CN117504446A - High-efficient gas-liquid separation device - Google Patents
High-efficient gas-liquid separation device Download PDFInfo
- Publication number
- CN117504446A CN117504446A CN202311503478.1A CN202311503478A CN117504446A CN 117504446 A CN117504446 A CN 117504446A CN 202311503478 A CN202311503478 A CN 202311503478A CN 117504446 A CN117504446 A CN 117504446A
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- liquid
- liquid level
- gas
- tank body
- baffle plate
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- 239000007788 liquid Substances 0.000 title claims abstract description 159
- 238000000926 separation method Methods 0.000 title claims abstract description 24
- 238000009825 accumulation Methods 0.000 claims abstract description 16
- 238000006243 chemical reaction Methods 0.000 claims abstract description 14
- 238000007789 sealing Methods 0.000 claims description 62
- 238000011010 flushing procedure Methods 0.000 claims description 23
- 238000005192 partition Methods 0.000 claims 1
- 235000014113 dietary fatty acids Nutrition 0.000 abstract description 22
- 229930195729 fatty acid Natural products 0.000 abstract description 22
- 239000000194 fatty acid Substances 0.000 abstract description 22
- 150000004665 fatty acids Chemical class 0.000 abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 12
- 239000006260 foam Substances 0.000 abstract description 10
- 241000521257 Hydrops Species 0.000 description 6
- 206010030113 Oedema Diseases 0.000 description 6
- 238000004140 cleaning Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000009835 boiling Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000005187 foaming Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000005856 abnormality Effects 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004581 coalescence Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000002035 prolonged effect Effects 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
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
- B01D45/08—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by impingement against baffle separators
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
- B01D45/06—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by reversal of direction of flow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/18—Cleaning-out devices
-
- 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
- B01D53/26—Drying gases or vapours
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)
- Degasification And Air Bubble Elimination (AREA)
Abstract
The invention belongs to the technical field of gas-liquid separation, and discloses a high-efficiency gas-liquid separation device, which comprises a tank body, wherein the tank body is provided with a gas inlet, a liquid outlet and a gas outlet; a baffle plate, a baffle plate and a blade separator are arranged in the tank body; the baffle plate divides the tank body into a gas cavity and a liquid accumulation cavity, the baffle plate is arranged opposite to the gas inlet, the blade separator is connected with the gas outlet, and the bottom of the blade separator is provided with a flow guide pipe connected with the liquid accumulation cavity; the baffle includes first swash plate and second swash plate, and first swash plate is located the baffling board below, all is equipped with the fender flow board on first swash plate and the second swash plate, and the lower extreme of fender flow board is equipped with the weeping hole. The mixed gas of the fatty acid foam layer, the liquid drops and the water vapor discharged from the reaction kettle is discharged into the high-efficiency gas-liquid separation device, the foam layer and the liquid drops of the fatty acid foam layer are collected into the liquid accumulation cavity through the baffle plate, the flow baffle plate and the blade separator, finally the mixed gas flows back into the reaction kettle, and the water vapor enters the rear-stage condenser for treatment.
Description
Technical Field
The invention belongs to the technical field of gas-liquid separation, and particularly relates to a high-efficiency gas-liquid separation device.
Background
In the production process of fatty acid products, the generated water is required to be separated, the temperature of the mixture in the reaction kettle is higher than the boiling point of water under the corresponding pressure and lower than the boiling point of fatty acids, the water evaporates from the reaction kettle in the vapor-gas phase state, and the fatty acid foaming and tiny liquid drop entrainment are accompanied in the water evaporation process due to the characteristics of fatty acid substances and the evaporation gas speed, so that the fatty acid foaming layer, the liquid drop and the water vapor are mixed together and are taken out from the reaction kettle, and if the water vapor is directly discharged, air is polluted, and meanwhile, the fatty acid entrained in the water vapor is wasted.
Disclosure of Invention
The present invention aims to solve the above technical problems at least to some extent. Therefore, the invention aims to provide a high-efficiency gas-liquid separation device.
The technical scheme adopted by the invention is as follows:
the high-efficiency gas-liquid separation device comprises a tank body which is transversely arranged, wherein the tank body is provided with a gas inlet, a liquid outlet and a gas outlet; a baffle plate, a baffle plate and a blade separator are arranged in the tank body; the baffle plate divides the tank body into a gas cavity and a liquid accumulation cavity, the baffle plate and the blade separator are both arranged in the gas cavity, the baffle plate is arranged opposite to the air inlet, the blade separator is connected with the air outlet, and the bottom of the blade separator is provided with a flow guide pipe connected with the liquid accumulation cavity; the baffle plate comprises a first inclined plate and a second inclined plate, the first inclined plate is positioned below the baffle plate, the lower end of the first inclined plate is adjacent to the lower end of the second inclined plate, a gap is formed between the lower end of the first inclined plate and the lower end of the second inclined plate, and the gap forms a liquid leakage groove; the first sloping plate and the second sloping plate are respectively provided with a flow baffle, the flow baffles on the first sloping plate are parallel to each other, the flow baffles on the second sloping plate are parallel to each other, and the lower end of the flow baffles is provided with a liquid leakage hole.
Preferably, the lower end of the flow guide pipe is positioned below the liquid level of the liquid accumulation cavity, a liquid discharge valve is arranged at the liquid outlet, a liquid level sensor is arranged in the liquid accumulation cavity, the liquid discharge valve and the liquid level sensor are both connected with a controller, and the controller controls the liquid level sensor to be normally open and controls the liquid discharge valve to be normally closed; the liquid level sensor is used for collecting the liquid level value in the liquid accumulation cavity in real time and recording the liquid level value as a real-time liquid level value; when the real-time liquid level value acquired by the liquid level sensor is larger than the upper limit value of the standard liquid level range, the controller controls the liquid discharge valve to be opened for liquid discharge, and when the real-time liquid level value acquired by the liquid level sensor is smaller than the lower limit value of the standard liquid level range, the controller controls the liquid discharge valve to be closed.
Preferably, the lead of the liquid level sensor passes through the circuit leading-out cylinder of the tank body, a sealing cylinder is arranged in the circuit leading-out cylinder, a first limiting piece and a rubber piece are arranged in the sealing cylinder, a sealing cover is arranged on the circuit leading-out cylinder, the sealing cover is in pressure contact with the outer end of the sealing cylinder, the sealing cylinder is in pressure contact with the outer end of the first limiting piece, the first limiting piece is in pressure contact with the outer end of the rubber piece, and the lead passes through the rubber piece, the first limiting piece, the sealing cylinder and the sealing cover.
Preferably, the rubber part, the first limiting part, the sealing cylinder and the sealing cover are provided with wire guide holes, and the wire guide holes are in sealing fit with the wires after the rubber part is pressed and deformed. The sealing cylinder is internally provided with a second limiting piece, the inner end of the second limiting piece is abutted against a circle of step in the circuit leading-out cylinder, and the outer end of the second limiting piece is contacted with the inner end of the rubber piece. The inner end of the sealing cylinder is abutted against a circle of step in the circuit leading-out cylinder, and the sealing cylinder is provided with a sealing ring opposite to the step. The sealing cover is connected with the circuit leading-out cylinder through an adjusting bolt.
Preferably, the tank body is provided with a first flushing port, a second flushing port and a third flushing port, the first flushing port is opposite to the blade separator, the second flushing port is arranged in the middle of the tank body, and the third flushing port is arranged at the bottom of the tank body. The air inlet is connected with the outlet of the reaction kettle, the liquid outlet is connected with the inlet of the reaction kettle, and the air outlet is connected with the condenser.
The beneficial effects of the invention are as follows:
the mixed gas of the fatty acid foam layer, the liquid drops and the water vapor discharged from the reaction kettle is discharged into the high-efficiency gas-liquid separation device, the foam layer and the liquid drops of the fatty acid foam layer are collected into the liquid accumulation cavity through the baffle plate, the flow baffle plate and the blade separator, finally the mixed gas flows back into the reaction kettle, and the water vapor enters the rear-stage condenser for treatment.
Drawings
FIG. 1 is a schematic view of a high efficiency gas-liquid separation apparatus of the present invention.
Fig. 2 is a schematic view of the internal structure of the can body of the present invention.
Fig. 3 is a cross-sectional view of the circuit outlet barrel of the present invention.
In the figure: 1-a tank body; 2-air inlet; 3-a liquid outlet; 4-an air outlet; 5-baffle plate; 6-a first sloping plate; 7-a second sloping plate; 8-blade separator; 9-a gas chamber; 10-effusion chamber; 11-a flow guiding pipe; 12-a liquid leakage groove; 13-a baffle plate; 14-a liquid level sensor; 15-conducting wires; 16-a circuit extraction barrel; 17-a sealing cylinder; 18-a first limiting piece; 19-a rubber member; 20-a second limiting piece; 21-capping; 22-adjusting bolts; 23-sealing rings; 24-a first flushing port; 25-a second flush port; 26-third flushing port.
Detailed Description
Embodiments of the present invention are described in detail below, examples of which are illustrated in the accompanying drawings, wherein like or similar reference numerals refer to like or similar elements or elements having like or similar functions throughout. The embodiments described below by referring to the drawings are illustrative and intended to explain the present invention and should not be construed as limiting the invention. The components of the embodiments of the present invention generally described and illustrated in the figures herein may be arranged and designed in a wide variety of different configurations.
In the present invention, unless explicitly specified and limited otherwise, the terms "mounted," "connected," "secured," and the like are to be construed broadly and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; can be directly connected or indirectly connected through an intermediate medium, and can be communication between two elements.
As shown in fig. 1 and 2, the efficient gas-liquid separation device of the embodiment comprises a sealed tank body 1, wherein the tank body 1 is transversely arranged and is installed on the horizontal ground through supporting legs, and an air inlet 2, a liquid outlet 3 and an air outlet 4 are formed in the tank body 1; a baffle plate 5, a baffle plate and a blade separator 8 are arranged in the tank body 1; the baffle plate divides the tank body 1 into an upper gas cavity 9 and a lower effusion cavity 10, and the baffle plate 5 and the vane separator 8 are arranged in the gas cavity 9.
The baffle plate comprises a first inclined plate 6 and a second inclined plate 7, the first inclined plate 6 is positioned below the baffle plate 5, the lower end of the first inclined plate 6 is adjacent to the lower end of the second inclined plate 7, a gap is formed between the lower end of the first inclined plate and the lower end of the second inclined plate, and the gap forms a liquid leakage groove 12; the first inclined plate 6 and the second inclined plate 7 are respectively provided with a flow baffle 13, the flow baffles 13 on the first inclined plate 6 are parallel to each other, the flow baffles 13 on the second inclined plate 7 are parallel to each other, and the lower end of the flow baffles 13 is provided with a liquid leakage hole.
The baffle plate 5 is arranged opposite to the air inlet 2, the air inlet 2 is arranged on the left side of the tank body 1, the baffle plate 5 is vertically arranged, the air inlet 2 is connected with the outlet of the reaction kettle, the mixed gas of the fatty acid foam layer, liquid drops and water vapor entering through the air inlet 2 firstly encounters the baffle plate 5 to flow to change, the mixed gas moves downwards to encounter the first inclined plate 6, then enters the right space of the gas cavity 9 through a gap between the first inclined plate 6 and the lower end of the baffle plate 5, the mixed gas changes in flow direction again when passing through the first inclined plate 6, contacts with the baffle plate 13 on the first inclined plate 6, part of fatty acid foam layer and liquid drops are coalesced on the baffle plate 13 to form fatty acid liquid, and the fatty acid liquid flows to the liquid leakage groove 12 through the liquid leakage hole at the lower end of the baffle plate along the first inclined plate 6 to enter the liquid accumulation cavity 10.
Meanwhile, in the process of two rapid flow direction conversion, due to the action of inertia force, the fatty acid foam layer and liquid drops collide with the baffle plate and the first inclined plate continuously in kinetic energy, and the kinetic energy of the fatty acid foam layer and the liquid drops is reduced, so that the subsequent treatment of the blade separator 8 is facilitated.
The liquid outlet 3 is located the bottom of jar body 1, the gas outlet 4 is located the top of jar body 1, blade separator 8 links to each other with gas outlet 4, part in the mixed gas in the right side space of entering gas chamber 9 directly gets into blade separator 8, another part moves along second swash plate 7, the mixed gas along second swash plate 7 moves and keeps off the flow plate contact on the second swash plate 7, partial fatty acid bubble layer, liquid droplet coalesce on the flow baffle and form fatty acid liquid, the fatty acid liquid flows to drain groove 12 along second swash plate 7 through the weeping hole of the lower extreme of flow baffle and gets into hydrops chamber 10.
The blade separator 8 adopts commercial products, the honeycomb duct 11 that links to each other with hydrops chamber 10 is equipped with in blade separator 8 bottom, the mixed gas that gets into blade separator 8 can continue to carry out the flow direction through in the runner structure space of blade and change, produce simultaneously and rotate, because fatty acid bubble layer and liquid droplet kinetic energy decline behind baffle, first swash plate, radius of rotation drops sharply, fatty acid bubble layer and liquid droplet are collided with the blade surface and are coalesced the effect grow more and more owing to surface tension, along with the absorption of liquid droplet is bigger and bigger, thereby separate with the vapor, adsorb the coalescence on the blade surface, the fatty acid liquid that the entrapment was converged is collected along blade structure flow direction blade separator 8 bottom hydrops groove along the effect of self gravity, then discharge to hydrops chamber 10 through honeycomb duct 11, the remaining vapor then gets into the condenser through gas outlet 4 and handles.
The lower extreme of honeycomb duct 11 is located the liquid level of hydrops chamber 10, and the lower extreme of honeycomb duct 11 is sealed by the liquid, can prevent that the mixed gas from getting into hydrops chamber 10 along honeycomb duct 11 for the mixed gas can follow the runner structure motion of the blade of blade separator, thereby realizes the efficient gas-liquid separation.
The liquid outlet 3 is connected with the inlet of the reaction kettle, a liquid discharge valve is arranged at the liquid outlet 3, and a liquid level sensor 14 is arranged in the liquid accumulation cavity 10. The liquid discharge valve and the liquid level sensor 14 are connected with a controller, and the controller controls the liquid level sensor 14 to be normally opened and controls the liquid discharge valve to be normally closed; the liquid level sensor 14 is used for collecting the liquid level value in the liquid accumulation cavity 10 in real time and recording the liquid level value as a real-time liquid level value; when the real-time liquid level value acquired by the liquid level sensor 14 is within the standard liquid level range, the liquid level is represented as normal. When the real-time liquid level value acquired by the liquid level sensor 14 is larger than the upper limit value of the standard liquid level range, the controller controls the liquid discharge valve to be opened for liquid discharge until the real-time liquid level value acquired by the liquid level sensor 14 is smaller than the lower limit value of the standard liquid level range, and the controller controls the liquid discharge valve to be closed. When the real-time liquid level value acquired by the liquid level sensor 14 is smaller than the warning liquid level value, the controller gives out a liquid level abnormality alarm to remind the staff. The warning liquid level value is smaller than the lower limit value of the standard liquid level range.
In this embodiment, as shown in fig. 3, the circuit leading-out cylinder 16 is in a through cylindrical structure, the circuit leading-out cylinder 16 is welded on the side wall of the tank 1, a through hole connected with the circuit leading-out cylinder 16 is arranged on the tank 1, the lead 15 of the liquid level sensor 14 penetrates out of the circuit leading-out cylinder 16 of the tank 1, a sealing cylinder 17 is arranged in the circuit leading-out cylinder 16, a first limiting piece 18, a rubber piece 19 and a second limiting piece 20 are arranged in the sealing cylinder 17, a sealing cover 21 is arranged in the sealing cylinder 17, the sealing cover 21 is in pressure contact with the outer end of the sealing cylinder 17 through an adjusting bolt 22, the sealing cylinder 17 is in pressure contact with the outer end of the first limiting piece 18, the first limiting piece 18 is in pressure contact with the outer end of the rubber piece 19, the inner end of the second limiting piece 20 is in contact with a circle of step in the circuit leading-out cylinder 16, the outer end of the sealing cylinder 17 is in contact with a circle of step in the circuit leading-out cylinder 16, and a sealing ring 23 is arranged opposite to the sealing cylinder 17.
The second limiting piece 20, the rubber piece 19, the first limiting piece 18, the sealing barrel 17 and the sealing cover 21 are provided with wire holes, and the wires 15 sequentially pass through the wire holes on the second limiting piece 20, the rubber piece 19, the first limiting piece 18, the sealing barrel 17 and the sealing cover 21.
The first limiting piece 18, the rubber piece 19 and the second limiting piece 20 are all of cylindrical structures with equal diameters, the rubber piece 19 is easy to deform after not being extruded, and the first limiting piece 18 and the second limiting piece 20 are made of materials which are not easy to deform. The length sum of the first limiting piece 18, the rubber piece 19 and the second limiting piece 20 is larger than the length of the inside of the sealing cylinder 17; the first limiting piece 18, the rubber piece 19 and the second limiting piece 20 are installed in the sealing barrel 17, the adjusting bolt 22 is screwed, the sealing cover 21 applies pressure to the sealing barrel 17, the sealing barrel 17 applies pressure to the first limiting piece 18, and the second limiting piece 20 is pressed against the step, so that the rubber piece 19 is extruded by the first limiting piece 18 and the second limiting piece 20 at the same time, the rubber piece 19 is deformed, the outer wall of the rubber piece 19 is in sealing connection with the inner wall of the sealing barrel 17, meanwhile, the wire hole of the rubber piece 19 is in fit sealing with the outer wall of the wire 15 in the wire hole, the sealing barrel 17 is pressed and then the sealing ring 23 is pressed, so that the sealing barrel 17 and the step of the circuit leading-out barrel 16 are sealed, and therefore the pressure and liquid inside and outside the tank body 1 are separated through the sealing effect of the rubber piece 19 and the sealing ring 23.
Meanwhile, under the action of the restoring force of the rubber piece 19, the rubber piece 19 always generates a pre-pressure for pushing the sealing cover 21 outwards, and the pre-pressure can enable the adjusting bolt 22 to be fastened more and prevent loosening, so that too large torque is not needed when the adjusting bolt 22 is screwed, the sealing ring 23 does not need to be in a high-pressure compression state for a long time, and the service life is prolonged.
The tank body 1 is provided with a first flushing port 24, a second flushing port 25 and a third flushing port 26, the first flushing port 24 is opposite to the blade separator 8, the second flushing port 25 is arranged in the middle of the tank body 1, and the third flushing port 26 is arranged at the bottom of the tank body 1. When the high-efficiency gas-liquid separation device stops working, the blade separator 8 can be flushed by accessing the cleaning liquid through the first flushing port 24, the middle part of the inner wall of the tank body 1 can be flushed by accessing the cleaning liquid through the second flushing port 25, and the inner bottom of the tank body 1 can be flushed by accessing the cleaning liquid through the third flushing port 26.
The invention is not limited to the above-described alternative embodiments, and any person who may derive other various forms of products in the light of the present invention, however, any changes in shape or structure thereof, all falling within the technical solutions defined in the scope of the claims of the present invention, fall within the scope of protection of the present invention.
Claims (10)
1. A high-efficient gas-liquid separation device, its characterized in that: comprises a tank body (1) which is transversely arranged, wherein an air inlet (2), a liquid outlet (3) and an air outlet (4) are arranged on the tank body (1); a baffle plate (5), a baffle plate and a blade separator (8) are arranged in the tank body (1); the tank body (1) is divided into a gas cavity (9) and a liquid accumulation cavity (10) by the partition plate, the baffle plate (5) and the blade separator (8) are arranged in the gas cavity (9), the baffle plate (5) and the air inlet (2) are oppositely arranged, the blade separator (8) is connected with the air outlet (4), and a flow guide pipe (11) connected with the liquid accumulation cavity (10) is arranged at the bottom of the blade separator (8); the baffle plate comprises a first inclined plate (6) and a second inclined plate (7), the first inclined plate (6) is positioned below the baffle plate (5), the lower end of the first inclined plate (6) is adjacent to the lower end of the second inclined plate (7), a gap is formed between the lower end of the first inclined plate and the lower end of the second inclined plate, and a liquid leakage groove (12) is formed in the gap; the first sloping plate (6) and the second sloping plate (7) are both provided with a flow baffle (13), and the lower end of the flow baffle (13) is provided with a liquid leakage hole.
2. The efficient gas-liquid separation apparatus according to claim 1, wherein: the lower end of the flow guide pipe (11) is positioned below the liquid level of the liquid accumulation cavity (10), a liquid discharge valve is arranged at the liquid outlet (3), a liquid level sensor (14) is arranged in the liquid accumulation cavity (10), the liquid discharge valve and the liquid level sensor (14) are connected with a controller, and the controller controls the liquid level sensor (14) to be normally opened and controls the liquid discharge valve to be normally closed; the liquid level sensor (14) is used for collecting the liquid level value in the effusion cavity (10) in real time and recording the liquid level value as a real-time liquid level value; when the real-time liquid level value acquired by the liquid level sensor (14) is larger than the upper limit value of the standard liquid level range, the controller controls the liquid discharge valve to be opened for liquid discharge until the real-time liquid level value acquired by the liquid level sensor (14) is smaller than the lower limit value of the standard liquid level range, and the controller controls the liquid discharge valve to be closed.
3. The efficient gas-liquid separation apparatus according to claim 2, wherein: the lead (15) of the liquid level sensor (14) penetrates out of the circuit leading-out cylinder (16) of the tank body (1), a sealing cylinder (17) is arranged in the circuit leading-out cylinder (16), a first limiting piece (18) and a rubber piece (19) are arranged in the sealing cylinder (17), a sealing cover (21) is arranged on the circuit leading-out cylinder (16), the sealing cover (21) is in pressure contact with the outer end of the sealing cylinder (17), the sealing cylinder (17) is in pressure contact with the outer end of the first limiting piece (18), the first limiting piece (18) is in pressure contact with the outer end of the rubber piece (19), and the lead (15) penetrates through the rubber piece (19), the first limiting piece (18), the sealing cylinder (17) and the sealing cover (21).
4. A high efficiency gas-liquid separation apparatus according to claim 3, wherein: the rubber part (19), the first limiting part (18), the sealing cylinder (17) and the sealing cover (21) are provided with wire guide holes, and the wire guide holes are sealed and attached with the wires (15) after the rubber part (19) is pressed and deformed.
5. A high efficiency gas-liquid separation apparatus according to claim 3, wherein: the sealing cylinder (17) is internally provided with a second limiting piece (20), the inner end of the second limiting piece (20) is abutted with a circle of step in the circuit leading-out cylinder (16), and the outer end of the second limiting piece is contacted with the inner end of the rubber piece (19).
6. The efficient gas-liquid separation apparatus according to claim 5, wherein: the inner end of the sealing cylinder (17) is abutted against a circle of steps in the circuit leading-out cylinder (16), and a sealing ring (23) opposite to the steps is arranged on the sealing cylinder (17).
7. The efficient gas-liquid separation apparatus according to claims 3 to 6, characterized in that: the sealing cover (21) is connected with the circuit leading-out cylinder (16) through an adjusting bolt (22).
8. The efficient gas-liquid separation apparatus according to claim 1, wherein: the novel solar energy tank is characterized in that a first flushing port (24), a second flushing port (25) and a third flushing port (26) are arranged on the tank body (1), the first flushing port (24) and the blade separator (8) are oppositely arranged, the second flushing port (25) is arranged in the middle of the tank body (1), and the third flushing port (26) is arranged at the bottom of the tank body (1).
9. The efficient gas-liquid separation apparatus according to claim 1, wherein: the air inlet (2) is connected with the outlet of the reaction kettle, the liquid outlet (3) is connected with the inlet of the reaction kettle, and the air outlet (4) is connected with the condenser.
10. The efficient gas-liquid separation apparatus according to claim 1, wherein: the flow baffle plates on the first inclined plate (6) are parallel to each other, and the flow baffle plates on the second inclined plate (7) are parallel to each other.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202311503478.1A CN117504446B (en) | 2023-11-13 | 2023-11-13 | High-efficient gas-liquid separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202311503478.1A CN117504446B (en) | 2023-11-13 | 2023-11-13 | High-efficient gas-liquid separation device |
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| Publication Number | Publication Date |
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| CN117504446A true CN117504446A (en) | 2024-02-06 |
| CN117504446B CN117504446B (en) | 2024-06-18 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202311503478.1A Active CN117504446B (en) | 2023-11-13 | 2023-11-13 | High-efficient gas-liquid separation device |
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| CN212757890U (en) * | 2020-07-31 | 2021-03-23 | 山东兴泰机械装备工程有限责任公司 | High-efficiency gas-liquid separator |
| CN216498322U (en) * | 2021-11-11 | 2022-05-13 | 杰瑞石油天然气工程有限公司 | Gas-liquid separator |
| CN114939307A (en) * | 2022-06-24 | 2022-08-26 | 中钢集团天澄环保科技股份有限公司 | Gas-liquid separator |
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2023
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN206369082U (en) * | 2016-08-31 | 2017-08-01 | 中石化石油工程技术服务有限公司 | A kind of gas collector and delivery pipe hydrops capturing device |
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| CN212757890U (en) * | 2020-07-31 | 2021-03-23 | 山东兴泰机械装备工程有限责任公司 | High-efficiency gas-liquid separator |
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Also Published As
| Publication number | Publication date |
|---|---|
| CN117504446B (en) | 2024-06-18 |
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