CN220656498U - Gas-liquid separation device - Google Patents
Gas-liquid separation device Download PDFInfo
- Publication number
- CN220656498U CN220656498U CN202322226128.7U CN202322226128U CN220656498U CN 220656498 U CN220656498 U CN 220656498U CN 202322226128 U CN202322226128 U CN 202322226128U CN 220656498 U CN220656498 U CN 220656498U
- Authority
- CN
- China
- Prior art keywords
- baffle plate
- separation
- plate
- baffle
- flow channel
- 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.)
- Active
Links
- 238000000926 separation method Methods 0.000 title claims abstract description 152
- 239000007788 liquid Substances 0.000 title claims abstract description 62
- 238000007789 sealing Methods 0.000 claims abstract description 15
- 238000005452 bending Methods 0.000 description 16
- 238000005191 phase separation Methods 0.000 description 8
- 238000004140 cleaning Methods 0.000 description 7
- 239000012071 phase Substances 0.000 description 5
- 239000007791 liquid phase Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000002035 prolonged effect Effects 0.000 description 3
- 238000010276 construction Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 230000008093 supporting effect Effects 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
Abstract
The utility model provides a gas-liquid separation device, which comprises a separation main body, a baffle device and an end enclosure, wherein the separation main body is provided with a separation cavity; the baffle device is arranged at the upper part of the separation cavity and comprises a first baffle plate, a second baffle plate, a third baffle plate and a bottom plate, one side edges of the first baffle plate, the second baffle plate and the third baffle plate are connected together, the other side edges of the first baffle plate, the second baffle plate and the third baffle plate are respectively and detachably connected with the side wall of the separation cavity, and the upper space of the separation cavity is divided into a first runner, a second runner and a third runner by the first baffle plate, the second baffle plate and the third baffle plate; the upper end of the second baffle plate is provided with an upper notch, the upper notch is used for communicating the first flow channel with the second flow channel, the lower end of the third baffle plate is provided with a lower notch, the lower notch is used for communicating the second flow channel with the third flow channel, and the bottom plate is used for sealing the lower ends of the second flow channel and the third flow channel; the head detachably sets up in the upper end of separation main part.
Description
Technical Field
The utility model relates to the technical field of gas-liquid separation, in particular to a gas-liquid separation device.
Background
The MVR evaporator utilizes the steam compressor to do work on the secondary steam, the pressure and the temperature of the secondary steam are improved, the heated steam can be used as evaporation heat source steam again, the process is repeated continuously, and the continuous evaporation process is ensured. In this process, a gas-liquid separation chamber is required to perform gas-liquid separation of steam. In the existing gas-liquid separation chamber, the height is generally more than 3 meters, and the height is increased along with the increase of the treatment capacity so as to ensure that the gas-phase separation height and the liquid-phase separation height meet the requirements, however, the problems of increased equipment occupation height, increased manufacturing cost, difficult transportation and the like are caused.
At present, although a solution is provided for increasing the gas-liquid separation path without increasing the equipment height by adding a plurality of parallel baffles distributed along the horizontal direction, the parallel baffles are required to be welded inside the cylinder and at the top of the sealing head respectively to form a plurality of steam flow channels, the problem of inconvenient disassembly and cleaning exists, and the space between the parallel baffles is required to control the volume of each channel to calculate a reasonable space. In addition, when the number of baffles is increased, the distance is reduced, and the cleaning is not easy.
Therefore, it is necessary to provide a gas-liquid separation apparatus which can shorten the overall height of the apparatus and facilitate cleaning of the inside of the apparatus while satisfying the gas-phase separation height and the liquid-phase separation height.
Disclosure of Invention
The utility model aims to provide a gas-liquid separation device, which can shorten the overall height of the device and facilitate cleaning the inside of the device under the condition of meeting the gas-phase separation height and the liquid-phase separation height.
In order to achieve the above purpose, the utility model provides a gas-liquid separation device, which comprises a separation main body, a baffle device and an end enclosure, wherein a separation cavity with an upward opening is arranged in the separation main body, and a liquid inlet communicated with the separation cavity is arranged on the side wall of the separation main body; the baffle device is arranged at the upper part of the separation cavity and comprises a first baffle plate, a second baffle plate, a third baffle plate and a bottom plate, one side edge of the first baffle plate, one side edge of the second baffle plate and one side edge of the third baffle plate are connected together, the other side edge of the first baffle plate, the other side edge of the second baffle plate and the other side edge of the third baffle plate are respectively and detachably connected with the side wall of the separation cavity, and the first baffle plate, the second baffle plate and the third baffle plate divide the upper space of the separation cavity into a first flow passage between the first baffle plate and the second baffle plate, a second flow passage between the second baffle plate and the third baffle plate and a third flow passage between the third baffle plate and the first baffle plate along the circumferential direction of the separation cavity; the upper end of the second baffle plate is provided with an upper notch, the upper notch is used for communicating the first flow channel with the second flow channel, the lower end of the third baffle plate is provided with a lower notch, the lower notch is used for communicating the second flow channel with the third flow channel, and the bottom plate is connected to the lower ends of the first baffle plate and the third baffle plate and seals the lower ends of the second flow channel and the third flow channel; the seal head is detachably arranged at the upper end of the separation main body and seals the opening, and is provided with an exhaust outlet communicated with the third flow passage.
Preferably, the side wall of the separation main body is also provided with a liquid outlet communicated with the separation cavity, the liquid inlet and the liquid outlet are both positioned below the baffle device, and the bottom of the separation main body is provided with a concentrated liquid outlet communicated with the separation cavity.
Preferably, the other side edge of the first baffle plate is bent to form a first bending part which is attached to the side wall of the separation cavity, the other side edge of the second baffle plate is bent to form a second bending part which is attached to the side wall of the separation cavity, and the other side edge of the third baffle plate is bent to form a third bending part which is attached to the side wall of the separation cavity.
Preferably, contact surfaces of the first bending part, the second bending part and the third bending part, which are in contact with the side wall of the separation cavity, are smooth surfaces.
Preferably, the sides of the first baffle plate, the second baffle plate and the third baffle plate are connected together in a mutually rotatable and adjustable way.
Preferably, the bottom plate is bent downwards towards the edge of the side wall of the separation cavity to form a fourth bending part which is attached to the side wall of the separation cavity.
Preferably, a contact surface of the fourth bending portion, which is in contact with the side wall of the separation cavity, is a smooth surface.
Preferably, the baffle device further comprises a fixing plate and a demisting net, wherein the fixing plate is fixedly connected to the upper end of the third baffle plate and the upper end of the first baffle plate, the fixing plate is in contact connection with the side wall of the separation cavity, the fixing plate is used for blocking the upper end of the third flow channel, a steam port communicated with the third flow channel is formed in the fixing plate, and the demisting net is arranged on the fixing plate and located above the steam port.
Preferably, the baffle device further comprises a sealing plate and a top plate, the sealing plate is fixed on the fixing plate and surrounds the demisting net, the fixing plate is fixed at the upper end of the sealing plate, independent spaces are formed in the sealing plate, the top plate and the fixing plate in a surrounding mode, and an exhaust pipe orifice communicated between the independent spaces and the exhaust outlet is formed in the top plate.
Preferably, the gas-liquid separation device further comprises a support plate, wherein the support plate is fixed on the side wall of the separation cavity, and the bottom plate is placed on the support plate.
Compared with the prior art, the gas-liquid separation device has the advantages that the baffle device is arranged at the upper part of the separation cavity of the separation main body, one side edges of the first baffle plate, the second baffle plate and the third baffle plate of the baffle device are connected together, and the other side edges of the first baffle plate, the second baffle plate and the third baffle plate are respectively and detachably connected with the side wall of the separation cavity, so that the baffle device can be detached from the separation main body, and the separation cavity of the separation main body can be conveniently cleaned; the first baffle plate, the second baffle plate and the third baffle plate divide the upper space of the separation cavity into a first flow passage positioned between the first baffle plate and the second baffle plate, a second flow passage positioned between the second baffle plate and the third baffle plate and a third flow passage positioned between the third baffle plate and the first baffle plate along the circumferential direction of the separation cavity; the upper end of the second baffle plate is provided with an upper notch, the upper notch is used for communicating the first flow channel with the second flow channel, the lower end of the third baffle plate is provided with a lower notch, the lower notch is used for communicating the second flow channel with the third flow channel, the bottom plate is connected to the lower ends of the first baffle plate and the third baffle plate and seals the lower ends of the second flow channel and the third flow channel, so that after gas-liquid separation is carried out on liquid entering the separation cavity through the liquid inlet, steam can firstly rise to enter the first flow channel, rise to the top and then enter the second flow channel through the upper notch, then move downwards and enter the third flow channel through the lower notch and then rise to the top to be discharged, the path of the steam is prolonged, the separation height of the gas phase is increased, and the height of the gas phase of equipment is greatly reduced at the moment. Therefore, the gas-liquid separation device can shorten the overall height of the device and facilitate cleaning the inside of the device under the condition of meeting the gas-phase separation height and the liquid-phase separation height.
Drawings
FIG. 1 is a schematic diagram of a gas-liquid separator according to the present utility model.
FIG. 2 is a schematic view of the gas-liquid separator of the present utility model at the location of the baffle device.
FIG. 3 is a block diagram of another embodiment of a baffle device of a gas-liquid separation apparatus of the present utility model.
FIG. 4 is a partial block diagram of the baffle arrangement shown in FIG. 3.
FIG. 5 is a partial construction view of a gas-liquid separation apparatus according to the present utility model.
FIG. 6 is a view showing the construction of the bottom plate of the baffle device of the gas-liquid separator of the present utility model when it is placed on the support plate.
Detailed Description
In order to describe the technical content and constructional features of the present utility model in detail, the following description will be made with reference to the embodiments in conjunction with the accompanying drawings.
Referring to fig. 1 and 2, a gas-liquid separation device 100 of the present utility model includes a separation body 1, a baffle device 2 and a seal head 3, wherein a separation cavity 11 with an upward opening is arranged in the separation body 1, and a liquid inlet 12 communicating with the separation cavity 11 is arranged on a side wall of the separation body 1; the baffle device 2 is arranged at the upper part of the separation cavity 11, the baffle device 2 comprises a first baffle plate 21, a second baffle plate 22, a third baffle plate 23 and a bottom plate 24, one side edge of the first baffle plate 21, one side edge of the second baffle plate 22 and one side edge of the third baffle plate 23 are connected together, the other side edge of the first baffle plate 21, the other side edge of the second baffle plate 22 and the other side edge of the third baffle plate 23 are respectively and detachably connected with the side wall of the separation cavity 11, and the first baffle plate 21, the second baffle plate 22 and the third baffle plate 23 divide the upper space of the separation cavity 11 into a first flow passage 251 between the first baffle plate 21 and the second baffle plate 22, a second flow passage 252 between the second baffle plate 22 and the third baffle plate 23 and a third flow passage 253 between the third baffle plate 23 and the third baffle plate 21 along the circumferential direction of the separation cavity 11; the upper end of the second baffle 22 is provided with an upper notch 221, the upper notch 221 communicates the first flow channel 251 with the second flow channel 252, the lower end of the third baffle 23 is provided with a lower notch 231, the lower notch 231 communicates the second flow channel 252 with the third flow channel 253, and the bottom plate 24 is connected to the lower ends of the first baffle 21 and the third baffle 23 and seals the lower ends of the second flow channel 252 and the third flow channel 253; the head 3 is detachably provided at the upper end of the separation body 1 and closes the opening, and the head 3 is provided with an exhaust outlet 31 communicating with the third flow passage 253.
After the liquid entering the separation chamber 11 through the liquid inlet 12 is separated into gas and liquid, the steam can rise into the first flow channel 251, rise to the top and then enter the second flow channel 252 through the upper notch 221, then move downwards and enter the third flow channel 253 through the lower notch 231, rise to the top and be discharged, so that the path of the steam is prolonged, and the separation height of the gas phase is increased. The other side edges of the first baffle plate 21, the second baffle plate 22 and the third baffle plate 23 are respectively detachably connected with the side wall of the separation cavity 11, so that the baffle device 2 can be detached from the separation main body 1, thereby facilitating the cleaning of the separation cavity 11 of the separation main body 1.
Referring to fig. 1, in the present embodiment, a liquid outlet 13 is further disposed on a side wall of the separation body 1 and is communicated with the separation cavity 11, the liquid inlet 12 and the liquid outlet 13 are both disposed below the baffle device 2, and a concentrate outlet 14 is disposed at the bottom of the separation body 1 and is communicated with the separation cavity 11.
Referring to fig. 3, in one embodiment, the other side edge of the first baffle 21 is bent to form a first bending portion 211 that is attached to the sidewall of the separation chamber 11, the other side edge of the second baffle 22 is bent to form a second bending portion 222 that is attached to the sidewall of the separation chamber 11, and the other side edge of the third baffle 23 is bent to form a third bending portion (not shown) that is attached to the sidewall of the separation chamber 11. By providing the first curved portion 211, the second curved portion 222 and the third curved portion, the first baffle 21, the second baffle 22 and the third baffle 23 can be tightly attached to the sidewall of the separation chamber 11. Specifically, the first curved portion 211, the second curved portion 222, and the third curved portion are curved in the same direction. Further, the contact surfaces of the first curved portion 211, the second curved portion 222 and the third curved portion, which are in contact with the side wall of the separation chamber 11, are smooth surfaces, so that friction resistance applied when the baffle device 2 is detached from the separation main body 1 is reduced, and the side edges of the baffle plates are prevented from wearing the side wall of the separation chamber 11.
Referring to fig. 2, in one embodiment, the sides of the first baffle 21, the second baffle 22 and the third baffle 23 are rotatably and adjustably connected to each other. By rotating and adjusting the included angles among the first baffle plate 21, the second baffle plate 22 and the third baffle plate 23, the cross sectional areas of the first flow channel 251, the second flow channel 252 and the third flow channel 253 are the same or are changed from small to large, and the phenomenon that the flow velocity is increased due to the fact that the cross sectional areas of the first flow channel 251, the second flow channel 252 or the third flow channel 253 suddenly become small is avoided, so that the effect of gas-liquid separation of steam located in the first flow channel 251, the second flow channel 252 or the third flow channel 253 is avoided. For example, the first baffle 21, the second baffle 22 and the third baffle 23 may be rotatably connected by a rotation shaft, and the rotation shaft may be fixed at the center of the bottom plate 24, but is not limited to this structure. In other embodiments, the sides of the first baffle 21, the second baffle 22 and the third baffle 23 may be fixed together by designing the angles between the first baffle 21, the second baffle 22 and the third baffle 23.
Referring to fig. 3, in an embodiment, the bottom plate 24 is bent downward toward the edge of the sidewall of the separation chamber 11 to form a fourth bending portion 241 that is attached to the sidewall of the separation chamber 11. By providing the fourth bending portion 241, the bottom plate 24 can be closely attached to the side wall of the separation chamber 11. Further, the contact surface of the fourth bending portion 241 with the side wall of the separation chamber 11 is a smooth surface, so that friction resistance applied when the baffle device 2 is detached from the separation main body 1 is reduced, and the side edge of the bottom plate 24 is prevented from wearing the side wall of the separation chamber 11.
Referring to fig. 3 and 4, in an embodiment, the baffle device 2 further includes a fixing plate 26 and a demisting net 27, the fixing plate 26 is fixedly connected to the upper end of the third baffle 23 and the upper end of the first baffle 21, the fixing plate 26 is connected to the sidewall of the separation chamber 11 in a contact manner, the fixing plate 26 seals the upper end of the third flow channel 253, a steam port (not shown) communicating with the third flow channel 253 is provided on the fixing plate 26, and the demisting net 27 is disposed on the fixing plate 26 and above the steam port. By providing the demister net 27, the steam passing upward from the steam port is purified.
Referring to fig. 4, in an embodiment, the baffle device 2 further includes a sealing plate 28 and a top plate 29, the sealing plate 28 is fixed on the fixing plate 26 and is disposed around the demisting net 27, the fixing plate 26 is fixed on an upper end of the sealing plate 28, the top plate 29 and the fixing plate 26 enclose an independent space, and an exhaust nozzle 291 communicating between the independent space and the exhaust outlet 31 is provided on the top plate 29. An independent space is enclosed by the sealing plate 28 and the top plate 29, and the demister net 27 is positioned in the independent space, so that the steam passing through the demister net 27 is ensured not to be polluted. The steam passes through the demister mesh 27 and enters the independent space, and is then discharged from the exhaust nozzle 291 of the top plate 29.
Referring to fig. 5 and 6, in an embodiment, the gas-liquid separation apparatus 100 of the present utility model further includes a support plate 4, the support plate 4 is fixed on a sidewall of the separation chamber 11, and the bottom plate 24 is disposed on the support plate 4. The baffle 2 may be inserted directly into the upper portion of the separation chamber 11 and placed on the support plate 4, and the bottom plate 24 is supported by the support plate 4, thereby directly supporting the baffle 2. When the baffle device 2 needs to be disassembled, the baffle device 2 can be directly pulled out from the separation main body 1. Specifically, the fourth bending portion 241 at the edge of the bottom plate 24 is directly contacted with the support plate 4, and a corresponding and larger notch is cut at the direct contact portion of the support plate 4 for plugging the fourth bending portion 241 at the edge of the bottom plate 24. By providing the support plate 4, a supporting effect can be met, and a slight rotation space can be reserved for withdrawing the baffle device 2.
Referring to fig. 1 to 6, the specific operation principle of the gas-liquid separation apparatus 100 of the present utility model is as follows:
after circulating liquid enters the middle position of the separation cavity 11 through the liquid inlet 12 and is subjected to gas-liquid separation, separated steam can firstly rise into the first flow channel 251, rise to the top and then enter the second flow channel 252 through the upper notch 221, then move downwards and enter the third flow channel 253 through the lower notch 231 and rise to the top, then pass through the demisting net 27 from the steam port, and the purified steam enters the independent space and is discharged through the exhaust pipe orifice 291 of the top plate 29 and the exhaust outlet 31 of the sealing head 3. When the baffle device 2 needs to be disassembled, the end socket 3 can be disassembled, and then the baffle device 2 is directly extracted so as to be convenient for cleaning.
In summary, the first baffle plate 21, the second baffle plate 22 and the third baffle plate 23 of the gas-liquid separation apparatus 100 of the present utility model divide the upper space of the separation chamber 11 into a first flow channel 251 between the first baffle plate 21 and the second baffle plate 22, a second flow channel 252 between the second baffle plate 22 and the third baffle plate 23 and a third flow channel 253 between the third baffle plate 23 and the first baffle plate 21 along the circumferential direction of the separation chamber 11; the upper end of the second baffle 22 is provided with an upper notch 221, the upper notch 221 communicates the first flow channel 251 and the second flow channel 252, the lower end of the third baffle 23 is provided with a lower notch 231, the lower notch 231 communicates the second flow channel 252 and the third flow channel 253, and the bottom plate 24 is connected to the lower ends of the first baffle 21 and the third baffle 23 and seals the lower ends of the second flow channel 252 and the third flow channel 253, so that after gas-liquid separation is performed on the liquid entering the separation cavity 11 through the liquid inlet 12, steam can rise into the first flow channel 251, rise to the top and then enter the second flow channel 252 through the upper notch 221, then move downwards and enter the third flow channel 253 through the lower notch 231 and rise to the top to be discharged, the path of the steam is prolonged, the separation height of the gas phase of the device is increased, and the height of the gas phase of the device is greatly reduced at this time. Next, in the gas-liquid separation device 100 of the present utility model, the baffle device 2 is disposed at the upper portion of the separation chamber 11 of the separation main body 1, and one side edges of the first baffle plate 21, the second baffle plate 22 and the third baffle plate 23 of the baffle device 2 are connected together, so that the other side edges of the first baffle plate 21, the second baffle plate 22 and the third baffle plate 23 are respectively detachably connected to the side walls of the separation chamber 11, thereby the baffle device 2 can be detached from the separation main body 1, so that the separation chamber 11 of the separation main body 1 can be cleaned conveniently. The contact surfaces of the first curved portion 211, the second curved portion 222, the third curved portion and the fourth curved portion 241 with the side wall of the separation chamber 11 are smooth surfaces, so that friction resistance applied when the baffle device 2 is detached from the separation body 1 is reduced, and the side edges of the baffle plate and the side edges of the bottom plate 24 are prevented from wearing the side wall of the separation chamber 11. In addition, the sizes of the first flow channel 251, the second flow channel 252 and the third flow channel 253 can be directly adjusted by changing the included angles of the first flow channel 251, the second flow channel 252 and the third flow channel 253, the number of the first baffle plates 21, the second baffle plates 22 and the third baffle plates 23 can be increased, the number of baffle plates formed by combining the first baffle plates 21, the second baffle plates 22 and the third baffle plates 23 can be odd plates larger than 3, the number of baffle plates is increased, and the height of the separation chamber is reduced.
The foregoing disclosure is only illustrative of the preferred embodiments of the present utility model and is not to be construed as limiting the scope of the utility model, which is defined by the appended claims.
Claims (10)
1. A gas-liquid separation apparatus, comprising:
the separation device comprises a separation main body, wherein a separation cavity with an upward opening is arranged in the separation main body, and a liquid inlet communicated with the separation cavity is arranged on the side wall of the separation main body;
the baffle device is arranged at the upper part of the separation cavity and comprises a first baffle plate, a second baffle plate, a third baffle plate and a bottom plate, one side edge of the first baffle plate, one side edge of the second baffle plate and one side edge of the third baffle plate are connected together, the other side edge of the first baffle plate, the other side edge of the second baffle plate and the other side edge of the third baffle plate are respectively and detachably connected with the side wall of the separation cavity, and the first baffle plate, the second baffle plate and the third baffle plate divide the upper space of the separation cavity into a first flow passage between the first baffle plate and the second baffle plate, a second flow passage between the second baffle plate and the third baffle plate and a third flow passage between the third baffle plate and the first baffle plate along the circumferential direction of the separation cavity; the upper end of the second baffle plate is provided with an upper notch, the upper notch is used for communicating the first flow channel with the second flow channel, the lower end of the third baffle plate is provided with a lower notch, the lower notch is used for communicating the second flow channel with the third flow channel, and the bottom plate is connected to the lower ends of the first baffle plate and the third baffle plate and seals the lower ends of the second flow channel and the third flow channel;
the seal head is detachably arranged at the upper end of the separation main body and seals the opening, and the seal head is provided with an exhaust outlet communicated with the third flow passage.
2. The gas-liquid separation device according to claim 1, wherein a liquid outlet communicated with the separation cavity is further formed in the side wall of the separation main body, the liquid inlet and the liquid outlet are both located below the baffle device, and a concentrated liquid outlet communicated with the separation cavity is formed in the bottom of the separation main body.
3. The gas-liquid separation apparatus of claim 1, wherein the other side edge of the first baffle plate is curved to form a first curved portion that conforms to the sidewall of the separation chamber, the other side edge of the second baffle plate is curved to form a second curved portion that conforms to the sidewall of the separation chamber, and the other side edge of the third baffle plate is curved to form a third curved portion that conforms to the sidewall of the separation chamber.
4. A gas-liquid separation apparatus according to claim 3, wherein contact surfaces of the first curved portion, the second curved portion, and the third curved portion with the side wall of the separation chamber are smooth surfaces.
5. The gas-liquid separation apparatus of claim 1, wherein the sides of the first baffle, the second baffle, and the third baffle are rotatably adjustably coupled to one another.
6. The gas-liquid separation apparatus according to claim 1, wherein the bottom plate is bent downward toward an edge of the separation chamber side wall to form a fourth bent portion that is fitted to the separation chamber side wall.
7. The gas-liquid separation apparatus according to claim 6, wherein a contact surface of the fourth curved portion with the side wall of the separation chamber is a smooth surface.
8. The gas-liquid separation device according to claim 1, wherein the baffle device further comprises a fixing plate and a demisting net, the fixing plate is fixedly connected to the upper end of the third baffle plate and the upper end of the first baffle plate, the fixing plate is in contact connection with the side wall of the separation cavity, the fixing plate seals the upper end of the third flow channel, a steam port communicated with the third flow channel is formed in the fixing plate, and the demisting net is arranged on the fixing plate and located above the steam port.
9. The gas-liquid separation device of claim 8, wherein the baffle device further comprises a sealing plate and a top plate, the sealing plate is fixed on the fixing plate and is arranged around the demisting net, the fixing plate is fixed on the upper end of the sealing plate, independent spaces are surrounded by the sealing plate, the top plate and the fixing plate, and an exhaust pipe orifice communicated between the independent spaces and the exhaust outlet is arranged on the top plate.
10. The gas-liquid separation apparatus according to claim 1, further comprising a support plate fixed to a side wall of the separation chamber, the bottom plate being placed on the support plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322226128.7U CN220656498U (en) | 2023-08-17 | 2023-08-17 | Gas-liquid separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322226128.7U CN220656498U (en) | 2023-08-17 | 2023-08-17 | Gas-liquid separation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220656498U true CN220656498U (en) | 2024-03-26 |
Family
ID=90330252
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322226128.7U Active CN220656498U (en) | 2023-08-17 | 2023-08-17 | Gas-liquid separation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220656498U (en) |
-
2023
- 2023-08-17 CN CN202322226128.7U patent/CN220656498U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4434112A (en) | Heat transfer surface with increased liquid to air evaporative heat exchange | |
| US5727623A (en) | Dehumidifier having two heat exchangers | |
| CN103604258A (en) | Liquid-discharged gas-liquid separator | |
| US20120175091A1 (en) | Distribution system and heat exchanger apparatus | |
| KR20130047683A (en) | Device for compressing and drying gas | |
| JP4564177B2 (en) | Gas processing equipment | |
| CN203083207U (en) | Gas-liquid separation falling film type evaporator | |
| CN103062962B (en) | Gas-liquid separative falling film type evaporator | |
| EP1167910A3 (en) | Condenser | |
| JP3100372B1 (en) | Heat exchanger | |
| CN220656498U (en) | Gas-liquid separation device | |
| JP3990202B2 (en) | Internal heat exchange distillation column | |
| CN207365504U (en) | Heat exchanger package, heat exchanger and air conditioner | |
| US11236932B2 (en) | Evaporator and a method for vaporizing a substance in an evaporator | |
| CN211147362U (en) | Heat exchange dewatering structure of compressed gas dryer | |
| CN209630819U (en) | A kind of high efficiency furnace gas disposal spray column | |
| CN211435156U (en) | Novel high-efficient vacuum cold trap | |
| CN210495296U (en) | Ethanol steam recovery device | |
| JP2005009750A (en) | Filler unit used in closed type cross flow heat exchange tower, closed type cross flow heat exchange tower loaded with filler unit, and replacement method for filler unit | |
| CN209959465U (en) | Horizontal liquid separator, compressor comprising same and electric appliance | |
| CN207703068U (en) | A kind of tubular heat exchanger | |
| CN206739682U (en) | Heat exchanger and heat transmission equipment for heat transmission equipment | |
| CN214148930U (en) | Novel heat exchange plate | |
| CN202113722U (en) | Gas-liquid exchange device based on gas throttling | |
| RU2480699C2 (en) | Heat and mass exchange equipment with combined scheme of interaction of gas and liquid flows |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |