CN106139746B - Whirl slug flow catcher - Google Patents
Whirl slug flow catcher Download PDFInfo
- Publication number
- CN106139746B CN106139746B CN201610582159.8A CN201610582159A CN106139746B CN 106139746 B CN106139746 B CN 106139746B CN 201610582159 A CN201610582159 A CN 201610582159A CN 106139746 B CN106139746 B CN 106139746B
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- CN
- China
- Prior art keywords
- shell
- gas
- slug flow
- whirl
- place
- 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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Classifications
-
- 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
- B01D45/06—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by reversal of direction of flow
-
- 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
- B01D45/08—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by impingement against baffle separators
-
- 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
Abstract
The invention discloses a kind of whirl slug flow catcher, including shell, portion's tangential direction is equipped with gas feed in the housing, installs swirl cylinder in the shell at the gas feed, TP board group part of the installation with radial passage in the shell internal upper part gas compartment.The trap is vertical structure.The present invention can improve liquid phase separative efficiency, effectively solve influence of the oil and gas multiphase flow pipeline slug flow to production, be conducive to the progress of subsequent technique stable production process, reduce project cost.
Description
Technical field
The present invention relates to a kind of processing equipments of multiphase transportation pipeline slug flow, suitable for oil gas field surface gathering and transferring engineering
The trapping and elimination of slug flow.
Background technology
With the exploitation of ocean, land oil gas field and large-scale gas condensate field, multi-phase mixed delivering technique is constantly developed,
In multi-phase mixed delivering process and gas long-distance transmission pipeline, slug flow usually can be all generated.Serious slug flow can be to pipeline end
A series of problems, such as end oil gas separation equipment and subsequent technique device cause hydraulic blow, obstruction and level fluctuation, makes downstream
Process unit is difficult normal work.
Existing its entrance generally use inlet dispenser of slug catcher or degasification plate, by collide gentle liquid density contrast into
Row Gravity Separation needs longer residence time and sufficiently large separated space and liquid storage space, and the TP plates of the gas compartment
Segregational load weight, low separation efficiency.
Therefore, it is necessary to provide a kind of novel whirl slug flow catcher, slug flow is reduced caused by down stream train
Influence is vital.
Invention content
In order to overcome the disadvantages mentioned above of the prior art, the present invention provides a kind of new type high-efficient whirl slug flow catcher,
Gas-liquid separation and trapping slug can be effectively facilitated, operates steadily, solves influence of the mixed transporting tube line segment plug flow to production, is ensured
The safe operation of production.
The technical solution adopted by the present invention to solve the technical problems is：
A kind of whirl slug flow catcher, including shell, in the housing portion's tangential direction be equipped with gas feed, the gas
Swirl cylinder is installed in the shell of entrance, the TP board group parts with radial passage are installed in the shell internal upper part gas compartment.
The trap is vertical structure.
The swirl cylinder is made of several cyclone pipes；It is provided in the air inlet pipe at gas feed and is lacked with what cyclone pipe mutually passed through
Mouthful, it is welded with backing plate around the notch, support plate and connecting plate are equipped on backing plate, bolt hole, eddy flow are provided on connecting plate
Pipe is installed in the gap position of gas inlet tube by bolt and the connecting plate.
The TP board group parts with radial passage, center are gas passage, and top is equipped with baffle, and bottom is equipped with descending liquid
Pipe.
It is characteristic of the invention that：It is caught using the TP plates of the spiral flow at inlet cylinder gas-liquid pre-separation and gas-phase space radial passage
Collection separation, completion gas-liquid that can be rapidly and efficiently are separated, alleviate slug flow, so that fluidised form is tended to be steady, reach trapping slug flow
Effect, be conducive to subsequent art production process and stablize carry out, have very to reducing total investment of engineering, saving operating cost
Good effect.
Description of the drawings
Fig. 1 is main structure diagram of the present invention；
Fig. 2 is the vertical view of Fig. 1；
Fig. 3 is swirl cylinder vertical view of the present invention；
Fig. 4 is the A-A direction views in Fig. 1, i.e., TP board groups part schematic top plan view of the present invention.
In figure：1-2-liquid level gauge of skirt/3-liquid outlet of fluid level transmitter mouth 4-interior cat ladder
5-gas feed 6-swirl cylinder, 7-relief valve port, 8-shell, 9-TP plates
10-gauge port 11-gas vent, 12-downspout, 13-manhole, 14-vortex broken devices
15-sewage draining exit 16-lifting lug, 17-baffle, 18-cyclone pipe, 19-backing plate, 20-support plate, 21-connecting plates
22-bolts.
Specific implementation mode
Further to disclose technical scheme of the present invention, with reference to the accompanying drawings of the specification, it is elaborated by embodiment：
Referring to Fig.1,2,3,4, the present invention relates to a kind of for trapping the plug flow trapper for oil/gas mixed transport section device of slug flow,
Mainly by shell 8, TP board groups part 9, swirl cylinder 6, vortex broken device 14, downspout 12, gas vent 11, liquid outlet 3, sewage draining exit
15, safety valve 7, liquid level gauge/fluid level transmitter 2, pressure gauge 10, manhole 13 form.
A kind of whirl slug flow catcher, including shell, in the housing portion's tangential direction be equipped with gas feed, the gas
Swirl cylinder 6 is installed in the shell 8 at import 5, the TP board groups part 9 with radial passage is installed in the 8 internal upper part gas compartment of shell.
Slug flows through each cyclone pipe 18 that gas feed 5 tangentially enters swirl cylinder 6, carries out cyclonic separation.Drop therein
Along 18 inner wall of cyclone pipe to congregate, gas has diameter along 18 central upward flow of cyclone pipe, into described in upper part of the housing
To the TP board groups part 9 in channel.
The trap uses vertical structure, can effectively increase slug flow in the flowing space of short transverse, extend slug flow
The flowing time of middle gas phase and liquid phase can effectively improve liquid phase separative efficiency, eliminate slug flow.At the gas feed 5
Swirl cylinder 6 is installed in shell 8, liquid phase separative efficiency can be effectively improved.Trap is equipped with lifting lug, and both ends are welded with end socket, intermediate
Equipped with manhole, it is internally provided with cat ladder, is supported using skirt.
As shown in figure 3, the swirl cylinder 6 is made of several cyclone pipes 18；Be provided in the air inlet pipe at gas feed 5 with
Cyclone pipe（The notch that 8 phases are passed through is welded with backing plate 19 around the notch, and support plate 20 and connecting plate 21 are equipped on backing plate 19,
Bolt hole is provided on connecting plate 21, cyclone pipe 18 is installed in the notch of gas inlet tube 5 by bolt 22 and the connecting plate 21
Position.When slug flow flows through the gap position, it can tangentially enter cyclone pipe 18 and carry out cyclonic separation.The structure is installed
It is convenient, detachable.
The TP board groups part 9 with radial passage, center are gas passage, and top is equipped with baffle 17, and bottom is equipped with
Downspout 12.After gas enters upper gaseous phase space, direction can only be changed and pass radially through TP plates along shell around, from TP plates with
The gap of inner walls flows up.This structure increases the arrangements of TP plates, increase gas filtration space, and be varied multiple times
Gas flow direction can effectively trap the drop carried secretly in exit gas.
Lower part is fluid space in the shell 8, and vortex broken device 14 is installed in the fluid space.
8 top of the shell is equipped with gas vent 11, and pressure transmitter is installed on 8 top of shell at gas vent 11
10,8 bottom lowest point of shell is equipped with sewage draining exit 15；Safety valve 7 is installed on the shell 8 at the TP board groups part 9；The liquid
Liquid level gauge/fluid level transmitter 2 is installed on the shell 8 at space；8 bottom sides of shell install liquid outlet 3.
Its operation principle of whirl slug flow catcher and the course of work are：Gas enters by gas feed 5 inside container,
Inlet sets swirl cylinder 6, when gas flows through cyclone pipe 18, enters cyclone pipe along tangential direction, and form eddy flow, generates proportion
The centrifugal force that high times of power, since gas, liquid density is different, the difference of suffered centrifugal force is very big, gravity, centrifugal force and
Gas and liquid are separated under the comprehensive function of buoyancy, liquid is radially pushed to outside, and is discharged from leakage fluid dram downwards, and gas
The center of trap is then moved to, and arrives the gas compartment upwards.After gas is full of admission space, since plate washer 17, gas are arranged at top
Body can only change direction and pass radially through TP plates along shell around, be flowed up from the gap of TP plates and inner walls.Passing through
When TP board group parts 9, air-flow constantly changes direction, and small drop constantly collides with each other, and is constantly coalesced on 9 surface of TP board groups part,
Larger drop is formed, the bottom of container is collected in by collector tube 12, is discharged by liquid outlet 3, is become by liquid level gauge/liquid level
It send device 2 that can show that liquid level signal is sent to Central Control Room centralized control by liquid level, fluid level transmitter, can automatically set Liquid level
Range.The impurity such as solid particle can be discharged by sewage draining exit 15, and sewage draining exit 15 is equipped with vortex broken device 14 to prevent generating vortex.Gas is logical
It crosses after TP board groups part 9 takes off liquid, is full of air outlet space, is flowed out through gas vent 11.It is equipped with safety valve 7 on admission space top, it can
Overpressure protection is carried out, can control outlet pressure, skirt 1 equipped with pressure transmitter 10 on air outlet space top is the pedestal of shell,
Interior cat ladder 4 is arranged in order to facilitate installation and the maintenance of slug catcher, which may be implemented the automatic of gas and connect
Continuous gas-liquid separation and effective trapping of slug flow are eliminated.
Claims (5)
1. a kind of whirl slug flow catcher, including shell, portion's tangential direction is equipped with gas feed in the housing, and feature exists
In：The gas feed（5）The shell at place（8）Interior installation swirl cylinder（6）, shell（8）Installation has in the internal upper part gas compartment
The TP board group parts of radial passage（9）；The TP board group parts with radial passage（9）, center is gas passage, and top is equipped with
Baffle（17）, bottom is equipped with downspout（12）.
2. a kind of whirl slug flow catcher according to claim 1, it is characterised in that：The trap is vertical knot
Structure.
3. a kind of whirl slug flow catcher according to claim 1, it is characterised in that：The swirl cylinder（6）By several
Cyclone pipe（18）It constitutes；In gas feed（5）It is provided in the air inlet pipe at place and cyclone pipe（18）The notch to connect, notch week
Weld all around is connected to backing plate（19）, in backing plate（19）It is equipped with support plate（20）And connecting plate（21）, in connecting plate（21）On be provided with spiral shell
Keyhole, cyclone pipe (18) pass through bolt (22) and the connecting plate（21）It is installed in gas inlet tube（5）Gap position.
4. a kind of whirl slug flow catcher according to claim 1, it is characterised in that：The shell（8）Interior lower part is
Fluid space, the fluid space is interior to install vortex broken device（14）.
5. a kind of whirl slug flow catcher according to claim 4, it is characterised in that：The shell（8）Top is equipped with
Gas vent（11）, in gas vent（11）The shell at place（8）Top is installed by pressure transmitter（10）, shell（8）Bottom is minimum
Place is equipped with sewage draining exit（15）；The TP board groups part（9）The shell at place（8）Upper installation safety valve（7）；At the fluid space
Shell（8）Upper installation liquid level gauge/fluid level transmitter（2）；Shell（8）Bottom sides install liquid outlet（3）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610582159.8A CN106139746B (en) | 2016-07-22 | 2016-07-22 | Whirl slug flow catcher |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610582159.8A CN106139746B (en) | 2016-07-22 | 2016-07-22 | Whirl slug flow catcher |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106139746A CN106139746A (en) | 2016-11-23 |
| CN106139746B true CN106139746B (en) | 2018-10-30 |
Family
ID=58059881
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610582159.8A Active CN106139746B (en) | 2016-07-22 | 2016-07-22 | Whirl slug flow catcher |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106139746B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113862053B (en) * | 2021-11-05 | 2023-12-19 | 四川京海石油设备制造有限公司 | Sand-liquid separation device for shale gas |
| CN115337714B (en) * | 2022-10-14 | 2023-03-28 | 苏州恩都法汽车***股份有限公司 | Centrifugal separator and engine system |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2332632B (en) * | 1997-12-18 | 2001-08-15 | Stephen Crocker | Separating material containing a gas component, a liquid hydrocarbon based component, a water based component, and a solid component |
| CN1749634A (en) * | 2005-09-07 | 2006-03-22 | 胜利油田胜利工程设计咨询有限责任公司 | Plug flow trapper for oil/gas mixed transport section |
| CN101146584A (en) * | 2005-02-23 | 2008-03-19 | Dps布里斯托尔（控股）有限公司 | Separator to separate a liquid/liquid/gas/solid mixture |
| CN201300015Y (en) * | 2008-11-14 | 2009-09-02 | 西安长庆科技工程有限责任公司 | Vertical mist extracting and separating device |
| CN204051245U (en) * | 2014-08-06 | 2014-12-31 | 甘肃蓝科石化高新装备股份有限公司 | A kind of oil gas water separator gas catches mist device |
| CN206027253U (en) * | 2016-07-22 | 2017-03-22 | 甘肃蓝科石化高新装备股份有限公司 | Whirl section plug flow trap |
-
2016
- 2016-07-22 CN CN201610582159.8A patent/CN106139746B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2332632B (en) * | 1997-12-18 | 2001-08-15 | Stephen Crocker | Separating material containing a gas component, a liquid hydrocarbon based component, a water based component, and a solid component |
| CN101146584A (en) * | 2005-02-23 | 2008-03-19 | Dps布里斯托尔（控股）有限公司 | Separator to separate a liquid/liquid/gas/solid mixture |
| CN1749634A (en) * | 2005-09-07 | 2006-03-22 | 胜利油田胜利工程设计咨询有限责任公司 | Plug flow trapper for oil/gas mixed transport section |
| CN201300015Y (en) * | 2008-11-14 | 2009-09-02 | 西安长庆科技工程有限责任公司 | Vertical mist extracting and separating device |
| CN204051245U (en) * | 2014-08-06 | 2014-12-31 | 甘肃蓝科石化高新装备股份有限公司 | A kind of oil gas water separator gas catches mist device |
| CN206027253U (en) * | 2016-07-22 | 2017-03-22 | 甘肃蓝科石化高新装备股份有限公司 | Whirl section plug flow trap |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106139746A (en) | 2016-11-23 |
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