CN110006270A - A kind of labyrinth damp type condensation fog-dissipation water collector - Google Patents

A kind of labyrinth damp type condensation fog-dissipation water collector Download PDF

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Publication number
CN110006270A
CN110006270A CN201910051923.2A CN201910051923A CN110006270A CN 110006270 A CN110006270 A CN 110006270A CN 201910051923 A CN201910051923 A CN 201910051923A CN 110006270 A CN110006270 A CN 110006270A
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CN
China
Prior art keywords
labyrinth
heat
cold
passage
heat exchanger
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Pending
Application number
CN201910051923.2A
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Chinese (zh)
Inventor
王为术
徐维晖
刘军
郑毫楠
闫友志
黄志豪
罗晓宇
李全功
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North China University of Water Resources and Electric Power
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North China University of Water Resources and Electric Power
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Publication date
Application filed by North China University of Water Resources and Electric Power filed Critical North China University of Water Resources and Electric Power
Priority to CN201910051923.2A priority Critical patent/CN110006270A/en
Publication of CN110006270A publication Critical patent/CN110006270A/en
Pending legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28CHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
    • F28C1/00Direct-contact trickle coolers, e.g. cooling towers
    • F28C1/16Arrangements for preventing condensation, precipitation or mist formation, outside the cooler
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F25/00Component parts of trickle coolers
    • F28F25/02Component parts of trickle coolers for distributing, circulating, and accumulating liquid
    • F28F25/08Splashing boards or grids, e.g. for converting liquid sprays into liquid films; Elements or beds for increasing the area of the contact surface

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The invention discloses a kind of labyrinth damp type condensation fog-dissipation water collector, the cold dry air including two groups of opposite labyrinth type dividing wall type heat exchangers and middle section converges area;Labyrinth type dividing wall type heat exchanger is made of successively alternately arranged labyrinth type cold passage and the labyrinth type passage of heat, the gas flow in labyrinth type cold passage be it is horizontally disposed, gas flow in the labyrinth type passage of heat is to be vertically arranged;Cold dry air horizontally enters into labyrinth type cold passage from two sides, damp-heat air is from the bottom to top vertically into the labyrinth type passage of heat, hot and cold air carries out heat exchange in labyrinth type dividing wall type heat exchanger, and cold dry air enters cold dry air and converges area and flow up after heat exchange.The present invention, which can be achieved at the same time, improves hot and cold air heat exchange amount, solves the problems, such as the trapping of damp-heat air condensed water, and prevent cold air flows short circuit phenomenon from occurring.

Description

A kind of labyrinth damp type condensation fog-dissipation water collector
Technical field
The invention belongs to receive water fog dispersal technical field more particularly to a kind of labyrinth damp type condensation fog-dissipation water collector.
Background technique
Cooling tower is the important cooling equipment of industry, passes through air and cooling water Mass and heat transfer realization circulating cooling, fortune in tower Large quantity of moisture is evaporated during row and air forms damp-heat air and is directly discharged to outside tower, is causing huge water resource waste same When, damp-heat air go out tower easily condense formed plumage mist pollution environment.
Carrying out cooling condensation to damp-heat air using cold dry air, then mixing is most economical simple receipts water fog dispersal mode, Recycle-water, which can re-use, brings water-saving benefit simultaneously, also can reach fog dispersal purpose, brings certain environmental benefit.But it is damp and hot Air cooling-down will appear the problem of condensed water easily drifts when condensing, when cold dry air and damp-heat air depend on blower draft and provide When power, and cold air flows short circuit phenomenon occur will affect the normal work of cooling tower since cold air effluent journey is shorter easily Energy.So exploitation cooling performance is good, it is easy to trap condensed water, and can effectively prevent the generation of cold air flows short circuit phenomenon Condensation fog-dissipation water collector it is extremely urgent.
The patent of invention of notification number CN108800983A discloses a kind of water-saving fog dispersal cooling tower.This kind of water-saving fog dispersal Cooling tower, including cooling column body, collecting-tank, cooling coil, the first air inlet, packing layer, water distribution pipeline, set the first spray Head and exhaust blower, water distribution pipeline top are fixed with heat exchange fog dispersal mechanism, and heat exchange fog dispersal actuator base is provided with the second spray head;Collection Pond is connected to circulating water pipe, and circulating water pipe end is provided with the first water outlet and the second water outlet, the first water outlet and water distribution It is connected at the top of pipeline connection, the second water outlet and heat exchange fog dispersal mechanism;The is provided between heat exchange fog dispersal mechanism and water distribution pipeline Two air inlets.A kind of water-saving fog dispersal cooling tower of the invention is cooperated by heat exchange fog dispersal mechanism and the second air inlet, steams water Air cooling is solidifying to fall, and effectively eliminates spraying cooling water evaporation loss, overall structure is simple, and manufacturing cost is low, economical and practical.
In the technical solution heat exchange fog dispersal mechanism include left side fixed plate, right side fixed plate, be set to left side fixed plate and The hollow continuous bending plate in multiple longitudinal directions between the fixed plate of right side, two be set at the top of left side fixed plate and right side fixed plate First water-supply-pipe and three second water-supply-pipes for being set to left side fixed plate and right side fixed plate bottom.First water-supply-pipe Bottom be successively connected to the top of hollow continuous bending plate longitudinally in each, the top of second water-supply-pipe successively with it is each vertical It is connected to the bottom of hollow continuous bending plate.It is hollow structure, right side fixed plate top and circulation at the top of the right side fixed plate Second water outlet of water pipe is connected to.It is cold that the hollow Curved Continuous folded structure in longitudinal direction of heat exchange fog dispersal mechanism is conducive to increase vapor The solidifying time, and the small water droplet for effectivelying prevent vapor or condensing into is carried over outside cooling tower under fan action.
But the heat exchange amount of above-mentioned technical proposal is lower, influences the trapping of damp-heat air condensed water, still can there is cold sky The phenomenon of throughput short circuit.
The patent of invention of notification number CN102901397A discloses a kind of wet cooling tower fog dispersal water collector, device setting More than cooling tower original water collection device, the following cooling tower air duct lower end position of blower, partition is set in collection water-dividing chamber, composition is catchmented Room and water-dividing chamber, upper hose connect collecting chamber, collecting chamber connection condensation water service pipe one end, and the condensation water service pipe other end connects return water Room top, backwater room lower part reconnect condensation water service pipe one end, and the condensation water service pipe other end returns to point of connection collection water-dividing chamber Water chamber, constitutes closed cycle structure, and water-dividing chamber lower end connects spray tube;Condensation water service pipe is integrated with concave-convex cooling fin attachment; Positioning poling is set to the upper and lower ends of concave-convex cooling fin;Waterstop is set on convex surface on the inside of concave-convex cooling fin;Upper hose upper end Connection integral water chamber, lower end connects pressure pump, and then connects mixing tank, constitutes fog dispersal water collector.The present invention will be saturated Damp and hot fog is condensed into water, avoids the evaporation of water, has saved water resource, avoids the pollution of environment.
But that there is also heat exchange amounts is lower, influences the problem of damp-heat air condensed water trapping for above-mentioned technical proposal, causes The generation of cold air flows short circuit phenomenon.
Summary of the invention
The purpose of the present invention is to provide a kind of labyrinth damp type condensation fog-dissipation water collectors, and it is cold and hot that raising can be achieved at the same time Air heat-exchange amount, solves the problems, such as the trapping of damp-heat air condensed water, and prevents cold air flows short circuit phenomenon from occurring.
In order to solve the above technical problems, the present invention adopts the following technical scheme:
A kind of labyrinth damp type condensation fog-dissipation water collector, including two groups of opposite labyrinth type dividing wall type heat exchangers and middle part The cold dry air divided converges area;Labyrinth type dividing wall type heat exchanger is led to by successively alternately arranged labyrinth type cold passage and labyrinth type heat Road is constituted, the gas flow in labyrinth type cold passage be it is horizontally disposed, gas flow in the labyrinth type passage of heat is is vertically arranged; Cold dry air horizontally enters into labyrinth type cold passage from two sides, damp-heat air from the bottom to top vertically into the labyrinth type passage of heat, Hot and cold air carries out heat exchange in labyrinth type dividing wall type heat exchanger, and cold dry air enters cold dry air and converges area simultaneously after heat exchange It flows up.
It is V-shape that cold dry air, which converges area,.
Labyrinth type cold passage and the labyrinth type passage of heat are referred to as heat exchanger channels, and heat exchanger channels are by two pieces of opposite heat exchanger plates It constitutes, heat exchanger plates are zigzag;The peak valley of every two pieces of heat exchanger plates, which contrasts, constitutes a labyrinth type channel, and labyrinth type channel is formed Periodic dilation and contraction.
Crest height is without delay height on heat exchanger plates.
Heat exchanger plates are surrounded by the sealing plate exchange passage of heat and are sealed.
Every two is with respect to being respectively equipped with the seal convexity and sealed groove that several are mutually matched on the sealing plate of heat exchanger plates.
Two pieces of heat exchanger plates middle sections of every group of composition heat exchanger channels are disposed with raised butt joint docking.
Every piece of heat exchanger plates, which are located on the surface of labyrinth type passage of heat side, is coated with hydrophilic coating.
Two pieces of heat exchanger plates of every group of composition heat exchanger channels are arranged using mirror image corresponding form.
Two pieces of heat exchanger plates of every group of composition labyrinth type cold passage arrange that every group of composition labyrinth type is warm using parallel corresponding form Two pieces of heat exchanger plates in channel are arranged using mirror image corresponding form.
Beneficial effects of the present invention:
The present invention, which can be achieved at the same time, improves hot and cold air heat exchange amount, solves the problems, such as the trapping of damp-heat air condensed water, and prevent cold Air mass flow short circuit phenomenon occurs.
Labyrinth type cold passage is the labyrinth type channel of periodic dilation and contraction in the present invention, and cold air is cold logical in labyrinth type In road during bottom horizontal flow sheet flow area constantly change can increase cold air disturbance increase the coefficient of heat transfer and meanwhile play balance hinder Power effect promotes the resistance balance of damp and hot air-flow and cold airflow, prevents the generation of cold air flows short circuit phenomenon, and channel is Labyrinth type can also extend air flow and increase heat-exchange time.
The heat exchange hot plate that cold and hot channel is constituted in the present invention is labyrinth shape, and crest height is to play without height is detained Enhancing is reinforced cold air will not being made to generate delay again when air agitation effect.
Each pair of heat exchanger plates for constituting heat exchanger channels are docked by being arranged in raised butt joint opposite on heat exchanger plates in the present invention, Exchange hot plate is played a supporting role.
Heat exchange plate surface in the present invention positioned at passage of heat two sides is coated with hydrophilic material coating, is conducive to cold to damp-heat air The trapping of condensate.
The present invention is partially equipped with V-shape cold dry air therebetween and converges area, can make by labyrinth type dividing wall type heat exchanger Cold air have a component velocity obliquely, convenient for heat exchange after hot and cold air mixing.
Detailed description of the invention
Attached drawing 1 is the structural schematic diagram of the embodiment of the present invention one;
Attached drawing 2 is single heat exchanger plates structure chart in the embodiment of the present invention one;
Attached drawing 3 is the top view of single heat exchanger plates in the embodiment of the present invention one;
Attached drawing 4 is heat exchanger channels structure chart in the embodiment of the present invention one
Attached drawing 5 is heat exchanger channels heat exchanger plates corresponding form schematic diagram in the embodiment of the present invention one
Attached drawing 6 is schematic view of the mounting position of the embodiment of the present invention one in cooling tower;
Attached drawing 7 is heat exchanger channels heat exchanger plates corresponding form schematic diagram in the embodiment of the present invention two.
The appended drawing reference of each component in figure: 1- tower body;2- filler;3- water injector;4- water collection device;5- labyrinth type partition changes Hot device;6-V font cold dry air converges area;7- heater;8- air duct;9- blower;10- mixing section gas chamber;11- heat exchanger plates; 501- labyrinth type cold passage;The 502- labyrinth type passage of heat;503- protrusion connector;504- seal convexity;505- sealed groove.
Specific embodiment
Below in conjunction with attached drawing, detailed description of the preferred embodiments.It should be understood that this place is retouched The specific embodiment stated is merely to illustrate and explain the present invention, and is not intended to restrict the invention.
As shown in Figures 1 to 6, a kind of labyrinth damp type condensation fog-dissipation water collector of the present embodiment, including two groups opposite Labyrinth type dividing wall type heat exchanger 5 and the V-shape cold dry air of middle section converge area 6.
Labyrinth type dividing wall type heat exchanger is by successively 502 structure of alternately arranged labyrinth type cold passage 501 and the labyrinth type passage of heat Be at, the gas flow in labyrinth type cold passage 501 it is horizontally disposed, the gas flow in the labyrinth type passage of heat 502 is vertically to set It sets;Cold dry air horizontally enters into labyrinth type cold passage 501 from two sides, and damp-heat air is logical vertically into labyrinth type heat from the bottom to top In road 502, hot and cold air carries out heat exchange in labyrinth type dividing wall type heat exchanger 5, and cold dry air enters dry and cold sky after heat exchange Gas converges area 6.Since V-shape cold dry air converges the setting in area 6, can make after heat exchange cold dry air have one obliquely Component velocity, conducive to the mixing of hot and cold air after heat exchange.
Above-mentioned labyrinth type cold passage 501 and the labyrinth type passage of heat 502 are referred to as heat exchanger channels, and heat exchanger channels are by two pieces of phases Pair heat exchanger plates 11 constitute, heat exchanger plates 11 be labyrinth shape;It is logical that the peak valley of every two pieces of heat exchanger plates 11 contrasts one labyrinth type of composition Road, labyrinth type channel form periodic dilation and contraction.
In the present embodiment, two pieces of heat exchanger plates 11 of every composition heat exchanger channels use the combining form of mirror image corresponding form.
Heat exchanger plates 11 are surrounded by sealing plate and are sealed to cold and hot channel, and downside is close on it for labyrinth type cold passage 501 Envelope closing, the labyrinth type passage of heat 502 are closed in its left and right side seal, and every two with respect to setting respectively on the sealing plate of heat exchanger plates The seal convexity 504 and sealed groove 505 for having several to be mutually matched are for sealing.
Two pieces of heat exchanger plates middle sections of every group of composition heat exchanger channels are disposed with raised butt joint 503, two pieces of heat exchanger plates 11 The bonding of butt joint 503 can play a supporting role to channel and prevent channel from collapsing.
The crest height of heat exchanger plates 11 is that will not make again when playing the role of enhancing and reinforcing air agitation cold without height is detained Air generates delay, and 11 material of heat exchanger plates uses high thermal conductivity coefficient light material, exchanges heat conducive to hot and cold air.Position simultaneously It is coated with hydrophilic material coating in 11 surface of heat exchanger plates of labyrinth type passage of heat two sides, is caught conducive to damp-heat air condensed water Collection.
Flow area constantly changes and can increase cold air and disturb cold air during bottom horizontal flow sheet in labyrinth type cold passage 501 The dynamic coefficient of heat transfer that increases plays the role of the resistance balance that balancing resistance promotes damp and hot air-flow and cold airflow simultaneously, prevents cold air stream The generation of short circuit phenomenon is measured, and channel is that labyrinth type can also extend air flow increase heat-exchange time.
Labyrinth damp type condensation fog-dissipation water collector of the invention is applied in cooling tower, if Fig. 2 is the embodiment of the present invention Schematic view of the mounting position in cooling tower.
The cooling tower course of work is as follows: high temperature circulation cooling water is sprayed on filler 2 by high temperature circulation water by water injector 3 Enter cold air progress caloic with the 1 lower part air inlet of tower body from cooling tower to exchange, circulating cooling coolant-temperature gage reduces;By caloic The air temperature entered below cooling tower after exchange rises, and water capacity increases, and forms the damp-heat air being substantially saturated;It is damp and hot Wandering water is captured when air is by water collection device 4, continues to ascend into labyrinth type condensation receipts water fog-dissipation device of the present invention later It is cold logical with labyrinth type in labyrinth type condensation receipts water fog-dissipation device of the present invention is entered from cooling tower two sides in the labyrinth type passage of heat 502 The cold dry air in road 501 exchanges heat;Damp-heat air cools down condensation in the passage of heat, and condensed water is by passage of heat surface hydrophilicity Coating trapping, cold dry air temperature increase, and two sides cold air condenses V-shape among receipts water fog-dissipation device in labyrinth type of the present invention and does Cold air converges area 6 and converges rising, mixes in mixing section gas chamber 10 with by the hot-air of the labyrinth type passage of heat 502, mixes When air is by the heater 7 that is arranged in mixing section gas chamber 10, it can be heated, atmosphere is finally being expelled to by blower 9.
Embodiment two:
As shown in fig. 7, the present embodiment and embodiment one the difference is that: two pieces of every group of composition labyrinth type cold passage 501 Heat exchanger plates arrange that two pieces of heat exchanger plates of every group of composition labyrinth type passage of heat 502 correspond to shape using mirror image using parallel corresponding form Formula arrangement.
The above embodiments are only used to illustrate and not limit the technical solutions of the present invention, although referring to above-described embodiment to this hair It is bright to be described in detail, those skilled in the art should understand that: still the present invention can be modified or be waited With replacement, without departing from the spirit or scope of the invention, or any substitutions, should all cover in power of the invention In sharp claimed range.

Claims (10)

1. a kind of labyrinth damp type condensation fog-dissipation water collector, it is characterised in that: changed including two groups of opposite labyrinth type dividing wall types Hot device and the cold dry air of middle section converge area;Labyrinth type dividing wall type heat exchanger is cold logical by successively alternately arranged labyrinth type Road and the labyrinth type passage of heat are constituted, and the gas flow in labyrinth type cold passage is horizontally disposed, in the labyrinth type passage of heat gas Flow direction is to be vertically arranged;Cold dry air horizontally enters into labyrinth type cold passage from two sides, damp-heat air from the bottom to top vertically into In the labyrinth type passage of heat, hot and cold air carries out heat exchange in labyrinth type dividing wall type heat exchanger, and cold dry air enters after heat exchange Cold dry air converges area and flows up.
2. a kind of labyrinth damp type condensation fog-dissipation water collector according to claim 1, it is characterised in that: cold dry air converges Conjunction area is V-shape.
3. a kind of labyrinth damp type condensation fog-dissipation water collector according to claim 1 or 2, it is characterised in that: labyrinth type Cold passage and the labyrinth type passage of heat are referred to as heat exchanger channels, and heat exchanger channels are made of two pieces of opposite heat exchanger plates, and heat exchanger plates are Zigzag;The peak valley of every two pieces of heat exchanger plates contrast constitute a labyrinth type channel, labyrinth type channel formed periodic dilation and It shrinks.
4. a kind of labyrinth damp type condensation fog-dissipation water collector according to claim 3, it is characterised in that: heat exchanger plates upper ripple Peak heights are without delay height.
5. a kind of labyrinth damp type condensation fog-dissipation water collector according to claim 3, it is characterised in that: heat exchanger plates surrounding It is sealed equipped with the sealing plate exchange passage of heat.
6. a kind of labyrinth damp type condensation fog-dissipation water collector according to claim 5, it is characterised in that: every two is opposite The seal convexity and sealed groove that several are mutually matched are respectively equipped on the sealing plate of heat exchanger plates.
7. a kind of labyrinth damp type condensation fog-dissipation water collector according to claim 3, it is characterised in that: every group of composition is changed Two pieces of heat exchanger plates middle sections of the passage of heat are disposed with raised butt joint docking.
8. a kind of labyrinth damp type condensation fog-dissipation water collector according to claim 3, it is characterised in that: every piece of heat exchanger plates Hydrophilic coating is coated on the surface of labyrinth type passage of heat side.
9. a kind of labyrinth damp type condensation fog-dissipation water collector according to claim 3, it is characterised in that: every group of composition is changed Two pieces of heat exchanger plates of the passage of heat are arranged using mirror image corresponding form.
10. a kind of labyrinth damp type condensation fog-dissipation water collector according to claim 3, it is characterised in that: every group of composition Two pieces of heat exchanger plates of labyrinth type cold passage are using parallel corresponding form arrangement, two pieces of heat exchanger plates of every group of composition labyrinth type passage of heat It is arranged using mirror image corresponding form.
CN201910051923.2A 2019-01-21 2019-01-21 A kind of labyrinth damp type condensation fog-dissipation water collector Pending CN110006270A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110455113A (en) * 2019-09-04 2019-11-15 福建立信换热设备制造股份公司 A kind of water collection device
WO2022007296A1 (en) * 2020-07-07 2022-01-13 山东贝诺冷却设备股份有限公司 Vapor dissipation device and cooling tower

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CN203464783U (en) * 2013-07-03 2014-03-05 烟台荏原空调设备有限公司 Reverse-flow closed cooling tower
CN103727805A (en) * 2014-01-07 2014-04-16 山东蓝想环境科技股份有限公司 Deep condensation and demisting environment-friendly device
CN203657541U (en) * 2014-01-07 2014-06-18 山东蓝想环境科技股份有限公司 Environment-friendly cooling tower capable of deep condensing and demisting
CN106403637A (en) * 2016-11-10 2017-02-15 湖南元亨科技发展有限公司 Fog-dispersing and water-saving cooling tower
CN107179009A (en) * 2017-05-31 2017-09-19 西安交通大学 A kind of gas-gas heat exchange device for the solidifying water that dispersed fog for cooling tower
CN206656618U (en) * 2017-03-23 2017-11-21 湖南元亨科技股份有限公司 A kind of industrial cooling tower fog-dissipation device
CN209672866U (en) * 2019-01-21 2019-11-22 华北水利水电大学 A kind of labyrinth damp type condensation fog-dissipation water collector

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Publication number Priority date Publication date Assignee Title
JP3020715U (en) * 1995-07-18 1996-02-06 神鋼パンテツク株式会社 cooling tower
JPH0989472A (en) * 1995-09-25 1997-04-04 Shinko Pantec Co Ltd Cooling tower
JPH1163884A (en) * 1997-08-21 1999-03-05 Ishikawajima Harima Heavy Ind Co Ltd Cooling water tower
CN1888802A (en) * 2006-07-21 2007-01-03 清华大学 Antifreezing and fogging water-saving cooling tower
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CN209672866U (en) * 2019-01-21 2019-11-22 华北水利水电大学 A kind of labyrinth damp type condensation fog-dissipation water collector

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110455113A (en) * 2019-09-04 2019-11-15 福建立信换热设备制造股份公司 A kind of water collection device
CN110455113B (en) * 2019-09-04 2023-12-01 福建立信换热设备制造股份公司 Water collector
WO2022007296A1 (en) * 2020-07-07 2022-01-13 山东贝诺冷却设备股份有限公司 Vapor dissipation device and cooling tower

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