CN215832519U - Multilayer mixing efficient fog dissipation water-saving cooling tower - Google Patents
Multilayer mixing efficient fog dissipation water-saving cooling tower Download PDFInfo
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- CN215832519U CN215832519U CN202122311826.8U CN202122311826U CN215832519U CN 215832519 U CN215832519 U CN 215832519U CN 202122311826 U CN202122311826 U CN 202122311826U CN 215832519 U CN215832519 U CN 215832519U
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Abstract
The utility model relates to the technical field of cooling towers, in particular to a multilayer mixed efficient fog-dissipation water-saving cooling tower; comprises a tower body, a water distribution system, a filler and a fan; an air chamber is arranged above the water distribution system, a plurality of groups of heat exchange modules are transversely arranged in the air chamber, a plurality of groups of damp and hot air heat exchange channels and a plurality of groups of dry and cold air heat exchange channels are respectively arranged in the plurality of groups of heat exchange modules, the tops of the plurality of groups of damp and hot air heat exchange channels are respectively communicated with a damp and hot air outlet, the tops of the plurality of groups of dry and cold air heat exchange channels are respectively communicated with a dry and cold air outlet, the bottoms of the plurality of groups of heat exchange modules are respectively provided with a plurality of groups of damp and hot air channels and a plurality of groups of dry and cold air channels, the bottoms of the plurality of groups of dry and cold air channels are respectively provided with an adjustable air door, the front end and the rear end of the tower body are respectively provided with a first air inlet communicated with the dry and cold air channels, and the lower half area of the tower body is provided with a second air inlet; the cooling tower saves water resources, improves fog dispersal effect, and reduces the influence of fog on the surrounding environment and traffic.
Description
Technical Field
The utility model relates to the technical field of cooling towers, in particular to a multilayer mixed efficient fog-dissipation water-saving cooling tower.
Background
The cooling tower is a device for cooling industrial circulating water, and the existing cooling tower generally comprises a tower body, a fan, a water distribution system and a filler, and a large amount of circulating water is evaporated in the evaporation of the cooling tower, which wastes water resources, and a large amount of visible fog can be generated in cold seasons, so that the pollution to the air environment is caused, and the traffic safety is influenced.
SUMMERY OF THE UTILITY MODEL
Technical problem to be solved
Aiming at the defects of the prior art, the utility model provides the multilayer mixed efficient fog dispersal water-saving cooling tower, which saves water resources, improves the fog dispersal effect, reduces the influence of fog on the surrounding environment and traffic, and improves the applicability.
(II) technical scheme
In order to achieve the purpose, the utility model provides the following technical scheme: a multilayer mixed efficient fog-dissipation water-saving cooling tower comprises a tower body, wherein a water distribution system and a filler are arranged inside the tower body, an air cylinder is arranged at the top of the tower body, and a fan is arranged at the air cylinder; an air chamber is arranged above the water distribution system, a plurality of groups of heat exchange modules are transversely arranged in the air chamber, a plurality of groups of damp and hot air heat exchange channels and a plurality of groups of dry and cold air heat exchange channels are respectively arranged in the plurality of groups of heat exchange modules, the plurality of groups of damp and hot air heat exchange channels and the plurality of groups of dry and cold air heat exchange channels are arranged at intervals, the tops of the plurality of groups of damp and hot air heat exchange channels are respectively communicated with a damp and hot air outlet, the tops of the plurality of groups of dry and cold air heat exchange channels are respectively communicated with a dry and cold air outlet, the bottom ends of the plurality of groups of heat exchange modules are respectively provided with a plurality of groups of damp and hot air channels and a plurality of groups of dry and cold air channels, the bottoms of the plurality of groups of damp and hot air heat exchange channels are respectively communicated with a damp and hot air inlet communicated with the damp and hot air channels, the bottom ends of the multiple groups of dry and cold air heat exchange channels are all communicated with dry and cold air inlets communicated with the dry and cold air channels, and the lower half area of the tower body is provided with a second air inlet.
Preferably, a plurality of groups of clapboards are vertically arranged in the air chamber and are positioned below the plurality of groups of heat exchange modules, and the plurality of groups of wet hot air channels and the plurality of groups of dry cold air channels are separated by the plurality of groups of clapboards.
Preferably, the transverse lengths of the hot humid air heat exchange channel and the dry cold air heat exchange channel are matched with the transverse length of the heat exchange module.
Preferably, the hot humid air channel has a lateral width equal to that of the cold dry air channel.
Preferably, the hot and humid air channel has a lateral width greater than that of the cold and dry air channel.
Preferably, the hot humid air channel has a transverse width smaller than that of the cold dry air channel.
Preferably, a hot and humid air distribution channel is arranged between the hot and humid air heat exchange channel and the hot and humid air inlet, the top of the hot and humid air distribution channel is communicated with the hot and humid air heat exchange channel, the bottom of the hot and humid air distribution channel is gradually contracted and communicated with the hot and humid air inlet, a dry and cold air distribution channel is arranged between the dry and cold air channel and the dry and cold air inlet, the top of the dry and cold air distribution channel is communicated with the dry and cold air heat exchange channel, and the bottom of the dry and cold air distribution channel is gradually contracted and communicated with the dry and cold air inlet.
Preferably, the heat exchange module comprises a plurality of groups of A plastic sheets and B plastic sheets which are arranged at intervals, a plurality of groups of concave-convex positioning connection structures which are matched with each other are arranged on the A plastic sheets and the B plastic sheets and are used for buckling the adjacent A plastic sheets and the adjacent B plastic sheets together, the moist heat air heat exchange channel and the moist heat air distribution channel are positioned between the adjacent group of A plastic sheets and the adjacent group of B plastic sheets, and the dry cold air heat exchange channel and the dry cold air distribution channel are positioned between the adjacent group of B plastic sheets and the adjacent group of A plastic sheets.
Preferably, a plurality of groups of sine wave structures which are arranged in a staggered mode are arranged on the plastic sheet A and the plastic sheet B.
(III) advantageous effects
Compared with the prior art, the utility model provides a multilayer mixed efficient fog dispersal water-saving cooling tower which has the following beneficial effects:
1. the multilayer mixed efficient fog-dissipation water-saving cooling tower sprays circulating hot water on fillers in a tower body through a water distribution system, a water film is formed on the fillers, external dry cold air enters the tower body from a second air inlet and exchanges heat with the circulating hot water at the filler position to cool the circulating hot water, the dry cold air is changed into damp hot air after passing through the fillers, the damp hot air enters a damp hot air channel and enters a damp hot air heat exchange channel of a heat exchange module through a damp hot air inlet, external dry cold air enters a dry cold air channel through first air inlets on the front side and the rear side and enters a dry cold air heat exchange channel of the heat exchange module through a dry cold air inlet, the damp hot air and the dry cold air carry out partition wall heat transfer in the heat exchange module, the saturated wet hot air is cooled and condensed to form small water drops to fall down, and water resources are saved;
2. according to the multilayer mixed efficient fog-dissipation water-saving cooling tower, the wet and hot air is cooled and condensed by the heat exchange module to form small water drops to fall back, the dry and cold air is changed into dry and warm air after temperature rise, and the dry and warm air and the wet and hot air after temperature reduction and condensation are mixed at the top outlet of the heat exchange module to reduce the relative humidity of the air, so that the fog is eliminated, and the wet and hot air outlet and the dry and cold air outlet are arranged at intervals, so that the gas can be ensured to be fully mixed, and the fog dissipation effect is good;
3. according to the multilayer mixed efficient fog-dissipation water-saving cooling tower, moist hot air and dry cold air enter the heat exchange module in the same direction and are discharged out of the heat exchange module in the same direction, and the air flow direction in the heat exchange module is consistent with the air flow direction in the cooling tower, so that the wind resistance is reduced, and the energy consumption of a motor is reduced;
4. this high-efficient fog dispersal water conservation cooling tower is mixed to multilayer, and hot humid air and dry cold air syntropy get into heat transfer module, and syntropy discharge heat transfer module compares in current rhombus and arranges heat transfer module, can be so that gas after the heat transfer more abundant mix behind discharge heat transfer module, improves fog dispersal effect.
Drawings
FIG. 1 is a schematic plan view of the present invention;
FIG. 2 is a schematic side view of the present invention;
FIG. 3 is a partial perspective view of a heat exchange module according to the present invention;
FIG. 4 is an enlarged view of a portion of FIG. 3;
FIG. 5 is a partial schematic view of another angle configuration of the heat exchange module of the present invention;
FIG. 6 is a schematic perspective view of a plastic sheet A according to the present invention;
FIG. 7 is an enlarged view of a portion of FIG. 6B;
FIG. 8 is a schematic perspective view of a plastic sheet B according to the present invention;
in the drawings, the reference numbers: 1. a tower body; 2. a water distribution system; 3. a filler; 4. an air duct; 5. a fan; 6. an air chamber; 7. a heat exchange module; 8. a hot and humid air heat exchange channel; 9. a dry and cold air heat exchange channel; 10. a hot and humid air outlet; 11. a dry and cold air outlet; 12. a hot and humid air path; 13. a dry and cool air channel; 14. an adjustable air door; 15. a first air inlet; 16. a hot and humid air inlet; 17. a dry and cold air inlet; 18. a second air inlet; 19. a partition plate; 20. a hot and humid air distribution channel; 21. a dry and cool air distribution channel; 22. a, plastic sheets; 23. b, plastic sheet; 24. a concave-convex positioning connection structure; 25. a sine wave structure; 26. a blind window.
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. 1-8, the multilayer mixed efficient fog-dispersal water-saving cooling tower comprises a tower body 1, a water distribution system 2 and a filler 3 are arranged inside the tower body 1, an air duct 4 is arranged at the top of the tower body 1, and a fan 5 is arranged at the air duct 4; an air chamber 6 is arranged above the water distribution system 2, a plurality of groups of heat exchange modules 7 are transversely arranged in the air chamber 6, a plurality of groups of damp and hot air heat exchange channels 8 and a plurality of groups of dry and cold air heat exchange channels 9 are arranged in each group of heat exchange modules 7, the plurality of groups of damp and hot air heat exchange channels 8 and the plurality of groups of dry and cold air heat exchange channels 9 are arranged at intervals, the tops of the plurality of groups of damp and hot air heat exchange channels 8 are communicated with a damp and hot air outlet 10, the tops of the plurality of groups of dry and cold air heat exchange channels 9 are communicated with a dry and cold air outlet 11, the bottom end of each group of heat exchange modules 7 is provided with a plurality of groups of damp and hot air channels 12 and a plurality of groups of dry and cold air channels 13, the bottoms of the plurality of dry and cold air channels 13 are provided with adjustable air doors 14, the front end and the rear end of each group of heat exchange modules 1 are provided with a first air inlet 15 communicated with the dry and cold air channels 13, a shutter 26 is arranged at the first air inlet 15 to adjust the air inlet amount, the optimal fog dissipation effect is ensured, the multiple groups of wet and hot air channels 12 and the multiple groups of dry and cold air channels 13 are arranged at intervals, wet and hot air inlets 16 communicated with the wet and hot air channels 12 are formed in the bottom ends of the multiple groups of wet and hot air heat exchange channels 8, dry and cold air inlets 17 communicated with the dry and cold air channels 13 are formed in the bottom ends of the multiple groups of dry and cold air heat exchange channels 9, and second air inlets 18 are formed in the lower half area of the tower body 1.
In the application, circulating hot water is sprayed on the filler 3 in the tower body 1 through the water distribution system 2, a water film is formed on the filler 3, external dry and cold air enters the tower body 1 from the second air inlet 18 and exchanges heat with the circulating hot water at the filler 3, the circulating hot water is cooled, the dry and cold air is changed into damp and hot air after passing through the filler 3, the damp and hot air enters the damp and hot air channel 12 and enters the damp and hot air heat exchange channel 8 of the heat exchange module 7 through the damp and hot air inlet 16, external dry and cold air enters the dry and cold air channel through the first air inlets 15 on the front side and the rear side and enters the dry and cold air heat exchange channel 9 of the heat exchange module 7 through the dry and cold air inlet 17, the damp and hot air and the dry air carry out heat transfer partition wall in the heat exchange module 7, the saturated wet and hot air is cooled and condensed to form small water drops to fall, and water resources are saved; the damp and hot air is cooled and condensed by the heat exchange module 7 to form small water drops to fall back, the dry and cold air is changed into dry and warm air after temperature rise, the dry and warm air and the warm and damp and hot air after temperature reduction and condensation are mixed at the top outlet of the heat exchange module 7, the relative humidity of the air is reduced, and therefore, the fog is eliminated, the damp and hot air outlet 10 and the dry and cold air outlet 11 are arranged at intervals, so that the gas can be fully mixed, and the fog elimination effect is good; the wet hot air and the dry cold air enter the heat exchange module 7 in the same direction and are discharged out of the heat exchange module 7 in the same direction, and the air flow direction in the heat exchange module 7 is consistent with the air flow direction in the cooling tower, so that the wind resistance is reduced, and the energy consumption of the motor is reduced; humid hot air and dry cold air syntropy get into heat transfer module 7, syntropy discharge heat transfer module 7 compares in current rhombus and arranges heat transfer module 7, can be so that the gas after the heat transfer more abundant mix behind discharge heat transfer module 7, improves fog dispersal effect.
Optionally, a plurality of groups of partition plates 19 are vertically arranged in the air chamber 6, the plurality of groups of partition plates 19 are located below the plurality of groups of heat exchange modules 7, and the plurality of groups of hot and humid air channels 12 and the plurality of groups of cold and dry air channels 13 are separated by the plurality of groups of partition plates 19.
A damp and hot air channel 12 and a dry and cold air channel 13 are separated below a heat exchange module 7 in an air chamber 6 through a partition plate 19, the bottom of the damp and hot air channel 12 is communicated with the air chamber 6, the dry and cold air channel 13 is sealed with the air chamber 6 through an adjustable air door 14, in the specific use process, the adjustable air door 14 can be fully or partially opened, and when the adjustable air door 14 is closed, a shutter of a corresponding first air inlet 15 is opened.
Optionally, the transverse lengths of the hot and humid air heat exchange channels 8 and the dry and cold air heat exchange channels 9 are matched with the transverse length of the heat exchange module 7.
Humid and hot air heat transfer passageway 8 and dry and cold air heat transfer passageway 9 distribute in the transverse section of whole heat transfer module 7, and the air is vertical upflow in humid and hot air heat transfer passageway 8 and dry and cold air heat transfer passageway 9 in addition, reduces the windage to the at utmost, improves the heat transfer effect, improves the mixed effect behind the gas outgoing heat transfer module 7.
Optionally, a hot and humid air distribution channel 20 is disposed between the hot and humid air heat exchange channel 8 and the hot and humid air inlet 16, the top of the hot and humid air distribution channel 20 is communicated with the hot and humid air heat exchange channel 8, the bottom of the hot and humid air distribution channel 20 is gradually contracted and communicated with the hot and humid air inlet 16, a dry and cold air distribution channel 21 is disposed between the dry and cold air channel 13 and the dry and cold air inlet 17, the top of the dry and cold air distribution channel 21 is communicated with the dry and cold air heat exchange channel 9, and the bottom of the dry and cold air distribution channel 21 is gradually contracted and communicated with the dry and cold air inlet 17.
The damp and hot air enters the damp and hot air distribution channel 20 from the damp and hot air inlet 16 to be uniformly distributed and dispersed, and then is distributed in the whole damp and hot air heat exchange channel 8; the dry cold air gets into dry cold air distribution passageway 21 from dry cold air inlet 17 and carries out the equipartition dispersion, then distributes in whole dry cold air heat transfer passageway 9, compares in the unchangeable heat transfer form of current heat transfer passageway one-tenth, and the space in the cooling tower that can make full use of increases heat transfer area under the condition of same heat exchange module 7 height, improves heat transfer effect.
Alternatively, the transverse width of the hot humid air channel 12 is equal to the transverse width of the cold dry air channel 13.
Alternatively, the transverse width of the hot humid air channel 12 is greater than the transverse width of the cold dry air channel 13.
Alternatively, the transverse width of the hot humid air channel 12 is smaller than the transverse width of the cold dry air channel 13.
The hot humid air path 12 and the cold dry air path 13 may be arranged in different proportions according to actual circumstances.
Specifically, the width of the hot and humid air path 12 may be set to be greater than the width of the dry and cold air path 13 for an area where the temperature is low in winter, and the width of the hot and humid air path 12 may be set to be less than the width of the dry and cold air path 13 for an area where the temperature is not significant in winter.
Referring to fig. 3-8, the heat exchange module 7 includes a plurality of sets of a plastic sheets 22 and B plastic sheets 23 arranged at intervals, a plurality of sets of concave-convex positioning connection structures 24 matched with each other are arranged on the a plastic sheets 22 and the B plastic sheets 23 for fastening the adjacent a plastic sheets 22 and B plastic sheets 23 together, the hot and humid air heat exchange channel 8 and the hot and humid air distribution channel 20 are located between the adjacent set of a plastic sheets 22 and the set of B plastic sheets 23, and the dry and cold air heat exchange channel 9 and the dry and cold air distribution channel 21 are located between the adjacent set of B plastic sheets 23 and the set of a plastic sheets 22.
A moulds piece 22 and B and moulds piece 23 and carry out the location assembly through unsmooth location connection structure 24, convenient equipment to guarantee to assemble heat exchange module 7's stability, heat exchange module 7 is the cuboid structure, need not to hoist in tower body 1, and is easy to assemble, and improves stability.
Specifically, the concave-convex positioning connection structure 24 at the hot and humid air distribution passage 20 and the cold and dry air distribution passage 21 is a long strip with a guiding function.
The concave-convex positioning and connecting structure 24 positioned at the hot and humid air heat exchange channel 8 and the dry and cold air heat exchange channel 9 is in a cylindrical or circular truncated cone structure.
The hot and humid air distribution channel 20 and the dry and cold air distribution channel 21 are separated by convex strips on the plastic sheets A22 and the plastic sheets B23, and each hot and humid air heat exchange channel 8 corresponds to a plurality of hot and humid air distribution channels 20, so that the hot and humid air can be uniformly distributed in the hot and humid air heat exchange channels 8; each of the dry and cool air heat exchange channels 9 corresponds to a plurality of dry and cool air distribution channels 21 so that the dry and cool air can be uniformly distributed to the dry and cool air heat exchange channels 9.
The plastic sheet A22 and the plastic sheet B23 are provided with a plurality of groups of sine wave structures 25 which are arranged in a staggered manner; the positive sine wave structures are distributed at the positions of the moist heat exchange channel and the dry cold heat exchange channel of the A plastic sheet 22 and the B plastic sheet 23, and the positive sine wave structures which are arranged in a staggered mode are beneficial to forming air turbulence in the flowing process of moist heat air and dry cold air, so that the heat exchange performance is enhanced.
A water distributor is arranged below the heat exchange module 7 and is positioned at a hot and humid air inlet of the heat exchange module; the water condensed and collected by the heat exchange module 7 is guided by the water guide mechanism, and the water is guided to the lower water tank by the guide mechanism.
The working process of the application is as follows:
circulating hot water is sprayed on the filler 3 in the tower body 1 through the water distribution system 2, a water film is formed on the filler 3, outside dry and cold air enters the tower body 1 from the second air inlet 18 and exchanges heat with the circulating hot water at the filler 3, the circulating hot water is cooled, the dry and cold air is changed into damp and hot air after passing through the filler 3, the damp and hot air enters the damp and hot air channel 12 and enters the damp and hot air heat exchange channel 8 of the heat exchange module 7 through the damp and hot air inlet 16, outside dry and cold air enters the dry and cold air channel through the first air inlets 15 at the front side and the rear side and enters the dry and cold air heat exchange channel 9 of the heat exchange module 7 through the dry and cold air inlet 17, the damp and hot air and the dry and cold air carry out partition wall heat transfer in the heat exchange module 7, saturated damp and hot air is cooled and condensed to form small water drops to fall, and water resources are saved; the damp and hot air is cooled and condensed by the heat exchange module 7 to form small water drops to fall back, the dry and cold air is changed into dry and warm air after temperature rise, the dry and warm air and the warm and damp and hot air after temperature reduction and condensation are mixed at the top outlet of the heat exchange module 7, the relative humidity of the air is reduced, and therefore, the fog is eliminated, the damp and hot air outlet 10 and the dry and cold air outlet 11 are arranged at intervals, so that the gas can be fully mixed, and the fog elimination effect is good; the wet hot air and the dry cold air enter the heat exchange module 7 in the same direction and are discharged out of the heat exchange module 7 in the same direction, and the air flow direction in the heat exchange module 7 is consistent with the air flow direction in the cooling tower, so that the wind resistance is reduced, and the energy consumption of the motor is reduced; humid hot air and dry cold air syntropy get into heat transfer module 7, syntropy discharge heat transfer module 7 compares in current rhombus and arranges heat transfer module 7, can be so that the gas after the heat transfer more abundant mix behind discharge heat transfer module 7, improves fog dispersal effect.
It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
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 (9)
1. A multilayer mixed efficient fog-dissipation water-saving cooling tower comprises a tower body (1), wherein a water distribution system (2) and a filler (3) are arranged inside the tower body (1), an air cylinder (4) is arranged at the top of the tower body (1), and a fan (5) is arranged at the air cylinder (4); the device is characterized in that an air chamber (6) is arranged above the water distribution system (2), a plurality of groups of heat exchange modules (7) are transversely arranged in the air chamber (6), a plurality of groups of wet hot air heat exchange channels (8) and a plurality of groups of dry cold air heat exchange channels (9) are respectively arranged in the plurality of groups of heat exchange modules (7), the plurality of groups of wet hot air heat exchange channels (8) and the plurality of groups of dry cold air heat exchange channels (9) are arranged at intervals, wet hot air outlets (10) are respectively communicated with the tops of the plurality of groups of wet hot air heat exchange channels (8), dry cold air outlets (11) are respectively communicated with the tops of the plurality of groups of dry cold air heat exchange channels (9), a plurality of groups of wet hot air channels (12) and a plurality of groups of dry cold air channels (13) are arranged at the bottom of the plurality of groups of heat exchange modules (7), and adjustable air doors (14) are respectively arranged at the bottoms of the plurality of groups of dry cold air channels (13), both ends all are provided with first air intake (15) with dry cold air passageway (13) intercommunication around tower body (1), multiunit damp and hot air passageway (12) with multiunit dry cold air passageway (13) interval sets up, and the bottom of multiunit damp and hot air heat transfer passageway (8) all communicates and is provided with communicating damp and hot air inlet (16) with damp and hot air passageway (12), and the bottom of multiunit dry cold air heat transfer passageway (9) all communicates and is provided with communicating dry cold air inlet (17) with dry cold air passageway (13), the lower half region of tower body (1) is provided with second air intake (18).
2. The multilayer mixing efficient fog dispersal water-saving cooling tower according to claim 1, wherein a plurality of groups of partition plates (19) are vertically arranged in the air chamber (6), the plurality of groups of partition plates (19) are positioned below a plurality of groups of heat exchange modules (7), and the plurality of groups of wet hot air channels (12) and the plurality of groups of dry cold air channels (13) are separated by the plurality of groups of partition plates (19).
3. The multilayer mixed efficient fog dispersal water-saving cooling tower as claimed in claim 1, wherein the transverse length of said hot humid air heat exchange channel (8) and said cold dry air heat exchange channel (9) matches the transverse length of said heat exchange module (7).
4. The multi-layer mixing high-efficiency fog dispersal water-saving cooling tower as claimed in claim 3, wherein the transverse width of the hot and humid air channel (12) is equal to the transverse width of the dry and cold air channel (13).
5. The multi-layer mixing high-efficiency fog dispersal water-saving cooling tower of claim 3, wherein the transverse width of the hot and humid air channel (12) is greater than the transverse width of the cold and dry air channel (13).
6. The multi-layer mixing high-efficiency fog dispersal water-saving cooling tower of claim 3, wherein the transverse width of the hot and humid air channel (12) is smaller than the transverse width of the cold and dry air channel (13).
7. The multilayer mixing high-efficiency fog-dissipating water-saving cooling tower as claimed in claim 1, wherein a hot and humid air distribution channel (20) is arranged between the hot and humid air heat exchange channel (8) and the hot and humid air inlet (16), the top of the hot and humid air distribution channel (20) is communicated with the hot and humid air heat exchange channel (8), the bottom of the hot and humid air distribution channel (20) is gradually contracted and communicated with the hot and humid air inlet (16), a dry and cold air distribution channel (21) is arranged between the dry and cold air channel (13) and the dry and cold air inlet (17), the top of the dry and cold air distribution channel (21) is communicated with the dry and cold air heat exchange channel (9), and the bottom of the dry and cold air distribution channel (21) is gradually contracted and communicated with the dry and cold air inlet (17).
8. The multilayer mixed efficient fog-dissipating water-saving cooling tower according to claim 7, wherein the heat exchange module (7) comprises a plurality of sets of a plastic sheets (22) and B plastic sheets (23) which are arranged at intervals, a plurality of sets of concave-convex positioning connection structures (24) which are matched with each other are arranged on the a plastic sheets (22) and the B plastic sheets (23) and are used for buckling the adjacent a plastic sheets (22) and B plastic sheets (23), the hot and humid air heat exchange channel (8) and the hot and humid air distribution channel (20) are arranged between the adjacent set of the a plastic sheets (22) and the set of the B plastic sheets (23), and the cold and dry air heat exchange channel (9) and the cold and dry air distribution channel (21) are arranged between the adjacent set of the B plastic sheets (23) and the set of the a plastic sheets (22).
9. The multilayer mixing efficient fog dispersal water-saving cooling tower as claimed in claim 8, wherein the A plastic sheet (22) and the B plastic sheet (23) are provided with a plurality of groups of sine wave structures (25) which are arranged in a staggered manner.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122311826.8U CN215832519U (en) | 2021-09-24 | 2021-09-24 | Multilayer mixing efficient fog dissipation water-saving cooling tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122311826.8U CN215832519U (en) | 2021-09-24 | 2021-09-24 | Multilayer mixing efficient fog dissipation water-saving cooling tower |
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| Publication Number | Publication Date |
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| CN215832519U true CN215832519U (en) | 2022-02-15 |
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| CN202122311826.8U Active CN215832519U (en) | 2021-09-24 | 2021-09-24 | Multilayer mixing efficient fog dissipation water-saving cooling tower |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115196811A (en) * | 2022-09-16 | 2022-10-18 | 中化工程沧州冷却技术有限公司 | Wastewater circulating treatment system and heat exchange module thereof |
-
2021
- 2021-09-24 CN CN202122311826.8U patent/CN215832519U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115196811A (en) * | 2022-09-16 | 2022-10-18 | 中化工程沧州冷却技术有限公司 | Wastewater circulating treatment system and heat exchange module thereof |
| CN115196811B (en) * | 2022-09-16 | 2023-02-03 | 中化工程沧州冷却技术有限公司 | Wastewater circulating treatment system and heat exchange module thereof |
| WO2024055680A1 (en) * | 2022-09-16 | 2024-03-21 | 中化工程沧州冷却技术有限公司 | Wastewater recycling treatment system and heat exchange module thereof |
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