CN216592351U - Gas-liquid separation device and self-cascade refrigeration system comprising same - Google Patents
Gas-liquid separation device and self-cascade refrigeration system comprising same Download PDFInfo
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- CN216592351U CN216592351U CN202123287204.2U CN202123287204U CN216592351U CN 216592351 U CN216592351 U CN 216592351U CN 202123287204 U CN202123287204 U CN 202123287204U CN 216592351 U CN216592351 U CN 216592351U
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- 238000000926 separation method Methods 0.000 title claims abstract description 99
- 239000007788 liquid Substances 0.000 title claims abstract description 78
- 238000005057 refrigeration Methods 0.000 title claims description 12
- 238000009833 condensation Methods 0.000 claims description 18
- 230000005494 condensation Effects 0.000 claims description 18
- 238000001704 evaporation Methods 0.000 claims description 15
- 230000008020 evaporation Effects 0.000 claims description 14
- 238000001514 detection method Methods 0.000 claims description 13
- 238000001914 filtration Methods 0.000 claims description 4
- 230000005484 gravity Effects 0.000 abstract description 6
- 238000009835 boiling Methods 0.000 description 32
- 239000003507 refrigerant Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
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Abstract
The utility model provides a gas-liquid separation reaches from overlapping refrigerating system including it. The gas-liquid separation device includes: the separation device comprises a shell, a separation chamber is formed in the shell, and a gas outlet at the upper end and a liquid outlet at the lower end are formed in the shell; the mixed working medium inlet pipe comprises a spiral separation section positioned in the separation cavity; a screen structure disposed within the separation chamber and between the gas outlet and the spiral separation section; and the heat exchange auxiliary separator is arranged at a position close to the gas outlet and/or a position close to the liquid outlet. The utility model discloses a multiple separation makes gas-liquid separation more abundant, and multiple separation includes: the first heavy mixed working medium is separated by centrifugal force at high flow speed in the spiral separation section; second-mass impingement vessel wall separation; thirdly, the gas rises in the container under the action of gravity, and the liquid falls and is separated; and the fourth gas working medium with part of the liquid working medium is separated by the filter screen structure.
Description
Technical Field
The utility model relates to a refrigeration plant technical field especially relates to a gas-liquid separation device reaches including it from overlapping refrigerating system.
Background
The conventional gas-liquid separator commonly used in the auto-cascade system is a rectifying tower or a flash tank, and the problem of insufficient gas-liquid separation exists; gas-liquid separation is insufficient, the high-boiling-point refrigerant and the low-boiling-point refrigerant on the high-temperature side are doped with more low-boiling-point refrigerants, and the low-boiling-point refrigerant on the low-temperature side are doped with more high-boiling-point refrigerants, so that the performance of the system is adversely affected.
The existing gas-liquid separation device is complex in structure for ensuring sufficient separation, for example, part of devices can use a filter device to carry out secondary filtration on a refrigerant at an inlet and a gas outlet, the structure is complex, the filter device is internally provided with a filler, the manufacturing cost is high, the system is easy to pollute, and the reliability of the system is influenced.
SUMMERY OF THE UTILITY MODEL
In view of this, the utility model provides a gas-liquid separation device reaches from overlapping refrigerating system including it is used for solving the insufficient technical problem of gas-liquid separation that exists among the prior art at least, specifically:
the utility model provides a gas-liquid separation device, include:
the separation device comprises a shell, a separation chamber is formed in the shell, and a gas outlet at the upper end and a liquid outlet at the lower end are formed in the shell;
the mixed working medium inlet pipe comprises a spiral separation section positioned in the separation cavity;
a screen structure disposed within the separation chamber and between the gas outlet and the spiral separation section;
and the heat exchange auxiliary separator is arranged at a position close to the gas outlet and/or a position close to the liquid outlet.
Further optionally, the spiral separation section is of a spiral pipe structure, an outlet of the spiral separation section is located at the lower side, and the mixed working medium passing through the outlet of the spiral separation section impacts the inner wall surface of the shell.
Further optionally, the heat exchange assisted separator comprises a condensation assisted separator located between the gas outlet and the screen structure.
Further optionally, the screen structure is a heat-conducting screen,
the heat conduction filter screen forms a convex filtering surface towards the direction far away from the gas outlet.
Further optionally, the screen structure is integrally connected with the condensation-assisted separator.
Further optionally, the heat exchange assisted separator comprises an evaporation assisted separator disposed proximate the liquid outlet.
Further optionally, a reservoir is formed at the bottom of the housing, the liquid outlet being in communication with the reservoir,
the evaporation auxiliary separator is positioned in the liquid storage tank.
Further optionally, the gas-liquid separation device further comprises a pressure detection device and a temperature detection device,
the pressure detection device and the temperature detection device are arranged in the separation cavity, and the heat exchange auxiliary separator is opened or closed according to the pressure and/or the temperature in the separation cavity.
In a second aspect, the present invention provides a self-cascade refrigeration system, comprising the above gas-liquid separation device.
Further optionally, the heat exchange auxiliary separator is connected with a cold source and/or a heat source of the self-cascade refrigeration system.
The utility model discloses a multiple separation makes gas-liquid separation more abundant, and multiple separation includes: the first heavy mixed working medium is separated by centrifugal force at high flow speed in the spiral separation section; second-mass impingement vessel wall separation; thirdly, the gas rises in the container under the action of gravity, and the liquid falls and is separated; and the fourth gas working medium with part of the liquid working medium is separated by a filter screen structure.
Drawings
The above and other objects, features and advantages of the present disclosure will become more apparent by describing in detail exemplary embodiments thereof with reference to the attached drawings. The drawings described below are merely some embodiments of the present disclosure, and other drawings may be derived from those drawings by those of ordinary skill in the art without inventive effort.
FIG. 1 shows a schematic cross-sectional view of a gas-liquid separation apparatus according to an embodiment of the present invention;
FIG. 2 is a schematic cross-sectional view of a second gas-liquid separator according to an embodiment of the present invention;
fig. 3 shows a schematic cross-sectional view of a three-gas-liquid separation apparatus according to an embodiment of the present invention.
In the figure:
1. a housing; 2. a spiral separation section; 3. a gas outlet; 4. a liquid outlet; 5. a screen structure; 6. a condensation-assisted separator; 7. an evaporation assisted separator.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are some, but not all, embodiments of the present invention. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts all belong to the protection scope of the present invention.
The terminology used in the embodiments of the invention is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention. As used in the embodiments of the present invention and the appended claims, the singular forms "a," "an," and "the" are intended to include the plural forms as well, unless the context clearly indicates otherwise, and "a plurality" typically includes at least two, but does not exclude the presence of at least one.
It should be understood that the term "and/or" as used herein is merely a relationship that describes an associated object, meaning that three relationships may exist, e.g., a and/or B, may represent: a exists alone, A and B exist simultaneously, and B exists alone. In addition, the character "/" herein generally indicates that the former and latter related objects are in an "or" relationship.
It is also noted that the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a good or system that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such good or system. Without further limitation, an element defined by the phrase "comprising an … …" does not exclude the presence of other like elements in a commodity or system that includes the element.
The utility model discloses a multiple separation makes gas-liquid separation more abundant, and multiple separation includes: the first heavy mixed working medium is separated by centrifugal force at high flow speed in the spiral separation section; second-mass impingement vessel wall separation; thirdly, the gas rises in the container under the action of gravity, and the liquid falls and is separated; and the fourth gas working medium with part of the liquid working medium is separated by the filter screen structure.
In response to the limit working condition (the general working temperature is between the boiling point temperature of a high boiling point working medium and the boiling point temperature of a low boiling point working medium), the working temperature is close to the boiling point temperature of the high boiling point working medium or the low boiling point working medium under the working pressure (1. the working temperature is close to the boiling point temperature of the high boiling point working medium under the working pressure, the high boiling point working medium is possibly insufficiently condensed, and the high boiling point working medium can still be separated from the gas; 2. the working temperature is close to the boiling point temperature of the low boiling point working medium under the working pressure, the low boiling point working medium has condensation risk, and the low boiling point working medium can be mixed into the liquid), a heat exchange auxiliary separator is arranged at a gas outlet and/or a liquid outlet, and the high boiling point working medium or the low boiling point working medium is further purified according to the working condition of the working medium. The following detailed description of the present invention is provided in connection with the following embodiments:
as shown in fig. 1, 2 and 3, the present invention provides a gas-liquid separation apparatus, including:
the separation device comprises a shell 1, wherein a separation cavity is formed in the shell 1, the shell 1 is preferably of a vertically arranged columnar structure, the separation cavity is a columnar cavity, and a gas outlet 3 at the upper end and a liquid outlet 4 at the lower end are formed in the shell 1;
the mixed working medium inlet pipe comprises an inlet end positioned at the outer side of the shell 1 and a spiral separation section 2 positioned in the separation cavity;
the filter screen structure 5 is arranged in the separation cavity and is positioned between the gas outlet 3 and the spiral separation section 2;
and the heat exchange auxiliary separator is arranged at a position close to the gas outlet 3 and/or a position close to the liquid outlet 4.
The spiral separation section 2 is formed by spirally winding along the inner wall of the shell 1, the outlet of the spiral separation section 2 is positioned at the lower side, and the mixed working medium passing through the outlet of the spiral separation section 2 impacts the inner wall surface of the shell 1. Preferably, the spiral separation section 2 is attached to the inner peripheral wall of the shell 1 and is spirally arranged, and the outlet of the spiral separation section faces the inner wall of the shell 1 or forms a certain included angle with the inner wall of the shell 1, so that the mixed working medium can impact the inner wall of the shell 1 after flowing out from the outlet to separate the gas-liquid working medium.
The heat exchange auxiliary separator comprises a condensation auxiliary separator 6, the condensation auxiliary separator 6 is positioned between the gas outlet 3 and the filter screen structure 5 and is used for providing a cold source, condensing high-boiling-point working media in the gas working media into liquid and further separating and purifying the gas working media. Preferably, the condensation auxiliary separator 6 may be a cold pipe introduced from a refrigeration system, or an externally introduced cold source, such as a semiconductor refrigeration structure.
The heat exchange auxiliary separator further comprises an evaporation auxiliary separator 7, the evaporation auxiliary separator 7 being arranged adjacent to the liquid outlet 4. The bottom of the shell 1 forms a liquid storage tank, the liquid outlet 4 is communicated with the liquid storage tank, and the evaporation auxiliary separator 7 is positioned in the liquid storage tank. The heat source is used for providing a heat source, evaporating the working medium with low boiling point in the liquid working medium into gas, further separating and purifying the liquid working medium, and the form of the heat source can be a heat pipe introduced from a refrigerating system or an externally introduced heat source, such as an electric heating device and the like.
The gas-liquid separation device also comprises a pressure detection device and a temperature detection device, the pressure detection device and the temperature detection device are arranged in the separation cavity, and the heat exchange auxiliary separator is opened or closed according to the pressure and/or the temperature in the separation cavity.
Specifically, in the first embodiment, as shown in fig. 1, the auxiliary condensation separator 6 and the auxiliary evaporation separator 7 are provided at the same time, so that the method is suitable for efficiently separating the non-azeotropic working mixture under the condition of large working condition fluctuation range. The mixed working medium enters the shell 1 through the mixed working medium inlet pipe and is subjected to high-speed centrifugal separation in the spiral separation section 2, the mixed working medium coming out of the spiral separation section 2 impacts on the inner wall surface of the shell 1, gas and liquid are separated again, the gas working medium rises in the shell 1 under the action of gravity, the mixed liquid is scattered and separated again through the filter screen structure 5, and the liquid working medium descends to the bottom of the shell 1 to be stored and conveyed. The pressure and temperature detection device in the container detects the pressure Pi and the temperature Ti, the boiling point TH of the high boiling point working medium and the boiling point TL of the low boiling point working medium are obtained according to a comparison table of the pressure and the high and low boiling point working media under each pressure, if Ti-TH is larger than Tsh, the Tsh is a preset value, the condensation auxiliary separator 6 is started, and condensation separation of the high boiling point working medium from gas is promoted; if Ti-TL < Tsl, Tsl is a certain preset value, the evaporation auxiliary separator 7 is started to promote the evaporation separation of the low boiling point gas from the liquid.
In the second embodiment, as shown in fig. 2, the heat exchange auxiliary separator only includes the condensation auxiliary separator 6, and is suitable for the case where the tool state is relatively determined and the high boiling point working medium is difficult to separate from the gas working medium. The mixed working medium enters the shell 1 through the mixed working medium inlet pipe and is subjected to high-speed centrifugal separation in the spiral separation section 2, the mixed working medium coming out of the spiral separation section 2 impacts on the inner wall surface of the shell 1, gas and liquid are separated again, the gas working medium rises in the shell 1 under the action of gravity, the mixed liquid is scattered and separated again through the filter screen structure 5, and the liquid working medium descends to the bottom of the shell 1 to be stored and conveyed. The gas working medium rises after passing through the filter screen, the doped high boiling point working medium is condensed under the action of the condensation auxiliary separator 6, and the high boiling point working medium and the low boiling point working medium are further separated.
In the third specific embodiment, as shown in fig. 3, the heat exchange auxiliary separator only includes the evaporation auxiliary separator 7, and is suitable for the case where the tool state is relatively determined and the low-boiling point working medium is difficult to separate from the liquid working medium. The mixed working medium enters the shell 1 through the mixed working medium inlet pipe and is subjected to high-speed centrifugal separation in the spiral separation section 2, the mixed working medium coming out of the spiral separation section 2 impacts on the inner wall surface of the shell 1, gas and liquid are separated again, the gas working medium rises in the shell 1 under the action of gravity, the mixed liquid is scattered and separated again through the filter screen structure 5, and the liquid working medium descends to the bottom of the shell 1 to be stored and conveyed. The liquid stored at the bottom of the shell 1 is evaporated by the evaporation auxiliary separator 7, and the working medium with low boiling point is further separated from the working medium with high boiling point.
The utility model also provides a from cascade refrigeration system, including above-mentioned gas-liquid separation. Preferably, the heat exchange auxiliary separator is connected with a cold source and/or a heat source of the self-cascade refrigeration system, specifically, the condensation auxiliary separator 6 is a cold pipe introduced from the system, and the evaporation auxiliary separator 7 is a hot pipe introduced from the system, so as to fully utilize the heat source of the system.
Exemplary embodiments of the present disclosure are specifically illustrated and described above. It is to be understood that the present disclosure is not limited to the precise arrangements, instrumentalities, or instrumentalities described herein; on the contrary, the disclosure is intended to cover various modifications and equivalent arrangements included within the spirit and scope of the appended claims.
Claims (10)
1. A gas-liquid separation apparatus, comprising:
the separation device comprises a shell, a separation chamber is formed in the shell, and a gas outlet at the upper end and a liquid outlet at the lower end are formed in the shell;
the mixed working medium inlet pipe comprises a spiral separation section positioned in the separation cavity;
a screen structure disposed within the separation chamber and between the gas outlet and the spiral separation section;
and the heat exchange auxiliary separator is arranged at a position close to the gas outlet and/or a position close to the liquid outlet.
2. The gas-liquid separation device according to claim 1, wherein the spiral separation section has a spiral tube structure, an outlet of the spiral separation section is located at a lower side, and the mixed working medium passing through the outlet of the spiral separation section impinges on an inner wall surface of the casing.
3. The gas-liquid separation device of claim 1, wherein the heat exchange assisted separator comprises a condensation assisted separator located between the gas outlet and the screen structure.
4. The gas-liquid separation device according to claim 3, wherein the screen structure is a heat conductive screen,
the heat conduction filter screen forms a convex filtering surface towards the direction far away from the gas outlet.
5. The gas-liquid separation device according to claim 4, wherein the screen structure is integrally connected to the condensation-assisted separator.
6. The gas-liquid separation device of claim 1, wherein the heat exchange assisted separator comprises an evaporation assisted separator disposed proximate the liquid outlet.
7. The gas-liquid separation device according to claim 6, wherein a sump is formed at a bottom of the casing, the liquid outlet communicates with the sump,
the evaporation auxiliary separator is positioned in the liquid storage tank.
8. The gas-liquid separation device according to any one of claims 1 to 7, further comprising a pressure detection device and a temperature detection device,
the pressure detection device and the temperature detection device are arranged in the separation cavity, and the heat exchange auxiliary separator is opened or closed according to the pressure and/or the temperature in the separation cavity.
9. A self-cascade refrigeration system comprising the gas-liquid separation device of any one of claims 1 to 8.
10. The self-cascade refrigeration system of claim 9, wherein the heat exchange auxiliary separator is coupled to a cold source and/or a heat source of the self-cascade refrigeration system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123287204.2U CN216592351U (en) | 2021-12-24 | 2021-12-24 | Gas-liquid separation device and self-cascade refrigeration system comprising same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123287204.2U CN216592351U (en) | 2021-12-24 | 2021-12-24 | Gas-liquid separation device and self-cascade refrigeration system comprising same |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216592351U true CN216592351U (en) | 2022-05-24 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202123287204.2U Active CN216592351U (en) | 2021-12-24 | 2021-12-24 | Gas-liquid separation device and self-cascade refrigeration system comprising same |
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| Country | Link |
|---|---|
| CN (1) | CN216592351U (en) |
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- 2021-12-24 CN CN202123287204.2U patent/CN216592351U/en active Active
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