CN210425648U - Evaporator - Google Patents
Evaporator Download PDFInfo
- Publication number
- CN210425648U CN210425648U CN201921383477.7U CN201921383477U CN210425648U CN 210425648 U CN210425648 U CN 210425648U CN 201921383477 U CN201921383477 U CN 201921383477U CN 210425648 U CN210425648 U CN 210425648U
- Authority
- CN
- China
- Prior art keywords
- pipeline
- evaporation
- working medium
- liquid
- pipelines
- 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.)
- Expired - Fee Related
Links
- 238000001704 evaporation Methods 0.000 claims abstract description 52
- 230000008020 evaporation Effects 0.000 claims abstract description 42
- 239000007788 liquid Substances 0.000 claims abstract description 36
- 229910052751 metal Inorganic materials 0.000 claims abstract description 10
- 239000002184 metal Substances 0.000 claims abstract description 10
- 229920006395 saturated elastomer Polymers 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 9
- LVGUZGTVOIAKKC-UHFFFAOYSA-N 1,1,1,2-tetrafluoroethane Chemical compound FCC(F)(F)F LVGUZGTVOIAKKC-UHFFFAOYSA-N 0.000 description 7
- 239000003507 refrigerant Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 239000005431 greenhouse gas Substances 0.000 description 4
- 238000005057 refrigeration Methods 0.000 description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- 230000006378 damage Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
An evaporator is composed of a group of parallel evaporating pipelines, a liquid working medium pipeline and a gas working medium pipeline, which are communicated with each other at their inlet ends, and a discharge pipeline communicated with the outlet ends of said evaporating pipelines. Dry air and liquid working medium conveyed from a refrigerating system respectively enter an evaporation pipeline through a gas working medium pipeline and a liquid working medium pipeline, liquid is evaporated, and the dry air entering an evaporator drives saturated steam to leave the surface of the liquid, so that the evaporation is continuously carried out; the metal heat conducting wires enable low temperature generated by evaporation to be transmitted to the evaporation pipeline in time so as to be subjected to heat exchange utilization by people; after the liquid and the gas enter the discharge pipeline, the gas is discharged from the upper end of the channel, and the liquid is discharged from the lower end of the channel, so that the condition is provided for continuous circulation.
Description
Technical Field
The utility model relates to a refrigeration technology, specifically speaking are evaporators.
Background
The evaporator in the refrigerating equipment has the function of utilizing the liquid refrigerant to evaporate into steam under low pressure and absorb the heat of the cooled medium so as to achieve the aim of refrigeration. The structure of the evaporator which is widely used at present is designed according to Freon or tetrafluoroethane as a working medium, although most of the existing refrigeration systems use tetrafluoroethane as a working medium instead of Freon, and the medium overcomes the defects of the Freon such as ozone layer damage, and the like, the evaporator as a refrigerant has the following problems: 1. tetrafluoroethane is extremely strong greenhouse gas, the effect of which on the greenhouse gas in the earth atmosphere is 3300 times that of the greenhouse gas carbon dioxide within 20 years of entering the atmosphere, and is still 1300 times that of the carbon dioxide within the next 100 years although attenuation is realized later, and is 400 times that within 500 years; 2. tetrafluoroethane is used as a refrigerant, although no obvious toxicity exists, the phenomenon that air conditioners do not refrigerate and the like frequently occurs when users use the tetrafluoroethane, and most of the phenomenon is the phenomenon of 'lack of fluorine', namely, the refrigerant leaks, and in fact, the refrigerant runs into the atmosphere; 3. the production of tetrafluoroethane is a huge industrial group, and a large amount of toxic and harmful substances inevitably pollute the environment and even cause damage in the production and production process of tetrafluoroethane. The above problems are solved by using a clean refrigerant as the working medium which does not produce the effect of warm room gases, but the current evaporators are not designed successfully in this respect.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide an evaporator, this evaporator use water and air, or water and the mixed liquid and the air of the liquid (for example ethanol) that evaporate easily and environmental protection under the low pressure environment as working medium.
In order to achieve the above purpose, the utility model adopts the following scheme: an evaporator is composed of a group of parallel evaporating pipelines, a liquid working medium pipeline and a gas working medium pipeline, which are communicated with each other at their inlet ends, and a discharge pipeline communicated with the outlet ends of said evaporating pipelines.
The utility model provides an evaporating temperature of evaporimeter is higher than 0 ℃, considers the relatively dull characteristics of working medium evaporation characteristic, adopts a set of evaporating line that stands side by side, and it uses in need inserting a circulation refrigerating system at the during operation, and the last port of escape canal is connected with circulation refrigerating system's vacuum generator for have higher vacuum in the evaporating pipe, in order to impel working medium's evaporation, its theory of operation is as follows: dry air and liquid working medium conveyed by a first-stage device in a refrigeration system respectively enter an evaporation pipeline through a gas working medium pipeline and a liquid working medium pipeline, liquid is evaporated due to the fact that the inside of the evaporation pipeline is in a vacuum state, saturated steam generated by evaporation can prevent the liquid from continuously evaporating, and at the moment, the dry air entering an evaporator can drive the saturated steam to leave the surface of the liquid, so that the evaporation can be continuously carried out; the metal heat conducting wires in the evaporation pipeline not only increase the evaporation area of the working medium liquid, but also can timely transfer the temperature with the evaporation pipeline, so that the low temperature generated by evaporation is timely transferred to the evaporation pipeline so as to be subjected to heat exchange utilization by people; after the liquid and the gas enter the discharge pipeline, the gas is discharged from the upper end of the channel, and the liquid is discharged from the lower end of the channel, so that the condition is provided for continuous circulation.
The working medium liquid is water or a mixed liquid of water and liquid which is easy to evaporate in a low-pressure environment and is environment-friendly, for example, the mixed liquid of water and ethanol forms combined evaporation, and the evaporation efficiency can be improved.
The utility model discloses rational in infrastructure, performance safe and reliable, it makes to evaporate easily and the liquid of environmental protection and air become possible as working medium with low pressure environment down, provides the evaporimeter of an ideal for people avoid greenhouse gas's harm.
Drawings
Fig. 1 is a schematic structural diagram of an embodiment of the present invention;
FIG. 2 is a cross-sectional view A-A of FIG. 1;
fig. 3 is a view from direction B of fig. 1.
Detailed Description
The present invention will be further described with reference to the following specific embodiments and the accompanying drawings.
See fig. 1, 2, 3
The utility model provides an evaporator has a set of evaporating pipe 2 that stands side by side, and evaporating pipe 2 adopts the good material of heat conductivity, like aluminium, copper. A heat exchange channel 4 is formed in a gap between every two adjacent evaporation pipelines 2, the inlet end of each evaporation pipeline 2 is communicated with a liquid working medium pipeline 5 and a gas working medium pipeline 6, the outlet end of each evaporation pipeline 2 is communicated with a discharge pipeline 1, metal heat conducting wires 3 are filled in each evaporation pipeline 2, the evaporation pipelines 2 are filled with the metal heat conducting wires 3, and the metal heat conducting wires 3 are reliably contacted with the inner walls of the evaporation pipelines 2.
In this embodiment, the liquid working medium pipeline 5 and the gas working medium pipeline 6 are connected in parallel, the inlet end of each evaporation pipeline 2 is connected with the outer surfaces of the liquid working medium pipeline 5 and the gas working medium pipeline 6, the liquid working medium pipeline 5 is provided with liquid discharge holes 5a which are communicated with the evaporation pipelines 2 in a one-to-one correspondence manner, and the gas working medium pipeline 6 is provided with exhaust holes 6a which are communicated with the evaporation pipelines in a one-to-one correspondence manner.
In this embodiment, the outlet ends of the evaporation pipelines 2 are connected to the outer wall of the discharge pipeline 1, and the working medium discharge pipeline 1 is provided with through holes 1c communicated with the evaporation pipelines in a one-to-one correspondence manner. The upper port 1a of the working medium discharge pipeline 1 is a vacuumizing interface, and the lower port 1b is a water outlet.
In order to better promote the evaporation of the liquid, in the embodiment, the metal heat conducting wires 3 in the evaporation pipe 2 are in a disordered net shape or a flocculent shape.
In addition, the evaporator can also be used for concentrating and purifying industrial liquid.
Claims (4)
1. An evaporator, characterized by: the device comprises a group of parallel evaporation pipelines, wherein the inlet end of each evaporation pipeline is communicated with a liquid working medium pipeline and a gas working medium pipeline, the outlet end of each evaporation pipeline is communicated with a discharge pipeline together, each evaporation pipeline is filled with metal heat conducting wires, the evaporation pipelines are filled with the metal heat conducting wires, and the metal heat conducting wires are reliably contacted with the inner walls of the evaporation pipelines.
2. An evaporator according to claim 1 wherein: the liquid working medium pipeline and the gas working medium pipeline are connected in parallel into a whole, the inlet end of each evaporation pipeline is connected with the liquid working medium pipeline and the outer surface of the gas working medium pipeline, the liquid working medium pipeline is provided with liquid discharge holes communicated with the evaporation pipelines in a one-to-one correspondence mode, and the gas working medium pipeline is provided with exhaust holes communicated with the evaporation pipelines in a one-to-one correspondence mode.
3. An evaporator according to claim 1 wherein: the outlet ends of the evaporation pipelines are connected with the outer wall of the discharge pipeline together, and the discharge pipeline is provided with through holes which are communicated with the evaporation pipelines in a one-to-one correspondence manner.
4. An evaporator according to claim 1 wherein: the metal heat-conducting wires in the evaporation pipeline are in a disordered net shape or a flocculent shape.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201921383477.7U CN210425648U (en) | 2019-08-24 | 2019-08-24 | Evaporator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201921383477.7U CN210425648U (en) | 2019-08-24 | 2019-08-24 | Evaporator |
Publications (1)
Publication Number | Publication Date |
---|---|
CN210425648U true CN210425648U (en) | 2020-04-28 |
Family
ID=70364234
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201921383477.7U Expired - Fee Related CN210425648U (en) | 2019-08-24 | 2019-08-24 | Evaporator |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN210425648U (en) |
-
2019
- 2019-08-24 CN CN201921383477.7U patent/CN210425648U/en not_active Expired - Fee Related
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20200428 |
|
CF01 | Termination of patent right due to non-payment of annual fee |