CN217058427U - Evaporative heat exchanger capable of treating air - Google Patents
Evaporative heat exchanger capable of treating air Download PDFInfo
- Publication number
- CN217058427U CN217058427U CN202220925711.XU CN202220925711U CN217058427U CN 217058427 U CN217058427 U CN 217058427U CN 202220925711 U CN202220925711 U CN 202220925711U CN 217058427 U CN217058427 U CN 217058427U
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- CN
- China
- Prior art keywords
- heat exchange
- heat exchanger
- heating panel
- wall
- exchange structure
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- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims abstract description 46
- 239000010949 copper Substances 0.000 claims abstract description 46
- 229910052802 copper Inorganic materials 0.000 claims abstract description 46
- 239000007788 liquid Substances 0.000 claims abstract description 29
- 238000010438 heat treatment Methods 0.000 claims abstract description 23
- 239000007921 spray Substances 0.000 claims abstract description 18
- 238000007670 refining Methods 0.000 claims abstract description 15
- 230000017525 heat dissipation Effects 0.000 claims description 28
- 239000010410 layer Substances 0.000 claims description 22
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 21
- 238000005507 spraying Methods 0.000 claims description 19
- 238000001179 sorption measurement Methods 0.000 claims description 15
- 239000011229 interlayer Substances 0.000 claims description 12
- 239000000463 material Substances 0.000 claims description 12
- 229910052799 carbon Inorganic materials 0.000 claims description 9
- 238000000889 atomisation Methods 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 5
- 239000000110 cooling liquid Substances 0.000 abstract description 21
- 239000002826 coolant Substances 0.000 abstract description 13
- 239000011148 porous material Substances 0.000 abstract description 10
- 230000001413 cellular effect Effects 0.000 abstract description 4
- 238000009434 installation Methods 0.000 abstract description 3
- 239000004744 fabric Substances 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 230000000694 effects Effects 0.000 description 4
- 238000002309 gasification Methods 0.000 description 4
- 238000004804 winding Methods 0.000 description 4
- 239000012530 fluid Substances 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses a can be with evaporative heat exchanger of air treatment, including the major structure, spray structure and heat exchange structure, the lower extreme outside of major structure is provided with sprays the structure, and the inside middle-end of major structure is provided with reposition of redundant personnel pipeline group, the outer wall connection of reposition of redundant personnel pipeline group has the heat exchange structure, the heat exchange structure includes that copper heating panel, round platform recess, hydrothermal solution advance the pipeline, the cold liquid goes out the pipeline and crisscross refining intermediate layer. This can be with evaporative heat exchanger of air treatment, through slope installation heat exchange structure in atomizing spray assembly below, improve area of contact between heat exchange structure and the cold liquid medium, utilize the round platform recess can increase the area of contact between copper heating panel and the air, the cooling medium, crisscross refining intermediate layer is cellular, and has seted up the connection pore each other, can be with inside the copper heating panel of required cooling liquid evenly distributed through the pore of cross connection to make the copper heating panel be heated relatively evenly.
Description
Technical Field
The utility model relates to an evaporation formula heat exchanger technical field specifically is an evaporation formula heat exchanger that can handle air.
Background
The evaporative heat exchanger can be regarded as a combined heat exchanger of a cooler and a cooling tower using water as a cooling medium. The evaporative heat exchanger flows cooled process fluid in the pipe, water and air flow outside the pipe at the same time, the heat of the fluid in the pipe is transferred to the air through the water outside the pipe, so as to achieve the purpose of cooling, the fluid to be cooled is uniformly distributed in the evaporative heat exchanger through the inclined hollow heat dissipation plate, the contact area with a cooling medium is increased, and meanwhile, the radiation heat dissipation work can be carried out, so that the heat dissipation efficiency is improved, and the full contact with the cooling liquid is realized.
The evaporative heat exchangers on the market do not have an inclined heat exchange structure, the area between the required cooling liquid and the cooling medium is generally increased through a winding pipeline, the winding pipeline only increases the cross section area, the cooling medium cannot be in full contact, and the waste of the cooling medium is easily caused.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide an evaporative heat exchanger that can handle air to solve the evaporative heat exchanger that proposes on the market among the above-mentioned background art and do not have the heat exchange structure of slope form, generally be through the area between required cooling liquid of winding's pipeline increase and the cooling medium, its winding's pipeline only increases cross sectional area, and can't fully contact between the cooling medium, causes the extravagant problem of cooling medium use easily.
In order to achieve the above object, the utility model provides a following technical scheme: the utility model provides a can be with evaporative heat exchanger of air treatment, includes major structure, sprays structure and heat exchange structure, the lower extreme outside of major structure is provided with sprays the structure, and the inside middle-end of major structure is provided with reposition of redundant personnel pipeline group, the outer wall connection of reposition of redundant personnel pipeline group has the heat exchange structure, the heat exchange structure includes copper heating panel, round platform recess, hydrothermal solution inlet pipe, cold liquid outlet pipe and crisscross refining intermediate layer, and the round platform recess has been seted up to the outer wall both sides of copper heating panel, hydrothermal solution inlet pipe has been seted up to the upper end outer wall both sides of copper heating panel, and the lower extreme outer wall both sides of copper heating panel have seted up cold liquid outlet pipe, the inside of copper heating panel is provided with crisscross refining intermediate layer.
Furthermore, the heat exchange structure is communicated with the shunt pipeline group, and the heat exchange structure is even in an inclined shape and is connected with the shunt pipeline group.
Further, round platform recess evenly distributed is in copper heating panel outer wall both sides, and mutually supports between round platform recess and the reposition of redundant personnel pipeline group.
Furthermore, the copper heat dissipation plate is wrapped on the staggered material refining interlayer, and the staggered material refining interlayer is in a staggered hollow shape.
Further, the major structure includes organism, collecting vat, even cloth ware, honeycomb dislocation vortex subassembly and active carbon adsorption layer, and the inside lower extreme of organism is provided with the collecting vat, the inside upper end of organism is provided with even cloth ware, and just the top of even cloth ware is provided with and is provided with honeycomb dislocation vortex subassembly, the top of honeycomb dislocation vortex subassembly is provided with active carbon adsorption layer.
Furthermore, the activated carbon adsorption layer is clamped inside the machine body, and the activated carbon adsorption layer is matched with the uniform distributor and the honeycomb dislocation turbulent flow assembly.
Further, the spraying structure comprises a cold liquid storage tank body, a booster pump, a spraying pipeline and an atomization spraying assembly, wherein the booster pump is arranged on one side of the outer wall of the cold liquid storage tank body, the spraying pipeline is connected to one side of the outer wall of the booster pump, and one end of the outer wall of the spraying pipeline is connected with the atomization spraying assembly.
Compared with the prior art, the beneficial effects of the utility model are that: this can be with evaporative heat exchanger of air treatment, through slope installation heat exchange structure in atomizing spray assembly below, improve area of contact between heat exchange structure and the cold liquid medium, utilize the round platform recess can increase the area of contact between copper heating panel and the air, the cooling medium, crisscross refining intermediate layer is cellular, and has seted up the connection pore each other, can be with inside the copper heating panel of required cooling liquid evenly distributed through the pore of cross connection to make the copper heating panel be heated relatively evenly.
Be linked together between heat exchange structure and the reposition of redundant personnel pipeline group, through slope installation heat exchange structure in atomizing spray assembly below, improve area of contact between heat exchange structure and the cold liquid medium, and misplace each other between the heat exchange structure to the rate of utilization of effectual improvement cold liquid medium reduces cooling liquid and uses extravagantly.
The round platform grooves are evenly distributed on two sides of the outer wall of the copper heat dissipation plate, and the contact area between the copper heat dissipation plate and air and cooling media can be increased through the round platform grooves arranged on the outer wall of the copper heat dissipation plate, so that the heat dissipation effect is improved.
Copper heating panel wraps up in crisscross refining intermediate layer, and crisscross refining intermediate layer is cellular, and has seted up the connecting pore each other, and can be inside required cooling liquid evenly distributed copper heating panel through cross connection's pore to it is relatively even to make copper heating panel be heated, and compares the evaporative heat exchanger of pipeline form, improves cooling liquid and copper heating panel area of contact in step, supplementary improvement radiating effect.
Drawings
FIG. 1 is a schematic view of the internal front view structure of the present invention;
FIG. 2 is a schematic view of the heat exchange structure of the present invention;
FIG. 3 is a schematic view of the heat exchange structure of the present invention in a partial interior elevation view;
fig. 4 is a schematic view of a part of an enlarged structure at a in fig. 3 according to the present invention.
In the figure: 1. a body structure; 101. a body; 102. collecting tank; 103. a cloth evening device; 104. A honeycomb dislocation spoiler assembly; 105. an activated carbon adsorption layer; 2. a spraying structure; 201. a cold liquid storage tank; 202. a booster pump; 203. a spray pipe; 204. an atomizing spray assembly; 3. A shunt pipe group; 4. a heat exchange structure; 401. a copper heat dissipation plate; 402. a circular truncated cone groove; 403. Hot liquid enters a pipeline; 404. a cold liquid outlet pipeline; 405. and (4) staggered material homogenizing interlayers.
Detailed Description
As shown in fig. 1, an evaporative heat exchanger for treating air, comprising: the main structure 1, a spraying structure 2 is arranged outside the lower end of the main structure 1, a diversion pipeline group 3 is arranged at the middle end inside the main structure 1, a heat exchange structure 4 is connected to the outer wall of the diversion pipeline group 3, the main structure 1 comprises a machine body 101, a collecting tank 102, a cloth distributor 103, a honeycomb dislocation turbulent flow component 104 and an active carbon adsorption layer 105, the collecting tank 102 is arranged at the lower end inside the machine body 101, the cloth distributor 103 is arranged at the upper end inside the machine body 101, the honeycomb dislocation turbulent flow component 104 is arranged above the cloth distributor 103, the active carbon adsorption layer 105 is arranged above the honeycomb dislocation turbulent flow component 104, the active carbon adsorption layer 105 is clamped inside the machine body 101, the active carbon adsorption layer 105 is matched with the cloth distributor 103 and the honeycomb dislocation turbulent flow component 104, cooling liquid generally works by spraying low-temperature water, water vapor can be uniformly distributed and guided to the honeycomb dislocation turbulent flow component 104 by the cloth distributor 103, utilize honeycomb dislocation vortex subassembly 104 increase area of contact between steam and its inner wall, thereby make the condensation of part gasification cooling liquid become liquid, be convenient for collect, last accessible activated carbon adsorption layer 105 filters all the other inside air impurity of gasification cooling liquid, improve the standard of collecting, reduce the condition that the too much impurity of recycling leads to connecting tube and machine to appear blockking up easily, it includes cold liquid storage tank body 201 to spray structure 2, the booster pump 202, spray pipe 203 and atomizing spray subassembly 204, and outer wall one side of cold liquid storage tank body 201 is provided with booster pump 202, outer wall one side of booster pump 202 is connected with spray pipe 203, and the outer wall one end of spray pipe 203 is connected with atomizing spray subassembly 204.
As shown in fig. 2-4, an evaporative heat exchanger capable of treating air, a heat exchange structure 4 comprises a copper heat dissipation plate 401, circular truncated cone grooves 402, hot liquid inlet pipes 403, cold liquid outlet pipes 404 and staggered material refining interlayers 405, the circular truncated cone grooves 402 are formed on two sides of the outer wall of the copper heat dissipation plate 401, the hot liquid inlet pipes 403 are formed on two sides of the outer wall of the upper end of the copper heat dissipation plate 401, the cold liquid outlet pipes 404 are formed on two sides of the outer wall of the lower end of the copper heat dissipation plate 401, the staggered material refining interlayers 405 are formed inside the copper heat dissipation plate 401, the heat exchange structure 4 is communicated with a diversion pipe set 3, the heat exchange structure 4 is uniformly connected with the diversion pipe set 3 in an inclined manner, the heat exchange structure 4 is obliquely installed below an atomizing spray assembly 204, the contact area between the heat exchange structure 4 and a cold liquid medium is increased, and the heat exchange structures 4 are staggered with each other, thereby effectively improving the utilization rate of a cold liquid medium and reducing the use waste of cooling liquid, the circular truncated cone grooves 402 are uniformly distributed at two sides of the outer wall of the copper heat dissipation plate 401, the circular truncated cone grooves 402 are matched with the flow distribution pipeline group 3, the contact area between the copper heat dissipation plate 401 and air and the cooling medium can be increased through the circular truncated cone grooves 402 arranged at the outer wall of the copper heat dissipation plate 401, thereby improving the heat dissipation effect, the copper heat dissipation plate 401 is wrapped in the staggered material uniformizing interlayer 405, the staggered material uniformizing interlayer 405 is in a staggered hollow shape, the staggered material uniformizing interlayer 405 is in a honeycomb shape, and connecting pore channels are arranged among the staggered material uniformizing interlayers, the required cooling liquid can be uniformly distributed inside the copper heat dissipation plate 401 through the pore channels which are in staggered connection, thereby enabling the copper heat dissipation plate 401 to be heated relatively uniformly, and compared with an evaporative heat exchanger in a pipeline shape, the contact area between the cooling liquid and the copper heat dissipation plate 401 is synchronously improved, and the heat dissipation effect is improved in an auxiliary manner.
In summary, in the evaporative heat exchanger capable of processing air, firstly, one end of the upper end diversion pipe group 3 is connected with the input port of the required cooling liquid, one end of the lower end diversion pipe group 3 is connected with the collection storage tank, then the booster pump 202 is synchronously started, the cooling liquid is conveyed to the atomization spraying component 204 through the cold liquid storage tank 201 and the spraying pipeline 203 for covering spraying work, then the input port valve is started, the cooling liquid is conveyed to the hot liquid inlet pipe 403 through the diversion pipe group 3, the staggered material homogenizing interlayer 405 is cellular and is provided with connecting pore channels, the required cooling liquid can be uniformly distributed in the copper heat dissipation plate 401 through the staggered connecting pore channels, so that the copper heat dissipation plate 401 is heated relatively uniformly, and meanwhile, the circular platform grooves 402 arranged on the outer wall of the copper heat dissipation plate 401 can increase the size of the copper heat dissipation plate 401 and the air dissipation plate 401, the air dissipation plate and the cooling plate, Area of contact between the cooling medium, install heat exchange structure 4 in atomizing spray assembly 204 below through the slope after that, area of contact between improvement heat exchange structure 4 and the cold liquid medium, and misplace each other between the heat exchange structure 4, thereby effectual improvement cold liquid medium rate of utilization, it is extravagant to reduce the cooling liquid use, the gasification that is heated of final part cooling medium rises, can be with water vapor evenly distributed water conservancy diversion to honeycomb dislocation vortex subassembly 104 department through even cloth ware 103, utilize honeycomb dislocation vortex subassembly 104 increase water vapor and the area of contact between its inner wall, filter all the other inside air impurity of gasification cooling liquid through active carbon adsorption layer 105, part cooling liquid directly flows in collecting vat 102, collect through the connecting tube.
Claims (7)
1. An evaporative heat exchanger capable of treating air, which comprises a main body structure (1), a spraying structure (2) and a heat exchange structure (4), and is characterized in that: the utility model discloses a copper cooling plate, including main structure (1), the lower extreme outside of main structure (1) is provided with sprays structure (2), and the inside middle-end of main structure (1) is provided with reposition of redundant personnel pipeline group (3), the outer wall connection of reposition of redundant personnel pipeline group (3) has heat exchange structure (4), heat exchange structure (4) are including copper heating panel (401), round platform recess (402), hydrothermal solution inlet pipe way (403), cold liquid outlet pipe way (404) and crisscross refining intermediate layer (405), and round platform recess (402) have been seted up to the outer wall both sides of copper heating panel (401), hydrothermal solution inlet pipe way (403) have been seted up to the upper end outer wall both sides of copper heating panel (401), and the cold liquid outlet pipe way (404) have been seted up to the lower extreme outer wall both sides of copper heating panel (401), the inside of copper heating panel (401) is provided with crisscross refining intermediate layer (405).
2. An evaporative heat exchanger for the treatment of air according to claim 1, wherein: the heat exchange structure (4) is communicated with the shunt pipeline set (3), and the heat exchange structure (4) is in an inclined shape and is uniformly connected with the shunt pipeline set (3).
3. An evaporative heat exchanger for the treatment of air, according to claim 1, wherein: circular truncated cone recess (402) evenly distributed is in copper heating panel (401) outer wall both sides, and mutually supports between circular truncated cone recess (402) and reposition of redundant personnel pipeline group (3).
4. An evaporative heat exchanger for the treatment of air according to claim 1, wherein: the copper heat dissipation plate (401) is wrapped on the staggered material refining interlayer (405), and the staggered material refining interlayer (405) is in a staggered hollow shape.
5. An evaporative heat exchanger for the treatment of air, according to claim 1, wherein: main part structure (1) is including organism (101), collecting vat (102), even ware (103), honeycomb dislocation vortex subassembly (104) and active carbon adsorption layer (105), and the inside lower extreme of organism (101) is provided with collecting vat (102), the inside upper end of organism (101) is provided with even ware (103), and the top of even ware (103) is provided with honeycomb dislocation vortex subassembly (104), the top of honeycomb dislocation vortex subassembly (104) is provided with active carbon adsorption layer (105).
6. An evaporative heat exchanger for the treatment of air according to claim 5, wherein: the activated carbon adsorption layer (105) is clamped inside the machine body (101), and the activated carbon adsorption layer (105) is matched with the uniform distributor (103) and the honeycomb dislocation turbulent flow component (104).
7. An evaporative heat exchanger for the treatment of air, according to claim 1, wherein: the spraying structure (2) comprises a cold liquid storage tank body (201), a booster pump (202), a spraying pipeline (203) and an atomization spraying assembly (204), wherein the booster pump (202) is arranged on one side of the outer wall of the cold liquid storage tank body (201), the spraying pipeline (203) is connected on one side of the outer wall of the booster pump (202), and the atomization spraying assembly (204) is connected on one end of the outer wall of the spraying pipeline (203).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220925711.XU CN217058427U (en) | 2022-04-21 | 2022-04-21 | Evaporative heat exchanger capable of treating air |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220925711.XU CN217058427U (en) | 2022-04-21 | 2022-04-21 | Evaporative heat exchanger capable of treating air |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217058427U true CN217058427U (en) | 2022-07-26 |
Family
ID=82473844
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202220925711.XU Expired - Fee Related CN217058427U (en) | 2022-04-21 | 2022-04-21 | Evaporative heat exchanger capable of treating air |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217058427U (en) |
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2022
- 2022-04-21 CN CN202220925711.XU patent/CN217058427U/en not_active Expired - Fee Related
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| 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: 20220726 |
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| CF01 | Termination of patent right due to non-payment of annual fee |