CN110006269A - A kind of labyrinth damp type depth fog dispersal receipts water cooling tower - Google Patents
A kind of labyrinth damp type depth fog dispersal receipts water cooling tower Download PDFInfo
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- CN110006269A CN110006269A CN201910051757.6A CN201910051757A CN110006269A CN 110006269 A CN110006269 A CN 110006269A CN 201910051757 A CN201910051757 A CN 201910051757A CN 110006269 A CN110006269 A CN 110006269A
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- labyrinth
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- heat exchanger
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
- F28C1/00—Direct-contact trickle coolers, e.g. cooling towers
- F28C1/16—Arrangements for preventing condensation, precipitation or mist formation, outside the cooler
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F25/00—Component parts of trickle coolers
- F28F25/02—Component parts of trickle coolers for distributing, circulating, and accumulating liquid
- F28F25/08—Splashing boards or grids, e.g. for converting liquid sprays into liquid films; Elements or beds for increasing the area of the contact surface
Abstract
It disperses fog the invention discloses a kind of labyrinth damp type depth and receives water cooling tower, including tower body, filler portion, spray equipment, water collection device, condensation heat exchange device and heating device are successively arranged in tower body from the bottom to top, is additionally provided with air duct at the top of tower body, air duct is equipped with air ducting；It is located at position between condensation heat exchange device top and air duct import in tower body and is provided with mixing section gas chamber, heating device is located in mixing section gas chamber.The present invention has the advantages that low energy consumption, easy for installation, system reliability is high, it combines air in parallel fog dispersal technology with heating fog dispersal technology, have the characteristics that structure is simple and convenient to operate, disperses fog thorough, can be used for recirculating cooling water system, energy conservation and environment protecting are obvious.
Description
Technical field
The invention belongs to cooling tower technical fields more particularly to a kind of fog dispersal of labyrinth damp type depth to receive water cooling tower.
Background technique
It is promoted with industrialization, whole nation industry water consumption dramatically increases, and has accounted for about whole society's total water consumption 25%, wherein 80% uses
In industry cooling, industry cooling water consumption is big, and circulating and recovering is low, and water loss is high, and research industry cooling is water-saving, reconstructs industry cooling
Water saving art optimizes cooling water system, researches and develops crucial cooling water-saving equipment, significantly reduces cooling water loss, greatly improve work
Industry water effect is of great significance to the industrial plumage mist pollution of industrial water consumption and effectively inhibition is significantly reduced.
Cooling tower realizes circulating water with air and recirculated water contact sensible heat transfer and moisture evaporation latent heat heat exchange mode,
Its own evaporation causes cooling water loss excessive simultaneously, and tower damp-heat air, which easily condenses, out forms plumage mist, influences nearby residents
Area and traffic route visibility cause environmental pollution while road surface slippery situation around cooling tower also being made to influence service personnel's work.Exploitation
Force ventilation tower receives water fog dispersal technology, and to Industrial Water Saving is realized, prevention and treatment cooling tower plumage mist pollution is of great significance.
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 above-mentioned technical proposal still has the defect of fog dispersal not enough thoroughly, energy saving and bad environment protecting.
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 above-mentioned technical proposal still has the defect of fog dispersal not enough thoroughly, energy saving and bad environment protecting.
Summary of the invention
The purpose of the present invention is to provide a kind of low energy consumption, the labyrinth damp type depth that easy for installation, system reliability is high
Fog dispersal receive water cooling tower, have the characteristics that structure be simple and convenient to operate, disperse fog it is thorough, energy conservation with environment protecting it is obvious.
In order to solve the above technical problems, the present invention adopts the following technical scheme:
Water cooling tower, including tower body are received in a kind of fog dispersal of labyrinth damp type depth, are successively arranged filler portion, spray in tower body from the bottom to top
Shower device, water collection device, condensation heat exchange device and heating device, tower body top are additionally provided with air duct, and air duct is equipped with air ducting；Tower
It is located at position between condensation heat exchange device top and air duct import in vivo and is provided with mixing section gas chamber, heating device is located at mixing section
In gas chamber；
High temperature circulation cooling water is passed through by spray equipment to be sprayed in filler portion, and with the cold sky that enters from tower body lower part air inlet
Gas carries out caloic and exchanges to form damp-heat air, and damp-heat air enters condensation heat exchange device from the bottom to top, and cold dry air is by being arranged in
The air inlet of tower body two sides horizontally enters into condensation heat exchange device.
Heating device or so is positioned opposite, and heating device is oriented to air duct entrance and tilts.
Condensation heat exchange device includes the dry and cold sky of V-shape of two groups of opposite labyrinth type dividing wall type heat exchangers and middle section
Gas 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, fan
Gas flow in the type cold passage of palace be it is horizontally disposed, gas flow in the labyrinth type passage of heat is to be vertically arranged；Cold dry air
Horizontally enter into the labyrinth type cold passage of condensation heat exchange device, 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.
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 distinguished with respect on the sealing plate of heat exchanger plates
The seal convexity and sealed groove being mutually matched equipped with several.
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 has the advantages that low energy consumption, easy for installation, system reliability is high, and air in parallel fog dispersal technology is disappeared with heating
Mist technology combines, and has the characteristics that structure is simple and convenient to operate, disperses fog thorough, can be used for recirculating cooling water system, energy conservation and
Environment protecting is obvious.
For mixed air vessel's section between condensation heat exchange device and air duct import, being inside disposed with heating device can in the present invention
Mixing air is heated, makes mixing air state point further away from saturation curve, reaches depth fog dispersal purpose.
The setting of heating device in the present invention is heated mixing air using fume afterheat, or is followed using heat
Ring water is passed through heat exchanger and is heated to mixing air and can also directly adopt Electric heating and directly heat；And heating device is left
It is right positioned opposite, and heating device is oriented to air duct entrance and tilts, and guide functions can be played to two sides air and promote air mixed
It closes.
Condensation heat exchange device includes the V word of two groups of opposite labyrinth type dividing wall type heat exchangers and middle section in the present invention
Type cold dry air converges area, can be achieved at the same time and 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.
Labyrinth type cold passage is the labyrinth type channel of periodic dilation and contraction, cold air in condensation heat exchange device of the present invention
In labyrinth type cold passage during bottom horizontal flow sheet flow area constantly change can increase cold air disturbance increase the coefficient of heat transfer it is same
When play the role of the resistance balance that balancing resistance promotes damp and hot air-flow and cold airflow, prevent the hair of cold air flows short circuit phenomenon
It is raw, and channel is that labyrinth type can also extend air flow increase heat-exchange time.
The heat exchange hot plate that cold and hot channel is constituted in condensation heat exchange device of the present invention is labyrinth shape, and crest height is no delay
Highly, cold air will not be made to generate delay again when playing the role of enhancing and reinforcing air agitation.
Each pair of heat exchanger plates for constituting heat exchanger channels are opposite convex on heat exchanger plates by being arranged in condensation heat exchange device of the present invention
Butt joint docking is played, exchange hot plate is played a supporting role.
Heat exchange plate surface in condensation heat exchange device of the present invention positioned at passage of heat two sides is coated with hydrophilic material coating, is conducive to
Trapping to damp-heat air condensed water.
Condensation heat exchange device of the present invention is partially equipped with V-shape cold dry air therebetween and converges area, can make by labyrinth type
The cold air of dividing wall type heat exchanger has a component velocity obliquely, convenient for the mixing of hot and cold air after heat exchange.
Detailed description of the invention
Attached drawing 1 is the structural schematic diagram of the embodiment of the present invention；
Attached drawing 2 is the structural schematic diagram of condensation heat exchange device in the embodiment of the present invention；
Attached drawing 3 is single heat exchanger plates structure chart in the embodiment of the present invention；
Attached drawing 4 is heat exchanger channels structure chart in the embodiment of the present invention；
Attached drawing 5 is the air psychrometric chart that the embodiment of the present invention installs cooling tower after condensation heat exchange device additional；
Attached drawing 6 is the air psychrometric chart of cooling tower after installing heating device in mixing section of embodiment of the present invention gas chamber additional；
Attached drawing 7 is one of heat exchanger channels heat exchanger plates corresponding form schematic diagram in the embodiment of the present invention；
Attached drawing 8 is two of heat exchanger channels heat exchanger plates corresponding form schematic diagram in the embodiment of the present invention.
The appended drawing reference of component in figure: 1- tower body；2- filler portion；3- spray equipment；4- water collection device；5- labyrinth type partition
Heat exchanger；6-V font cold dry air converges area；7- heating device；8- air duct；9- blower；10- mixing section gas chamber；11- heat exchange
Plate；501- cold passage；The 502- 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 7, water cooling tower, including tower body 1 are received in a kind of labyrinth damp type depth fog dispersal of the present embodiment,
Filler portion 2, spray equipment 3, water collection device 4, condensation heat exchange device, heating device 7, tower body 1 are successively arranged in tower body 1 from the bottom to top
Top is equipped with air duct 8, and blower 9 is equipped in air duct as air ducting；Be located in tower body 15 top of condensation heat exchange device and
Position is provided with mixing section gas chamber 10 between 8 import of air duct, and heater 7 is located in mixing section gas chamber 10.
High temperature circulation cooling water is passed through by spray equipment 3 and is sprayed in filler portion 2, and is entered with from tower body lower part air inlet
Cold air carry out caloic and exchange to form damp-heat air, damp-heat air enters condensation heat exchange device 5 from the bottom to top, cold dry air by
The air inlet for being arranged in 1 two sides of tower body horizontally enters into condensation heat exchange device.
Heating device 7 is oppositely disposed in mixing section gas chamber 10 in splayed configuration or so in the present invention, and heating device 7 is aweather
Cylinder 8 entrances guiding inclination, makes heating device 7 be arranged in obtuse angle respectively with cooling tower or so wall surface, can be to left and right sides air
Certain guide functions are played, conducive to being sufficiently mixed for mixing section gas chamber air.
Heating device 7 is disposed in mixing section gas chamber, heating device can utilize the low-quality heat sources such as fume afterheat or will be sharp
Heating is carried out to mixing section gas chamber air with heat recirculated water or is directly heated using Electric heating, mixing air state point is made
Further away from saturation curve, reach depth fog dispersal purpose.
Condensation heat exchange device includes the V of two groups of opposite labyrinth type dividing wall type heat exchangers 5 and middle section in the present invention
Font cold dry air converges 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, such as
Shown in Fig. 7.It can also use form as shown in Figure 8, and two pieces of heat exchanger plates of every group of composition labyrinth type cold passage 501 are using parallel
Two pieces of heat exchanger plates of corresponding form arrangement, every group of composition labyrinth type passage of heat 502 are arranged using 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.
The course of work that water cooling tower is received in the labyrinth damp type depth fog dispersal of the embodiment of the present invention is as follows:
Spray equipment 3 by high temperature circulation cooling water be sprayed in filler portion 2 and with the cold sky that enters from cooling tower lower part air inlet
Gas carries out caloic exchange, and circulating cooling coolant-temperature gage reduces；The air temperature entered below cooling tower after caloic exchanges
Rise, water capacity increases, and forms the damp-heat air being substantially saturated；Wandering water is captured when damp-heat air is by water collection device 4, later
Continue to ascend into the labyrinth type passage of heat 502 of condensation heat exchange device 5, enters condensation heat exchange device 5 with from cooling tower two sides
The cold dry air of middle labyrinth type cold passage 501 exchanges heat；Damp-heat air cools down condensation in the passage of heat, and condensed water is logical by heat
The trapping of road surface hydrophilicity coating, cold dry air temperature increase, the dry and cold sky of two sides cold air V-shape among condensation heat exchange device
Gas 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, mixing air
When by the heating device 7 that is arranged in mixing section gas chamber 10, it can be heated, atmosphere is finally being expelled to by blower 9.
The working principle of the invention is described further below in conjunction with air psychrometric chart, Fig. 5 is to install condensing heat-exchange dress additional
The psychrometric chart of cooling tower is postponed, point 20 is damp-heat air state point above water collection device, and point 24 is outside air state point, damp and hot sky
Gas exchanges heat in condensation heat exchange device with the cold air for entering condensation heat exchange device, and damp-heat air temperature and water capacity are along full
State point 21 is dropped to curve there is condensation reach water-saving purpose, cold dry air temperature increases water capacity and is basically unchanged,
Becoming 23 from state point 24, the damp-heat air 21 and cold air 23 after exchanging heat are mixed, and mixed state point is 22, it
After can be discharged outside tower by blower, mix with the outside air for being located at state point 24, the outer air blend section of tower is 24-23.
Air psychrometric chart of the Fig. 6 for present invention cooling tower after installation heater in mixing section gas chamber, state point 25,
26,27,29,30 correspond respectively to state point 20 in Fig. 4, and 21,22,23,24, it, will after mixing section gas chamber installs heater additional
Mixing air heats in the tower of state point 27, so that mixed gas state point is along saturation curve, temperature
Section 27-28 is increased, and is discharged outside tower by blower later, is mixed with the outside air for being located at state point 30, the outer air blend section of tower
Become 30-29, the outer air blend section 30-29 slope ratio Fig. 4 middle conductor 24-22 slope of tower is small in Fig. 5, and the outer air of tower is mixed
The smaller proof fog dispersal of zygonema slope over 10 is more thorough.
It may indicate that the invention patent purpose that can realize that cooling tower is water-saving and depth disperses fog by thermodynamic analysis, can bring
Certain economic benefit and environmental benefit.
The present invention has the advantages that low energy consumption, easy for installation, system reliability is high, passes through condensation heat exchange device and heating
The water-saving depth that water technology, air parallel connection type fog dispersal technology and hot type fog dispersal technology combine realization cooling tower is received in condensation by device
Degree fog dispersal has the characteristics that structure is simple and convenient to operate, disperses fog thorough, can be used for recirculating cooling water system, energy conservation and environmental protection are imitated
Fruit is obvious.
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. water cooling tower, including tower body are received in a kind of labyrinth damp type depth fog dispersal, it is characterised in that: in tower body from the bottom to top successively
Equipped with filler portion, spray equipment, water collection device, condensation heat exchange device and heating device, air duct is additionally provided at the top of tower body, air duct is arranged
There is air ducting；It is located above condensation heat exchange device in tower body and position between air duct import is provided with mixing section gas chamber, heating
Device is located in mixing section gas chamber；
High temperature circulation cooling water is passed through by spray equipment to be sprayed in filler portion, and with the cold sky that enters from tower body lower part air inlet
Gas carries out caloic and exchanges to form damp-heat air, and damp-heat air enters condensation heat exchange device from the bottom to top, and cold dry air is by being arranged in
The air inlet of tower body two sides horizontally enters into condensation heat exchange device.
2. water cooling tower is received in a kind of labyrinth damp type depth fog dispersal according to claim 1, it is characterised in that: heating device
Left and right is positioned opposite, and heating device is oriented to air duct entrance and tilts.
3. water cooling tower is received in a kind of labyrinth damp type depth fog dispersal according to claim 1, it is characterised in that: condensing heat-exchange
Device includes that the V-shape cold dry air of 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 in labyrinth type cold passage
Body flow direction be it is horizontally disposed, gas flow in the labyrinth type passage of heat is is vertically arranged；Cold dry air horizontally enters into condensing heat-exchange
In the labyrinth type cold passage of device, damp-heat air is from the bottom to top vertically into the labyrinth type passage of heat, and hot and cold air is in labyrinth type
Heat exchange is carried out in dividing wall type heat exchanger, cold dry air enters cold dry air and converges area and flow up after heat exchange.
4. water cooling tower is received in a kind of labyrinth damp type depth fog dispersal according to claim 3, it is characterised in that: labyrinth type is cold
Channel 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 saw
Tooth form；The peak valley of every two pieces of heat exchanger plates, which contrasts, constitutes a labyrinth type channel, and labyrinth type channel forms periodic dilation and receipts
Contracting.
5. water cooling tower is received in a kind of labyrinth damp type depth fog dispersal according to claim 4, it is characterised in that: on heat exchanger plates
Crest height is without delay height.
6. water cooling tower is received in a kind of labyrinth damp type depth fog dispersal according to claim 4, it is characterised in that: heat exchanger plates four
The sealing plate exchange passage of heat is equipped with week to be sealed；Every two is with respect to being respectively equipped with several mutual on the sealing plate of heat exchanger plates
The seal convexity and sealed groove matched.
7. water cooling tower is received in a kind of labyrinth damp type depth fog dispersal according to claim 4, it is characterised in that: every group of composition
Two pieces of heat exchanger plates middle sections of heat exchanger channels are disposed with raised butt joint docking.
8. water cooling tower is received in a kind of labyrinth damp type depth fog dispersal according to claim 4, it is characterised in that: every piece of heat exchange
Plate, which is located on the surface of labyrinth type passage of heat side, is coated with hydrophilic coating.
9. water cooling tower is received in a kind of labyrinth damp type depth fog dispersal according to claim 4, it is characterised in that: every group of composition
Two pieces of heat exchanger plates of heat exchanger channels are arranged using mirror image corresponding form.
10. water cooling tower is received in a kind of labyrinth damp type depth fog dispersal according to claim 4, it is characterised in that: every group of structure
It is arranged at two pieces of heat exchanger plates of labyrinth type cold passage using parallel corresponding form, two pieces of heat exchange of every group of composition labyrinth type passage of heat
Plate is arranged using mirror image corresponding form.
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| CN201910051757.6A CN110006269A (en) | 2019-01-21 | 2019-01-21 | A kind of labyrinth damp type depth fog dispersal receipts water cooling tower |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110345777A (en) * | 2019-08-10 | 2019-10-18 | 济南蓝辰能源技术有限公司 | A kind of dual condensation mixed water-saving fog dispersal cooling system |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN103743289A (en) * | 2014-01-26 | 2014-04-23 | 德州贝诺风力机械设备有限公司 | Cooling tower fog dispersal and water collection device |
| CN206001939U (en) * | 2016-07-30 | 2017-03-08 | 山东蓝想环境科技股份有限公司 | A kind of combination type fog dispersal water saving cooling tower |
| CN107560453A (en) * | 2017-10-08 | 2018-01-09 | 江苏丰泰节能环保科技有限公司 | A kind of hyperbolic natural-draft cooling tower with cold coagulation liquid fog dispersal function |
| CN108332575A (en) * | 2018-04-13 | 2018-07-27 | 江苏海鸥冷却塔股份有限公司 | Band fog dispersal module fog dispersal cooling tower |
| WO2018181504A1 (en) * | 2017-03-28 | 2018-10-04 | 三菱日立パワーシステムズ株式会社 | Ship desulfurization device, hull-integrated desulfurization device, and method for mounting ship desulfurization device and hull-integrated desulfurization device to ship |
| CN208075612U (en) * | 2018-04-13 | 2018-11-09 | 江苏海鸥冷却塔股份有限公司 | A kind of packing type fog-dissipation device |
| CN108800983A (en) * | 2018-08-07 | 2018-11-13 | 德州贝泰制冷设备有限公司 | A kind of water-saving fog dispersal cooling tower |
| CN209672868U (en) * | 2019-01-21 | 2019-11-22 | 华北水利水电大学 | A kind of labyrinth damp type depth fog dispersal receipts water cooling tower |
-
2019
- 2019-01-21 CN CN201910051757.6A patent/CN110006269A/en active Pending
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN103743289A (en) * | 2014-01-26 | 2014-04-23 | 德州贝诺风力机械设备有限公司 | Cooling tower fog dispersal and water collection device |
| CN206001939U (en) * | 2016-07-30 | 2017-03-08 | 山东蓝想环境科技股份有限公司 | A kind of combination type fog dispersal water saving cooling tower |
| WO2018181504A1 (en) * | 2017-03-28 | 2018-10-04 | 三菱日立パワーシステムズ株式会社 | Ship desulfurization device, hull-integrated desulfurization device, and method for mounting ship desulfurization device and hull-integrated desulfurization device to ship |
| CN107560453A (en) * | 2017-10-08 | 2018-01-09 | 江苏丰泰节能环保科技有限公司 | A kind of hyperbolic natural-draft cooling tower with cold coagulation liquid fog dispersal function |
| CN108332575A (en) * | 2018-04-13 | 2018-07-27 | 江苏海鸥冷却塔股份有限公司 | Band fog dispersal module fog dispersal cooling tower |
| CN208075612U (en) * | 2018-04-13 | 2018-11-09 | 江苏海鸥冷却塔股份有限公司 | A kind of packing type fog-dissipation device |
| CN108800983A (en) * | 2018-08-07 | 2018-11-13 | 德州贝泰制冷设备有限公司 | A kind of water-saving fog dispersal cooling tower |
| CN209672868U (en) * | 2019-01-21 | 2019-11-22 | 华北水利水电大学 | A kind of labyrinth damp type depth fog dispersal receipts water cooling tower |
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| CN110345777A (en) * | 2019-08-10 | 2019-10-18 | 济南蓝辰能源技术有限公司 | A kind of dual condensation mixed water-saving fog dispersal cooling system |
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