CN219390155U - Dual-vertical gas-liquid separator ammonia separation plate exchange pry block - Google Patents
Dual-vertical gas-liquid separator ammonia separation plate exchange pry block Download PDFInfo
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- CN219390155U CN219390155U CN202320002142.6U CN202320002142U CN219390155U CN 219390155 U CN219390155 U CN 219390155U CN 202320002142 U CN202320002142 U CN 202320002142U CN 219390155 U CN219390155 U CN 219390155U
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Abstract
The utility model relates to an ammonia separating plate exchanging pry block of a double vertical gas-liquid separator, which is formed by connecting a first-stage vertical gas-liquid separator, a second-stage vertical gas-liquid separator and a plate heat exchanger through pipelines, wherein the vertical gas-liquid separator is arranged above the plate heat exchanger; the pipeline comprises a pipeline III for connecting a liquid port of the primary vertical gas-liquid separator/a liquid port of the secondary vertical gas-liquid separator with a cooling medium inlet of the plate heat exchanger; the pipeline III is formed by three sections of pipe connection, and first section pipe is on, is horizontal pipe, and second section pipe is on, is standpipe, third section pipe is down, is horizontal pipe, is provided with on the first section pipe and connects the inlet with the vertical gas-liquid separator liquid mouth of one-level/the vertical gas-liquid separator liquid mouth of second grade, is provided with on the third section pipe and is connected the liquid outlet with plate heat exchanger cooling medium access connection, and the second section pipe is the liquid pipe and is located vertical gas-liquid separator below, and its upper port is level sensor installing port, installs level sensor in the level sensor installing port.
Description
Technical Field
The utility model relates to an ammonia separation plate exchange skid block, in particular to an ammonia separation plate exchange skid block of a double-vertical gas-liquid separator.
Background
The ammonia separating plate prying block is mainly used for cooling water, alcohol, ethanol, beer and other cold-carrying media, and is relatively suitable for the food industry with high requirements on sanitary cleanliness.
The traditional ammonia separation plate prying block is designed by using a single horizontal vertical gas-liquid separator or a vertical gas-liquid separator, and has the defect of larger ammonia storage amount or higher overall height, and if the overall height is higher, the injection amount of cooling medium is necessarily required to be larger.
Disclosure of Invention
In order to solve the problems, the utility model provides an ammonia separating plate exchange pry block of a double-vertical gas-liquid separator, which avoids ammonia storage and greatly reduces the whole height.
The technical scheme of the utility model is as follows:
the ammonia separation plate exchange skid block of the double vertical gas-liquid separator is formed by connecting a vertical gas-liquid separator and a plate heat exchanger through a pipeline, and the vertical gas-liquid separator is arranged above the plate heat exchanger; the two vertical gas-liquid separators are respectively a first-stage vertical gas-liquid separator and a second-stage vertical gas-liquid separator, and the pipeline comprises a pipeline I for connecting a cooling medium outlet of the plate heat exchanger with a liquid supplementing port of the first-stage vertical gas-liquid separator, a pipeline II for connecting a gas port of the first-stage vertical gas-liquid separator with a liquid supplementing port of the second-stage vertical gas-liquid separator, and a pipeline III for connecting a liquid port of the first-stage vertical gas-liquid separator/the second-stage vertical gas-liquid separator with a cooling medium inlet of the plate heat exchanger;
the pipeline III is formed by three sections of pipe connection, the first section of pipe is arranged on the upper side and is a horizontal pipe, the second section of pipe is arranged on the middle side and is a vertical pipe, the third section of pipe is arranged on the lower side and is a horizontal pipe, the first section of pipe is provided with a liquid inlet connected with a liquid port of the primary vertical gas-liquid separator/a liquid port of the secondary vertical gas-liquid separator, the third section of pipe is provided with a liquid outlet connected with a cooling medium inlet of the plate heat exchanger, the second section of pipe is a lower liquid pipe positioned below the vertical gas-liquid separator, an upper port of the second section of pipe is a liquid level sensor mounting port, and a liquid level sensor is mounted in the liquid level sensor mounting port.
The vertical gas-liquid separator comprises a shell and an umbrella-shaped baffle plate arranged in the shell, wherein the upper part of the shell is a cylinder, the lower part of the shell is a cone, an opening at the top of the shell is a gas port of the vertical gas-liquid separator, an opening at the bottom of the shell is a liquid port of the vertical gas-liquid separator, a tangential opening of the side wall of the shell is a liquid supplementing port of the vertical gas-liquid separator, the umbrella-shaped baffle plate is shielded above the opening at the bottom of the shell and below the tangential opening of the side wall of the shell, and a gap is reserved between the edge of the umbrella-shaped baffle plate and the inner wall of the shell.
The first-stage vertical gas-liquid separator and the second-stage vertical gas-liquid separator are staggered up and down, and the liquid supplementing port of the second-stage vertical gas-liquid separator is positioned above the gas port of the first-stage vertical gas-liquid separator.
The foam remover is arranged in the primary vertical gas-liquid separator and covers the gas port of the primary vertical gas-liquid separator.
The ammonia separation plate prying block further comprises a frame, wherein the frame is arranged above the plate heat exchanger, and the vertical gas-liquid separator is fixed and supported. The cooling medium adopted by the plate heat exchanger is ammonia or freon.
The utility model has the advantages that the design is reasonable, the structure is simple, and the two independent vertical gas-liquid separators are used for reducing the whole height, and can better ensure that no wet air return phenomenon occurs; the structure of the vertical gas-liquid separator is optimized, the size is reduced, and when the vertical gas-liquid separator is used, the liquid level in the liquid discharging pipe is monitored by the liquid level sensor so as to keep the vertical gas-liquid separator in an empty tank state, and the filling amount of the refrigerant is controlled to the utmost extent.
Drawings
FIG. 1 is a front view of an ammonia separation plate exchange skid of a dual vertical gas-liquid separator.
FIG. 2 is a side view of an ammonia separation plate exchange skid of a dual vertical gas-liquid separator.
FIG. 3 is a top view of an ammonia separation plate exchange skid of a dual vertical gas-liquid separator.
FIG. 4 is a schematic diagram of a primary vertical gas-liquid separator.
FIG. 5 is a schematic diagram of a two-stage vertical gas-liquid separator.
In the figure, a primary vertical gas-liquid separator 1, a shell 1-1, an umbrella-shaped baffle plate 1-2, a secondary vertical gas-liquid separator 2, a shell 2-1, an umbrella-shaped baffle plate 2-2, a plate heat exchanger 3, a pipeline I4, a pipeline II 5, a pipeline III 6, a first-section pipe 6-1, a second-section pipe 6-2, a third-section pipe 6-3, a liquid level sensor mounting port 7, a demister 8 and a frame 9.
Detailed Description
As shown in fig. 1-5, an ammonia separation plate exchange skid block of a double vertical gas-liquid separator is formed by connecting a vertical gas-liquid separator with a plate heat exchanger 3 through a pipeline, and the vertical gas-liquid separator is arranged above the plate heat exchanger; the two vertical gas-liquid separators are respectively a first-stage vertical gas-liquid separator 1 and a second-stage vertical gas-liquid separator 2, and the pipelines comprise a pipeline I4 for connecting a cooling medium outlet of the plate heat exchanger 3 with a liquid supplementing port of the first-stage vertical gas-liquid separator 1, a pipeline II 5 for connecting a gas port of the first-stage vertical gas-liquid separator 1 with a liquid supplementing port of the second-stage vertical gas-liquid separator 2, and a pipeline III 6 for connecting a liquid port of the first-stage vertical gas-liquid separator 1/a liquid port of the second-stage vertical gas-liquid separator 2 with a cooling medium inlet of the plate heat exchanger 3;
the pipeline III 6 is formed by connecting three sections of pipes, the first section of pipe 6-1 is an upper horizontal pipe, the second section of pipe 6-2 is a middle vertical pipe, the third section of pipe 6-3 is a lower horizontal pipe, the first section of pipe 6-1 is provided with a liquid inlet connected with a liquid inlet of the first-stage vertical gas-liquid separator 1/a liquid inlet of the second-stage vertical gas-liquid separator 2, the third section of pipe 6-3 is provided with a liquid outlet connected with a cooling medium inlet of the plate heat exchanger 3, the second section of pipe 6-2, namely a lower liquid pipe, is positioned below the first-stage vertical gas-liquid separator 1 and the second-stage vertical gas-liquid separator 2, the upper port of the second section of pipe is a liquid level sensor mounting port 7, and a liquid level sensor is mounted in the liquid level sensor mounting port 7;
the primary vertical gas-liquid separator 1 comprises a shell 1-1 and an umbrella-shaped baffle plate 1-2 arranged in the shell 1-1, wherein the upper part of the shell 1-1 is a cylinder, the lower part of the shell is a cone, the top opening of the shell 1-1 is a gas port of the primary vertical gas-liquid separator 1, the bottom opening of the shell 1-1 is a liquid port of the primary vertical gas-liquid separator 1, the tangential opening of the side wall of the shell 1-1 is a liquid supplementing port of the primary vertical gas-liquid separator 1, the umbrella-shaped baffle plate 1-2 is shielded above the opening at the bottom of the shell 1-1 and is positioned below the tangential opening of the side wall of the shell 1-1, and a gap is reserved between the edge of the umbrella-shaped baffle plate and the inner wall of the shell 1-1;
the secondary vertical gas-liquid separator 2 comprises a shell 2-1 and an umbrella-shaped baffle plate 2-2 arranged in the shell 2-1, wherein the upper part of the shell 2-1 is a cylinder, the lower part of the shell is a cone, the top opening of the shell 2-1 is a gas port of the secondary vertical gas-liquid separator 2, the bottom opening of the shell 2-1 is a liquid port of the secondary vertical gas-liquid separator 2, the tangential opening of the side wall of the shell 2-1 is a liquid supplementing port of the secondary vertical gas-liquid separator 2, the umbrella-shaped baffle plate 2-2 is shielded above the opening at the bottom of the shell 2-1 and is positioned below the tangential opening of the side wall of the shell 2-1, and a gap is reserved between the edge of the umbrella-shaped baffle plate and the inner wall of the shell 2-1;
the primary vertical gas-liquid separator 1 and the secondary vertical gas-liquid separator 2 are staggered up and down, and the liquid supplementing port of the secondary vertical gas-liquid separator 2 is positioned above the gas port of the primary vertical gas-liquid separator 1;
a foam remover 8 is arranged in the primary vertical gas-liquid separator 1, and the foam remover 8 covers the gas port of the primary vertical gas-liquid separator 1;
the ammonia separation plate exchange skid block further comprises a frame 9, wherein the frame 9 is arranged above the plate heat exchanger 3 and is used for fixing and supporting the primary vertical gas-liquid separator 1 and the secondary vertical gas-liquid separator 2;
the cooling medium adopted by the plate heat exchanger 3 is ammonia or freon.
While certain exemplary embodiments of the present utility model have been described above by way of illustration only, it will be apparent to those of ordinary skill in the art that modifications may be made to the described embodiments in various different ways without departing from the spirit and scope of the utility model. Accordingly, the drawings and description are to be regarded as illustrative in nature and not as restrictive of the scope of the utility model, which is defined by the appended claims.
Claims (6)
1. The ammonia separation plate exchange skid block of the double vertical gas-liquid separator is formed by connecting a vertical gas-liquid separator and a plate heat exchanger through a pipeline, and the vertical gas-liquid separator is arranged above the plate heat exchanger; the vertical gas-liquid separator is characterized in that the two vertical gas-liquid separators are a first-stage vertical gas-liquid separator and a second-stage vertical gas-liquid separator respectively, and the pipeline comprises a pipeline I for connecting a cooling medium outlet of the plate heat exchanger with a liquid supplementing port of the first-stage vertical gas-liquid separator, a pipeline II for connecting a gas port of the first-stage vertical gas-liquid separator with a liquid supplementing port of the second-stage vertical gas-liquid separator, and a pipeline III for connecting a liquid port of the first-stage vertical gas-liquid separator/a liquid port of the second-stage vertical gas-liquid separator with a cooling medium inlet of the plate heat exchanger;
the pipeline III is formed by three sections of pipe connection, the first section of pipe is arranged on the upper side and is a horizontal pipe, the second section of pipe is arranged on the middle side and is a vertical pipe, the third section of pipe is arranged on the lower side and is a horizontal pipe, the first section of pipe is provided with a liquid inlet connected with a liquid port of the primary vertical gas-liquid separator/a liquid port of the secondary vertical gas-liquid separator, the third section of pipe is provided with a liquid outlet connected with a cooling medium inlet of the plate heat exchanger, the second section of pipe is a lower liquid pipe positioned below the vertical gas-liquid separator, an upper port of the second section of pipe is a liquid level sensor mounting port, and a liquid level sensor is mounted in the liquid level sensor mounting port.
2. The ammonia separation plate exchange pry block of the double-vertical gas-liquid separator according to claim 1, wherein the vertical gas-liquid separator comprises a shell and an umbrella-shaped baffle plate arranged in the shell, the upper part of the shell is a cylinder, the lower part of the shell is a cone, the top opening of the shell is a vertical gas-liquid separator air port, the bottom opening of the shell is a vertical gas-liquid separator liquid port, the tangential opening of the side wall of the shell is a vertical gas-liquid separator liquid supplementing port, the umbrella-shaped baffle plate is shielded above the opening of the bottom of the shell and below the tangential opening of the side wall of the shell, and a gap is reserved between the edge of the umbrella-shaped baffle plate and the inner wall of the shell.
3. The ammonia separation plate exchange skid block of the double-vertical gas-liquid separator according to claim 2, wherein the primary vertical gas-liquid separator and the secondary vertical gas-liquid separator are staggered up and down, and the liquid supplementing port of the secondary vertical gas-liquid separator is positioned above the gas port of the primary vertical gas-liquid separator.
4. The ammonia separation plate prying block of the double-vertical gas-liquid separator according to claim 2, wherein a foam remover is arranged in the primary vertical gas-liquid separator and covers the gas port of the primary vertical gas-liquid separator.
5. The ammonia separation plate exchange skid of a dual vertical gas-liquid separator according to claim 1, further comprising a frame, wherein the frame is arranged above the plate heat exchanger, and is used for fixing and supporting the vertical gas-liquid separator.
6. The ammonia separation plate prying block of the double-vertical gas-liquid separator according to claim 1, wherein the cooling medium adopted by the plate heat exchanger is ammonia or freon.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320002142.6U CN219390155U (en) | 2023-01-03 | 2023-01-03 | Dual-vertical gas-liquid separator ammonia separation plate exchange pry block |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320002142.6U CN219390155U (en) | 2023-01-03 | 2023-01-03 | Dual-vertical gas-liquid separator ammonia separation plate exchange pry block |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219390155U true CN219390155U (en) | 2023-07-21 |
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ID=87199625
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202320002142.6U Active CN219390155U (en) | 2023-01-03 | 2023-01-03 | Dual-vertical gas-liquid separator ammonia separation plate exchange pry block |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219390155U (en) |
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2023
- 2023-01-03 CN CN202320002142.6U patent/CN219390155U/en active Active
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