CN110064251A - A kind of gas-liquid separator - Google Patents
A kind of gas-liquid separator Download PDFInfo
- Publication number
- CN110064251A CN110064251A CN201910485884.7A CN201910485884A CN110064251A CN 110064251 A CN110064251 A CN 110064251A CN 201910485884 A CN201910485884 A CN 201910485884A CN 110064251 A CN110064251 A CN 110064251A
- Authority
- CN
- China
- Prior art keywords
- gas
- vaporium
- collet
- liquid separator
- air inlet
- 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.)
- Pending
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- 239000007788 liquid Substances 0.000 title claims abstract description 35
- 238000007747 plating Methods 0.000 claims abstract description 21
- 108091006146 Channels Proteins 0.000 claims description 15
- 238000005192 partition Methods 0.000 claims description 9
- 238000000926 separation method Methods 0.000 claims description 7
- 238000007789 sealing Methods 0.000 claims description 4
- 102000010637 Aquaporins Human genes 0.000 claims description 2
- 108010063290 Aquaporins Proteins 0.000 claims description 2
- 238000010025 steaming Methods 0.000 claims 1
- 238000009423 ventilation Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 15
- 239000007789 gas Substances 0.000 description 11
- 238000010586 diagram Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 3
- 239000003208 petroleum Substances 0.000 description 3
- 238000005119 centrifugation Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 230000008676 import Effects 0.000 description 1
- 238000010409 ironing Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 238000007634 remodeling Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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
- B01D45/02—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising gravity
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/24—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by centrifugal force
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/80—Water
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Cyclones (AREA)
- Separating Particles In Gases By Inertia (AREA)
Abstract
The invention discloses a kind of gas-liquid separators, it include separator body, the top of separator body is provided with vaporium, air inlet pipe is provided on the vaporium, it is provided with the collet of tubular structure below vaporium, collecting channel is formed between the inner plating and lamina rara externa of collet, the middle part of separator body is formed with cylinder chamber inside the inner plating of collet, cylinder chamber is provided centrally with escape pipe, and the upper end of the escape pipe is stretched out outside separator body；Apopore is provided on the inner plating of collet, collecting chamber is provided with below collet, collecting chamber is communicated with the collecting channel, and the lower part of collecting chamber is provided with outlet pipe, the outer rim of vaporium is being provided with air inlet on the inside of inner plating, and the air inlet is arranged along a tangential direction.The present invention has the advantages that structure is simple, separative efficiency is high, good separating effect.
Description
Technical field
The present invention relates to steam-water separation technical field, a kind of especially gas-liquid separator.
Background technique
Gas-liquid separator is widely used in many fields such as boiler, chemical industry, food, PETROLEUM PROCESSING, and main function is
Gas-liquid is sufficiently separated, the higher steam of purity or other gases are obtained.For example the vapor generated in boiler usually contains water,
Or condensed water is had by long distance delivery, just there is large effect with energy process (such as ironing) to certain in this way, therefore must
Liquid and steam must be separated；Having again will be in the petroleum of a certain temperature section and the volatile component point of the temperature section in petroleum refinery process
Gas-liquid separation device can also be used by opening.The height of the separative efficiency of gas-liquid separator is most important.
Gas-liquid separator currently on the market is broadly divided into two classes: one is iris types, by adding in gas-liquid channel
Many partitions are filled to separate liquid；Another kind is cyclone separator, forces steam to do eddying motion using water conservancy diversion spiral plate,
It allows moisture and steam to separate using the principle of centrifugation, then dry saturated steam is discharged by intermediate pipe.
Traditional whirlwind gas-liquid separator, steam water interface are inputted from import, are flowed downward by the rotation of water conservancy diversion spiral plate,
Air-flow moves in a circle around intermediate exhaust pipe, and the moisture in steam is got rid of to side wall under the influence of centrifugal force during exercise
Out, steam has then been left on immediate vicinity, is exported by conduit then by outlet discharge, this steam-water separator is obvious excellent
In partition separator, but because its structure causes the linear velocity of rotation not fast enough, centrifugation can be in centrifugal force in the water of side wall
Conduit is expressed under effect nearby as steam flows out, therefore, there are also very big rooms for promotion for centrifugal effect.
Summary of the invention
It is simple that the technical problem to be solved by the invention for the present situation of prior art is to provide structures, and separative efficiency is high,
A kind of gas-liquid separator of good separating effect.
The technical scheme of the invention to solve the technical problem is:
A kind of gas-liquid separator includes separator body, and the top of separator body is provided with vaporium, is set on the vaporium
It is equipped with air inlet pipe, the collet of tubular structure is provided with below vaporium, is formed with collection between the inner plating and lamina rara externa of collet
Aquaporin, the middle part of separator body are formed with cylinder chamber inside the inner plating of collet, and cylinder chamber is provided centrally with outlet
The upper end of pipe, the escape pipe is stretched out outside separator body；It is provided with apopore on the inner plating of collet, is provided with below collet
Collecting chamber, collecting chamber are communicated with the collecting channel, and the lower part of collecting chamber is provided with outlet pipe, and the outer rim of vaporium is within being located at
Air inlet is provided on the inside of laminate, air inlet is arranged along a tangential direction.
The technical measures of optimization further include:
Above-mentioned vaporium is made of head sealing cover and partition, and air inlet is the diversion trench being set on the partition, diversion trench edge
Tangential direction setting.
The number of above-mentioned diversion trench is 2-6.
Snorkel is connected on above-mentioned vaporium, snorkel is placed in the top of the cylinder chamber, and diametrically sets
It sets, air inlet is the escape pipe for being correspondingly arranged in snorkel both ends.
Above-mentioned escape pipe and snorkel are perpendicular, and the escape pipe at both ends is towards on the contrary.
Above-mentioned collecting chamber is made of bottom plate and bottom cover, and the periphery of bottom plate is formed with limbers.
Above-mentioned bottom cover is in the arcuate structure of convex, and outlet pipe is set to the bottom centre of bottom cover.
A kind of gas-liquid separator of the invention, structure is simple, uses the air inlet for the outer rim for being set to vaporium that will steam
Vapour pours into cylinder chamber, and radius of turn is big, and centrifugal force is big, can obtain bigger linear velocity, overcomes existing gas-liquid separator
Radius of turn is small, the small disadvantage of centrifugal force, and the air inlet of existing gas-liquid separator is directly directed at body centre, then leads in spiral plate
It is forced to move in a circle under the guidance of stream, is to move in a circle around central tube, therefore radius of turn is small, centrifugal force is small.Meanwhile
Spiral deflector structure is saved, steam can be made faster, more to move in a circle to multi-turn number, keep gas-liquid separation more abundant.
In addition, collet is arranged in cylinder chamber in this gas-liquid separator, it is formed with and catchments between the inner plating and lamina rara externa of collet
Channel, during steam moves in a circle in cylinder chamber, under the action of the centrifugal force, moisture is entered by inner plating upper water-out hole
In collecting channel, and the air in collecting channel is opposing stationary, and the water being centrifuged out not will form high speed rotation water flow and be attached to bucket
The escape pipe that wall finally flows to center causes separation to be not thorough.The water separated in collecting channel flows under the influence of gravity into collection
Water chamber, it is final to be discharged.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the embodiment of the present invention one；
Fig. 2 is the structural schematic diagram of Fig. 1 insole board；
Fig. 3 is the structural schematic diagram of the embodiment of the present invention two；
Fig. 4 is the overlooking structure diagram of Fig. 3 Center Vent tube.
Specific embodiment
The present invention will be described in further detail below with reference to the embodiments of the drawings.
It is as shown in Figures 1 to 4 structural schematic diagram of the invention,
Appended drawing reference therein are as follows: vaporium 1, air inlet pipe 11, head sealing cover 12, partition 13, diversion trench 13a, snorkel 14, outlet
Pipe 14a, collet 2, collecting channel 2a, cylinder chamber 2b, inner plating 21, apopore 21a, lamina rara externa 22, escape pipe 3, collecting chamber 4,
Outlet pipe 41, bottom plate 42, limbers 42a, bottom cover 43.
Embodiment one, as shown in Figure 1 to Figure 2,
A kind of gas-liquid separator includes separator body, and the top of separator body is provided with vaporium 1, on the vaporium 1
Be provided with air inlet pipe 11, the lower section of vaporium 1 is provided with the collet 2 of tubular structure, the inner plating 21 and lamina rara externa 22 of collet 2 it
Between be formed with collecting channel 2a, the middle part of separator body is formed with cylinder chamber 2b, cylinder chamber inside the inner plating 21 of collet 2
2b's is provided centrally with escape pipe 3, and the upper end of the escape pipe 3 is stretched out outside separator body；It is provided on the inner plating 21 of collet 2
Apopore 21a, the lower section of collet 2 are provided with collecting chamber 4, and collecting chamber 4 is communicated with the collecting channel 2a, the lower part of collecting chamber 4
It is provided with outlet pipe 41, the outer rim of vaporium 1 is provided with air inlet in the inside for being located at inner plating 21, and the air inlet edge is cut
The setting of line direction.
In embodiment, vaporium 1 is made of head sealing cover 12 and partition 13, and air inlet is to be set to leading on the partition 13
Chute 13a, diversion trench 13a are arranged along a tangential direction.
In embodiment, the number of diversion trench 13a is 2-6.
In embodiment, collecting chamber 4 is made of bottom plate 42 and bottom cover 43, and the periphery of bottom plate 42 is formed with limbers 42a.
In embodiment, bottom cover 43 is in the arcuate structure of convex, and outlet pipe 41 is set to the bottom centre of bottom cover 43.So
Setting, the water that can be separated preferably are assembled to outlet pipe 41, and the discharge of moisture is also more smoothly.
Embodiment two, as shown in Figure 3 to Figure 4,
Structure of gas liquid separator in the present embodiment is similar in embodiment one, the difference is that in the present embodiment, vaporium
Snorkel 14 is connected on 1, snorkel 14 is placed in the top of the cylinder chamber 2b, and diametrically disposed, and air inlet is pair
The escape pipe 14a at 14 both ends of snorkel should be set to.
In embodiment, escape pipe 14a and snorkel 14 are perpendicular, and the escape pipe 14a at both ends is towards on the contrary.So set,
Steam is set to enter cylinder chamber 2b with tangential direction, to obtain bigger linear velocity.
Working principle:
Steam enters in vaporium 1 from air inlet pipe 11, then from the outer rim for being set to vaporium 1 and positioned at the inside of inner plating 21
Air inlet enters along a tangential direction in cylinder chamber 2b, into the steam in cylinder chamber 2b under gas pressure in cylinder chamber 2b it is high
Speed rotates and generates centrifugal force, and in centrifugal force effect, contained humidity (liquid phase) is thrown toward the folder of the periphery cylinder chamber 2b in steam
Set 2, moisture is entered in collecting channel 2a by the apopore 21a of inner plating 21, since gas is opposing stationary in collecting channel 2a,
Moisture no longer moves in a circle in collecting channel 2a, but passes downwardly through limbers 42a under the effect of gravity and enter collecting chamber
4, finally it is discharged from outlet pipe 41, and the gas (gas phase) for having been separated moisture is then discharged from escape pipe 3 upwards, to realize gas
Liquid separation.
Traditional gas-liquid separator air inlet is directly directed at body centre, is forced to do circumference under the guidance of spiral plate water conservancy diversion
Movement, rotation speed is low, and rotation is moved in a circle around central tube, and radius of turn is small, and centrifugal force is small；And this gas-liquid separator
Air inlet is set to the outer rim of vaporium 1, radius of turn is big, and centrifugal force is big, and rotation speed is fast, energy under identical inlet air conditions
Enough to obtain bigger linear velocity, separating effect is more preferable.
For traditional gas-liquid separator because the circle number of spiral deflector is limited, steam does the circumference of limited circle number in cylinder
Movement, separating effect are unsatisfactory；This gas-liquid separator has cast out spiral deflector structure, and the air-flow entered along a tangential direction mentions
For rotating energy, steam moves in a circle incessantly in cylinder chamber 2b, and in cylinder chamber 2b, outside is close to 2 position of collet
Gas density it is big, and close to center escape pipe 3 gas density it is small, be conducive to gas-liquid and be sufficiently separated.
In addition, 2 structure of collet, collecting channel 2a between 2 inner plating 21 of collet and lamina rara externa 22 are arranged outside cylinder chamber 2b
Interior gas is opposing stationary, and moisture no longer moves in a circle after entering in collecting channel 2a, and the water after avoiding separation is again with gas
The circular motion of body, which enters caused by escape pipe 3 to separate, to be not thorough.
Highly preferred embodiment of the present invention has illustrated, and the various change or remodeling made by those of ordinary skill in the art are not
It can depart from the scope of the present invention.
Claims (7)
1. a kind of gas-liquid separator includes separator body, it is characterized in that: the top of the separator body is provided with steaming
Steam chest (1) is provided with air inlet pipe (11) on the vaporium (1), the folder of tubular structure is provided with below the vaporium (1)
It covers (2), is formed with collecting channel (2a), the separation between the inner plating (21) and lamina rara externa (22) of the collet (2)
The middle part of device ontology is formed with cylinder chamber (2b) inside the inner plating (21) of collet (2), the center of the cylinder chamber (2b)
Escape pipe (3) are provided with, the upper end of the escape pipe (3) is stretched out outside separator body；On the inner plating (21) of the collet (2)
It is provided with apopore (21a), is provided with below the collet (2) collecting chamber (4), the collecting chamber (4) and the collection
Aquaporin (2a) communicates, and the lower part of the collecting chamber (4) is provided with outlet pipe (41), and the outer rim of the vaporium (1) exists
Air inlet is provided on the inside of inner plating (21), the air inlet is arranged along a tangential direction.
2. a kind of gas-liquid separator according to claim 1, it is characterized in that: the vaporium (1) is by head sealing cover (12)
It is constituted with partition (13), the air inlet is the diversion trench (13a) being set on the partition (13), the diversion trench
(13a) is arranged along a tangential direction.
3. a kind of gas-liquid separator according to claim 2, it is characterized in that: the number of the diversion trench (13a) is 2-6
It is a.
4. a kind of gas-liquid separator according to claim 1, it is characterized in that: being connected with ventilation on the vaporium (1)
It manages (14), the snorkel (14) is placed in the top of the cylinder chamber (2b), and diametrically disposed, described air inlet
For the escape pipe (14a) for being correspondingly arranged in snorkel (14) both ends.
5. a kind of gas-liquid separator according to claim 4, it is characterized in that: the escape pipe (14a) and snorkel
(14) perpendicular, the escape pipe (14a) at both ends is towards on the contrary.
6. a kind of gas-liquid separator according to any one of claims 1 to 5, it is characterized in that: the collecting chamber
(4) it is made of bottom plate (42) and bottom cover (43), the periphery of the bottom plate (42) is formed with limbers (42a).
7. a kind of gas-liquid separator according to claim 6, it is characterized in that: the bottom cover (43) is in the arc of convex
Structure, the outlet pipe (41) are set to the bottom centre of bottom cover (43).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910485884.7A CN110064251A (en) | 2019-06-05 | 2019-06-05 | A kind of gas-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910485884.7A CN110064251A (en) | 2019-06-05 | 2019-06-05 | A kind of gas-liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110064251A true CN110064251A (en) | 2019-07-30 |
Family
ID=67372705
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910485884.7A Pending CN110064251A (en) | 2019-06-05 | 2019-06-05 | A kind of gas-liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110064251A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110898630A (en) * | 2019-12-23 | 2020-03-24 | 安徽环球星新能源科技有限公司 | Transcritical CO2Gas-liquid separation device with high separation efficiency for heat pump system |
| CN111470483A (en) * | 2020-06-05 | 2020-07-31 | 于龙 | Utilize freon to concentrate system as cold and hot carrier's nitric acid |
| CN115954503A (en) * | 2023-03-14 | 2023-04-11 | 西安旭旌再生资源有限公司 | Hydrogen fuel cell water-gas separation system |
| CN118794272A (en) * | 2024-09-13 | 2024-10-18 | 江苏巨衡机械有限公司 | Recovery device for condensate water of steam turbine cooler |
| CN118794272B (en) * | 2024-09-13 | 2024-11-15 | 江苏巨衡机械有限公司 | Recovery device for condensate water of steam turbine cooler |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201940295U (en) * | 2010-10-28 | 2011-08-24 | 中国石油集团渤海钻探工程有限公司 | Jacket type gas-liquid cyclone separator |
| CN210186616U (en) * | 2019-06-05 | 2020-03-27 | 宁波金名片能源科技有限公司 | Gas-liquid separator |
-
2019
- 2019-06-05 CN CN201910485884.7A patent/CN110064251A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201940295U (en) * | 2010-10-28 | 2011-08-24 | 中国石油集团渤海钻探工程有限公司 | Jacket type gas-liquid cyclone separator |
| CN210186616U (en) * | 2019-06-05 | 2020-03-27 | 宁波金名片能源科技有限公司 | Gas-liquid separator |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110898630A (en) * | 2019-12-23 | 2020-03-24 | 安徽环球星新能源科技有限公司 | Transcritical CO2Gas-liquid separation device with high separation efficiency for heat pump system |
| CN110898630B (en) * | 2019-12-23 | 2023-05-09 | 河南昊立智能科技有限公司 | Transcritical CO 2 Gas-liquid separation device with high separation efficiency for heat pump system |
| CN111470483A (en) * | 2020-06-05 | 2020-07-31 | 于龙 | Utilize freon to concentrate system as cold and hot carrier's nitric acid |
| CN115954503A (en) * | 2023-03-14 | 2023-04-11 | 西安旭旌再生资源有限公司 | Hydrogen fuel cell water-gas separation system |
| CN118794272A (en) * | 2024-09-13 | 2024-10-18 | 江苏巨衡机械有限公司 | Recovery device for condensate water of steam turbine cooler |
| CN118794272B (en) * | 2024-09-13 | 2024-11-15 | 江苏巨衡机械有限公司 | Recovery device for condensate water of steam turbine cooler |
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|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20190730 |