CN110260682A - A kind of cooling tower - Google Patents
A kind of cooling tower Download PDFInfo
- Publication number
- CN110260682A CN110260682A CN201910551313.9A CN201910551313A CN110260682A CN 110260682 A CN110260682 A CN 110260682A CN 201910551313 A CN201910551313 A CN 201910551313A CN 110260682 A CN110260682 A CN 110260682A
- Authority
- CN
- China
- Prior art keywords
- evaporator section
- cooling tower
- heat
- tower body
- cooling
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
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Classifications
-
- 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
- F28C1/14—Direct-contact trickle coolers, e.g. cooling towers comprising also a non-direct contact heat exchange
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
- F28D15/02—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
- F28D15/0266—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes with separate evaporating and condensing chambers connected by at least one conduit; Loop-type heat pipes; with multiple or common evaporating or condensing chambers
-
- 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
-
- 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
- F28F25/04—Distributing or accumulator troughs
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention discloses a kind of cooling towers, tower body including being equipped with air inlet, it is provided with water distributing area and heat transfer zone from top to bottom inside the tower body, water distribution system is arranged in the water distributing area, it further include at least one hot-pipe system, each hot-pipe system includes interconnected condensation segment and evaporator section, and each condensation segment is set to outside the tower body, each evaporator section all has heat transmission fin in the evenly distributed setting in the heat transfer zone.This cooling tower can promote water-saving result and cooling efficiency simultaneously.
Description
Technical field
The present invention relates to cooling devices, particularly relate to a kind of cooling tower.
Background technique
The waste heat generated in industrial production or refrigeration process is generally taken away with cooling water.Cooling tower is to make hot fluid (packet
Include cooled water) it is cooled to set temperature equipment below, cooling tower is of wide application, for example, can be applied to sky
Adjust cooling system, refrigeration system, electric furnace, injection molding, process hides, power generation, steam turbine, aluminum profile processing, air compressor machine and industry water cooling
Equal fields.
Cooling tower is come into full contact with cooled water and unsaturated air using heat and mass principle, by cooled water
Heat exchange is carried out with air, air is delivered heat to and spills into atmosphere, achievees the effect that heat exchange cooling.Cooled water
Heat is pulled away in two ways, first is that after air and the heat exchange of cooled water, the latent heat taken away in water vapour, second is that water vapour
The sensible heat taken away, above-mentioned heat exchanging process need to consume a large amount of water.Therefore, to be that a kind of water consumption is more serious set cooling tower
Standby, water saving potential is huge, develops water-saving cooling tower, will be important research direction at this stage.
On the other hand, it to come into full contact with cooled water with unsaturated air, therefore, is generally set in existing cooling tower
Set can water distribution uniformity packing layer, packing layer can increase cooled water retention time, increase heat exchange area, promote saturated water and steam
The ratio of vapour, and then promote cooling efficiency.
A kind of heat pipe-type water saving fixtures for crossflow cooling tower are disclosed to save water consumption, in CN105737631A,
Including tower body, the tower body two sides are air inlet, are respectively arranged with filler on the inside of the air inlet described in two sides；Cooling water is from described
It is flowed into above filler；The cold air entered from the air inlet is with the cooling water flowed into from above the filler in the filler
Vertical heat exchange forms High Temperature Moist Air into the cooling tower inner cavity on the inside of the filler；Heat is separately installed on the inside of the filler
Pipe array, the heat pipe of the heat pipe array is by being arranged in the heat pipe evaporator section of the tower body inner cavity and being arranged on the tower body
The heat pipe condenser section of side is formed by connecting；Working solution is equipped in the heat pipe；The working solution the heat pipe evaporator section with it is described
High Temperature Moist Air, which exchanges heat and flashes to working solution steam, rises to the heat pipe condenser section, and the High Temperature Moist Air is condensed into liquid
Body；The working solution steam after evaporation is condensed into liquid with cold air heat exchange outside tower in the heat pipe condenser section and flows back to the heat
Pipe evaporator section.The present invention can make the saturated moist air in wet type crossflow cooling tower tower before being discharged outside tower using heat pipe
Secondary heat exchange, to solving, wet type crossflow cooling tower water loss is big, goes out the problems such as tower saliva mist is more certain effect.
In above-mentioned heat pipe-type water saving fixtures, the substance of the condensation segment of heat pipe condensation is High Temperature Moist Air, and from cooling water
Exchange heat to form High Temperature Moist Air in filler position, then exchange heat to form condensed fluid from High Temperature Moist Air in heat pipe position, need through
After gas-liquid heat exchange process twice, heat transfer effect is poor, it is clear that heat pipe play the role of it is limited, therefore, although can be in certain journey
Water-saving purpose is played on degree, but can not promote cooling efficiency.
Summary of the invention
The present invention provides a kind of cooling towers, and its object is to promote water-saving result and cooling efficiency simultaneously.
Technical scheme is as follows:
A kind of cooling tower is provided with water distributing area from top to bottom and changes including the tower body equipped with air inlet inside the tower body
Water distribution system is arranged in hot-zone, the water distributing area, it is characterised in that: and it further include at least one hot-pipe system, each hot-pipe system
It include interconnected condensation segment and evaporator section, each condensation segment is set to outside the tower body, and each evaporator section is in institute
The evenly distributed setting in heat transfer zone is stated, and all has heat transmission fin.
In use, air-flow (cold air) enters tower body from air inlet, heat exchange, shape are carried out in cooling tower with cooled water
At water vapour, heat is taken away；Cooled water also carries out heat exchange with the cooling medium in evaporator section simultaneously, and cooling medium is heated to steam
Hair, and heat is taken away, it flows to condensation segment and exchanges heat with atmosphere, cooling medium condenses into liquid, under gravity, cooling
Media fluid flows back into evaporator section, thus moves in circles, and constantly cooled hydro-thermal amount is discharged into the atmosphere and is cooled.
In this way, the heat of cooled water is mainly taken away by three parts, when one is the liquid cooling medium vaporization of evaporator section
The heat Q1 taken away, secondly the heat Q2 taken away when to form water vapour, thirdly for air-flow (or water vapour) heating institute
The heat Q3 taken away.And substance undergo phase transition process absorb or release heat, significantly larger than substance heating and cooling process absorb or
The heat of releasing, therefore, the heat of the heat of Q1 and Q2 considerably beyond Q3.
And be that packing layer is set in heat transfer zone in existing cooling tower, the cold air and cooled water that air inlet enters exist
Packing layer carries out heat exchange, takes away the heat of cooled water by two parts, and one is the heat taken away when forming water vapour,
Secondly the heat taken away by air-flow (or water vapour) heating.
For existing cooling tower, the present invention passes through significant component of heat in heat pipe by heat pipe principle
The heat transfer medium in portion rejects heat in atmosphere, to save a large amount of water resource.
In the present invention, cooling medium used in opposite heat tube system is unlimited, and single pure material or mixture can be used
Matter, or different compounding substances can be selected, or change mixing according to the demand of different phase transition temperature or heat conduction efficiency
The proportion of substance.
In the present invention, there are mainly two types of hot-pipe systems, and one is the hot-pipe system with capillary wick, the steamings of opposite heat tube
Hair section, condensation segment position do not require, the cooling medium of condensation segment passes through the work of capillary wick after being condensed into liquid
With returning in evaporator section, but the production cost of this heat pipe is relatively high；Another kind is gravity assisted heat pipe system, relies primarily on gravity
Effect flows back into cooling medium liquid in evaporator section from condensation segment, and structure is simple, lower production costs.
In the embodiment of recommendation, the hot-pipe system is gravity hot-pipe system, and each condensation segment is located at each corresponding
Evaporator section on position.
In the embodiment of recommendation, the work for the cooling medium that the hot-pipe system injects under vacuum conditions, which condenses, steams
Sending out temperature is 5 DEG C -80 DEG C.By selecting the cooling medium of different condensation evaporation temperature, cooling tower can be used for cooling down 10 DEG C -90 DEG C
Cooled water.The cooling medium is single pure material or compounding substances, for example, the heat transfer medium is selected from water, third
Alcohol or freon R134a etc., the compounding substances are freon R407C etc..Can also according to different phase transition temperature demand or
The demand of heat conduction efficiency selects different compounding substances, or changes the proportion of compounding substances.
It further include being arranged in the embodiment of recommendation, in the tower body in the gathering ground of bottom, the gathering ground
The collecting-tank.
In the embodiment of recommendation, the uniform monolayers structure or equal of each evaporator section composition is set in the heat transfer zone
Height tower body where the sum of the horizontal sectional area of even multilayered structure, each evaporator section outside and heat transmission fin maximum accounts for
The 54%-82% of internal horizontal sectional area, height where the sum of horizontal sectional area inside each evaporator section maximum accounts for
The 18-32% of horizontal sectional area inside tower body.In this way, helping to be uniformly distributed cooled water, make to enter from air inlet
Air can carry out heat exchange with cooling water, promote water-saving result and cooling efficiency.
In the present invention, any restrictions are not done to the heat transmission fin thickness of the evaporator section, are 0.1mm- in general
10mm。
In the embodiment of recommendation, the surface area of the heat transmission fin is the 1-5 of the tube surface product of the evaporator section
Times.
In the embodiment of recommendation, the single layer structure of each evaporator section composition, setting are set in the heat transfer zone
It is uniformly distributed on different height, and in overlook direction.This mode belongs to variant embodiment of the invention, also belongs to this
The protection scope of invention.
In addition to the arrangement mode of the above-mentioned several frequently seen evaporator section enumerated, in the present invention, to the mode of arrangement evaporator section
Do not do it is specifically limited, as long as each evaporator section can with cooled water realize uniform heat exchange, in this way, promotion can be realized
The technical effect of water-saving result and cooling efficiency.
In addition, not doing any restrictions to the setting direction of evaporator section in the present invention, evaporator section can be horizontally arranged, can also
To be slant setting.
In the embodiment of recommendation, the cooling tower be it is reverse-flow, the air inlet is located under the evaporator section, from
The air-flow that the air inlet enters is to be upwardly into or enter obliquely.Certainly, according to different needs, also can choose cross
Streaming or mixed-flow, at this point, air-flow can enter from the side wall of cooling tower, or from the oblique entrance of side wall of cooling tower, or
Person enters from the bottom and side wall of cooling tower simultaneously.
It further include the packing layer of 10mm-100mm thickness in the embodiment of recommendation, described filler layer is arranged described
Between water distribution system and the evaporator section.The effect of packing layer is to evenly distribute cooled water, can be uniformly distributed
Onto each evaporator section, to promote water-saving result and cooling rate.
In the present invention, the evaporator section can also be set in described filler layer, or in the evaporator section and described
Packing layer is set between gathering ground, above two mode can promote cooling efficiency to a certain extent, but with by packing layer
Setting is compared between water distribution system and evaporator section, while the effect for promoting water-saving result and cooling efficiency is poor.
In the embodiment of recommendation, through-hole, the heat transmission fin and the air inlet are distributed on the heat transmission fin
The airflow direction monoclinic phase of entrance is handed over or positive intersection.
It is cylinder or rectangular inside the tower body in the embodiment of recommendation, is arranged in the heat transfer zone each described
The uniform monolayers structure of evaporator section composition or uniform multilayered structure, each evaporator section is at the height of place in the tower body
The heart or center of gravity are that the center of circle is radially distributed.
In the embodiment of recommendation, the heat transmission fin is parallel with the airflow direction that the air inlet enters or monoclinic phase
It hands over.In this way, heat transmission fin will not stop the movement of air-flow, facilitates cooled water and air-flow carries out heat exchange.
In the embodiment of recommendation, the heat transmission fin is wavy.
In the embodiment of recommendation, the cooling tower is a kind of cooling tower by free convection.
In the embodiment of recommendation, suction ventilator is set at the air outlet of the tower body.
In the embodiment of recommendation, the condensation segment is arranged in the middle part of the periphery of the tower body or periphery top.In this way,
It can use high aerial free convection and high altitude wind to radiate to the heat in radiator from cooling medium conveying,
So as to make full use of natural cooling source, setting blower is no longer needed to, there is more preferably energy-saving effect.
In the embodiment of recommendation, the high vacancy of 30m-80m is arranged in the condensation segment.It is natural under this height
The flow velocity of wind can use the rapid cooling that natural wind realizes condensation segment in 5m/s-10m/s or so.
In the embodiment of recommendation, the evaporator section and the condensation segment of each gravity assisted heat pipe system each by
Heat-insulated piping connection.
In the embodiment of recommendation, each evaporator section is placed longitudinally, at the top of cooling medium outlet be all connected with water
The cooling medium inlet of first surge tank of flat setting, the cooling medium outlet of first surge tank connect longitudinally disposed the
The cooling medium outlet of the cooling medium inlet of two surge tanks, second surge tank connects horizontally disposed each condensation
Section.In this way, can simplify the structure of gravity assisted heat pipe heat-exchange system, production cost is reduced.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of embodiment one.
Fig. 2 is the structural schematic diagram of the embodiment of the present invention three.
Specific embodiment
Illustrate a specific embodiment of the invention with reference to the accompanying drawings.
Embodiment 1
Referring to fig. 1, a kind of cooling tower, including the cylindrical tower body 1 equipped with air inlet 11, from upper inside tower body 1
And it is arranged with water distributing area 12, heat transfer zone 13 and the gathering ground 14 positioned at bottom, water distribution system 15, gathering ground is arranged in water distributing area 12
Collecting-tank 15 is set in 14.
It further include multiple gravity assisted heat pipe systems 2, each gravity assisted heat pipe system 2 all has condensation segment 21 and evaporator section 22, gravity
The work condensation evaporation temperature for the cooling medium that hot-pipe system injects under vacuum conditions is 30 DEG C.
Each condensation segment 21 is all set in the periphery of tower body 1, and is located at the high vacancy of 50m.In this way, can use high aerial
Free convection and high altitude wind radiate to each condensation segment 21.
The uniform monolayers structure that horizontal positioned each evaporator section 22 forms is set in heat transfer zone 13, and at the height of place with
The center of tower body 1 is the radially even distribution in the center of circle, and each evaporator section is cylindrical structure, another one end of which is fixed on tower body 1
End then extends near the center of circle.The sum of the horizontal sectional area of each 22 outside of evaporator section and heat transmission fin (current obstruction area) maximum accounts for
50% of horizontal sectional area inside place height tower body 1, the sum of horizontal sectional area inside each evaporator section 22 maximum account for institute
20% of horizontal sectional area inside height tower body 1.Each evaporator section 22 all has multiple heat transmission fins, each heat transmission fin it is total
Surface area is 5 times of the surface area of the evaporator section, and or monoclinic phase parallel with the airflow direction that air inlet 11 enters is handed over respectively.
Each condensation segment 21 is located at the position on each corresponding evaporator section 22.
Cooling tower be it is reverse-flow, air inlet 11 is located under evaporator section 22, from air inlet 11 entrance air-flow can be from tower
1 bottom of body is upwardly into.
Embodiment 2
Embodiment 2 difference from example 1 is that:
The work condensation evaporation temperature for the cooling medium that gravity assisted heat pipe system is injected under vacuum conditions is 30 DEG C.
Each condensation segment 21 is all set in the periphery of tower body 1, and is located at the high vacancy of 80m.
The uniform monolayers structure that each evaporator section 22 forms, as shown in table 1, embodiment 2.1-2.5 are set in heat transfer zone 13
In, where the sum of horizontal sectional area of each 22 outside of evaporator section and heat transmission fin (current obstruction area) maximum accounts in height tower body 1
The 54%-82% (a%) of the horizontal sectional area in portion, height where the sum of horizontal sectional area inside each evaporator section 22 maximum accounts for
The 18-32% (b%) of horizontal sectional area inside tower body 1.Each evaporator section 22 all has multiple heat transmission fins, and heat transmission fin is in wave
Shape wave, total surface area are 1 times of surface area of the evaporator section, and it is parallel with the airflow direction that air inlet 11 enters respectively or
Monoclinic phase is handed over.
Embodiment 3
Embodiment 3 difference from example 1 is that:
It as shown in Figure 2, further include the packing layer 4 of 10mm-100mm thickness in embodiment 3.1-3.3, packing layer 4 is arranged
Between water distribution system 15 and evaporator section 22.
Through-hole is distributed on heat transmission fin, the airflow direction monoclinic phase that heat transmission fin and the air inlet enter is handed over or positive
It hands over.
Suction ventilator 3 is set at the air outlet of tower body 1.
Comparative example 1
A kind of cooling tower is provided with water distributing area inside tower body from top to bottom, changes including the cylindrical tower body equipped with air inlet
Hot-zone and gathering ground positioned at bottom, water distributing area are arranged water distribution system, collecting-tank 15 are arranged in gathering ground.
Filler is filled in heat transfer zone, forms the packing layer of 500mm thickness.
Cooling tower be it is reverse-flow, air inlet is located under evaporator section, from air inlet entrance air-flow can be from tower body bottom
It is upwardly into.
Comparative example 2
Comparative example 2 has used the cooling tower disclosed in CN105737631A embodiment.
Test example
The temperature for the cooled water that water distribution system provides is 50 DEG C.And embodiment 1-3 is uniformly sprayed by rotary nozzle
In the heat transfer zone of comparative example 1-2.
The gas flow temperature entered from air inlet is 28 DEG C.
Test result such as table 1:
The test data of each cooling tower of table 1
The above is only a specific embodiment of the present invention, but the design concept of the present invention is not limited to this, all to utilize this
Design makes a non-material change to the present invention, and should all belong to behavior that violates the scope of protection of the present invention.
Claims (10)
1. a kind of cooling tower is provided with water distributing area and heat exchange inside the tower body including the tower body equipped with air inlet from top to bottom
Water distribution system is arranged in area, the water distributing area, it is characterised in that: further includes at least one hot-pipe system, each hot-pipe system is equal
Including interconnected condensation segment and evaporator section, each condensation segment is set to outside the tower body, and each evaporator section is described
The evenly distributed setting in heat transfer zone, and all have heat transmission fin.
2. a kind of cooling tower as described in claim 1, it is characterised in that: the hot-pipe system is gravity hot-pipe system, each institute
State the top that evaporator section is respectively positioned on corresponding each condensation segment.
3. a kind of cooling tower as claimed in claim 2, it is characterised in that: the cooling medium of the hot-pipe system is in vacuum state
Under work condensation evaporation temperature be 5 DEG C -80 DEG C.
4. a kind of cooling tower as claimed in claim 1 or 2, it is characterised in that: further include the collection positioned at bottom in the tower body
The collecting-tank is arranged in the gathering ground in pool.
5. a kind of cooling tower as claimed in claim 1 or 2, it is characterised in that: in the heat transfer zone, be provided with each evaporation
The uniform monolayers structure of Duan Zucheng or uniform multilayered structure, the horizontal sectional area of each the evaporator section outside and the heat transmission fin
The sum of it is maximum account for where horizontal sectional area inside height tower body 54%-82%, the level inside each evaporator section cuts
The 18-32% of horizontal sectional area where the sum of area maximum accounts for inside height tower body.
6. a kind of cooling tower as described in claim 1, it is characterised in that: the surface area of the heat transmission fin is the evaporator section
1-5 times of surface area.
7. a kind of cooling tower as claimed in claim 5, it is characterised in that: the cooling tower is reverse-flow, the air inlet position
Under the evaporator section, the air-flow entered from the air inlet is to be upwardly into or enter obliquely.
8. a kind of cooling tower as claimed in claim 5, it is characterised in that: further include the packing layer of 10mm-100mm thickness, institute
Packing layer is stated to be arranged between the water distribution system and the evaporator section.
9. a kind of cooling tower as claimed in claim 5, it is characterised in that: through-hole is distributed on the heat transmission fin, it is described to lead
Hot fin is handed over the airflow direction monoclinic phase that the air inlet enters or is just intersected.
10. a kind of cooling tower as claimed in claim 5, it is characterised in that: described to be cylindrical or rectangular inside the tower body
The uniform monolayers structure or uniform multilayered structure that each evaporator section forms are set in heat transfer zone, and each evaporator section is in place height
Degree sentences the center of the tower body or center of gravity is that the center of circle is radially distributed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910551313.9A CN110260682A (en) | 2019-06-24 | 2019-06-24 | A kind of cooling tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910551313.9A CN110260682A (en) | 2019-06-24 | 2019-06-24 | A kind of cooling tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110260682A true CN110260682A (en) | 2019-09-20 |
Family
ID=67921097
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910551313.9A Pending CN110260682A (en) | 2019-06-24 | 2019-06-24 | A kind of cooling tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110260682A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110779350A (en) * | 2019-11-04 | 2020-02-11 | 北京金茂绿建科技有限公司 | Shell-and-tube heat pipe cooling tower |
| CN112791438A (en) * | 2020-12-28 | 2021-05-14 | 魏永阳 | Cold energy desalination system and process for treating salt water |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH11159973A (en) * | 1997-11-29 | 1999-06-15 | Toshiba Eng & Constr Co Ltd | Cooling tower and method for preventing white smoke from it |
| CA2327936A1 (en) * | 1999-12-10 | 2001-06-10 | Hudson Products Corporation | Passive wet cooling tower plume abatement system |
| CN108986935A (en) * | 2018-05-25 | 2018-12-11 | 中国核电工程有限公司 | A kind of nuclear power plant's accident hot trap water tank passive cooling system |
| CN208333155U (en) * | 2018-06-19 | 2019-01-04 | 北京时代科仪新能源科技有限公司 | A kind of heat pipe-type water-cooling apparatus |
| CN109916189A (en) * | 2019-02-16 | 2019-06-21 | 黄德夫 | A kind of dry-wet integrated type cooling tower of casing heat pipe-type |
-
2019
- 2019-06-24 CN CN201910551313.9A patent/CN110260682A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH11159973A (en) * | 1997-11-29 | 1999-06-15 | Toshiba Eng & Constr Co Ltd | Cooling tower and method for preventing white smoke from it |
| CA2327936A1 (en) * | 1999-12-10 | 2001-06-10 | Hudson Products Corporation | Passive wet cooling tower plume abatement system |
| CN108986935A (en) * | 2018-05-25 | 2018-12-11 | 中国核电工程有限公司 | A kind of nuclear power plant's accident hot trap water tank passive cooling system |
| CN208333155U (en) * | 2018-06-19 | 2019-01-04 | 北京时代科仪新能源科技有限公司 | A kind of heat pipe-type water-cooling apparatus |
| CN109916189A (en) * | 2019-02-16 | 2019-06-21 | 黄德夫 | A kind of dry-wet integrated type cooling tower of casing heat pipe-type |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110779350A (en) * | 2019-11-04 | 2020-02-11 | 北京金茂绿建科技有限公司 | Shell-and-tube heat pipe cooling tower |
| CN112791438A (en) * | 2020-12-28 | 2021-05-14 | 魏永阳 | Cold energy desalination system and process for treating salt water |
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Application publication date: 20190920 |