CN105999950B - A kind of high efficiency air liquid separation device - Google Patents
A kind of high efficiency air liquid separation device Download PDFInfo
- Publication number
- CN105999950B CN105999950B CN201610507581.7A CN201610507581A CN105999950B CN 105999950 B CN105999950 B CN 105999950B CN 201610507581 A CN201610507581 A CN 201610507581A CN 105999950 B CN105999950 B CN 105999950B
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- chamber
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- gas
- partition
- high efficiency
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0031—Degasification of liquids by filtration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0042—Degasification of liquids modifying the liquid flow
- B01D19/0052—Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused
- B01D19/0057—Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused the centrifugal movement being caused by a vortex, e.g. using a cyclone, or by a tangential inlet
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separating Particles In Gases By Inertia (AREA)
Abstract
The invention discloses a kind of high efficiency air liquid separation devices,Including cylinder,Escape pipe,Outlet tube,Gas-liquid ingress pipe,First partition,Second partition,Third partition board,First chamber,Second chamber,Third chamber and the 4th chamber,The cylinder upper end is equipped with escape pipe,The cylinder lower end is equipped with outlet tube,Gas-liquid ingress pipe is equipped at left and right sides of the cylinder,The inner barrel is equipped with first partition successively from the bottom up,Second partition and third partition board,The first partition,Cylinder is divided into four chambers by second partition and third partition board,It is first chamber successively from the bottom up,Second chamber,Third chamber and the 4th chamber,The high efficiency air liquid separation device is detached using secondary centrifuging,Filler detaches,Gas-liquid separation mode in silk screen separation and micro porous filtration separation four,Efficiently gas-liquid can be collaborated to detach,Solves the problems, such as the single and low separation efficiency of conventional separators methods and structure.
Description
Technical field
The present invention relates to gas-liquid separator field, specially a kind of high efficiency air liquid separation device.
Background technology
Gas-liquid separation is a kind of basic chemical process of petroleum chemical industry, and meaning is also extremely important, existing at present
Or gas-liquid separator it is complicated, expensive or methods and structure are single, and separative efficiency is low, in consideration of it,
It is proposed that a kind of high efficiency air liquid separation device.
Invention content
The purpose of the present invention is to provide a kind of high efficiency air liquid separation devices, to solve mentioned above in the background art ask
Topic.
To achieve the above object, the present invention provides the following technical solutions：A kind of high efficiency air liquid separation device, including cylinder,
Escape pipe, outlet tube, gas-liquid ingress pipe, first partition, second partition, third partition board, first chamber, second chamber, third chamber
Room and the 4th chamber, the cylinder upper end are equipped with escape pipe, and the cylinder lower end is equipped with outlet tube, is set at left and right sides of the cylinder
There is gas-liquid ingress pipe, is equipped with the first filter screen in the gas-liquid ingress pipe, the gas-liquid ingress pipe is passed through inside second chamber, institute
State inner barrel from the bottom up successively be equipped with first partition, second partition and third partition board, the first partition, second partition and
Cylinder is divided into four chambers by third partition board, is first chamber, second chamber, third chamber and the 4th chamber successively from the bottom up
Room；
It is equipped with drain pipe in the first chamber, is passed through inside second chamber for one section above the drain pipe, described first
Demister is equipped among chamber, the demister is located at the top of drain pipe end port；
Motor is installed, the motor is fixed in first partition, is equipped with and is protected around the motor in the second chamber
Sheath, the motor are fixedly connected by output shaft with rotating cylinder, and the rotating cylinder side inner walls are equipped with packing layer, the rotating cylinder side
Several through-holes are provided with, gas-guide tube, the gas-guide tube connection second chamber and the indoor rotation point of third chamber are equipped with above the rotating cylinder
Tin, centre position is equipped with spray tube in the second chamber, and the spray tube upper end is connected to gas-liquid ingress pipe, the spray tube
Centre is equipped with high-pressure pump, is located inside rotating cylinder for one section below the spray tube, and positioned at one section inside rotating cylinder equipped with several
Spray head；
Rotation is installed in the third chamber and divides cylinder, the rotation divides cylinder to be fixed on third partition board, on the third partition board
Several circular holes are provided with, the rotation divides cylinder inner upper to be equipped with motor, is equipped with protective layer around the motor, the motor passes through
Output shaft is fixedly connected with rotation leaflet, and the rotation divides cylinder side to be provided with several through-holes, and the rotation divides cylinder lower end to be connected to gas-guide tube,
The third chamber and second partition junction are provided with two leakage fluid drams in left and right, be equipped at the leakage fluid dram connection third chamber and
The return duct of second chamber, the return duct are connected with drain pipe side；
Centre position is equipped with microporous filter screen in 4th chamber, and the 4th chamber and third partition board junction are provided with
Two leakage fluid drams are controlled, the return duct of the 4th chamber and second chamber of connection is equipped at the leakage fluid dram.
Preferably, the microporous filter screen is in inverted V-shaped, convenient for flowing down under the effect of gravity along V-arrangement after liquid condensation.
Preferably, the demister is in inverted V-shaped, convenient for flowing down under the effect of gravity along V-arrangement after liquid condensation.
Preferably, described filler layer thickness is 20mm to 50mm, is in dense mesh structure.
Preferably, the spray head is radially distributed on spray tube.
Preferably, the gas-guide tube is radially arranged at least provided with two, and around body centre axis.
Preferably, the rotation is divided to cylinder and its internal component at least provided with two groups, each rotation divide cylinder and gas-guide tube one by one
Corresponding connection.
Preferably, the drain pipe is at least provided with two, and is passed through one section of drain pipe side and reflux inside second chamber
Pipe is connected, and the other side is close to rotating cylinder lower outer surface.
Compared with prior art, the beneficial effects of the invention are as follows：Gas-liquid interflow is imported from gas-liquid ingress pipe, through the first filtering
The preliminary filtering of net, may filter that some bulky grain drops and some sundries, then imports spray tube, from spray after high-pressure pump pressurizes
Head atomization sprays, and into high-speed rotating rotating cylinder, under the influence of centrifugal force, gas-liquid interflow enters packing layer, three-dimensional netted to fill out
The bed of material can make the blocking of liquid collect wall area increase, and liquid is through multiple baffling repeatedly, finally under centrifugal force and gravity
It is thrown out of wall and imports drain pipe and enter first chamber, gas, which is then hampered, to be kept off baffling and walk, and into gas-guide tube, and rises to rotation
Cylinder, rotation leaflet rotation is divided to generate centrifugal force, be centrifuged again, wherein liquid is thrown out of wall and enters return line flow
To first chamber, gas enters the 4th chamber through the circular hole on third partition board, the microporous filter screen of the 4th chamber to it again
Secondary filter, liquid are filtered and enter return line flow to first chamber, and gas is discharged from escape pipe, into the residual of first chamber
Stay gas-liquid interflow be separated by filtration through demister, liquid flow down, from outlet tube be discharged, the high efficiency air liquid separation device using it is secondary from
Gas-liquid separation mode in heart separation, filler separation, silk screen separation and micro porous filtration separation four, can be efficiently by gas-liquid interflow point
From solving the problems, such as the single and low separation efficiency of conventional separators methods and structure.
Description of the drawings
Fig. 1 is schematic structural view of the invention；
Fig. 2 is third chamber vertical view.
In figure：Cylinder 1, escape pipe 2, outlet tube 3, gas-liquid ingress pipe 4, the first filter screen 5, first partition 6, second partition
7, third partition board 8, first chamber 9, second chamber 10, third chamber 11, the 4th chamber 12, return duct 13, circular hole 14, drain pipe
15, demister 16, spray tube 17, spray head 18, high-pressure pump 19, motor 20, output shaft 21, rotating cylinder 22, protective layer 23, through-hole
24, packing layer 25, gas-guide tube 26, rotation divide cylinder 27, rotation leaflet 28, microporous filter screen 29 and leakage fluid dram 30.
Specific implementation mode
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation describes, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
- 2 are please referred to Fig.1, the present invention provides a kind of technical solution：A kind of high efficiency air liquid separation device, including cylinder 1, go out
Tracheae 2, outlet tube 3, gas-liquid ingress pipe 4, first partition 6, second partition 7, third partition board 8, first chamber 9, second chamber 10,
Third chamber 11 and the 4th chamber 12,1 upper end of cylinder are equipped with escape pipe 2, and 1 lower end of cylinder is equipped with outlet tube 3, cylinder 1 or so two
Side is equipped with gas-liquid ingress pipe 4, and the first filter screen 5 is equipped in gas-liquid ingress pipe 4, and gas-liquid ingress pipe 4 is passed through inside second chamber 10,
It is equipped with first partition 6, second partition 7 and third partition board 8, first partition 6,7 and of second partition inside cylinder 1 successively from the bottom up
Third partition board 8 divides cylinder 1 for four chambers, is first chamber 9, second chamber 10,11 and of third chamber successively from the bottom up
4th chamber 12；
Drain pipe 15 is equipped in first chamber 9,15 one section of top of drain pipe is passed through inside second chamber 10, drain pipe 15 to
It there are two setting less, and is passed through 10 one section of 15 side of drain pipe in inside of second chamber and is connected with return duct 13, the other side is close to be turned
22 lower outer surfaces of cylinder, 9 centre of first chamber are equipped with demister 16, and demister 16 is in inverted V-shaped, is convenient for after liquid condensation in gravity
It flows down along V-arrangement under effect, demister 16 is located at the top of 15 end port of drain pipe；
Motor 20 is installed, motor 20 is fixed in first partition 6, and protective layer is equipped with around motor 20 in second chamber 10
23, motor 20 is fixedly connected by output shaft 21 with rotating cylinder 22, and 22 side inner walls of rotating cylinder are equipped with packing layer 25,25 thickness of packing layer
It is in dense mesh structure for 20mm to 50mm, 22 side of rotating cylinder is provided with several through-holes 24, and 22 top of rotating cylinder is equipped with gas-guide tube 26,
Gas-guide tube 26 is radially arranged at least provided with two, and around 1 central axis of cylinder, and gas-guide tube 26 is connected to 10 He of second chamber
Rotation in third chamber 11 divides cylinder 27, and centre position is equipped with spray tube 17 in second chamber 10, and 17 upper end of spray tube is led with gas-liquid
Enter the connection of pipe 4, high-pressure pump 19 is installed, one section of 17 lower section of spray tube is located inside rotating cylinder 22, and is located at and turns among spray tube 17
One section of 22 inside of cylinder is equipped with several spray heads 18, and spray head 18 is radially distributed on spray tube 17；
Rotation is installed in third chamber 11 and divides cylinder 27, rotation is divided to cylinder 27 and its internal component at least provided with two groups, Mei Gexuan
Cylinder 27 is divided to be connected to the one-to-one correspondence of gas-guide tube 26, rotation divides cylinder 27 to be fixed on third partition board 8, is provided on third partition board 8 several
Circular hole 14, rotation divide 27 inner upper of cylinder to be equipped with motor 20, are equipped with protective layer 23 around motor 20, motor 20 passes through output shaft 21
It is fixedly connected with rotation leaflet 28, rotation divides 27 side of cylinder to be provided with several through-holes 24, and rotation divides 27 lower end of cylinder to be connected to gas-guide tube 26, third
Chamber 11 and 7 junction of second partition are provided with two leakage fluid drams 30 in left and right, and connection third chamber 11 and the are equipped at leakage fluid dram 30
The return duct 13 of two chambers 10, return duct 13 are connected with 15 side of drain pipe；
Centre position is equipped with microporous filter screen 29 in 4th chamber 12, and microporous filter screen 29 is in inverted V-shaped, is convenient for liquid condensation
It flows down under the effect of gravity along V-arrangement afterwards, the 4th chamber 12 and 8 junction of third partition board are provided with two leakage fluid drams 30 in left and right, drain
The return duct 13 of connection the 4th chamber 12 and second chamber 10 is equipped at mouth 30.
Operation principle：Gas-liquid interflow is imported from gas-liquid ingress pipe 4, through the first tentatively filtering of filter screen 5, may filter that some are big
Particle droplet and some sundries then import spray tube 17, are atomized and spray from spray head 18 after the pressurization of high-pressure pump 19, into height
The rotating cylinder 22 of speed rotation, under the influence of centrifugal force, gas-liquid interflow enter packing layer 25, and three-dimensional netted packing layer can make liquid
Blocking is collected wall area and is increased, and liquid is finally thrown out of wall and is converged under centrifugal force and gravity through multiple baffling repeatedly
Enter drain pipe 15 and enter first chamber 9, gas, which is then hampered, to be kept off baffling and walk, and into gas-guide tube 26, and is risen to rotation and is divided cylinder 27, revolves
The rotation of leaflet 28 generates centrifugal force, is centrifuged again, and wherein liquid is thrown out of wall and enters return duct 13 and flows to
First chamber 9, gas enter the 4th chamber 12, the microporous filter screen 29 of the 4th chamber 12 through the circular hole 14 on third partition board 8
To its secondary filter again, liquid is filtered and flows to first chamber 9 into return duct 13, and gas is discharged from escape pipe 2, enters
The residual gas-liquid interflow of first chamber 9 is separated by filtration through demister 16, and liquid flows down, and is discharged from outlet tube 3.
It although an embodiment of the present invention has been shown and described, for the ordinary skill in the art, can be with
Understanding without departing from the principles and spirit of the present invention can carry out these embodiments a variety of variations, modification, replace
And modification, the scope of the present invention is defined by the appended.
Claims (8)
1. a kind of high efficiency air liquid separation device, including cylinder（1）, escape pipe（2）, outlet tube（3）, gas-liquid ingress pipe（4）, first
Partition board（6）, second partition（7）, third partition board（8）, first chamber（9）, second chamber（10）, third chamber（11）With the 4th chamber
Room（12）, it is characterised in that：The cylinder（1）Upper end is equipped with escape pipe（2）, the cylinder（1）Lower end is equipped with outlet tube（3）,
The cylinder（1）The left and right sides is equipped with gas-liquid ingress pipe（4）, the gas-liquid ingress pipe（4）Inside it is equipped with the first filter screen（5）, institute
State gas-liquid ingress pipe（4）It is passed through second chamber（10）Inside, the cylinder（1）It is internal to be equipped with first partition successively from the bottom up
（6）, second partition（7）With third partition board（8）, the first partition（6）, second partition（7）With third partition board（8）By cylinder
（1）It is divided into four chambers, is first chamber successively from the bottom up（9）, second chamber（10）, third chamber（11）With the 4th chamber
（12）；
The first chamber（9）It is interior to be equipped with drain pipe（15）, the drain pipe（15）One section of top is passed through second chamber（10）It is interior
Portion, the first chamber（9）Centre is equipped with demister（16）, the demister（16）Positioned at drain pipe（15）End port it is upper
Side；
The second chamber（10）Motor is inside installed（20）, the motor（20）It is fixed on first partition（6）On, the motor
（20）Surrounding is equipped with protective layer（23）, the motor（20）Pass through output shaft（21）And rotating cylinder（22）It is fixedly connected, the rotating cylinder
（22）Side inner walls are equipped with packing layer（25）, the rotating cylinder（22）Side is provided with several through-holes（24）, the rotating cylinder（22）Top
Equipped with gas-guide tube（26）, the gas-guide tube（26）It is connected to second chamber（10）With third chamber（11）Interior rotation divides cylinder（27）, institute
State second chamber（10）Interior centre position is equipped with spray tube（17）, the spray tube（17）Upper end and gas-liquid ingress pipe（4）Connection,
The spray tube（17）Centre is equipped with high-pressure pump（19）, the spray tube（17）One section of lower section is located at rotating cylinder（22）Inside, and
Positioned at rotating cylinder（22）Internal one section is equipped with several spray heads（18）；
The third chamber（11）Rotation is inside installed and divides cylinder（27）, the rotation divides cylinder（27）It is fixed on third partition board（8）On, it is described
Third partition board（8）On be provided with several circular holes（14）, the rotation divides cylinder（27）Inner upper is equipped with motor（20）, the motor
（20）Surrounding is equipped with protective layer（23）, the motor（20）Pass through output shaft（21）It is fixedly connected with rotation leaflet（28）, the rotation
Divide cylinder（27）Side is provided with several through-holes（24）, the rotation divides cylinder（27）Lower end and gas-guide tube（26）Connection, the third chamber
（11）And second partition（7）Junction is provided with two leakage fluid drams in left and right（30）, the leakage fluid dram（30）Place is equipped with connection third chamber
Room（11）And second chamber（10）Return duct（13）, the return duct（13）And drain pipe（15）Side is connected；
4th chamber（12）Interior centre position is equipped with microporous filter screen（29）, the 4th chamber（12）With third partition board
（8）Junction is provided with two leakage fluid drams in left and right（30）, the leakage fluid dram（30）Place is equipped with the 4th chamber of connection（12）With the second chamber
Room（10）Return duct（13）.
2. a kind of high efficiency air liquid separation device according to claim 1, it is characterised in that：The microporous filter screen（29）It is in
Inverted V-shaped, convenient for flowing down under the effect of gravity along V-arrangement after liquid condensation.
3. a kind of high efficiency air liquid separation device according to claim 1, it is characterised in that：The demister（16）In V
Shape, convenient for flowing down under the effect of gravity along V-arrangement after liquid condensation.
4. a kind of high efficiency air liquid separation device according to claim 1, it is characterised in that：Described filler layer（25）Thickness is
20mm to 50mm is in dense mesh structure.
5. a kind of high efficiency air liquid separation device according to claim 1, it is characterised in that：The spray head（18）It is spraying
Pipe（17）On be radially distributed.
6. a kind of high efficiency air liquid separation device according to claim 1, it is characterised in that：The gas-guide tube（26）At least set
There are two, and surround cylinder（1）Central axis radially arranges.
7. a kind of high efficiency air liquid separation device according to claim 1, it is characterised in that：The rotation divides cylinder（27）And its it is interior
For portion's component at least provided with two groups, each rotation divides cylinder（27）Equal and gas-guide tube（26）Correspond connection.
8. a kind of high efficiency air liquid separation device according to claim 1, it is characterised in that：The drain pipe（15）At least set
There are two, and it is passed through second chamber（10）Internal one section of drain pipe（15）Side and return duct（13）It is connected, the other side is close
Rotating cylinder（22）Lower outer surface.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610507581.7A CN105999950B (en) | 2016-06-30 | 2016-06-30 | A kind of high efficiency air liquid separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610507581.7A CN105999950B (en) | 2016-06-30 | 2016-06-30 | A kind of high efficiency air liquid separation device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105999950A CN105999950A (en) | 2016-10-12 |
| CN105999950B true CN105999950B (en) | 2018-11-06 |
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ID=57104890
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610507581.7A Active CN105999950B (en) | 2016-06-30 | 2016-06-30 | A kind of high efficiency air liquid separation device |
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| Country | Link |
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| CN (1) | CN105999950B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106635741A (en) * | 2016-12-01 | 2017-05-10 | 沈奇光 | Fermentation tank overflow collecting, separating and recycling device |
| CN109731380A (en) * | 2019-01-30 | 2019-05-10 | 深圳市芭田生态工程股份有限公司 | A kind of slurry filtering device, slurry filtration method |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2004110638A1 (en) * | 2003-06-16 | 2004-12-23 | Bunri Incorporation | Cyclonic foreign object separator separating foreign objects by centrifugal force |
| CN203648334U (en) * | 2014-01-16 | 2014-06-18 | 中国矿业大学 | Circulating gas-liquid separation device |
| CN103977665A (en) * | 2014-05-30 | 2014-08-13 | 攀钢集团西昌钢钒有限公司 | Gas-liquid separator |
| CN204261525U (en) * | 2014-11-21 | 2015-04-15 | 张智豪 | Combined type gas-liquid separator |
| CN205988643U (en) * | 2016-06-30 | 2017-03-01 | 泉州市知产茂业工业设计有限公司 | A kind of efficient gas-liquid separator |
-
2016
- 2016-06-30 CN CN201610507581.7A patent/CN105999950B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2004110638A1 (en) * | 2003-06-16 | 2004-12-23 | Bunri Incorporation | Cyclonic foreign object separator separating foreign objects by centrifugal force |
| CN203648334U (en) * | 2014-01-16 | 2014-06-18 | 中国矿业大学 | Circulating gas-liquid separation device |
| CN103977665A (en) * | 2014-05-30 | 2014-08-13 | 攀钢集团西昌钢钒有限公司 | Gas-liquid separator |
| CN204261525U (en) * | 2014-11-21 | 2015-04-15 | 张智豪 | Combined type gas-liquid separator |
| CN205988643U (en) * | 2016-06-30 | 2017-03-01 | 泉州市知产茂业工业设计有限公司 | A kind of efficient gas-liquid separator |
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| CN105999950A (en) | 2016-10-12 |
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Effective date of registration: 20190214 Address after: 257000 No. 120, Xierlu, Dongying District, Dongying City, Shandong Province Patentee after: Shengli Oilfield Wuhua Petroleum Equipment Manufacturing Co., Ltd. Address before: 362201 Block C 202, Huayuan New Village Commercial Building, Meiling Street, Jinjiang City, Quanzhou City, Fujian Province Patentee before: Quanzhou Industrial Co., Ltd. |