CN109821275A - A kind of liquid-phase separation equipment - Google Patents
A kind of liquid-phase separation equipment Download PDFInfo
- Publication number
- CN109821275A CN109821275A CN201910244768.6A CN201910244768A CN109821275A CN 109821275 A CN109821275 A CN 109821275A CN 201910244768 A CN201910244768 A CN 201910244768A CN 109821275 A CN109821275 A CN 109821275A
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- Prior art keywords
- liquid
- shell
- phase separation
- outer tube
- phase
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- 239000007791 liquid phase Substances 0.000 title claims abstract description 50
- 238000005191 phase separation Methods 0.000 title claims abstract description 24
- 239000012530 fluid Substances 0.000 claims abstract description 13
- 230000000694 effects Effects 0.000 claims abstract description 11
- 239000012071 phase Substances 0.000 claims description 27
- 239000007788 liquid Substances 0.000 claims description 13
- 230000004888 barrier function Effects 0.000 claims description 6
- 239000010865 sewage Substances 0.000 claims description 6
- 238000007789 sealing Methods 0.000 claims description 3
- 230000035939 shock Effects 0.000 claims description 3
- 238000003466 welding Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000003628 erosive effect Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 230000007480 spreading Effects 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
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Abstract
The present invention provides a kind of liquid-phase separation equipment, the interior of shell of equipment is provided with inner and outer tubes, one end of inner tube is inserted into the highest point in outer tube and being lower than outer tube, and the other end stretches out to form leakage fluid dram in shell lower end；The lower part of outer tube is arranged to bell shape, and the inner wall of outer tube and shell is welded and fixed；Upper shell is provided with outlet tube, and outlet tube protrudes into the opening in shell close to the opening on outer tube top；Shell is provided with inlet, and longitudinal lip ring of multiple tracks interlaced arrangement is provided between inlet and outer tube.The invention can ensure that mutual exclusive liquid-phase separation effect, while can avoid causing layering to divide incomplete phenomenon not in time because the flow period increases suddenly.
Description
Technical field
The present invention relates to a kind of liquid phase separating devices, and in particular to a kind of liquid-phase separation equipment.
Background technique
In the practical operation of liquid-phase separation, mostly to stand based on split-phase, dynamic split-phase is prominent because spreading uneven or flow
So the reasons such as increase cause split-phase incomplete or split-phase failure.
When considering dynamic split-phase, considered according to liquid phase mixture homogeneity and split-phase effect, novel liquid-phase phase splitting device
It is imperative to research and develop, and the utility model liquid-phase separation equipment will be widely used in needing in all industries carrying out two-phase the demand of split-phase
In.
Summary of the invention
The present invention provides a kind of liquid-phase separation equipment, for solving the problems, such as mutual exclusive liquid-phase separation, by liquid phase
It is introduced into this equipment, the purpose of two-phase laminated flow is finally reached by internal structure.It is described that its technical solution is as follows:
A kind of liquid-phase separation equipment is provided with inner and outer tubes in the interior of shell of equipment, and one end of inner tube is inserted into outer
Highest point in pipe and lower than outer tube, the other end stretch out to form leakage fluid dram in shell lower end；The lower part of outer tube is arranged to horn mouth
The inner wall of shape, outer tube and shell is welded and fixed；Upper shell is provided with outlet tube, and the opening that outlet tube protrudes into shell is leaned on
The opening on nearly outer tube top；Shell is provided with inlet, and the vertical of multiple tracks interlaced arrangement is provided between inlet and outer tube
To lip ring.
The upper surface of shell is fixedly installed upper cover, and the gasket for sealing is provided between upper cover and shell.
It is provided with the lateral liquid barrier for protecting against shock effect at inlet, is able to extend the service life of longitudinal lip ring
With buffer phase charging rate.
Longitudinal lip ring plays the role of being uniformly distributed liquid phase in equipment according to amount of liquid phase combination settings 4-n group.
Upper cover is equipped with exhaust outlet, to drain gas in equipment.
Outlet tube protrudes into the end in shell and forms adapter tube, and the nozzle of adapter tube is upward.
Upper cover is provided with hand hole, and staff can adjust the height of nozzle of outlet tube by hand hole, and carry out part
Maintenance.
Observation panel is set on shell, to observe split-phase effect at any time.
Outer casing bottom is equipped with sewage draining exit, to drain liquid phase in equipment close to leakage fluid dram position.
Outer tube passes through reinforced bar support structure welding wall inside the shell.
The positive effect of the present invention is as follows:
1, the present invention has uniform immixture to feed liquor.
2, outer pipe bottom setting horn mouth has collection and guiding function to liquid phase.
3, it is set as liquid channel among inner and outer tubes, is designed and is realized by the height of inner and outer pipes, outlet tube, leakage fluid dram
Liquid-phase separation.
4, this equipment can realize dynamic split-phase.
The invention can ensure that mutual exclusive liquid-phase separation effect, while can avoid leading due to increasing suddenly the flow period
Cause layering point incomplete phenomenon not in time.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of liquid-phase separation equipment provided by the invention；
Fig. 2 is the top view of Fig. 1；
Fig. 3 is the side structure schematic diagram of Fig. 1；
In figure, 1- inner tube, 2- leakage fluid dram, 3- horn mouth, 4- outlet tube, 5- hand hole, 6- exhaust outlet, 7- transverse direction liquid barrier,
8- inlet, the longitudinal direction 9- lip ring, 10- observation panel, 11- upper cover, 12- gasket, 13- shell, 14- sewage draining exit, 15- outer tube,
16- adapter tube.
Specific embodiment
As shown in Figure 1-Figure 3, the present invention include inner tube 1, leakage fluid dram 2, horn mouth 3, outlet tube 4, hand hole 5, exhaust outlet 6,
Lateral liquid barrier 7, inlet 8, longitudinal lip ring 9, observation panel 10, upper cover 11, gasket 12, shell 13, sewage draining exit 14, outer tube
15。
Shell 13 is cuboid-type, and upper surface is fixedly installed upper cover 11, is provided with and is used between upper cover 11 and shell 13
The gasket 12 of sealing, guarantees the leakproofness of equipment.Upper cover 11, gasket 12, shell 13 are bolted to connection.
The right side of shell 13 is provided with inlet 8, and the lateral liquid barrier for protecting against shock effect is provided at inlet
7, it is able to extend the service life and buffer phase charging rate of longitudinal lip ring 9.
In shell 13, from inlet 8 to the direction of leakage fluid dram 2, liquid is blocked in the longitudinal direction for being disposed with multiple tracks interlaced arrangement
Plate 9, longitudinal lip ring 9 play the role of being uniformly distributed liquid phase in equipment according to amount of liquid phase combination settings 4-n group.It blocks longitudinal direction
The lower end of liquid plate 9 is connected with shell 13, and the height of upper end is not less than the opening on outer tube top.Adjacent longitudinal lip ring 9
It is formed with the serpentine channel advanced for liquid phase.
Inside 13 left side of shell of equipment, one end is provided with inner tube 1 and outer tube 15, and one end of inner tube 1 is inserted into outer tube
Highest point in 15 and lower than outer tube 15, the other end stretch out to form leakage fluid dram 2 in 13 lower end of shell；Inner tube 1 inside outer tube 15,
There is certain spacing to pass through between two pipes for liquid phase.
The lower part of outer tube 15 is shaped to horn mouth 3, and outer tube 15 is by reinforced bar support structure welding in shell 13
Inner wall.
13 upper end of shell is provided with outlet tube 4, and outlet tube protrudes into the opening in shell close to the opening on outer tube top；
Outlet tube 4 protrudes into the end in shell and forms adapter tube 16, and the nozzle of adapter tube 16 is upward.The opening of adapter tube 16 is higher than inner tube 1
Highest point, lower than the opening on outer tube top.
Liquid phase enters outer tube 15 by horn mouth 3 and carries out split-phase, and horn mouth 3 has receipts while playing the guiding role to liquid phase flow direction
Collection effect.
Inner tube 1 is connected with leakage fluid dram 2, and heavy phase (i.e. the larger substance of relative density) liquid phase is discharged via inner tube 1- leakage fluid dram 2.
Outlet tube 4 is identical as shell 13 and cabinet inner connecting tube upward, light phase (i.e. the smaller substance of relative density) liquid phase is via 4 row of outlet tube
Out.
In addition, observation panel is arranged on shell 13, to observe split-phase effect at any time.Upper cover 11 is equipped with exhaust outlet 6, to arrange
Gas in equipment to the greatest extent.Upper cover 11 is provided with hand hole, and staff can adjust the height of nozzle of outlet tube, Yi Jijin by hand hole
Row local overhauling.13 bottom of shell is equipped with sewage draining exit, to drain liquid phase in equipment close to leakage fluid dram position.Portion in equipment
Part is all fully welded by structure.
In the use of the present invention, liquid phase enters in equipment via inlet 8, lateral liquid barrier 7 plays protection against erosion and protection
The effect of longitudinal lip ring 9, liquid phase can uniformly mix reliable, the liquid for guaranteeing subsequent hierarchy under the action of longitudinal lip ring 9
Mutually finally flow at horn mouth 3.
With the raising of liquid level, liquid phase enters in inner tube 1 and the spacing of outer tube 15, liquid under the action of longitudinal lip ring 9
The upper lower leaf of weight two-phase liquid phase is mutually just realized in flow process, heavy phase is discharged by inner tube 1 by drain pipe 2, light phase
It is discharged by outlet tube 4, outlet tube 4 is equipped with adapter tube and nozzle upward to guarantee that heavy phase does not enter wherein inside equipment.
Observation panel 10 is used to observe the actual effect and liquid level of split-phase, and sewage draining exit 14 is for finally draining in equipment
Raffinate, exhaust outlet 6 is for emptying, and hand hole 5 is for local overhauling and adjustment 4 equipment inner tube open height of outlet tube, upper cover 11 and outer
Gasket 12 is equipped between shell 13.
The present invention realizes liquid-phase separation, it can be achieved that dynamic split-phase and liquid phase of the liquid phase in flow process are in standing process
In static split-phase.
The foregoing description of the disclosed embodiments enables those skilled in the art to implement or use the present invention.
Various modifications to these embodiments will be readily apparent to those skilled in the art, as defined herein
In the case that General Principle can not depart from the spirit or scope of the present invention, realize in other embodiments.Therefore, the present invention will
It will not be intended to be limited to the embodiments shown herein, but meet consistent with the principles and novel features disclosed in this article
Widest scope.
Claims (10)
1. a kind of liquid-phase separation equipment, it is characterised in that: the interior of shell of equipment is provided with inner and outer tubes, one end of inner tube
It is inserted into outer tube and is lower than the highest point of outer tube, the other end stretches out to form leakage fluid dram in shell lower end；The lower part of outer tube is arranged
At bell shape, the inner wall of outer tube and shell is welded and fixed；Upper shell is provided with outlet tube, and outlet tube protrudes into shell
Opening of the opening close to outer tube top；Shell is provided with inlet, and multiple tracks is provided between inlet and outer tube and is interlocked
Longitudinal lip ring of arrangement.
2. liquid-phase separation equipment according to claim 1, it is characterised in that: the upper surface of shell is fixedly installed upper cover,
The gasket for sealing is provided between upper cover and shell.
3. liquid-phase separation equipment according to claim 1, it is characterised in that: be provided at inlet and acted on for protecting against shock
Lateral liquid barrier, be able to extend the service life and buffer phase charging rate of longitudinal lip ring.
4. liquid-phase separation equipment according to claim 1, it is characterised in that: longitudinal lip ring is according to amount of liquid phase combination settings
4-n group plays the role of being uniformly distributed liquid phase in equipment.
5. liquid-phase separation equipment according to claim 2, it is characterised in that: upper cover is equipped with exhaust outlet, to drain equipment
Interior gas.
6. liquid-phase separation equipment according to claim 1, it is characterised in that: the end that outlet tube protrudes into shell forms and connects
Pipe, the nozzle of adapter tube is upward.
7. liquid-phase separation equipment according to claim 6, it is characterised in that: upper cover is provided with hand hole, and staff can
The height of nozzle of outlet tube is adjusted by hand hole, and carries out local overhauling.
8. liquid-phase separation equipment according to claim 1, it is characterised in that: observation panel is arranged on shell, to see at any time
Examine split-phase effect.
9. liquid-phase separation equipment according to claim 1, it is characterised in that: outer casing bottom is equipped with close to leakage fluid dram position
Sewage draining exit, to drain liquid phase in equipment.
10. liquid-phase separation equipment according to claim 1, it is characterised in that: outer tube is existed by reinforced bar support structure welding
Outer casing inner wall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910244768.6A CN109821275A (en) | 2019-03-28 | 2019-03-28 | A kind of liquid-phase separation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910244768.6A CN109821275A (en) | 2019-03-28 | 2019-03-28 | A kind of liquid-phase separation equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109821275A true CN109821275A (en) | 2019-05-31 |
Family
ID=66873212
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910244768.6A Pending CN109821275A (en) | 2019-03-28 | 2019-03-28 | A kind of liquid-phase separation equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109821275A (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0459444A1 (en) * | 1990-05-31 | 1991-12-04 | Santec Gmbh | Method and system for in situ decontamination of ground water mixed with hydrocarbons |
| CN202376804U (en) * | 2011-12-21 | 2012-08-15 | 常熟绣珀纤维有限公司 | Mixed liquid separation device special for production of ultra-high molecular weight polyethylene fiber by gel spinning |
| CN205340225U (en) * | 2015-12-29 | 2016-06-29 | 天津普莱化工技术有限公司 | Continuous phase splitting device of interface adjustable liquid |
| CN207163516U (en) * | 2017-08-29 | 2018-03-30 | 恒泰艾普（盘锦）企业发展有限公司 | Oil gas water test device and separation storage device |
| CN208465382U (en) * | 2018-06-01 | 2019-02-05 | 郑宗标 | Spiral-flow type beans slurrying trash separator |
| CN208465254U (en) * | 2018-05-25 | 2019-02-05 | 杨慧 | A kind of organic solvent recycling separator |
| CN209997241U (en) * | 2019-03-28 | 2020-01-31 | 奥星制药设备（石家庄）有限公司 | liquid phase separation equipment |
-
2019
- 2019-03-28 CN CN201910244768.6A patent/CN109821275A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0459444A1 (en) * | 1990-05-31 | 1991-12-04 | Santec Gmbh | Method and system for in situ decontamination of ground water mixed with hydrocarbons |
| CN202376804U (en) * | 2011-12-21 | 2012-08-15 | 常熟绣珀纤维有限公司 | Mixed liquid separation device special for production of ultra-high molecular weight polyethylene fiber by gel spinning |
| CN205340225U (en) * | 2015-12-29 | 2016-06-29 | 天津普莱化工技术有限公司 | Continuous phase splitting device of interface adjustable liquid |
| CN207163516U (en) * | 2017-08-29 | 2018-03-30 | 恒泰艾普（盘锦）企业发展有限公司 | Oil gas water test device and separation storage device |
| CN208465254U (en) * | 2018-05-25 | 2019-02-05 | 杨慧 | A kind of organic solvent recycling separator |
| CN208465382U (en) * | 2018-06-01 | 2019-02-05 | 郑宗标 | Spiral-flow type beans slurrying trash separator |
| CN209997241U (en) * | 2019-03-28 | 2020-01-31 | 奥星制药设备（石家庄）有限公司 | liquid phase separation equipment |
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