CN105999950A - Novel high-efficiency gas-liquid separating device - Google Patents
Novel high-efficiency gas-liquid separating device Download PDFInfo
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- CN105999950A CN105999950A CN201610507581.7A CN201610507581A CN105999950A CN 105999950 A CN105999950 A CN 105999950A CN 201610507581 A CN201610507581 A CN 201610507581A CN 105999950 A CN105999950 A CN 105999950A
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- dividing plate
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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 novel high-efficiency gas-liquid separating device. The novel high-efficiency gas-liquid separating device comprises a cylinder, a gas outlet pipe, a liquid outlet pipe, gas-liquid leading-in pipes, a first partition plate, a second partition plate, a third partition plate, a first chamber, a second chamber, a third chamber and a fourth chamber; the gas outlet pipe is arranged at the upper end of the cylinder; the liquid outlet pipe is arranged at the lower end of the cylinder; the gas-liquid leading-in pipes are arranged on the left side and the right side of the cylinder; the first partition plate, the second partition plate and the third partition plate are arranged in the cylinder in sequence from the bottom to the top; the cylinder is divided into four chambers, namely, the first chamber, the second chamber, the third chamber and the fourth chamber, in sequence from the bottom to the top, by the first partition plate, the second partition plate and the third partition plate. According to the novel high-efficiency gas-liquid separating device, four gas-liquid separation modes, namely, secondary centrifugal separation, packing separation, screen mesh separation and micro-porous filtration separation, are adopted, so that gas-liquid confluence can be separated effectively, and the problems that the conventional separator is single in mode, method and structure, and low in separating efficiency are solved.
Description
Technical field
The present invention relates to gas-liquid separator field, be specially a kind of efficient gas-liquid separator.
Background technology
Gas-liquid separation is a kind of basic chemical process of petroleum chemical industry, and its meaning is the most extremely important, current existing gas-liquid separator or structure complexity, cost intensive, otherwise methods and structure single, separation efficiency is low, in consideration of it, it is proposed that a kind of efficient gas-liquid separator.
Summary of the invention
It is an object of the invention to provide a kind of efficient gas-liquid separator, with the problem solving to propose in above-mentioned background technology.
For achieving the above object, the present invention provides following technical scheme: a kind of efficient gas-liquid separator, including cylinder, escape pipe, drain pipe, gas-liquid ingress pipe, first dividing plate, second partition, 3rd dividing plate, first chamber, second chamber, 3rd chamber and the 4th chamber, described cylinder upper end is provided with escape pipe, described cylinder lower end is provided with drain pipe, the described cylinder left and right sides is provided with gas-liquid ingress pipe, it is provided with the first drainage screen in described gas-liquid ingress pipe, described gas-liquid ingress pipe is passed through the second chamber interior, described inner barrel is sequentially provided with the first dividing plate from the bottom up, second partition and the 3rd dividing plate, described first dividing plate, cylinder is divided into four chambers by second partition and the 3rd dividing plate, it is the first chamber the most successively, second chamber, 3rd chamber and the 4th chamber；
Being provided with discharging tube in described first chamber, above described discharging tube, one section is passed through the second chamber interior, is provided with demister in the middle of described first chamber, and described demister is positioned at the top of discharging tube end port；
In described second chamber, motor is installed, described motor is fixed on the first dividing plate, described motor is provided around protective layer, described motor connects by output shaft and rotating cylinder are fixing, described rotating cylinder side inner walls is provided with packing layer, described rotating cylinder side has some through holes, described rotating cylinder is arranged over airway, the rotation that described airway connects in the second chamber and the 3rd chamber divides cylinder, in described second chamber, centre position is provided with shower, described shower upper end connects with gas-liquid ingress pipe, in the middle of described shower, high-pressure pump is installed, below described shower, one section is positioned at inside rotating cylinder, and be positioned at internal one section of rotating cylinder and be provided with some spray heads；
Rotation point cylinder is installed in described 3rd chamber, described rotation divides cylinder to be fixed on the 3rd dividing plate, some circular holes are had on described 3rd dividing plate, described rotation divides an inner upper to be provided with motor, described motor is provided around protective layer, described motor is fixedly connected with rotation leaflet by output shaft, described rotation divides a side to have some through holes, described rotation divides a lower end to connect with airway, described 3rd chamber and second partition junction have two leakage fluid drams in left and right, the 3rd chamber and the return duct of the second chamber it is communicated with at described leakage fluid dram, described return duct is connected with discharging tube side；
In described 4th chamber, centre position is provided with microporous filter screen, and described 4th chamber and the 3rd dividing plate junction have two leakage fluid drams in left and right, are communicated with the 4th chamber and the return duct of the second chamber at described leakage fluid dram.
Preferably, described microporous filter screen is inverted V-shaped, it is simple to prolong V-arrangement after liquid condensation under gravity dirty.
Preferably, described demister is inverted V-shaped, it is simple to prolong V-arrangement after liquid condensation under gravity dirty.
Preferably, described packing layer thickness is 20mm to 50mm, in dense mesh structure.
Preferably, described spray head is distributed on shower radially.
Preferably, described airway is at least provided with two, and arranges radially around body centre axis.
Preferably, described rotation divides cylinder and internals thereof all at least provided with two groups, and each rotation divides cylinder all to connect with airway one_to_one corresponding.
Preferably, described discharging tube is at least provided with two, and is passed through one section of discharging tube side of the second chamber interior and is connected with return duct, and opposite side is near rotating cylinder lower outer surface.
nullCompared with prior art，The invention has the beneficial effects as follows: gas-liquid interflow imports from gas-liquid ingress pipe，Tentatively filter through the first drainage screen，May filter that some bulky grain drops and some foreign material，Import shower subsequently，From spray head atomization ejection after high-pressure pump pressurizes，Enter the rotating cylinder of high speed rotating，Under the influence of centrifugal force，Gas-liquid interflow enters packing layer，Three-dimensional netted packing layer can make the stop of liquid collect wall area increase，Liquid is through baffling the most repeatedly，Final under centrifugal force and action of gravity, it be thrown out of wall and import discharging tube and enter the first chamber，Gas is then hampered and keeps off baffling and walk，Enter airway，And rise to rotation point cylinder，Rotation leaflet rotates and produces centrifugal force，It is centrifuged again separating，Wherein liquid is thrown out of wall and enters return line flow to the first chamber，Circular hole on gas permeation the 3rd dividing plate enters the 4th chamber，The microporous filter screen of the 4th chamber is to its secondary filter again，Liquid is filtered and is entered return line flow to the first chamber，Gas is discharged from escape pipe，Separation is filtered through demister in the residual gas-liquid interflow entering the first chamber，Liquid is dirty，Discharge from drain pipe，This efficient gas-liquid separator uses secondary centrifuging to separate、Filler separates、Silk screen separates and microporous filter separates gas-liquid separation mode in four，Efficiently gas-liquid interflow can be separated，Solve the single and separation efficiency of conventional separators methods and structure low problem.
Accompanying drawing explanation
Fig. 1 is present configuration schematic diagram；
Fig. 2 is the 3rd chamber top view.
In figure: cylinder 1, escape pipe 2, drain pipe 3, gas-liquid ingress pipe 4, first drainage screen 5, first dividing plate 6, second partition 7, 3rd dividing plate 8, first chamber 9, second chamber 10, 3rd chamber 11, 4th chamber 12, return duct 13, circular hole 14, discharging tube 15, demister 16, shower 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, airway 26, rotation point cylinder 27, rotation leaflet 28, microporous filter screen 29 and leakage fluid dram 30.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is clearly and completely described, it is clear that described embodiment is only a part of embodiment of the present invention rather than whole embodiments.Based on the embodiment in the present invention, the every other embodiment that those of ordinary skill in the art are obtained under not making creative work premise, broadly fall into the scope of protection of the invention.
nullRefer to Fig. 1-2，The present invention provides a kind of technical scheme: a kind of efficient gas-liquid separator，Including cylinder 1、Escape pipe 2、Drain pipe 3、Gas-liquid ingress pipe 4、First dividing plate 6、Second partition 7、3rd dividing plate 8、First chamber 9、Second chamber 10、3rd chamber 11 and the 4th chamber 12，Cylinder 1 upper end is provided with escape pipe 2，Cylinder 1 lower end is provided with drain pipe 3，Cylinder 1 left and right sides is provided with gas-liquid ingress pipe 4，The first drainage screen 5 it is provided with in gas-liquid ingress pipe 4，It is internal that gas-liquid ingress pipe 4 is passed through the second chamber 10，Cylinder 1 is internal is sequentially provided with the first dividing plate 6 from the bottom up、Second partition 7 and the 3rd dividing plate 8，First dividing plate 6、Cylinder 1 is divided into four chambers by second partition 7 and the 3rd dividing plate 8，It is the first chamber 9 the most successively、Second chamber 10、3rd chamber 11 and the 4th chamber 12；
It is provided with discharging tube 15 in first chamber 9, above discharging tube 15, one section is passed through the second chamber 10 inside, discharging tube 15 is at least provided with two, and be passed through the second internal one section of discharging tube 15 side of chamber 10 and be connected with return duct 13, opposite side is provided with demister 16 in the middle of rotating cylinder 22 lower outer surface, the first chamber 9, and demister 16 is in inverted V-shaped, prolonging V-arrangement after being easy to liquid condensation under gravity dirty, demister 16 is positioned at the top of discharging tube 15 end port；
nullIn second chamber 10, motor 20 is installed，Motor 20 is fixed on the first dividing plate 6，Motor 20 is provided around protective layer 23，Motor 20 is by output shaft 21 and the fixing connection of rotating cylinder 22，Rotating cylinder 22 side inner walls is provided with packing layer 25，Packing layer 25 thickness is 20mm to 50mm，In dense mesh structure，Rotating cylinder 22 side has some through holes 24，Rotating cylinder 22 is arranged over airway 26，Airway 26 is at least provided with two，And arrange radially around cylinder 1 central axis，The rotation that airway 26 connects in the second chamber 10 and the 3rd chamber 11 divides cylinder 27，In second chamber 10, centre position is provided with shower 17，Shower 17 upper end connects with gas-liquid ingress pipe 4，In the middle of shower 17, high-pressure pump 19 is installed，Below shower 17, one section is positioned at rotating cylinder 22 inside，And be positioned at internal one section of rotating cylinder 22 and be provided with some spray heads 18，Spray head 18 is distributed on shower 17 radially；
Rotation point cylinder 27 is installed in the 3rd chamber 11, rotation point cylinder 27 and internals thereof are all at least provided with two groups, each rotation divides cylinder 27 all to connect with airway 26 one_to_one corresponding, rotation point cylinder 27 is fixed on the 3rd dividing plate 8, some circular holes 14 are had on 3rd dividing plate 8, rotation point cylinder 27 inner upper is provided with motor 20, motor 20 is provided around protective layer 23, motor 20 is fixedly connected with rotation leaflet 28 by output shaft 21, rotation point cylinder 27 side has some through holes 24, rotation point cylinder 27 lower end connects with airway 26, 3rd chamber 11 and second partition 7 junction have two leakage fluid drams 30 in left and right, the 3rd chamber 11 and the return duct 13 of the second chamber 10 it is communicated with at leakage fluid dram 30, return duct 13 is connected with discharging tube 15 side；
In 4th chamber 12, centre position is provided with microporous filter screen 29, microporous filter screen 29 is in inverted V-shaped, V-arrangement is prolonged under gravity dirty after being easy to liquid condensation, 4th chamber 12 and the 3rd dividing plate 8 junction have two leakage fluid drams 30 in left and right, are communicated with the 4th chamber 12 and the return duct 13 of the second chamber 10 at leakage fluid dram 30.
nullOperation principle: gas-liquid interflow imports from gas-liquid ingress pipe 4，Tentatively filter through the first drainage screen 5，May filter that some bulky grain drops and some foreign material，Import shower 17 subsequently，From spray head 18 atomization ejection after high-pressure pump 19 pressurizes，Enter the rotating cylinder 22 of high speed rotating，Under the influence of centrifugal force，Gas-liquid interflow enters packing layer 25，Three-dimensional netted packing layer can make the stop of liquid collect wall area increase，Liquid is through baffling the most repeatedly，Final under centrifugal force and action of gravity, it be thrown out of wall and import discharging tube 15 and enter the first chamber 9，Gas is then hampered and keeps off baffling and walk，Enter airway 26，And rise to rotation point cylinder 27，Rotation leaflet 28 rotates and produces centrifugal force，It is centrifuged again separating，Wherein liquid is thrown out of wall and enters return duct 13 and flow to the first chamber 9，Circular hole 14 on gas permeation the 3rd dividing plate 8 enters the 4th chamber 12，The microporous filter screen 29 of the 4th chamber 12 is to its secondary filter again，Liquid is filtered and is entered return duct 13 and flowed to the first chamber 9，Gas is discharged from escape pipe 2，Separation is filtered through demister 16 in the residual gas-liquid interflow entering the first chamber 9，Liquid is dirty，Discharge from drain pipe 3.
Although an embodiment of the present invention has been shown and described, for the ordinary skill in the art, being appreciated that and these embodiments can carry out multiple change without departing from the principles and spirit of the present invention, revise, replace and modification, the scope of the present invention be defined by the appended.
Claims (8)
- null1. an efficient gas-liquid separator，Including cylinder (1)、Escape pipe (2)、Drain pipe (3)、Gas-liquid ingress pipe (4)、First dividing plate (6)、Second partition (7)、3rd dividing plate (8)、First chamber (9)、Second chamber (10)、3rd chamber (11) and the 4th chamber (12)，It is characterized in that: described cylinder (1) upper end is provided with escape pipe (2)，Described cylinder (1) lower end is provided with drain pipe (3)，Described cylinder (1) left and right sides is provided with gas-liquid ingress pipe (4)，It is provided with the first drainage screen (5) in described gas-liquid ingress pipe (4)，It is internal that described gas-liquid ingress pipe (4) is passed through the second chamber (10)，Described cylinder (1) is internal is sequentially provided with the first dividing plate (6) from the bottom up、Second partition (7) and the 3rd dividing plate (8)，Described first dividing plate (6)、Cylinder (1) is divided into four chambers by second partition (7) and the 3rd dividing plate (8)，It is the first chamber (9) the most successively、Second chamber (10)、3rd chamber (11) and the 4th chamber (12)；It is provided with discharging tube (15) in described first chamber (9), it is internal that one section, described discharging tube (15) top is passed through the second chamber (10), being provided with demister (16) in the middle of described first chamber (9), described demister (16) is positioned at the top of discharging tube (15) end port；nullIn described second chamber (10), motor (20) is installed，Described motor (20) is fixed on the first dividing plate (6)，Described motor (20) is provided around protective layer (23)，Described motor (20) connects by output shaft (21) and rotating cylinder (22) are fixing，Described rotating cylinder (22) side inner walls is provided with packing layer (25)，Described rotating cylinder (22) side has some through holes (24)，Described rotating cylinder (22) is arranged over airway (26)，The rotation that described airway (26) connects in the second chamber (10) and the 3rd chamber (11) divides cylinder (27)，The interior centre position of described second chamber (10) is provided with shower (17)，Described shower (17) upper end connects with gas-liquid ingress pipe (4)，In the middle of described shower (17), high-pressure pump (19) is installed，It is internal that one section, described shower (17) lower section is positioned at rotating cylinder (22)，And be positioned at internal one section of rotating cylinder (22) and be provided with some spray heads (18)；nullRotation point cylinder (27) is installed in described 3rd chamber (11)，Described rotation divides cylinder (27) to be fixed on the 3rd dividing plate (8)，Some circular holes (14) are had on described 3rd dividing plate (8)，Described rotation divides cylinder (27) inner upper to be provided with motor (20)，Described motor (20) is provided around protective layer (23)，Described motor (20) is fixedly connected with rotation leaflet (28) by output shaft (21)，Described rotation divides cylinder (27) side to have some through holes (24)，Described rotation divides cylinder (27) lower end to connect with airway (26)，Described 3rd chamber (11) and second partition (7) junction have two leakage fluid drams (30) in left and right，Described leakage fluid dram (30) place is communicated with the return duct (13) of the 3rd chamber (11) and the second chamber (10)，Described return duct (13) is connected with discharging tube (15) side；Described 4th chamber (12) interior centre position is provided with microporous filter screen (29), described 4th chamber (12) and the 3rd dividing plate (8) junction have two leakage fluid drams (30) in left and right, and described leakage fluid dram (30) place is communicated with the return duct (13) of the 4th chamber (12) and the second chamber (10).
- A kind of efficient gas-liquid separator the most according to claim 1, it is characterised in that: described microporous filter screen (29) is in inverted V-shaped, it is simple to prolong V-arrangement after liquid condensation under gravity dirty.
- A kind of efficient gas-liquid separator the most according to claim 1, it is characterised in that: described demister (16) is in inverted V-shaped, it is simple to prolong V-arrangement after liquid condensation under gravity dirty.
- A kind of efficient gas-liquid separator the most according to claim 1, it is characterised in that: described packing layer (25) thickness is 20mm to 50mm, in dense mesh structure.
- A kind of efficient gas-liquid separator the most according to claim 1, it is characterised in that: described spray head (18) is distributed on shower (17) radially.
- A kind of efficient gas-liquid separator the most according to claim 1, it is characterised in that: described airway (26) is at least provided with two, and arranges radially around cylinder (1) central axis.
- A kind of efficient gas-liquid separator the most according to claim 1, it is characterised in that: described rotation divides cylinder (27) and internals thereof all at least provided with two groups, and each rotation divides cylinder (27) all to connect with airway (26) one_to_one corresponding.
- A kind of efficient gas-liquid separator the most according to claim 1, it is characterized in that: described discharging tube (15) is at least provided with two, and be passed through internal one section of discharging tube (15) side of the second chamber (10) and be connected with return duct (13), opposite side is near 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 |
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| Publication Number | Publication Date |
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| CN105999950A true CN105999950A (en) | 2016-10-12 |
| CN105999950B CN105999950B (en) | 2018-11-06 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201610507581.7A Active CN105999950B (en) | 2016-06-30 | 2016-06-30 | A kind of high efficiency air liquid separation device |
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Cited By (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 |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4276000B2 (en) * | 2003-06-16 | 2009-06-10 | 株式会社ブンリ | Cyclone type foreign matter separator |
| CN203648334U (en) * | 2014-01-16 | 2014-06-18 | 中国矿业大学 | Circulating gas-liquid separation device |
| CN103977665B (en) * | 2014-05-30 | 2015-12-30 | 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
Cited By (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 | Publication date |
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| CN105999950B (en) | 2018-11-06 |
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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. |
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