CN216409381U - Low horizontal vapour and liquid separator that fills - Google Patents
Low horizontal vapour and liquid separator that fills Download PDFInfo
- Publication number
- CN216409381U CN216409381U CN202123091897.8U CN202123091897U CN216409381U CN 216409381 U CN216409381 U CN 216409381U CN 202123091897 U CN202123091897 U CN 202123091897U CN 216409381 U CN216409381 U CN 216409381U
- Authority
- CN
- China
- Prior art keywords
- liquid
- pipe
- subassembly
- head
- assembly
- 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
Images
Landscapes
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
The utility model discloses a low-filling horizontal gas-liquid separator which comprises a barrel assembly, wherein a left end socket assembly is fixedly connected to one side of the barrel assembly, a right end socket assembly is fixedly connected to the other side, far away from the left end socket assembly, of the barrel assembly, a liquid dropping pipe assembly and a gas return pipe assembly are fixedly connected and communicated with the bottom of the barrel assembly, the gas return pipe assembly comprises a gas return pipe assembly and a liquid supply pipe assembly, and the outer wall of the gas return pipe assembly is fixedly connected and communicated with the liquid supply pipe assembly. By the arrangement of the range plates, in the moving process of gas and small liquid drops, the gas rises under the action of gravity and the liquid falls, and the range plates enable the liquid with the same cylinder size specification to extend the separation distance by times, reduce the separation height and further enable a separator with the size one time smaller to be used under the same refrigerating capacity; finally, the charging and storage amount of the refrigeration working medium is greatly reduced.
Description
Technical Field
The utility model belongs to the technical field of refrigeration air conditioners, and particularly relates to a low-filling horizontal gas-liquid separator.
Background
The refrigerating system generally takes ammonia and Freon as main materials, wherein the ammonia is a toxic and harmful substance and is strictly supervised by safety departments in the using process, and the lower the charging amount in the system is, the better the system is. China has officially approved the Bulgarian amendments, the use of Freon in the scheme also provides specific restriction reduction measures,
on this basis, it is necessary to conduct a related study of low charge and storage of refrigerant.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide a low-filling horizontal gas-liquid separator which has the effects of reducing the filling and storage amount of a refrigeration working medium and improving the safety and the advancement of a system.
In order to achieve the purpose, the utility model provides the following technical scheme: the utility model provides a fill horizontal vapour and liquid separator of notes, includes the barrel subassembly, the left head subassembly of one side fixedly connected with of barrel subassembly, the opposite side fixedly connected with right head subassembly of left head subassembly is kept away from to the barrel subassembly, the bottom fixed connection and the intercommunication of barrel subassembly have liquid dropping pipe subassembly and muffler subassembly, the muffler subassembly includes return air nest of tubes and feed pipe subassembly, the outer wall fixed connection and the intercommunication of return air nest of tubes have the feed pipe subassembly.
Preferably, the left sealing head assembly comprises a left elliptical sealing head and an air outlet pipe, one end of the air outlet pipe is fixedly connected with the left elliptical sealing head, the air outlet pipe is communicated with the inside of the left elliptical sealing head, and the air outlet pipe is located at the upper quarter diameter of the left elliptical sealing head.
Preferably, the barrel subassembly includes swash plate, drum body and stroke range board, the stroke range board is located the right side below of swash plate, the three bracing piece of bottom fixedly connected with of stroke range board, the both ends of bracing piece and the inner wall fixed connection of drum body, the seamless welding of the inner wall that comes both sides outer wall and drum body of stroke range board, the swash plate is located the middle part of drum body, the both sides outer wall of swash plate and the inner wall fixed connection of drum body.
Specifically, the elbow of the gas return pipe group is sprayed to the right elliptical head, then gas and small liquid drops flow to the left elliptical head along with gas flow, liquid flows downwards along the cylinder wall of the head, and the liquid level of the liquid dropping pipe assembly is not influenced stably under the action of the swash plate; and necessary conditions are provided for the stability of the lower liquid storage amount liquid dropping pipe group.
Preferably, three round holes are uniformly formed in the top of the wave breaker, and the wave breaker inclines downwards for five degrees from the right to the left direction.
Specifically, the range plates are arranged in the cylinder assembly in a five-degree inclined manner, so that liquid in the upper layer separation process can flow into the lower layer by gravity, and the separation efficiency is improved; the three circular holes which are uniformly distributed ensure the pressure balance distribution of the upper layer and the lower layer; the unstable operation of the gas distribution caused by the suction of the compressor behind the gas outlet pipe can be avoided.
Preferably, the right seal head assembly comprises a right elliptical seal head and a liquid level meter upper connecting pipe, the liquid level meter upper connecting pipe is located below the right elliptical seal head, one end of the liquid level meter upper connecting pipe is fixedly connected with the right elliptical seal head and communicated with the inside of the right elliptical seal head, the right end of the swash plate is welded with the inner wall of the right elliptical seal head in a seamless mode, and the right end of the stroke plate is welded with the right elliptical seal head in a seamless mode.
Preferably, the liquid dropping pipe assembly comprises a liquid dropping pipe and a liquid level lower connecting pipe, the upper end of the liquid dropping pipe is fixedly connected with the bottom of the cylinder body and is communicated with the inside of the cylinder body, the upper end of the liquid dropping pipe is flush with the bottom of the cylinder body, and one end of the liquid level lower connecting pipe is fixedly connected with the outer wall of the liquid dropping pipe and is communicated with the inside of the liquid level lower connecting pipe.
Preferably, the upper end of the air return pipe group passes through the cylinder body and extends to the inside of the cylinder body, the upper end of the cylinder body is bent rightwards by ninety degrees and faces the right elliptical head, the upper end of the air return pipe group is provided with a forty-five degree oblique angle, and one end of the liquid supply pipe assembly passes through the air return pipe group and is bent upwards by ninety degrees.
Specifically, a liquid supply pipe assembly is added in the air return pipe assembly, and the liquid supply pipe assembly are combined to form a jet pump principle, so that the flowing power of the air return pipe assembly is increased; the local resistance of the air return pipe group is reduced, the efficiency of the heat exchanger is improved, and the circulation volume of the working medium in the heat exchanger is reduced.
Compared with the prior art, the utility model has the beneficial effects that:
1. by the arranged range plates, the gas rises and the liquid falls under the action of gravity in the moving process of the gas and the small liquid drops; due to the existence of the range plates, the separation distance of liquid with the same cylinder size specification can be prolonged by times, and the separation height is reduced; so that the separator with one-time smaller specification can be used under the same refrigerating capacity; finally, the charging and storage amount of the refrigeration working medium is greatly reduced.
2. The liquid supply pipe assembly is added in the air return pipe assembly through the arranged liquid supply pipe assembly, and the liquid supply pipe assembly and the air return pipe assembly are combined to form a jet pump principle, so that the flowing power of the air return pipe assembly is increased; the local resistance of the air return pipe group is reduced, the efficiency of the heat exchanger is improved, and the circulation volume of the working medium in the heat exchanger is reduced.
3. Through the arranged range plates, the range plates are arranged in the cylinder assembly in an inclined five-degree angle manner, so that liquid in the upper-layer separation process can flow into the lower layer by virtue of gravity, and the separation efficiency is improved; the three circular holes which are uniformly distributed ensure the pressure balance distribution of the upper layer and the lower layer; the unstable operation of the gas distribution caused by the suction of the compressor behind the gas outlet pipe can be avoided.
Drawings
FIG. 1 is a schematic view of the overall structure of the present invention;
FIG. 2 is a schematic view of the internal structure of the present invention;
FIG. 3 is a schematic cross-sectional view of the present invention;
fig. 4 is a schematic sectional view of the air return pipe group according to the present invention.
In the figure: 1. a left head assembly; 2. a cartridge assembly; 3. a right head assembly; 4. a liquid dropping pipe assembly; 5. a return air duct assembly; 101. a left elliptical head; 102. an air outlet pipe; 201. a swash plate; 202. a support bar; 203. a range division plate; 204. a cylinder body; 205. a circular hole; 301. a right elliptical head; 302. an upper connecting pipe of the liquid level meter; 401. a liquid level lower connecting pipe; 402. a liquid dropping pipe; 501. a gas return pipe group; 502. a liquid supply tube assembly.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Referring to fig. 1-4, the present invention provides a technical solution: the utility model provides a horizontal vapour and liquid separator of low notes fill, includes barrel subassembly 2, barrel subassembly 2's one side fixedly connected with left head subassembly 1, barrel subassembly 2 keeps away from left head subassembly 1's opposite side fixedly connected with right head subassembly 3, barrel subassembly 2's bottom fixed connection and intercommunication have liquid dropping pipe subassembly 4 and muffler subassembly 5, muffler subassembly 5 includes return air pipe group 501 and feed pipe subassembly 502, return air pipe group 501's outer wall fixed connection and intercommunication have feed pipe subassembly 502.
The left seal head assembly 1 comprises a left elliptical seal head 101 and an air outlet pipe 102, one end of the air outlet pipe 102 is fixedly connected with the left elliptical seal head 101, the air outlet pipe 102 is communicated with the inside of the left elliptical seal head 101, and the air outlet pipe 102 is located at the upper quarter diameter of the left elliptical seal head 101.
Wherein, barrel subassembly 2 includes swash plate 201, drum body 204 and stroke range board 203, and stroke range board 203 is located swash plate 201's right side below, the three bracing piece 202 of the bottom fixedly connected with of stroke range board 203, the both ends of bracing piece 202 and the inner wall fixed connection of drum body 204, the seamless welding of the inner wall of coming both sides outer wall and drum body 204 of stroke range board 203, and swash plate 201 is located the middle part of drum body 204, the both sides outer wall of swash plate 201 and the inner wall fixed connection of drum body 204.
In the embodiment, the elbow of the gas return pipe group 501 is sprayed to the right elliptical head 301, then gas and small liquid drops flow to the left elliptical head 101 along with gas flow, liquid flows downwards along the cylinder wall of the head, and the liquid level of the liquid dropping pipe assembly 4 is not affected stably due to the action of the wave guard plate 201; and necessary conditions are provided for the stability of the lower liquid storage amount liquid falling pipe group 4.
Wherein, three round holes 205 are evenly opened at the top of the swash plate 201, and the swash plate 201 inclines five degrees from the right to the left direction.
In the embodiment, the range plates 203 are arranged in the cylinder component 2 in a five-degree inclined manner, so that liquid in the upper layer separation process can flow into the lower layer by gravity, and the separation efficiency is improved; meanwhile, the three uniformly distributed round holes 205 also ensure the pressure balance distribution of the upper layer and the lower layer; the unstable gas separation operation caused by the suction of the compressor behind the gas outlet pipe 102 can be avoided.
The right seal head assembly 3 comprises a right elliptical seal head 301 and a liquid level meter upper connecting pipe 302, the liquid level meter upper connecting pipe 302 is located below the right elliptical seal head 301, one end of the liquid level meter upper connecting pipe 302 is fixedly connected with the right elliptical seal head 301 and communicated with the inside of the right elliptical seal head 301, the right end of the swash plate 201 is welded to the inner wall of the right elliptical seal head 301 in a seamless mode, and the right end of the range plate 203 is welded to the right elliptical seal head 301 in a seamless mode.
The liquid dropping pipe assembly 4 comprises a liquid dropping pipe 402 and a liquid level lower connecting pipe 401, the upper end of the liquid dropping pipe 402 is fixedly connected with the bottom of the cylinder body 204 and communicated with the inside, the upper end of the liquid dropping pipe 402 is flush with the bottom of the cylinder body 204, and one end of the liquid level lower connecting pipe 401 is fixedly connected with the outer wall of the liquid dropping pipe 402 and communicated with the inside.
Wherein, the upper end of the air return pipe set 501 passes through the cylinder body 204 and extends to the inside of the cylinder body 204, the upper end of the cylinder body 204 bends ninety degrees to the right and faces the right elliptical head 301, the upper end of the air return pipe set 501 is provided with a forty-five degree oblique angle, and one end of the liquid supply pipe assembly 502 passes through the air return pipe set 501 and bends ninety degrees upwards.
In this embodiment, the liquid supply pipe assembly 502 is added in the air return pipe assembly 5, and the two assemblies can form a jet pump principle, so as to increase the flowing power of the air return pipe assembly 501; the local resistance of the air return pipe group 501 is reduced, the efficiency of the heat exchanger is improved, and the circulation volume of the working medium in the heat exchanger is reduced.
The working principle and the using process of the utility model are as follows: when the plate heat exchanger operates, ammonia gas and liquid after heat exchange of the plate heat exchanger enter the gas return assembly in a two-phase state, the ammonia gas and liquid are sprayed to the right elliptical head 301 from the elbow of the gas return tube group 501, then gas and small liquid drops flow to the left elliptical head 101 along with airflow, and liquid flows downwards along the cylinder wall of the head, so that the liquid level of the liquid falling tube assembly 4 is not influenced stably under the action of the wave-proof plate 201; and necessary conditions are provided for the stability of the lower liquid storage amount liquid falling pipe group 4.
In the process of moving the gas and the small liquid drops, the gas rises and the liquid falls under the action of gravity; due to the existence of the range plate 203, the separation distance of liquid with the same cylinder size specification can be doubled, and the separation height is reduced; so that the separator with one-time smaller specification can be used under the same refrigerating capacity; finally, the charging and storage amount of the refrigeration working medium is greatly reduced.
A liquid supply pipe assembly 502 is added in the air return pipe assembly 5, and the two assemblies can form a jet pump principle to increase the flowing power of the air return pipe assembly 501; the local resistance of the air return pipe group 501 is reduced, the efficiency of the heat exchanger is improved, and the circulation volume of the working medium in the heat exchanger is reduced.
The range plates 203 are arranged in the cylinder component 2 in an inclined manner at an angle of 5 degrees, so that liquid in the upper layer separation process can flow into the lower layer by gravity, and the separation efficiency is improved; meanwhile, the uniformly distributed 3 round holes 205 also ensure the pressure balance distribution of the upper layer and the lower layer; the unstable gas separation operation caused by the suction of the compressor behind the gas outlet pipe 102 can be avoided.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the utility model, the scope of which is defined in the appended claims and their equivalents.
Claims (7)
1. A low fill horizontal vapour and liquid separator, includes barrel subassembly (2), its characterized in that: the utility model discloses a disposable gas return tube, including barrel subassembly (2), one side fixedly connected with left head subassembly (1) of barrel subassembly (2), the opposite side fixedly connected with right head subassembly (3) of left head subassembly (1) are kept away from in barrel subassembly (2), the bottom fixed connection and the intercommunication of barrel subassembly (2) have liquid dropping pipe subassembly (4) and muffler subassembly (5), muffler subassembly (5) are including return-air nest of tubes (501) and feed pipe subassembly (502), the outer wall fixed connection and the intercommunication of return-air nest of tubes (501) have liquid feed pipe subassembly (502).
2. The low-fill horizontal gas-liquid separator of claim 1, wherein: the left sealing head assembly (1) comprises a left elliptical sealing head (101) and an air outlet pipe (102), one end of the air outlet pipe (102) is fixedly connected with the left elliptical sealing head (101), the air outlet pipe (102) is communicated with the inside of the left elliptical sealing head (101), and the air outlet pipe (102) is located at the upper quarter diameter of the left elliptical sealing head (101).
3. The low-fill horizontal gas-liquid separator of claim 1, wherein: barrel subassembly (2) include swash plate (201), drum body (204) and journey board (203), journey board (203) is located the right side below of swash plate (201), the three bracing piece of bottom fixedly connected with (202) of journey board (203), the both ends of bracing piece (202) and the inner wall fixed connection of drum body (204), the inner wall seamless welding of coming both sides outer wall and drum body (204) of journey board (203), swash plate (201) are located the middle part of drum body (204), the both sides outer wall of swash plate (201) and the inner wall fixed connection of drum body (204).
4. A low-fill horizontal gas-liquid separator as defined in claim 3 wherein: three round holes (205) are evenly opened at the top of the wave breaker (201), and the wave breaker (201) inclines downwards for five degrees from the right to the left direction.
5. A low-fill horizontal gas-liquid separator as defined in claim 3 wherein: right side head subassembly (3) are including right oval head (301) and level gauge upper pipe (302), the level gauge upper pipe (302) is located the below of right oval head (301), the one end and the right oval head (301) fixed connection and the inside of liquid level gauge upper pipe (302) communicate with each other, the right-hand member of swash plate (201) and the inner wall seamless welding of right oval head (301), divide journey board (203) right-hand member and right oval head (301) seamless welding.
6. A low-fill horizontal gas-liquid separator as defined in claim 3 wherein: the liquid dropping pipe assembly (4) comprises a liquid dropping pipe (402) and a liquid level lower connecting pipe (401), the upper end of the liquid dropping pipe (402) is fixedly connected with the bottom of the cylinder body (204) and is communicated with the inside of the cylinder body, the upper end of the liquid dropping pipe (402) is flush with the bottom of the cylinder body (204), and one end of the liquid level lower connecting pipe (401) is fixedly connected with the outer wall of the liquid dropping pipe (402) and is communicated with the inside of the liquid level lower connecting pipe.
7. The low-fill horizontal gas-liquid separator of claim 5, wherein: the upper end of the air return pipe group (501) penetrates through the cylinder body (204) and extends into the cylinder body (204), the upper end of the cylinder body (204) bends ninety degrees to the right and faces the right elliptical head (301), a forty-five degree oblique angle is formed in the upper end of the air return pipe group (501), and one end of the liquid supply pipe assembly (502) penetrates through the air return pipe group (501) and bends ninety degrees upwards.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123091897.8U CN216409381U (en) | 2021-12-10 | 2021-12-10 | Low horizontal vapour and liquid separator that fills |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123091897.8U CN216409381U (en) | 2021-12-10 | 2021-12-10 | Low horizontal vapour and liquid separator that fills |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216409381U true CN216409381U (en) | 2022-04-29 |
Family
ID=81282335
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202123091897.8U Active CN216409381U (en) | 2021-12-10 | 2021-12-10 | Low horizontal vapour and liquid separator that fills |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN216409381U (en) |
-
2021
- 2021-12-10 CN CN202123091897.8U patent/CN216409381U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202024538U (en) | Liquid baffle plate structure of flooded evaporator | |
| CN202792709U (en) | Spraying type evaporator | |
| CN216409381U (en) | Low horizontal vapour and liquid separator that fills | |
| CN113790614A (en) | Tank type heat exchanger and heat pump system | |
| CN204902329U (en) | Dry type evaporator of even cloth liquid | |
| CN210663986U (en) | Heat exchange structure of gas dryer | |
| CN203385245U (en) | Shell-and-tube condenser | |
| CN202973689U (en) | Gas-liquid separator of freon refrigerating system | |
| CN211147362U (en) | Heat exchange dewatering structure of compressed gas dryer | |
| CN207065934U (en) | A kind of flow-type evaporator peculiar to vessel | |
| CN205897631U (en) | Gas partial condenser | |
| CN112033048B (en) | Dry evaporator | |
| CN214437251U (en) | Gas-water separation device and vacuum system | |
| CN112161504A (en) | Micro-channel heat exchanger and heat pump system with same | |
| CN203848569U (en) | Horizontal liquid reservoir for refrigerating system | |
| CN206642473U (en) | A kind of gas-liquid separation device of built-in heat exchanger | |
| CN113007924A (en) | Heat exchanger and air conditioner with same | |
| CN216790573U (en) | Flooded evaporator with good heat transfer effect | |
| CN220227126U (en) | Gas cooling cavity for air compressor | |
| CN216924828U (en) | Efficient stainless steel horizontal condenser | |
| CN205718634U (en) | A kind of micro-channel heat exchanger of single header | |
| CN218237930U (en) | Oil-gas separation device for flooded refrigerating system | |
| CN219897393U (en) | Gas-water separator for tail gas water sealed tank | |
| CN212109071U (en) | Micro-channel heat exchanger and heat pump system with same | |
| CN220852671U (en) | Multistage pressure condenser |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |