CN106512484A - Detachable multi-cylinder centrifugal inlet internal part based on three-phase separator - Google Patents
Detachable multi-cylinder centrifugal inlet internal part based on three-phase separator Download PDFInfo
- Publication number
- CN106512484A CN106512484A CN201611071542.3A CN201611071542A CN106512484A CN 106512484 A CN106512484 A CN 106512484A CN 201611071542 A CN201611071542 A CN 201611071542A CN 106512484 A CN106512484 A CN 106512484A
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- China
- Prior art keywords
- shunting
- cyclone separating
- separating tube
- house steward
- cylinder
- 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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- 239000012071 phase Substances 0.000 claims abstract description 32
- 239000007788 liquid Substances 0.000 claims abstract description 10
- 239000007791 liquid phase Substances 0.000 claims abstract description 4
- 230000008676 import Effects 0.000 claims description 33
- 239000000463 material Substances 0.000 claims description 18
- 238000005119 centrifugation Methods 0.000 claims description 11
- 238000000926 separation method Methods 0.000 abstract description 16
- 239000012530 fluid Substances 0.000 abstract description 7
- 239000006260 foam Substances 0.000 abstract description 5
- 239000013043 chemical agent Substances 0.000 abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 2
- 239000013072 incoming material Substances 0.000 abstract 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 3
- 230000001133 acceleration Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 230000001869 rapid Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/02—Foam dispersion or prevention
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
- B01D45/16—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by the winding course of the gas stream, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Geology (AREA)
- Mining & Mineral Resources (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Environmental & Geological Engineering (AREA)
- Dispersion Chemistry (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Cyclones (AREA)
Abstract
The invention relates to a detachable multi-cylinder centrifugal inlet internal part based on a three-phase separator. The inlet internal part cooperates with the three-phase separator for use. The inlet internal part is characterized by comprising a shunting header, first cyclone separation cylinders, second cyclone separation cylinders, third cyclone separation cylinders and a guide plate; an incoming material passes through the shunting header and the guide plate and enters the six cyclone separation cylinders, cyclone separation is produced under the action of centrifugal force, a gas phase with the low liquid content is output from an upper port, and a liquid phase with the low gas content enters an oil and water separation phase; an inlet of the shunting header adopts a necked throat pipe structure, the speed of a fluid entering a shunting section of the shunting header is adjusted, foam is reduced, the use of chemical agents for removing foam is reduced, and the separation effect is improved.
Description
Technical field
The present invention relates to three phase separation technical field, more particularly to a kind of detachable many based on three phase separator from
Heart import internals.
Background technology
In oil gas field and its manufacture field, three phase separator is widely used in dividing for oil gas water three phase as its nucleus equipment
From.Three phase separator import internals are the one kind in its internals, and import internals mainly include：Baffle plate, bend pipe, centrifugation part.Wherein
Relatively broad with baffle plate and bend pipe application, major advantage is simple structure, cheap, but its shortcoming is it is also obvious that because work
Skill medium causes the turbulent flow of fierceness in porch, and the foam of generation is more, it is therefore desirable to supporting use foam-expelling chemical agent and
Its internals, while also increasing equipment volume design margin, counteracts the advantage of baffle plate and bend pipe low cost to a certain extent.
Under the relatively low operating mode of feed throughput and its pressure, it is proper using baffle plate and bend pipe.
But under the higher operating mode of feed throughput and its pressure, processing medium causes more fierce rapids in porch
Stream, if still adopting baffle plate and bend pipe, in order to meet technological requirement, its cost is dramatically increased.
Therefore under the operating mode, the kinetic energy of Inlet fluid itself is used, using centrifugal import internals, is flowed in the future
Entry design produces centrifugal force into along cylinder tangential direction, so that gas-liquid mixture carries out just separation in porch.
The content of the invention
The technical problem to be solved in the present invention is to provide a kind of detachable many centrifugation imports based on three phase separator
Internals, can solve the problem that the foam volume of the generation that original three phase separator is present is high, are used at chemical agent froth breaking, raw material in a large number
Reason amount is low, the problem more than low separation efficiency, gas entrained liquids amount.
To solve above-mentioned technical problem, the technical scheme is that：It is a kind of based on the detachable many of three phase separator
Cylinder centrifugation import internals, the import internals are used cooperatively with three phase separator；Its innovative point is：Including：
One horizontally disposed shunting house steward, the shunting house steward are disposed with feed zone, total speedup section and shunting from front to back
Section, installs adpting flange in feed zone front end, and in total speedup Duan Weiyi undergauge trunnion, shunting section is an isometrical body, and this is isometrical
The front end of body is connected with undergauge trunnion, and isometrical body rear end arranges end socket；
A pair first cyclone separating tubes, the axis of first cyclone separating tube are vertically arranged, the first cyclone separating tube pair of this pair
Claim on shunting house steward, and in the shunting section of the cylinder locally embedding shunting house steward of the first cyclone separating tube；In the first rotation
Be embedded on wind cylinder on the cylinder in shunting section first material import is provided with along the first cyclone separating tube cylinder tangential direction, and
The first described cyclone separating tube cylinder tangent line and the shunting section diameter parallel for shunting house steward；
A pair second cyclone separating tubes, the axis of second cyclone separating tube are vertically arranged, the second cyclone separating tube pair of this pair
Claim on shunting house steward, and in the shunting section of the cylinder locally embedding shunting house steward of the second cyclone separating tube；In the second rotation
Be embedded on wind cylinder on the cylinder in shunting section second material import is provided with along the second cyclone separating tube cylinder tangential direction, and
The second described cyclone separating tube cylinder tangent line and the shunting section diameter parallel for shunting house steward；On the axis direction of shunting section,
After second cyclone separating tube is located at the first cyclone separating tube；
A pair the 3rd cyclone separating tubes, the axis of the 3rd cyclone separating tube are vertically arranged, the 3rd cyclone separating tube pair of this pair
Claim on shunting house steward, and in the shunting section of the cylinder locally embedding shunting house steward of the 3rd cyclone separating tube；In the 3rd rotation
Be embedded on wind cylinder on the cylinder in shunting section 3 material import is provided with along the 3rd cyclone separating tube cylinder tangential direction, and
The 3rd described cyclone separating tube cylinder tangent line and the shunting section diameter parallel for shunting house steward；On the axis direction of shunting section,
After 3rd cyclone separating tube is located at the second cyclone separating tube；
One deflector, the deflector are that, in conical structure, deflector is built in the shunting section of shunting house steward, the axle of deflector
Line is gradually increased from front to back with the shunting section dead in line for shunting house steward, and the cross section of deflector；In the axis of shunting section
On direction, the cone apex of the deflector is located at the first material import rear of the first cyclone separating tube, the deflector
Cone bottom surface be located at the 3rd cyclone separating tube 3 material import in front of；The circle being located in the deflector on horizontal plane
The extended line of two bus of cone is each passed through two 3 material imports of the 3rd cyclone separating tube；
The diameter of the cyclone separating tube is 0.7 to 0.8 times of the shunting section diameter for shunting house steward.
Further, the location-plate in strap bolt hole is provided with above the shunting section of the shunting house steward, the location-plate passes through
Bolt will shunt house steward and separate cylinder with rotation and be fixedly linked.
Further, the bottom of the cyclone separating tube is connected with the liquid phase part of three phase separator, the cyclonic separation
The top of cylinder is connected with the liquid gas phase portion of three phase separator；Each pair is with regard to shunting the cyclone separating tube that house steward's axisymmetrical is arranged
Outside is connected by U-bolt.
It is an advantage of the current invention that：
1) import in shunting house steward adopts necking down throat tubular construction, adjusts the speed that fluid enters shunting house steward's straight tube structure, subtracts
The generation of foam is lacked, has reduced the use of foam-expelling chemical agent, improve separating effect；
2）By connecting with shunting house steward in cyclone separating tube tangential direction so that fluid tangentially enters cyclone separating tube
It is interior, produce centrifugal motion, gas-liquid two-phase can sharp separation, increase vapor-liquid separation speed, reduce gas outlet's liquid entrainment
Amount；
3）Deflector adopts conical structure so that fluid when through deflector, due to deflector with shunting house steward gap
It is gradually reduced, increased the flow velocity of fluid, fluid can produces acceleration when entering in cyclone cylinder from shunting house steward, be easy to
Centrifugal motion is produced in cyclone cylinder, speed up gas and liquid is separated.
Description of the drawings
The present invention is further detailed explanation with reference to the accompanying drawings and detailed description.
Fig. 1 is detachable many tin centrifugation import internals separation principle figures of the present invention based on three phase separator.
Fig. 2 is detachable many tin centrifugation import internals assembling top views of the present invention based on three phase separator.
Fig. 3 is detachable many tin centrifugation import internals assembling side elevations of the invention based on three phase separator.
Specific embodiment
The following examples can make professional and technical personnel that the present invention is more fully understood, but not therefore by this
It is bright be limited in described scope of embodiments among.
A kind of detachable many centrifugation import internals based on three phase separator as shown in Figure 1 to Figure 3, in the import
Part is used cooperatively with three phase separator；Including：
One horizontally disposed shunting house steward 1, the shunting house steward 1 are disposed with feed zone 11, total speedup section 12 from front to back
With shunting section 13, adpting flange 10 is installed in 11 front end of feed zone, is a undergauge trunnion in total speedup section 12, shunting section 13 is one
Isometrical body, the front end of the isometrical body are connected with undergauge trunnion, and isometrical body rear end arranges end socket 14；
A pair first cyclone separating tubes 2, the axis of first cyclone separating tube 2 are vertically arranged, the first cyclone separating tube of this pair 2
It is symmetrically mounted on shunting house steward 1, and in the shunting section 13 of the cylinder locally embedding shunting house steward 1 of the first cyclone separating tube 2；
Be embedded on first cyclone separating tube 2 on the cylinder in shunting section 13 first is provided with along 2 cylinder tangential direction of the first cyclone separating tube
Material inlet 21, and described 2 cylinder tangent line of the first cyclone separating tube is parallel with 13 line of shunting section axle of shunting house steward 1；
A pair second cyclone separating tubes 3, the axis of second cyclone separating tube 3 are vertically arranged, the second cyclone separating tube of this pair 3
It is symmetrically mounted on shunting house steward 1, and in the shunting section 13 of the cylinder locally embedding shunting house steward 1 of the second cyclone separating tube 3；
Be embedded on second cyclone separating tube 3 on the cylinder in shunting section 13 second is provided with along 3 cylinder tangential direction of the second cyclone separating tube
Material inlet 31, and described 3 cylinder tangent line of the second cyclone separating tube and 13 diameter parallel of shunting section for shunting house steward 1；Dividing
On the axis direction of stream section 13, after second cyclone separating tube 3 is located at the first cyclonic separation 2；
A pair the 3rd cyclone separating tubes 4, the axis of the 3rd cyclone separating tube 4 are vertically arranged, the 3rd cyclonic separation of this pair 4
It is symmetrically mounted on shunting house steward 1, and in the shunting section 13 of the cylinder locally embedding shunting house steward 1 of the 3rd cyclone separating tube 4；
Be embedded on 3rd cyclone separating tube 4 on the cylinder in shunting section 13 the 3rd is provided with along 4 cylinder tangential direction of the 3rd cyclone separating tube
Material inlet 41, and described 4 cylinder tangent line of the 3rd cyclone separating tube and 13 diameter parallel of shunting section for shunting house steward 1；Dividing
On the axis direction of stream section 13, after the 3rd cyclone separating tube 4 is located at the second cyclonic separation 2；
One deflector 5, the deflector 5 are that, in conical structure, deflector 5 is built in the shunting section 13 of shunting house steward 1, water conservancy diversion
The axis of plate 5 is gradually increased from front to back with 13 dead in line of shunting section for shunting house steward 1, and the cross section of deflector 5；Dividing
On the axis direction of stream section 13, the cone apex of the deflector 5 is located at the first material import 21 of the first cyclone separating tube 2
Rear, the cone bottom surface of the deflector 5 are located in front of the 3 material import 41 of the 3rd cyclone separating tube 4；The water conservancy diversion
The extended line of two bus of cone being located on horizontal plane in plate 5 is each passed through two 3 materials of the 3rd cyclone separating tube 4
Import 41；
The diameter of cyclone separating tube is 0.8 times of 13 diameter of shunting section for shunting house steward 1.
The top of the shunting section 13 of shunting house steward 1 is provided with the location-plate 6 in strap bolt hole, and the location-plate 6 will by bolt
Shunting house steward 1 is separated cylinder 13 and is fixedly linked with rotation.
The bottom of each pair cyclone separating tube is connected with the liquid phase part of three phase separator, the top of each pair cyclone separating tube
End is connected with the liquid gas phase portion of three phase separator；Each pair is with regard to shunting on the outside of the cyclone separating tube that 1 axisymmetrical of house steward is arranged
Connected by U-bolt 7.
It should be understood by those skilled in the art that, the present invention is not restricted to the described embodiments, above-described embodiment and explanation
Merely illustrating the principles of the invention described in book, without departing from the spirit and scope of the present invention, the present invention also has
Various changes and modifications, these changes and improvements are both fallen within scope of the claimed invention.The claimed scope of the invention
By appending claims and its equivalent thereof.
Claims (3)
1. a kind of detachable many centrifugation import internals based on three phase separator, the import internals and three phase separator cooperation
Use；It is characterized in that：Including：
One horizontally disposed shunting house steward, the shunting house steward are disposed with feed zone, total speedup section and shunting from front to back
Section, installs adpting flange in feed zone front end, and in total speedup Duan Weiyi undergauge trunnion, shunting section is an isometrical body, and this is isometrical
The front end of body is connected with undergauge trunnion, and isometrical body rear end arranges end socket；
A pair first cyclone separating tubes, the axis of first cyclone separating tube are vertically arranged, the first cyclone separating tube pair of this pair
Claim on shunting house steward, and in the shunting section of the cylinder locally embedding shunting house steward of the first cyclone separating tube；In the first rotation
Be embedded on wind cylinder on the cylinder in shunting section first material import is provided with along the first cyclone separating tube cylinder tangential direction, and
The first described cyclone separating tube cylinder tangent line and the shunting section diameter parallel for shunting house steward；
A pair second cyclone separating tubes, the axis of second cyclone separating tube are vertically arranged, the second cyclone separating tube pair of this pair
Claim on shunting house steward, and in the shunting section of the cylinder locally embedding shunting house steward of the second cyclone separating tube；In the second rotation
Be embedded on wind cylinder on the cylinder in shunting section second material import is provided with along the second cyclone separating tube cylinder tangential direction, and
The second described cyclone separating tube cylinder tangent line and the shunting section diameter parallel for shunting house steward；On the axis direction of shunting section,
After second cyclone separating tube is located at the first cyclone separating tube；
A pair the 3rd cyclone separating tubes, the axis of the 3rd cyclone separating tube are vertically arranged, the 3rd cyclone separating tube pair of this pair
Claim on shunting house steward, and in the shunting section of the cylinder locally embedding shunting house steward of the 3rd cyclone separating tube；In the 3rd rotation
Be embedded on wind cylinder on the cylinder in shunting section 3 material import is provided with along the 3rd cyclone separating tube cylinder tangential direction, and
The 3rd described cyclone separating tube cylinder tangent line and the shunting section diameter parallel for shunting house steward；On the axis direction of shunting section,
After 3rd cyclone separating tube is located at the second cyclone separating tube；
One deflector, the deflector are that, in conical structure, deflector is built in the shunting section of shunting house steward, the axle of deflector
Line is gradually increased from front to back with the shunting section dead in line for shunting house steward, and the cross section of deflector；In the axis of shunting section
On direction, the cone apex of the deflector is located at the first material import rear of the first cyclone separating tube, the deflector
Cone bottom surface be located at the 3rd cyclone separating tube 3 material import in front of；The circle being located in the deflector on horizontal plane
The extended line of two bus of cone is each passed through two 3 material imports of the 3rd cyclone separating tube；
The diameter of the cyclone separating tube is 0.7 to 0.8 times of the shunting section diameter for shunting house steward.
2. according to claim 1 a kind of based on detachable many of three phase separator centrifugation import internals, its feature
It is：The location-plate in strap bolt hole is provided with above the shunting section of the shunting house steward, the location-plate will shunt total by bolt
Guan Yuxuan separates cylinder and is fixedly linked.
3. according to claim 1 a kind of based on detachable many of three phase separator centrifugation import internals, its feature
It is：The bottom of the cyclone separating tube is connected with the liquid phase part of three phase separator, the top of the cyclone separating tube and three
The liquid gas phase portion of phase separator is connected；Each pair is with regard to shunting on the outside of the cyclone separating tube that house steward's axisymmetrical is arranged by U-shaped
Bolt connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611071542.3A CN106512484A (en) | 2016-11-29 | 2016-11-29 | Detachable multi-cylinder centrifugal inlet internal part based on three-phase separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611071542.3A CN106512484A (en) | 2016-11-29 | 2016-11-29 | Detachable multi-cylinder centrifugal inlet internal part based on three-phase separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106512484A true CN106512484A (en) | 2017-03-22 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611071542.3A Pending CN106512484A (en) | 2016-11-29 | 2016-11-29 | Detachable multi-cylinder centrifugal inlet internal part based on three-phase separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106512484A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108654144A (en) * | 2018-06-04 | 2018-10-16 | 马毛毛 | A kind of medicament phase separation simulation experimental provision |
| WO2018189651A1 (en) * | 2017-04-12 | 2018-10-18 | Koch-Glitsch, Lp | An inlet device for separating phases of a liquid stream in a vessel and method involving same |
| CN112811629A (en) * | 2020-12-31 | 2021-05-18 | 江苏华普泰克石油装备有限公司 | Three-phase separator for urban sewage treatment |
| CN113063050A (en) * | 2021-04-08 | 2021-07-02 | 章信武 | Tap water pipeline capable of separating gas |
| CN114225603A (en) * | 2021-12-22 | 2022-03-25 | 常州大学 | Multiple air purification and filth recovery unit based on passageway circles round |
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| AU2018253401B2 (en) * | 2017-04-12 | 2020-10-15 | Koch-Glitsch, Lp | An inlet device for separating phases of a liquid stream in a vessel and method involving same |
| KR102345203B1 (en) | 2017-04-12 | 2021-12-31 | 코크-글리취 엘피 | Inlet device for separating phases of a liquid stream in a vessel and method accompanying the same |
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| JP2020512933A (en) * | 2017-04-12 | 2020-04-30 | コーク−グリッシュ，リミティド パートナーシップ | Inlet device for separating the phases of a liquid stream in a container and a method including the same |
| US10792592B2 (en) | 2017-04-12 | 2020-10-06 | Koch-Glitsch, Lp | Inlet device for separating phases of a liquid stream in a vessel and method involving same |
| WO2018189651A1 (en) * | 2017-04-12 | 2018-10-18 | Koch-Glitsch, Lp | An inlet device for separating phases of a liquid stream in a vessel and method involving same |
| RU2735610C1 (en) * | 2017-04-12 | 2020-11-05 | Кох-Глич, Лп | Inlet device for separation of phases of liquid medium flow in vessel and method using device thereof |
| CN110430927B (en) * | 2017-04-12 | 2021-07-09 | 科氏-格利奇有限合伙公司 | Inlet device for separating a liquid flow phase in a container and method relating thereto |
| JP7051896B2 (en) | 2017-04-12 | 2022-04-11 | コーク－グリッシュ，リミティド パートナーシップ | A method including an inlet device and the device for separating the phases of the liquid flow in the container. |
| CN108654144A (en) * | 2018-06-04 | 2018-10-16 | 马毛毛 | A kind of medicament phase separation simulation experimental provision |
| CN112811629A (en) * | 2020-12-31 | 2021-05-18 | 江苏华普泰克石油装备有限公司 | Three-phase separator for urban sewage treatment |
| CN113063050A (en) * | 2021-04-08 | 2021-07-02 | 章信武 | Tap water pipeline capable of separating gas |
| CN114225603A (en) * | 2021-12-22 | 2022-03-25 | 常州大学 | Multiple air purification and filth recovery unit based on passageway circles round |
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Inventor after: Wu Hui Inventor after: Li Dan Inventor after: Li Hongbin Inventor before: Wu Hui |
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Application publication date: 20170322 |