is provided with shock Fen Lin mechanism，Clash into Fen Lin mechanism and include point pouring orifice plate and lower point of pouring orifice plate，The lower point of lower section drenching orifice plate is provided with by upper point trickle catch tray、Under divide trickle catch tray、Upper gas separation umbrella、The separation umbrella mechanism of lower gas separation umbrella composition，Lower end sidepiece at lower house is provided with outlet pipe，Bottommost is provided with blow-off pipe；The bottom of described Swirling flow sand-removing mechanism is provided with sediment outflow pipe in eddy flow, and in eddy flow, sediment outflow pipe is drawn outside lower house by connecting eddy flow effluent sand pipe.
Above-mentioned Swirling flow sand-removing mechanism includes the outer water inlet pipe of eddy flow, water inlet pipe in eddy flow, eddy flow cylindrical section, overflow pipe, eddy flow conical section, sediment outflow pipe in eddy flow, silt collecting pipe, eddy flow effluent sand pipe, and eddy flow cylindrical section fixes pillar and gas-liquid runner separation bucket by first and is welded and fixed, eddy flow conical section on the downside of eddy flow cylindrical section is fixed pillar by second and is welded and fixed with gas-liquid runner separation bucket, eddy flow conical section lower end connects sediment outflow pipe in eddy flow, in eddy flow, the stage casing of sediment outflow pipe is provided with the silt collecting pipe that volume increases, and the lower end of sediment outflow pipe is flexibly connected with eddy flow effluent sand pipe in eddy flow.
The upper point pouring aperture plate center of above-mentioned shock Fen Lin mechanism coordinates with eddy flow conical section, and the upper point of outside drenching orifice plate connects above liquid retaining ring, and fixes pillar and the second guide rail and card slot fit by the 5th；The lower point of center drenching orifice plate coordinates with eddy flow conical section, and the lower point of outside drenching orifice plate connects lower liquid retaining ring, and fixes pillar and the second guide rail and card slot fit by the 6th.
The center of the above-mentioned upper point trickle catch tray separating umbrella mechanism coordinates with sediment outflow pipe in eddy flow, and the center of lower point of trickle catch tray coordinates with sediment outflow pipe in eddy flow, and lower point of trickle catch tray is positioned at a point lower section for trickle catch tray；Described upper point be provided with gas separation umbrella between trickle catch tray and lower point of trickle catch tray, be provided with lower gas separation umbrella in the lower section of lower point of trickle catch tray.
Above-mentioned upper point trickle catch tray is fixed pillar by the longitudinal the 7th and is connected to gas separation umbrella, and the 7th fixes pillar and fix pillar and the second guide rail and card slot fit by the horizontal the 9th.
Lower point of above-mentioned trickle catch tray is fixed pillar by the longitudinal the 8th and is connected to lower gas separation umbrella, and the 8th fixes pillar and fix pillar and the second guide rail and card slot fit by the horizontal the tenth.
The top inner chamber of above-mentioned eddy flow cylindrical section is provided with overflow pipe.
The bottom of above-mentioned drop catching net is fixed pillar by the 4th and is supported, and the 4th fixes the outside of pillar and the first guide rail and card slot fit.
In outside above-mentioned eddy flow, water inlet pipe is connected to the eddy flow of lower housing cavity, in water inlet pipe, and eddy flow, water inlet pipe is connected to the tangential direction of eddy flow cylindrical section.
The using method of a kind of GEOTHERMAL WATER gas-liquid-solid three-phase separator that the present invention mentions, comprises the following steps:
Gassiness, silt GEOTHERMAL WATER from eddy flow in water inlet, eddy flow water inlet tangent line enter in Swirling flow sand-removing mechanism, carry out solid-liquor separation by eddy flow cylindrical section and eddy flow conical section, silt is gone out by sediment outflow pipe, eddy flow effluent sand bank of tubes in eddy flow；
Gassy water passes through overflow pipe and overflows Swirling flow sand-removing mechanism, separates free-falling inside bucket at gas-liquid runner and, to clashing in Fen Lin mechanism, collides, divides and drench, increase exposed surface area, cause turbulent condition, make gas separate with liquid；Liquid after undue pouring forms tiny water column and continues to fall to a point trickle catch tray, liquid after collection falls to lower section by catch tray center and separates umbrella mechanism and carry out further gas-liquid separation with the gap of sediment outflow pipe in eddy flow, and the liquid after final separation is discharged from three phase separator bottom through outlet pipe；
The free gas separated in clashing into Fen Lin mechanism and separation umbrella mechanism separates bucket outer wall by gas-liquid runner and flows up, and discharges three phase separator through drop catching net and exhaustor, and pump-down process mode is determined by scene and is equipped with, and gas safety processes.
The invention has the beneficial effects as follows: the Swirling flow sand-removing mechanism that gassiness, the GEOTHERMAL WATER of silt enter in apparatus of the present invention carries out solid-liquor separation；Water after solid-liquor separation is overflowed Swirling flow sand-removing mechanism by overflow pipe, and inside gas-liquid runner partition, free-falling is to clashing into Fen Lin mechanism, carries out gas-liquid separation；Liquid after gas-liquid separation continues free-falling and extremely separates umbrella mechanism, carries out gas-liquid separation further；Liquid after gas-liquid-solid three-phase separates is discharged by bottom of device outlet pipe, and isolated silt solid is gone out by the sediment outflow bank of tubes of bottom of device, and isolated gas is discharged by the exhaustor at device top；Swirling flow sand-removing, shock point pouring, separation three kinds of separating technologies of umbrella are integrated in this device, compact conformation by the present invention, reduce occupation area of equipment；The shock Fen Lin mechanism that uses, separate umbrella mechanism and can multistage arrange, increase separating effect；It addition, the design of apparatus of the present invention ingenious utilization guide rail draw-in groove, device inner core can overall be extracted out, conveniently manufactures and maintenance.
Accompanying drawing explanation
Accompanying drawing 1 is the structural representation of the present invention；
Accompanying drawing 2 is the A-A sectional view of the present invention；
Accompanying drawing 3 is the structural representation of the cyclone desanding device of the present invention；
Accompanying drawing 4 is the top view of the cyclone desanding device of the present invention；
Accompanying drawing 5 is the top view of the shock Fen Lin mechanism of the present invention；
Accompanying drawing 6 is the structural representation that gas-liquid runner separates bucket；
Accompanying drawing 7 is the structural representation of the second guide rail and draw-in groove；
Accompanying drawing 8 is the structural representation separating umbrella mechanism；
nullIn upper figure: the outer water inlet pipe 1 of eddy flow、Water inlet pipe 2 in eddy flow、Eddy flow cylindrical section 3、Overflow pipe 4、Eddy flow conical section 5、Sediment outflow pipe 6 in eddy flow、Silt collecting pipe 7、Eddy flow effluent sand pipe 8、First fixes pillar 9、Gas-liquid runner separates bucket 10、Second fixes pillar 11、Baffle liner 12、3rd fixes pillar 13、Drop catching net 14、4th fixes pillar 15、First guide rail and draw-in groove 16、Upper shell 17、Upper-lower casing adpting flange 18、Exhaustor 19、Lower house 20、Upper point drenches orifice plate 21、Lower point drenches orifice plate 22、Upper liquid retaining ring 23、Lower liquid retaining ring 24、5th fixes pillar 25、6th fixes pillar 26、Upper point of trickle catch tray 27、Under divide trickle catch tray 28、Upper gas separation umbrella 29、Lower gas separation umbrella 30、7th fixes pillar 31、8th fixes pillar 32、9th fixes pillar 33、Tenth fixes pillar 34、11st fixes pillar 35、12nd fixes pillar 36、Second guide rail and draw-in groove 37、Outlet pipe 38、Blow-off pipe 39、Device mounting feet 40、Hanger 41.
Detailed description of the invention
nullA kind of GEOTHERMAL WATER gas-liquid-solid three-phase separator that the present invention mentions，Referring to the drawings 1、2 and 6，Including upper shell 17、Lower house 20、Swirling flow sand-removing mechanism、Clash into Fen Lin mechanism and separate umbrella mechanism，Described upper shell 17 and lower house 20 are flexibly connected，The top of upper shell 17 is provided with exhaustor 19，The middle part of upper shell 17 is provided with drop catching net 14，Described lower house 20 inner chamber installs Swirling flow sand-removing mechanism、Clash into Fen Lin mechanism and separate umbrella mechanism，Swirling flow sand-removing mechanism separates bucket 10 with gas-liquid runner and coordinates，Gas-liquid runner separates the bottom of bucket 10 and is provided with baffle liner 12，Described gas-liquid runner separates the lower section of bucket 10 and is provided with shock Fen Lin mechanism，Clash into Fen Lin mechanism and include point pouring orifice plate 21 and lower point of pouring orifice plate 22，The lower point of lower section drenching orifice plate 22 is provided with by upper point trickle catch tray 27、Under divide trickle catch tray 28、Upper gas separation umbrella 29、The separation umbrella mechanism of lower gas separation umbrella 30 composition，Lower end sidepiece at lower house 20 is provided with outlet pipe 38，Bottommost is provided with blow-off pipe 39；The bottom of described Swirling flow sand-removing mechanism is provided with sediment outflow pipe 6 in eddy flow, and in eddy flow, sediment outflow pipe 6 is drawn outside lower house 20 by connecting eddy flow effluent sand pipe 8.
null3-4 referring to the drawings，The Swirling flow sand-removing mechanism of the present invention includes the outer water inlet pipe 1 of eddy flow、Water inlet pipe 2 in eddy flow、Eddy flow cylindrical section 3、Overflow pipe 4、Eddy flow conical section 5、Sediment outflow pipe 6 in eddy flow、Silt collecting pipe 7、Eddy flow effluent sand pipe 8，And eddy flow cylindrical section 3 fixes pillar 9 by first and is welded and fixed with gas-liquid runner separation bucket 10，Eddy flow conical section 5 on the downside of eddy flow cylindrical section 3 is fixed pillar 11 by second and is welded and fixed with gas-liquid runner separation bucket 10，Eddy flow conical section 5 lower end connects sediment outflow pipe 6 in eddy flow，In eddy flow, the stage casing of sediment outflow pipe 6 is provided with the silt collecting pipe 7 that volume increases，And the lower end of sediment outflow pipe 6 is flexibly connected with eddy flow effluent sand pipe 8 in eddy flow，Specifically in eddy flow, the lower end of sediment outflow pipe 6 is connected with eddy flow effluent sand pipe 8 by flange，Eddy flow effluent sand pipe 8 is located at the outside of lower house.
Referring to the drawings 5, clash into Fen Lin mechanism upper point drench orifice plate 21 center and coordinate with eddy flow conical section 5, the upper point of outside drenching orifice plate 21 connects upper liquid retaining ring 23, and passes through the 5th and fix pillar 25 and coordinate with the second guide rail and draw-in groove 37；The lower point of center drenching orifice plate 22 coordinates with eddy flow conical section 5, liquid retaining ring 24 under the lower point outside connection drenching orifice plate 22, and passes through the 6th and fix pillar 26 and coordinate with the second guide rail and draw-in groove 37.
Referring to the drawings 7, two guide rails and draw-in groove design, device inner core can overall extract out, convenient manufactures and maintenance, specifically: the second guide rail and draw-in groove 37 are bent by whole piece steel plate and form, and are welded in inside apparatus casing.4th fix pillar the 15, the 5th fix pillar the 25, the 6th fix pillar the 26, the 9th fix pillar the 33, the tenth fix pillar 34 be all along guide rail slip down to correspondence draw-in groove at, slewing inner core makes fixing pillar be entered at draw-in groove by guide rail, so weight of inner core is transferred on draw-in groove by fixing pillar, and is delivered on housing by draw-in groove.
Referring to the drawings 8, the center of the upper point trickle catch tray 27 separating umbrella mechanism of the present invention coordinates with sediment outflow pipe 6 in eddy flow, and the center of lower point of trickle catch tray 28 coordinates with sediment outflow pipe 6 in eddy flow, and lower point of trickle catch tray 28 is positioned at a point lower section for trickle catch tray 27；Described upper point be provided with gas separation umbrella 29 between trickle catch tray 27 and lower point of trickle catch tray 28, be provided with lower gas separation umbrella 30 in the lower section of lower point of trickle catch tray 28.
It addition, upper point of trickle catch tray 27 fixes pillar 31 by the longitudinal the 7th is connected to gas separation umbrella 29, and the 7th fixes pillar 31 and fixes pillar 33 by the horizontal the 9th and coordinate with the second guide rail and draw-in groove 37；Above-mentioned lower point of trickle catch tray 28 is fixed pillar 32 by the longitudinal the 8th and is connected to lower gas separation umbrella 30, and the 8th fixes pillar 32 and fix pillar 34 by the horizontal the tenth and coordinate with the second guide rail and draw-in groove 37.
The top inner chamber of above-mentioned eddy flow cylindrical section 3 is provided with overflow pipe 4.
Furthermore, the bottom of drop catching net 14 is fixed pillar 15 by the 4th and is supported, and the 4th outside fixing pillar 15 coordinates with the first guide rail and draw-in groove 16；The outer water inlet pipe 1 of above-mentioned eddy flow is connected to water inlet pipe 2 in the eddy flow of lower house 20 inner chamber, and in eddy flow, water inlet pipe 2 is connected to the tangential direction of eddy flow cylindrical section 3；Upper shell 17, lower house 20 are connected by upper-lower casing adpting flange 18；Eddy flow cylindrical section 3, eddy flow conical section 5 are welded to connect.
The using method of a kind of GEOTHERMAL WATER gas-liquid-solid three-phase separator that the present invention mentions, comprises the following steps:
Gassiness, silt GEOTHERMAL WATER from eddy flow in water inlet 1, eddy flow water inlet 2 tangent line enter in Swirling flow sand-removing mechanism, carry out solid-liquor separation by eddy flow cylindrical section 3 and eddy flow conical section 5, silt is discharged by sediment outflow pipe 6, eddy flow effluent sand pipe 8 in eddy flow；
Gassy water overflows Swirling flow sand-removing mechanism by overflow pipe 4, separates free-falling inside bucket 10 at gas-liquid runner and, to clashing in Fen Lin mechanism, collides, divides and drench, increase exposed surface area, cause turbulent condition, make gas separate with liquid；Liquid after undue pouring forms tiny water column and continues to fall to a point trickle catch tray 27, liquid after collection falls to lower section by catch tray center and separates umbrella mechanism and carry out further gas-liquid separation with the gap of sediment outflow pipe 6 in eddy flow, and the liquid after final separation is discharged through outlet pipe 38 from three phase separator bottom；
The free gas separated in clashing into Fen Lin mechanism and separation umbrella mechanism separates bucket 10 outer wall by gas-liquid runner and flows up, and discharges three phase separator through drop catching net 14 and exhaustor 19, and pump-down process mode is determined by scene and is equipped with, and gas safety processes.
Claims (10)
- null1. a GEOTHERMAL WATER gas-liquid-solid three-phase separator，It is characterized in that: include upper shell (17)、Lower house (20)、Swirling flow sand-removing mechanism、Clash into Fen Lin mechanism and separate umbrella mechanism，Described upper shell (17) and lower house (20) are flexibly connected，The top of upper shell (17) is provided with exhaustor (19)，The middle part of upper shell (17) is provided with drop catching net (14)，Described lower house (20) inner chamber installs Swirling flow sand-removing mechanism、Clash into Fen Lin mechanism and separate umbrella mechanism，Swirling flow sand-removing mechanism separates bucket (10) with gas-liquid runner and coordinates，Gas-liquid runner separates the bottom of bucket (10) and is provided with baffle liner (12)，Described gas-liquid runner separates the lower section of bucket (10) and is provided with shock Fen Lin mechanism，Clash into Fen Lin mechanism and include point pouring orifice plate (21) and lower point of pouring orifice plate (22)，The lower point of lower section drenching orifice plate (22) is provided with by upper point trickle catch tray (27)、Under divide trickle catch tray (28)、Upper gas separation umbrella (29)、Lower gas separation umbrella (30) forms separation umbrella mechanism，Lower end sidepiece at lower house (20) is provided with outlet pipe (38)，Bottommost is provided with blow-off pipe (39)；The bottom of described Swirling flow sand-removing mechanism is provided with sediment outflow pipe (6) in eddy flow, and in eddy flow, sediment outflow pipe (6) draws lower house (20) outward by connecting eddy flow effluent sand pipe (8).
- nullGEOTHERMAL WATER gas-liquid-solid three-phase separator the most according to claim 1，It is characterized in that: described Swirling flow sand-removing mechanism includes the outer water inlet pipe (1) of eddy flow、Water inlet pipe (2) in eddy flow、Eddy flow cylindrical section (3)、Overflow pipe (4)、Eddy flow conical section (5)、Sediment outflow pipe (6) in eddy flow、Silt collecting pipe (7)、Eddy flow effluent sand pipe (8)，And eddy flow cylindrical section (3) fixes pillar (9) and gas-liquid runner separation bucket (10) by first and is welded and fixed，The eddy flow conical section (5) of eddy flow cylindrical section (3) downside is fixed pillar (11) by second and is welded and fixed with gas-liquid runner separation bucket (10)，Eddy flow conical section (5) lower end connects sediment outflow pipe (6) in eddy flow，In eddy flow, the stage casing of sediment outflow pipe (6) is provided with the silt collecting pipe (7) that volume increases，And the lower end of sediment outflow pipe (6) is flexibly connected with eddy flow effluent sand pipe (8) in eddy flow.
- GEOTHERMAL WATER gas-liquid-solid three-phase separator the most according to claim 1, it is characterized in that: upper point pouring orifice plate (21) center of described shock Fen Lin mechanism coordinates with eddy flow conical section (5), the upper point of outside drenching orifice plate (21) connects upper liquid retaining ring (23), and fixes pillar (25) by the 5th and coordinate with the second guide rail and draw-in groove (37)；The lower point of center drenching orifice plate (22) coordinates with eddy flow conical section (5), liquid retaining ring (24) under the outside connection of lower point pouring orifice plate (22), and passes through the 6th and fix pillar (26) and coordinate with the second guide rail and draw-in groove (37).
- GEOTHERMAL WATER gas-liquid-solid three-phase separator the most according to claim 1, it is characterized in that: the center of the described upper point trickle catch tray (27) separating umbrella mechanism coordinates with sediment outflow pipe (6) in eddy flow, the center dividing down trickle catch tray (28) coordinates with sediment outflow pipe (6) in eddy flow, and lower point of trickle catch tray (28) is positioned at a point lower section for trickle catch tray (27)；Described upper point be provided with gas separation umbrella (29) between trickle catch tray (27) and lower point of trickle catch tray (28), be provided with lower gas separation umbrella (30) in the lower section of lower point of trickle catch tray (28).
- GEOTHERMAL WATER gas-liquid-solid three-phase separator the most according to claim 4, it is characterized in that: described upper point trickle catch tray (27) is fixed pillar (31) by the longitudinal the 7th and is connected to gas separation umbrella (29), and the 7th fixes pillar (31) and fix pillar (33) by the horizontal the 9th and coordinate with the second guide rail and draw-in groove (37).
- GEOTHERMAL WATER gas-liquid-solid three-phase separator the most according to claim 4, it is characterized in that: lower point of described trickle catch tray (28) is fixed pillar (32) by the longitudinal the 8th and be connected to lower gas separation umbrella (30), and the 8th fixes pillar (32) and fix pillar (34) by the horizontal the tenth and coordinate with the second guide rail and draw-in groove (37).
- GEOTHERMAL WATER gas-liquid-solid three-phase separator the most according to claim 2, is characterized in that: the top inner chamber of described eddy flow cylindrical section (3) is provided with overflow pipe (4).
- GEOTHERMAL WATER gas-liquid-solid three-phase separator the most according to claim 1, it is characterized in that: the bottom of described drop catching net (14) is fixed pillar (15) by the 4th and supported, and the 4th outside fixing pillar (15) coordinates with the first guide rail and draw-in groove (16).
- GEOTHERMAL WATER gas-liquid-solid three-phase separator the most according to claim 2, it is characterized in that: the outer water inlet pipe (1) of described eddy flow is connected to water inlet pipe (2) in the eddy flow of lower house (20) inner chamber, and in eddy flow, water inlet pipe (2) is connected to the tangential direction of eddy flow cylindrical section (3).
- 10. a using method for GEOTHERMAL WATER gas-liquid-solid three-phase separator as claimed in any one of claims 1-9 wherein, is characterized in that:Gassiness, silt GEOTHERMAL WATER from eddy flow in water inlet (1), eddy flow water inlet (2) tangent line enter in Swirling flow sand-removing mechanism, carrying out solid-liquor separation by eddy flow cylindrical section (3) and eddy flow conical section (5), silt is discharged by sediment outflow pipe (6), eddy flow effluent sand pipe (8) in eddy flow；Gassy water overflows Swirling flow sand-removing mechanism by overflow pipe (4), separates bucket (10) inner side free-falling to clashing in Fen Lin mechanism at gas-liquid runner, collides, point drenches, increases exposed surface area, cause turbulent condition, make gas separate with liquid；Liquid after undue pouring forms tiny water column and continues to fall to a point trickle catch tray (27), liquid after collection falls to lower section by catch tray center and separates umbrella mechanism and carry out further gas-liquid separation with the gap of sediment outflow pipe (6) in eddy flow, and the liquid after final separation is discharged from three phase separator bottom through outlet pipe (38)；The free gas separated in clashing into Fen Lin mechanism and separation umbrella mechanism separates bucket (10) outer wall by gas-liquid runner and flows up, three phase separator is discharged through drop catching net (14) and exhaustor (19), pump-down process mode is determined by scene and is equipped with, and gas safety processes.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510167995.5A CN104771941B (en) | 2015-04-10 | 2015-04-10 | A kind of GEOTHERMAL WATER gas-liquid-solid three-phase separator and method |
| CN201610731146.2A CN106277398A (en) | 2015-04-10 | 2015-04-10 | A kind of oil-gas gathering and transportation GEOTHERMAL WATER three-phase separating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510167995.5A CN104771941B (en) | 2015-04-10 | 2015-04-10 | A kind of GEOTHERMAL WATER gas-liquid-solid three-phase separator and method |
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| CN201610731146.2A Division CN106277398A (en) | 2015-04-10 | 2015-04-10 | A kind of oil-gas gathering and transportation GEOTHERMAL WATER three-phase separating device |
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| CN104771941A CN104771941A (en) | 2015-07-15 |
| CN104771941B true CN104771941B (en) | 2017-01-04 |
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| CN201510167995.5A Active CN104771941B (en) | 2015-04-10 | 2015-04-10 | A kind of GEOTHERMAL WATER gas-liquid-solid three-phase separator and method |
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| CN106957082B (en) * | 2017-04-26 | 2023-09-22 | 中石化绿源地热能开发有限公司 | Geothermal water gas-liquid-solid separation device |
| CN111115753B (en) * | 2020-01-03 | 2022-03-01 | 西南石油大学 | Easily wash liftable geothermol power exploitation and use triphase separation device |
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| CN2759552Y (en) * | 2004-11-15 | 2006-02-22 | 新疆石油管理局井下作业公司 | Oil-water-sand eddy flow tri-phase separation apparatus |
| GB2423490B (en) * | 2005-02-23 | 2009-05-20 | Dps | Separator |
| JP2011083696A (en) * | 2009-10-15 | 2011-04-28 | Toshiba Corp | Solid-liquid separator |
| CN201701823U (en) * | 2010-03-20 | 2011-01-12 | 李瑞国 | Oil-gas separator |
| CN201949805U (en) * | 2010-12-31 | 2011-08-31 | 西安科源环保设备工程有限公司 | Independent water distribution type dedusting desulfurizer |
| CN203577481U (en) * | 2013-11-20 | 2014-05-07 | 四川科宏石油天然气工程有限公司 | Separator |
| CN103566698B (en) * | 2013-11-20 | 2015-11-04 | 四川科宏石油天然气工程有限公司 | Gas-liquid-solid three-phase separator |
| CN204582632U (en) * | 2015-04-10 | 2015-08-26 | 胜利油田森诺胜利工程有限公司 | A kind of GEOTHERMAL WATER gas-liquid-solid three-phase separator |
-
2015
- 2015-04-10 CN CN201610731146.2A patent/CN106277398A/en active Pending
- 2015-04-10 CN CN201510167995.5A patent/CN104771941B/en active Active
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| Publication number | Publication date |
|---|---|
| CN106277398A (en) | 2017-01-04 |
| CN104771941A (en) | 2015-07-15 |
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Address after: 257000 the Yellow River Road, Shandong city of Dongying province Dongying District No. 721 senuo Victory Mansion Patentee after: Suno Technology Co., Ltd Address before: 257000 the Yellow River Road, Shandong city of Dongying province Dongying District No. 721 senuo Victory Mansion Patentee before: Shengli Oilfield Sino Shengli Engineering Co., Ltd. |
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