CN207379318U - A kind of hyperbolic natural-draft cooling tower with cold coagulation liquid fog dispersal - Google Patents
A kind of hyperbolic natural-draft cooling tower with cold coagulation liquid fog dispersal Download PDFInfo
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- CN207379318U CN207379318U CN201721292129.XU CN201721292129U CN207379318U CN 207379318 U CN207379318 U CN 207379318U CN 201721292129 U CN201721292129 U CN 201721292129U CN 207379318 U CN207379318 U CN 207379318U
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Abstract
A kind of hyperbolic natural-draft cooling tower with cold coagulation liquid fog dispersal, including hyperbola tower body, natural cooling air inlet and water dispensing apparatus, natural cooling air inlet is arranged on the hypomere side of hyperbola tower body, air-cooled cohesion water collector is equipped in the top of water dispensing apparatus, cold wind is externally provided in hyperbola tower body to take out for device, air-cooled cohesion water collector is taken out by cold wind provides sub-cooled source of the gas for device.Cryogenic air is discharged into tower neck inner cavity again after being entered in hollow heat conduction shell after sufficient heat exchange, and the temperature of so hollow heat conduction shell approaches always with ambient temperature, and droplet will be quickly condensed into when high temperature saturated vapor runs into the hollow heat conduction shell of low temperature, as clean water, it is simple in structure, can disperse fog it is water-saving and, pure fresh water can also be obtained, meanwhile the natural pump drainage performance of cooling tower is improved, increase pump drainage pressure, ventilation resistance is reduced, improves cooling effect.
Description
Technical field:
Fog dispersal and water vapour recycling profit the utility model is related to a kind of Industrial cooling tower more particularly to power plant cooling tower
Use technology.
Background technology:
At present, power plant's hyperbolic natural-draft cooling tower water vapour recovery technology there are no successful application layer into
Fruit, in Chinese patent ZL201020162612.8《Water-saving device of power plant cooling tower》In disclose a kind of water-saving dress of power plant cooling tower
It puts, is arranged above collecting the cooling dome of water vapour at the top of cooling tower, the water vapour emerged by cooling dome to cooling tower top
It is condensed and catchments, fall into tower and be multiplexed, it can carry out a small amount of cohesions to the water vapour being discharged into air, and water vapour is turned
Condensation water is changed into be directly multiplexed；Since cooling tower is continuous duty, saturated vapor is continuously discharged in tower top, although being set in tower top
There is a cooling dome, but the temperature of the cooling dome saturated-steam temperature excessive with cooling tower is sufficiently close to, and condensation effect is undesirable, especially
Under the meteorological condition of summer 10% (under extreme weather conditions), cooling dome is under in burning sun, the sun shines, and temperature is far above cold
But the excessive vapor (steam) temperature of tower can so accelerate the volatilization of water vapour instead, it is impossible to play the role of agglomerating water mist.Meanwhile
Cooling dome is added at the top of cooling tower, steam discharge path is swerved 90 °, adds steam discharge resistance, increases energy consumption, and direct shadow
The steam discharge performance and cooling effect of cooling tower are rung, and enforcement difficulty is larger.Therefore, the program is not pushed away in practical applications
Wide application is only a kind of scenario.
Xi'an Polytechnic University is disclosed in application number 201420542186.9 " with reference to the hair of evaporation cooling and mechanical refrigeration
Power plant cooling tower water-saving system ".
It is a kind of water-saving with the power generating plant cooling tower of mechanical refrigeration by increasing auxiliary cold water spray combination evaporation cooling
System includes enclosed evaporation cooling handpiece Water Chilling Units, mechanical refrigeration system and the cooling stack connected by pipe network；Institute
Enclosed evaporation cooling handpiece Water Chilling Units are stated, include machine unit shell, the machine unit shell is respectively arranged with one on opposite two side
Secondary wind air inlet a, First air air inlet b；It is cold to be symmetrically arranged with the first tubular indirect evaporative for the left and right sides in the machine unit shell
But device, the second tube type indirect evaporative cooler, first tube type indirect evaporative cooler and the second tubular indirect evaporative cool down
Direct evaporative cooler is provided between device；First tube type indirect evaporative cooler be sequentially arranged above water fender c and
Wind turbine c；Second tube type indirect evaporative cooler has been sequentially arranged above water fender a and wind turbine a；It is described directly evaporate it is cold
But device has been sequentially arranged above water fender b and wind turbine b；On the wind turbine c, wind turbine b and the corresponding machine unit shell roofs of wind turbine a
It is both provided with exhaust outlet；The mechanical refrigeration system, includes compressor, the compressor successively with evaporator, throttle valve and
Condenser connects and composes closed circuit, and the evaporator is connected by the 3rd water pipe G3 with the second water pipe G2；Gravity-flow ventilation cools down
Tower, includes tower body, and the roof of the tower body is provided with wind exhausting outlet；Be provided with filler in the tower body, the filler it is upper
Side is disposed with water-distributing device, water collection device and multiple atomizers, and multiple atomizers pass through the 4th water pipe G4 and the second water
Pipe G2 connections；Collecting-tank is provided with below the filler, the collecting-tank is connected with cold water outlet pipe, and the filler is with catchmenting
It forms air flow channel between pond, air intake is provided on the corresponding tower body side wall of the air flow channel；The water-distributing device by
Hot water inlet pipe and the multiple nozzles composition being arranged on hot water inlet pipe, multiple nozzles are in be uniformly arranged；4th water pipe
Water pump is provided on G4.
It is that water supply installation and refrigerating plant are added outside cooling tower, added at the top of cooling tower cold water spray device and
Water collector first cools down the water of water supply installation by refrigerating plant, when the leaving water temperature of water supply installation reaches predetermined temperature
It sprays cooling water fog precipitation with pressure from cooling tower top down by spray equipment again afterwards to drip, so that on from water collection device gap
The high-temperature steam risen runs into the cohesion of low temperature fine liquid particles, and is fallen into successively through water collector, packing in collecting-tank with water droplet, from
And achieve the purpose that reduce water vapour outflow reuse.Although this power generating plant cooling tower water-saving system theory, which is said, can realize to water
The recycling of steam has water-saving function, but in the possibility very little actually promoted and applied, at home and abroad there are no actually make
Case, the reason is that the program is complicated, subsidiary engine include three small-sized cooling towers, three water pumps, an air-conditioning and
One booster pump, connection structure requirement is high, and cooling tower is equipped with direct plungeing into greatly, and in subsidiary engine operational process for this set subsidiary engine
Water consumption is big, and operation power consumption is high, and operation cost is high, while can also generate the pollution of secondary water barber, meanwhile, the steam of recycling
Water falls into packing with chilling spray water and the hot water sprayed from hot water inlet pipe, and two are generated by reheating heating
Secondary evaporation, the high-quality water of Steam Recovery are not utilized, deficiency in economic performance.In addition, spray equipment is from cooling tower top down
Cooling water fog precipitation drop with pressure is sprayed, directly obstruct cooling tower top mixing air goes out stream, and the air for playing cooling effect can not
Continuous smooth discharge, will seriously affect the cooling effect of cooling tower.
In order to which steam more effectively excessive to cooling tower recycles, mitigate white cigarette water pollution, improve cooling
Tower water-saving result reduces the operation cost of water-saving reuse, improves the overall economic efficiency of cooling tower water-saving technology, and applicant is practical
A kind of hyperbola gravity-flow ventilation power plant cooling tower of new poly- liquid that has the function of to disperse fog.
Utility model content：
The purpose of this utility model is to provide a kind of hyperbolic natural-draft cooling tower with cold coagulation liquid fog dispersal,
It is simple in structure, and small investment operation cost is low, but it can be to the high-temperature water vapor in hyperbola gravity-flow ventilation power plant cooling tower
Cold coagulation liquid is carried out, and is recycled, and can disperse fog and reduce white cigarette discharge, environmental protection of saving water and energy.
The technical solution that the utility model is taken is as follows：
A kind of hyperbolic natural-draft cooling tower with cold coagulation liquid fog dispersal, including hyperbola tower body, bottom collection
Pond, natural cooling air inlet, packing layer and water dispensing apparatus, underdrain pond are arranged on the bottommost of hyperbola tower body,
Natural cooling air inlet is arranged on the hypomere side of hyperbola tower body, and packing layer is arranged in hyperbola tower body, and position
In the top of natural cooling air inlet, water dispensing apparatus is arranged on the top of packing layer, it is characterized in that：In the upper of water dispensing apparatus
Side is equipped with air-cooled cohesion water collector, and being externally provided with cold wind in hyperbola tower body takes out for device, and air-cooled cohesion water collector is by cold wind
It takes out and provides sub-cooled source of the gas for device, approaching channel is connect equipped with pure water in the lower section of air-cooled cohesion water collector.
Further, the air-cooled cohesion water collector includes air-cooled fog dispersal lime set plate and Ta Nei appendixs, and air-cooled fog dispersal is solidifying
Liquid plate compartment of terrain is distributed in the top of water dispensing apparatus, and the air-cooled fog dispersal lime set plate is hardened for hollow slab construction or hollow curved surface
Structure, the cooling cavity of all air-cooled fog dispersal lime set plates are communicated with appendix in tower, and outlet is equipped on air-cooled fog dispersal lime set plate
Hole.
Further, the air-cooled fog dispersal lime set plate includes hollow heat conduction shell, cooling cavity, air admission hole and venthole, into
Stomata is arranged on the hypomere wall body of hollow heat conduction shell, and cooling cavity is communicated by air admission hole with appendix in tower, venthole
It is arranged on the epimere shell wall body of hollow heat conduction shell, and is communicated with space in tower.
Further, the raised line that shuts off is equipped on the outer surface of hollow heat conduction shell, after the installation of hollow heat conduction shell, is shut off
Angle is 0 °~75 ° between raised line and hollow heat conduction shell top.
Further, condensing ponding convex body is equipped on the outer surface of hollow heat conduction shell.
Further, there is folder in the direction that steam rises flowing in main condenser face and the tower of the air-cooled fog dispersal lime set plate
Angle.
Further, the material of the hollow heat conduction shell is any one of copper, stainless steel, aluminium alloy.
Further, the cold wind is taken out pumps unit for cold air of the device including M wind turbine and the outer appendix composition of tower, often
The fan induced draught mouth that a cold air is pumped in unit is communicated with the external world, and the air outlet of wind turbine passes through gas transmission in appendix outside tower and tower
The seal of tube docks, M=1~20.
Further, heat sink is equipped between appendix and wind turbine in tower.
Further, appendix and the outer appendix of tower are thermal insulation pipe in tower.
Since the utility model is on the basis of existing gravity-flow ventilation double-curve cooling column, by above water dispensing apparatus
Air-cooled cohesion water collector is added, air-cooled cohesion water collector is taken out by cold wind and carries out pressure cooling for device offer low-temperature cold wind,
By in the extraneous Cryogenic air hollow heat conduction shell of input with pressure, Cryogenic air is from the air inlet of air-cooled fog dispersal lime set plate into cold
But in cavity, fully with being discharged into after hollow heat conduction shell heat exchange from venthole in the tower neck inner cavity of hyperbola tower body, thus
The temperature of hollow heat conduction shell can be made to be approached always with ambient temperature, run into when flowing up high temperature saturated vapor in cooling tower
During the hollow heat conduction shell of low temperature, the high-temperature water vapor of script saturation shape will quickly be condensed into water on hollow heat conduction shell surface
Then pearl flows down along the surface of hollow heat conduction shell, due to connecing approaching channel equipped with pure water in the lower end of hollow heat conduction shell, by saturation
Steam, which condenses the distilled water to be formed and connects approaching channel by pure water, draws, and becomes clean water, while from the row suitable for reading of hyperbola tower body
The hot steam concentration gone out significantly declines, and elimination fog effect is notable.
In cooling tower operational process, when hot water to be cooled passes through cooling tower filler layer, air comes into full contact with hot water
It mixes, the partial pressure of water has reached the saturation pressure corresponding to temperature at that time, the natural cooling from hyperbola tower body downside in gas
The cold air that air inlet enters is become for saturation Hot wet air heating, and on cooling tower top, evaporation water damage is substantially wet with saturation heat
Existing for the form of air.
The saturation Hot wet air heating on cooling tower soaking filler top in uphill process, by it is air-cooled cohesion water collector when,
It will necessarily be contacted with hollow heat conduction shell, since what is circulated in hollow heat conduction shell is Cryogenic air outside cooling tower, according to
The operating energy loss parameter and statistics of conventional cooling stack, cold air and cooling tower soaking filler outside cooling tower
The temperature gap of top saturation Hot wet air heating maintains substantially 8.5 ° -11 °, can so be condensed by air-cooled cohesion water collector
Saturation Hot wet air heating in uphill process, condensed water enrichment and along hollow heat conduction shell surface on air-cooled cohesion water collector
Downslide, fall into pure water and connect in approaching channel, pure water connects approaching channel and collects condensed water to the collecting pipe of cooling tower one side, so recyclable cold
But the 20%-30% waters of tower evaporation capacity.The temperature and cooling tower soaking filler top saturation heat of air-cooled cohesion water collector are wet
Temperature gap between air is bigger, saturation Hot wet air heating just more, the recyclable cooling condensed by air-cooled cohesion water collector
Tower evaporation capacity is bigger, and elimination fog effect is better, and gas supply flow or reduction cold wind pumping for device are taken out for dress by increasing cold wind
The feed air temperature put can improve the fog dispersal condensate effect of cooling tower, evaporate the recycling ratio of vapour quantity and can obtain raising.
For the cooling stack of 10,000 square meters, by quantity of circulating water 70000m3/ h is calculated, and evaporation capacity presses 1.5%
It calculates, evaporation loss 1050m3/ h, recyclable condensed water are calculated by 25%, recyclable condensed water 262.5m3/h；As run per year
5500 consider when small, then 1 year 144.3750 ten thousand m of recyclable saving water3.If the cooling tower by national 200 10,000 square meters is same
Shi Yunhang, whole year can save 2.8875 hundred million m3, by 4 yuan per ton calculating, whole year can save 11.55 hundred million yuan.
Cold wind is taken out carries out pressure cooling by aspirating extraneous normal air for device to air-cooled cohesion water collector, even if
Summer, the temperature gap in hollow heat conduction shell and tower between saturation Hot wet air heating can also keep 8.5 ° -11 °, so can also make
Saturation Hot wet air heating 23%~25% is condensed into water in tower.If not only having increased cold wind takes out the gas supply flow for supplying device, but also to being inputted
Cold air carry out cooling processing, make the temperature gap in hollow heat conduction shell and tower between saturation Hot wet air heating be maintained at 20 °-
32 °, then recycle the ratio of condensed water with regard to 46%~50% can be reached.
The utility model takes out the cooling inner cavity continuously feed cooling for device to hollow heat conduction shell by cold wind
Air, the initial temperature of institute's moving air is exactly outside air temperature in the cooling inner cavity of hollow heat conduction shell, it in tower with treating
The temperature of the saturation high temperature water gas of discharge is there are larger temperature difference, when Cryogenic air flows into simultaneously from the bottom of hollow heat conduction shell
When constantly rising, Cryogenic air and the saturation Hot wet air heating of hollow heat conduction shell outer surface carry out heat exchange, can make saturation
Hot wet air heating is assembled to form pure aqueous in the surface condensation of hollow heat conduction shell, and can be promoted and be flowed in hollow heat conduction shell inner cavity
The temperature of dynamic air so as to improve pump drainage pressure at the top of cooling tower, is conducive to improve the pump drainage performance of cooling tower, reduces saturation heat
The content of humid air, so as to fulfill mist exhaust emission is reduced, in entirely fog dispersal water-saving system, as long as in existing cooling tower
Air-cooled cohesion water collector is added, the cold wind that cold air can constantly be provided to air-cooled cohesion water collector by being added outside tower is taken out for dress
It puts, simple in structure, reliable, low energy consumption, the pump drainage for going out wind pressure increase, being conducive to improve cooling tower at the top of cooling tower
Can, it is the ideal scheme of the water-saving fog dispersal of existing cooling tower.
The utility model is both applicable in fresh water cooled, seawater cooling is also applied for, when the hyperbola gravity-flow ventilation of seawater cooling
Cooling tower use the utility model after, can disperse fog it is water-saving and, moreover it is possible to obtain pure fresh water, meanwhile, improve it is cold
But the natural pump drainage performance of tower increases pump drainage pressure, reduces ventilation resistance, improves cooling effect.
Description of the drawings：
Fig. 1 is a kind of structure diagram of the utility model；
Fig. 2 is a kind of structure diagram of air-cooled cohesion water collector；
Fig. 3 is the A direction views of Fig. 2, i.e., a kind of structure diagram of air-cooled fog dispersal lime set plate；
Fig. 4 is the first structure diagram of heat sink；
Fig. 5 is second of structure diagram of heat sink；
Fig. 6 is the third structure diagram of heat sink；
In figure：1- hyperbola tower bodies；2- underdrains pond；3- natural cooling air inlets；4- packing layers；5- water distributions fill
It puts；The air-cooled cohesion water collectors of 6-；7- cold wind is taken out for device；8- pure water connects approaching channel；9- heat sinks；The air-cooled fog dispersal lime sets of 61-
Plate；Appendix in 62- towers；The hollow heat conduction shells of 611-；612- cools down cavity；613- air admission holes；614- ventholes；615- shuts off
Raised line；616- condensing ponding convex bodys；71- wind turbines；The outer appendix of 72- towers；91- heat conduction appendixs；92- cooling water pipes；93- is cycled
Water pump；94- cooling water sources；95- insulating layers；96- thermal sleeves；97- cools down sap cavity.
Specific embodiment：
The specific embodiment of the utility model is described in detail below in conjunction with the accompanying drawings：
Embodiment 1：A kind of hyperbolic natural-draft cooling tower with cold coagulation liquid fog dispersal, as shown in Figure 1, including
Water dress is received in hyperbola tower body 1, underdrain pond 2, natural cooling air inlet 3, packing layer 4, water dispensing apparatus 5, air-cooled cohesion
It puts 6, cold wind pumping and connects approaching channel 8 for device 7 and pure water, underdrain pond 2 is arranged on the bottommost of hyperbola tower body 1, natural cooling
Air inlet 3 is arranged on the hypomere side of hyperbola tower body 1, and packing layer 4 is arranged in hyperbola tower body 1, and positioned at certainly
The top of right cooling air inlet 3, water dispensing apparatus 5 are arranged on the top of packing layer 4, and air-cooled cohesion water collector 6 is arranged on
The top of water dispensing apparatus 5 is externally provided with cold wind in hyperbola tower body 1 and takes out for device 7, and cold wind is taken out receives water for device 7 for air-cooled cohesion
Device 6 provides sub-cooled source of the gas, and the air-cooled cohesion water collector 6 includes air-cooled fog dispersal lime set plate 61 and Ta Nei appendixs
62, several blocks of air-cooled fog dispersal lime set plates 61 are equally spacedly distributed in the top of water dispensing apparatus 5, and the master of air-cooled fog dispersal lime set plate 61 is cold
The direction of steam rising flowing has 15 °~30 ° angles in solidifying face and tower；The air-cooled fog dispersal lime set plate 61 is hollow tablet
Structure, the air-cooled fog dispersal lime set plate 61 include hollow heat conduction shell 611, cooling cavity 612, air admission hole 613, venthole 614,
Shut off raised line 615 and condensing ponding convex body 616, and air admission hole 613 is arranged on the lower face of hollow heat conduction shell 611, and cooling is empty
Chamber 612 is communicated by air admission hole 613 with appendix in tower 62, and venthole 614 is arranged on the upper surface of hollow heat conduction shell 611
On, venthole 614 is communicated with space in tower, and 12 ventholes are opened up in each hollow 611 upper surface compartment of terrain of heat conduction shell
614, the sum of aperture of all ventholes 614 is less than the aperture size of air admission hole 613, in the outer surface of hollow heat conduction shell 611
Shut off raised line 615 and condensing ponding convex body 616 are equipped with, the raised line 615 that shuts off is parallel with hollow 611 top of heat conduction shell, condensing
Ponding convex body 616 is evenly distributed on the outer surface of hollow heat conduction shell 611, and the material of the hollow heat conduction shell 611 is
Stainless steel connects approaching channel 8 in the lower section of each hollow heat conduction shell 611 equipped with pure water；The cold wind take out for device 7 include 4 by
The cold air that wind turbine 71 and the outer appendix 72 of tower form pumps unit, in each cold air pumps unit, the air draught of wind turbine 71
Mouthful communicated with the external world, the air outlet of wind turbine 71 is sealed with the outer appendix 72 of tower to be docked, all towers outside appendix 72 all with it is defeated in tower
Tracheae 62 communicates, and appendix 62 and the outer appendix 72 of tower are thermal insulation pipe in tower.
Embodiment 2：In order to further improve condensation defog effect, improve and receive water rate, on the basis of embodiment 1, in tower
Heat sink 9 is equipped between interior appendix and wind turbine, the heat sink 9 is as shown in figure 4, in the outer surface of heat conduction appendix 91
Coiling cooling water pipe 92, cooling water pipe 92 is communicated by water circulating pump 93 with cooling water source 94, in the outer surface of cooling water pipe 92
It is enclosed with insulating layer 95.
In upper example, the heat sink 9 can also take scheme as shown in Figure 5, be set in the outer surface of heat conduction appendix 91
There is thermal sleeve 96, closed cooling sap cavity 97 is formed between thermal sleeve 96 and heat conduction appendix 91, cooling sap cavity 97 passes through
Water circulating pump 93 is communicated with cooling water source 94.
The heat sink 9 can be simpler, as shown in fig. 6, the outer surface of heat conduction appendix 91 is directly immersed in cold
But in water source 94.
The temperature for inputting hollow 611 inner cavity air of heat conduction shell can be greatly lowered in above-mentioned three kinds of heat sinks 9, increase
Temperature difference between cooling air in hollow 611 inner cavity of heat conduction shell and the saturation Hot wet air heating outside hollow heat conduction shell 611,
The wet steam of more short grained saturation heat can be quickly condensed upon on hollow 611 outer surface of heat conduction shell, so as to improve in cooling tower
The wet steam recovery utilization rate of saturation heat, reduces " white cigarette " exhaust emission.
There are many embodiment of the utility model, do not enumerating one by one herein, the shape of hollow heat conduction shell 611, size,
Spacing distance sets angle of inclination that can be all changed at will by according to the design of people, and the scheme of heat sink 9 is also very much, only
It will can be to all schemes that the air in air inlet pipeline cools down.The utility model is cold especially suitable for seawater
But, pure fresh water can be obtained using the technical solution of the utility model, solves the daily drinking-water of people and the needs of life,
It is become apparent on nuclear power station using economic benefit and social benefit.
Claims (9)
1. a kind of hyperbolic natural-draft cooling tower with cold coagulation liquid fog dispersal, including hyperbola tower body (1), bottom collection
Pond (2), natural cooling air inlet (3), packing layer (4) and water dispensing apparatus (5), underdrain pond (2) are arranged on hyperbolic
The bottommost of transmission tower body (1), natural cooling air inlet (3) are arranged on the hypomere side of hyperbola tower body (1), packing layer
(4) it is arranged in hyperbola tower body (1), and positioned at the top of natural cooling air inlet (3), water dispensing apparatus (5) is arranged on water drenching
The top of packing layer (4), it is characterized in that：Air-cooled cohesion water collector (6) is equipped in the top of water dispensing apparatus (5), in hyperbola
Tower body (1) is externally provided with cold wind and takes out for device (7), and air-cooled cohesion water collector (6) is taken out by cold wind provides sub-cooled for device (7)
Source of the gas connects approaching channel (8) in the lower section of air-cooled cohesion water collector (6) equipped with pure water.
2. there is the hyperbolic natural-draft cooling tower of cold coagulation liquid fog dispersal according to claim 1, it is characterized in that：Institute
Stating air-cooled cohesion water collector (6) includes appendix (62) in air-cooled fog dispersal lime set plate (61) and tower, air-cooled fog dispersal lime set plate
(61) compartment of terrain is distributed in the top of water dispensing apparatus (5), and the air-cooled fog dispersal lime set plate (61) is hollow slab construction or hollow
Curved plate structure, the cooling cavity of all air-cooled fog dispersal lime set plates (61) is communicated with appendix in tower (62), in air-cooled fog dispersal
Lime set plate (61) is equipped with venthole.
3. there is the hyperbolic natural-draft cooling tower of cold coagulation liquid fog dispersal according to claim 2, it is characterized in that：Institute
Stating air-cooled fog dispersal lime set plate (61) includes hollow heat conduction shell (611), cooling cavity (612), air admission hole (613) and venthole
(614), air admission hole (613) is arranged on the hypomere wall body of hollow heat conduction shell (611), and cooling cavity (612) passes through air admission hole
(613) being communicated with appendix in tower (62), venthole (614) is arranged on the epimere shell wall body of hollow heat conduction shell (611), and
It is communicated with space in tower.
4. there is the hyperbolic natural-draft cooling tower of cold coagulation liquid fog dispersal according to claim 3, it is characterized in that：
The outer surface of hollow heat conduction shell (611) is equipped with the raised line (615) that shuts off, and after hollow heat conduction shell (611) installation, shuts off convex
Angle is 0 °~75 ° between item (615) and hollow heat conduction shell (611) top.
5. there is the hyperbolic natural-draft cooling tower of cold coagulation liquid fog dispersal according to claim 3, it is characterized in that：
The outer surface of hollow heat conduction shell (611) is equipped with condensing ponding convex body (616).
6. there is the hyperbolic natural-draft cooling tower of cold coagulation liquid fog dispersal according to claim 2, it is characterized in that：Institute
That states the direction that steam rising is flowed in the main condenser face and tower of air-cooled fog dispersal lime set plate (61) has angle.
7. there is the hyperbolic natural-draft cooling tower of cold coagulation liquid fog dispersal according to claim 1, it is characterized in that：Institute
It states cold wind pumping and pumps unit for cold air of the device (7) including M wind turbine (71) and outer appendix (72) composition of tower, each cold sky
Wind turbine (71) inlet scoop that gas is pumped in unit is communicated with the external world, air outlet and outer appendix (72) sealing pair of tower of wind turbine (71)
It connects, M=1~20.
8. there is the hyperbolic natural-draft cooling tower of cold coagulation liquid fog dispersal according to claim 1, it is characterized in that：
Heat sink (9) is equipped in tower between appendix (62) and wind turbine (71).
9. there is the hyperbolic natural-draft cooling tower of cold coagulation liquid fog dispersal according to claim 1, it is characterized in that：Tower
Interior appendix (62) and the outer appendix (72) of tower are thermal insulation pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721292129.XU CN207379318U (en) | 2017-10-08 | 2017-10-08 | A kind of hyperbolic natural-draft cooling tower with cold coagulation liquid fog dispersal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721292129.XU CN207379318U (en) | 2017-10-08 | 2017-10-08 | A kind of hyperbolic natural-draft cooling tower with cold coagulation liquid fog dispersal |
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| Publication Number | Publication Date |
|---|---|
| CN207379318U true CN207379318U (en) | 2018-05-18 |
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ID=62337873
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| Application Number | Title | Priority Date | Filing Date |
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| CN201721292129.XU Active CN207379318U (en) | 2017-10-08 | 2017-10-08 | A kind of hyperbolic natural-draft cooling tower with cold coagulation liquid fog dispersal |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN112484524A (en) * | 2020-11-18 | 2021-03-12 | 暨南大学 | Vertical multistage cooling wet cooling tower and cooling method |
-
2017
- 2017-10-08 CN CN201721292129.XU patent/CN207379318U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN112484524A (en) * | 2020-11-18 | 2021-03-12 | 暨南大学 | Vertical multistage cooling wet cooling tower and cooling method |
| CN112484524B (en) * | 2020-11-18 | 2021-09-14 | 暨南大学 | Vertical multistage cooling wet cooling tower and cooling method |
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