CN113896264A - Radiation refrigeration water resource acquisition device - Google Patents
Radiation refrigeration water resource acquisition device Download PDFInfo
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- CN113896264A CN113896264A CN202111200346.2A CN202111200346A CN113896264A CN 113896264 A CN113896264 A CN 113896264A CN 202111200346 A CN202111200346 A CN 202111200346A CN 113896264 A CN113896264 A CN 113896264A
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- radiation refrigeration
- water resource
- condensation
- water
- refrigeration coating
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0033—Other features
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0033—Other features
- B01D5/0042—Thermo-electric condensing; using Peltier-effect
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0057—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
- B01D5/006—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes with evaporation or distillation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0078—Condensation of vapours; Recovering volatile solvents by condensation characterised by auxiliary systems or arrangements
- B01D5/009—Collecting, removing and/or treatment of the condensate
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/043—Details
Abstract
The invention discloses a radiation refrigeration water resource acquisition device. The radiation refrigeration water resource acquisition device includes: the water vapor condensation device comprises an evaporation chamber, a condensation chamber and a communication device, wherein the evaporation chamber is communicated with the condensation chamber through the communication device, and a radiation refrigeration coating is arranged inside the condensation chamber to accelerate the condensation of water vapor; the radiation refrigeration coating comprises at least one high-reflectivity inorganic particle and at least one high molecular polymer, the surface of the radiation refrigeration coating comprises hydrophilic areas and hydrophobic areas, and the hydrophilic areas and the hydrophobic areas are arranged in a staggered mode. According to the radiation refrigeration water resource acquisition device provided by the invention, the specific radiation refrigeration coating is arranged in the condensation chamber, so that the surface temperature of the radiation refrigeration coating is far lower than the air temperature, the temperature difference required by condensed water vapor is sufficiently provided, and the condensation efficiency is further improved.
Description
Technical Field
The invention relates to a radiation refrigeration water resource acquisition device, and belongs to the technical field of fresh water resource acquisition.
Background
Sea water desalination, namely, sea water desalination is utilized to produce fresh water. The open source incremental technology for realizing water resource utilization can increase the total amount of fresh water, is not influenced by time, space and climate, and can ensure stable water supply of coastal resident drinking water, industrial boiler water supplement and the like. The process of obtaining fresh water from seawater is known as seawater desalination. The currently used methods for desalinating seawater include a seawater freezing method, an electrodialysis method, a distillation method, a reverse osmosis method, and an ammonium carbonate ion exchange method, and the currently applied reverse osmosis membrane method and the distillation method are the mainstream in the market.
In the seawater desalination device integrating evaporation and condensation, a device which does not need to consume a large amount of electric energy and has a simple structure exists, but the efficiency of obtaining clean water by the device is limited to a certain extent at present, the condensation efficiency is mainly limited, and the condensation efficiency becomes one of the main bottlenecks for efficiently preparing the clean water.
Therefore, it is necessary to provide a radiation refrigeration water resource obtaining device to solve the above problems in the background art.
Disclosure of Invention
The invention aims to provide a radiation refrigeration water resource acquisition device to overcome the defects in the prior art.
In order to achieve the purpose, the technical scheme adopted by the invention comprises the following steps: the embodiment of the invention provides a radiation refrigeration water resource acquisition device, which comprises: the water vapor condensation device comprises an evaporation chamber, a condensation chamber and a communication device, wherein the evaporation chamber is communicated with the condensation chamber through the communication device, and a radiation refrigeration coating is arranged inside the condensation chamber to accelerate the condensation of water vapor.
Preferably, the radiation refrigeration coating comprises at least one high-reflectivity inorganic particle and at least one high molecular polymer, and the surface of the radiation refrigeration coating comprises hydrophilic regions and hydrophobic regions, and the hydrophilic regions and the hydrophobic regions are arranged in a staggered manner.
Preferably, the reflectivity of the radiation refrigeration coating in a visible light wave band is more than 0.9, and the emissivity of the radiation refrigeration coating in a middle infrared atmosphere transparent window wave band is more than 0.9.
Preferably, the radiation refrigerating coating is inclined to one side to form a height difference, and the thickness of the radiation refrigerating coating is 20 to 150 μm.
Preferably, the ratio of the inorganic particles to the high molecular polymer is not less than 3: 2; and the particle diameter of the inorganic particles is 0.4 to 2 μm.
Preferably, a plurality of the hydrophilic regions are independently arranged, and the hydrophobic regions are intersected.
Preferably, the distance between two adjacent hydrophilic regions is 0.5-1.5 mm.
Preferably, the hydrophilic region has a diameter or side length of 0.5 to 1.0 mm.
Preferably, the hydrophilic regions are circular or oval in shape so that water vapor coalesces into droplets within the hydrophilic regions.
Preferably, a heat absorber is disposed in the evaporation chamber above the liquid surface.
Preferably, a water delivery mechanism and a heat insulation layer are arranged between the heat absorber and the liquid level, wherein the water delivery mechanism is in contact with liquid, the heat absorber is used for evaporating the liquid in the water delivery mechanism, and the heat insulation layer is arranged between the water delivery mechanism and the liquid level and used for cutting off temperature transmission.
Preferably, the water conveying mechanism comprises water absorbing cloth.
Preferably, the insulation layer comprises foam.
Preferably, the inner wall of the condensation chamber is continuously covered with an anti-convection layer, and the periphery of the condensation chamber is provided with a heat insulation layer;
preferably, a water collecting groove is formed in the condensing chamber at the water outlet of the radiation refrigeration coating.
Preferably, the communicating device is provided with an air suction switch.
Preferably, the communication device is continuously covered with a heat insulation layer.
Compared with the prior art, the invention has the advantages that:
1. according to the radiation refrigeration water resource acquisition device provided by the embodiment of the invention, the specific radiation refrigeration coating is arranged in the condensation chamber, so that the surface temperature of the radiation refrigeration coating is far lower than the air temperature, the temperature difference required by condensed water vapor is sufficiently provided, and the condensation efficiency is further improved.
2. According to the radiation refrigeration water resource acquisition device provided by the embodiment of the invention, the surface of the radiation refrigeration coating in the condensation chamber is subjected to specific surface hydrophilic and hydrophobic treatment, so that water condensed on the surface of the radiation refrigeration coating can spontaneously fall off from the surface and is collected, and the condensed water collection efficiency is improved.
3. According to the radiation refrigeration water resource acquisition device provided by the embodiment of the invention, the heat absorber is arranged in the evaporation chamber to heat part of liquid, so that heat diffusion is prevented, and the evaporation efficiency is improved.
Drawings
In order to more clearly illustrate the embodiments of the present application or the technical solutions in the prior art, the drawings needed to be used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments described in the present application, and other drawings can be obtained by those skilled in the art without creative efforts.
FIG. 1 is a schematic diagram of a radiation refrigeration water resource acquisition device according to an exemplary embodiment of the present invention;
FIG. 2 is a schematic diagram of a radiation refrigeration water resource capture device in accordance with an exemplary embodiment of the present invention;
FIG. 3 is an enlarged view of the surface of a radiant refrigerant coating in a radiant refrigerant water resource extraction device as provided in an exemplary embodiment of the present invention;
FIG. 4 is a graph showing the comparison of the surface temperature of the radiant cooling coating and the air temperature in a radiant cooling water resource obtaining apparatus according to an exemplary embodiment of the present invention;
FIG. 5 is a graph of experimental data for reflectivity of a radiant cooling coating in the visible near infrared for a radiant cooling water resource capture device in accordance with an exemplary embodiment of the present invention;
FIG. 6 is a graph of experimental data for emissivity of a radiant refrigeration coating in the mid-IR in a radiant refrigeration water resource acquisition device as provided in an exemplary embodiment of the present invention;
fig. 7 is a three-dimensional bionic diagram of a radiation refrigeration coating in a radiation refrigeration water resource obtaining apparatus according to an exemplary embodiment of the present invention;
fig. 8 is a contact angle test chart of a hydrophilic area of a radiation refrigeration coating in a radiation refrigeration water resource acquisition apparatus according to an exemplary embodiment of the present invention;
FIG. 9 is a side view of a contact angle of a hydrophobic region of a radiation refrigeration coating in a radiation refrigeration water resource acquisition device in accordance with an exemplary embodiment of the present invention;
description of reference numerals:
1. an evaporation chamber; 2. a condensing chamber; 3. a communication device; 301. a heat-insulating layer; 4. a radiation-cooled coating; 401. a hydrophilic region; 402. a hydrophobic region; 5. a liquid; 6. a water delivery mechanism; 7. a thermal insulation layer; 8. a heat absorber; 9. an anti-troposphere; 10. a water collection tank.
Detailed Description
In view of the deficiencies in the prior art, the inventors of the present invention have made extensive studies and extensive practices to provide technical solutions of the present invention. The technical solution, its implementation and principles, etc. will be further explained as follows.
Example (b): referring to fig. 1, a device for obtaining water resource of radiation refrigeration comprises: evaporating chamber 1, condensing chamber 2 and intercommunication device 3, evaporating chamber 1 warp intercommunication device 3 with condensing chamber 2 intercommunication, condensing chamber 2 is inside to be equipped with radiation refrigeration coating 4 in order to accelerate the vapor condensation.
Specifically, the radiation refrigeration coating 4 includes at least one high-reflectivity inorganic particle and at least one high molecular polymer, and the surface of the radiation refrigeration coating 4 includes hydrophilic regions 401 and hydrophobic regions 402, and the hydrophilic regions 401 and the hydrophobic regions 402 are arranged in a staggered manner.
Specifically, the inorganic particles having high reflectance are preferably one or more of zirconium oxide, hafnium oxide, calcium carbonate, aluminum oxide, titanium oxide, barium sulfate, and the like;
specifically, the high molecular polymer is preferably one or more of PTFE, PVDF, PEVE, NMP, and the like;
specifically, the radiation refrigeration coating 4 has a desert beetle bionic structure, the surface of the radiation refrigeration coating is formed by combining hydrophilic areas 401 and hydrophobic areas 402 in a staggered manner, and the hydrophilic areas 401 can condense water vapor into small water drops under the action of passive radiation refrigeration;
specifically, the hydrophobic region 402 collects the small water droplets to the fresh water storage chamber; avoid scraping through the manual work and get the collection comdenstion water, improve condensation efficiency.
Specifically, the heating of the seawater or the soil is completed through the photothermal conversion of sunlight, the condensation is refrigerated through passive radiation, the heat is radiated to the low-temperature universe while the sunlight is reflected, and the temperature of the condensation chamber 2 is reduced to be lower than the dew point temperature; more importantly, the bionic structure design of the radiation refrigeration coating 4 enables the radiation refrigeration coating to have higher condensed water collection efficiency compared with the traditional method.
In the present embodiment, the reflectance of the radiation refrigeration coating 4 in the visible band is greater than 0.9, an
Specifically, the emissivity of the radiation refrigeration coating 4 in the mid-infrared atmosphere transparent window waveband is greater than 0.9.
Specifically, as shown in fig. 5, fig. 5 is a reflectivity of the radiation refrigeration coating 4 in the visible near infrared, which illustrates that the coating has a reflectivity of 0.9 or more in the visible near infrared band, especially in the strong sunlight band of 400-700 nm.
Specifically, as shown in fig. 6, fig. 6 shows the emissivity of the radiation refrigeration coating in the mid-infrared range of 2-20 microns, illustrating that the coating has an average emissivity of above 0.9 in the mid-infrared atmospheric transparent window band.
In this embodiment, the radiation refrigeration coating 4 is inclined to one side to form a height difference, and an included angle between the radiation refrigeration coating 4 and a horizontal plane is 0 to 45 degrees, so that condensed water drops can slide from the radiation refrigeration coating 4, and manual scraping and collection are not needed.
Specifically, the two-dimensional bionic surface treatment with hydrophilic and hydrophobic areas staggered is carried out on the surface of the radiation refrigeration coating in the condensation chamber, so that condensed water on the surface of the radiation refrigeration coating is easy to gather and can spontaneously break away from the surface, and the problem that fresh water at a condensation end in the current evaporation and condensation system is difficult to gather and can be collected only by additionally consuming manpower or electric power is solved.
Specifically, the staggered arrangement mode of the hydrophilic areas and the hydrophobic areas can overcome the problem of overlarge or undersize surface tension, so that the condensation and the falling off of water drops can be realized simultaneously.
Specifically, when the surface of the radiation refrigeration coating in the condensation chamber is subjected to two-dimensional bionic surface treatment with hydrophilic and hydrophobic areas staggered, the included angle between the radiation refrigeration coating and the horizontal plane is 30-45 degrees, so that liquid drops can flow on the surface of the radiation refrigeration coating.
Specifically, when the surface of the radiation refrigeration coating in the condensation chamber is subjected to three-dimensional bionic surface treatment with hydrophilic and hydrophobic areas staggered, the included angle between the radiation refrigeration coating and the horizontal plane is 10-30 degrees, so that liquid drops can flow on the surface of the radiation refrigeration coating. It should be noted that the smaller the tilt angle of the radiation refrigeration coating, the better the refrigeration effect, but the adverse effect on water drop rolling; when the two-dimensional bionic surface is adopted, the required angle is large, so that water drops can roll off easily; after the three-dimensional bionic surface is made, water drops can roll down along a slope body (please refer to fig. 7, a hydrophilic area of the three-dimensional bionic surface of the radiation refrigeration coating is a semicircular slope body), so that the inclination angle of the radiation refrigeration coating is set to be smaller as much as possible.
Specifically, referring to fig. 7, the surface of the radiation refrigeration coating in the condensation chamber is subjected to three-dimensional bionic surface treatment with interlaced hydrophilic and hydrophobic regions, so as to further increase the condensed water collection efficiency of the coating. The method comprises the following steps of (1) obtaining a semi-circular slope-like body higher than a plane on an original coating by using the same type of slurry of a radiation refrigeration coating as a raw material and using methods such as silk-screen printing, 3D printing, mesh spraying and the like; the surface of the slope body is subjected to hydrophilic treatment, the diameter of the plane circle is 0.5mm-1mm, the height of the slope body is the same as the diameter of the circle, and the slope forms an inclination angle for the rolling of the liquid drops, so that the liquid drops are favorably separated from the surface and roll down to a bottom hydrophobic area along the slope. Wherein, the distance between the slope bodies is 0.5mm-1.5mm, which is beneficial to the accumulation of small drops among each other to form large drops as soon as possible and the accelerated rolling; the placing angle of the radiation refrigeration coating and the plane form 10-30 degrees, which is beneficial to the coating to achieve the maximum refrigeration effect.
Specifically, referring to fig. 8, the contact angle less than 10 ° is super-hydrophilic (the contact angle is labeled as 0 °), which illustrates that the hydrophilic region has super-hydrophilicity and has the ability to condense water droplets in the region.
Specifically, referring to fig. 9, the contact angle greater than 120 ° is super-hydrophobic (the contact angle is labeled as 137.6 degrees in the figure), which indicates that the hydrophobic region has super-hydrophobicity and the ability of causing the water droplet to roll spontaneously in the region.
Specifically, the thickness of the radiation refrigeration coating 4 is 20-150 μm.
Specifically, the thickness of the radiation refrigerating coating 4 is preferably 20 to 60 μm. The thickness of the radiation refrigeration coating 4 is 20-150 μm, which is beneficial to avoiding the transmission of sunlight and increasing the reflection; radiation cooling coatings 4 below 20 μm can cause sunlight penetration and radiation cooling coatings 4 above 150 μm can result in excess material.
In this embodiment, the ratio of the inorganic particles to the high molecular polymer is not less than 3: 2; and
the particle size of the inorganic particles is 0.4-2 μm.
Specifically, the particle size of the inorganic particles is preferably 0.4 to 2 μm, which is advantageous for scattering with sunlight and increasing reflection (the improvement of reflection effect is not significant if the particle size is not within this range).
Specifically, when the ratio of inorganic particles to high molecular weight polymer was 3: 2, as shown in FIG. 4, the air averaged 47.49 degrees and the radiation refrigeration coating 4 averaged 42.19 degrees. The radiation refrigeration coating 4 has a cooling effect of about 6 degrees lower than that of air, which indicates that the surface temperature of the radiation refrigeration coating 4 is far lower than that of air, and the temperature difference required by condensed water vapor is sufficiently provided, so that the condensation efficiency is improved.
In this embodiment, the plurality of hydrophilic regions 401 are independently disposed, and the hydrophobic regions 402 are disposed in an intersecting manner.
Specifically, the distance between two adjacent hydrophilic regions 401 is 0.5-1.5 mm; and/or the diameter or side length of the hydrophilic region 401 is 0.5-1.0 mm.
In particular, hydrophilic region 401 has a diameter or side length of 0.5-1.0mm, within which droplet size is formed just enough to break free from the surface against capillary forces. Which facilitates the droplets of hydrophilic area 401 to leave behind by rolling along hydrophobic area 402 after leaving the hydrophilic surface.
In particular, the diameter or side length of the hydrophilic region 401 is 0.5-1.0mm, and the diameter of the hydrophilic region 401 is preferably 0.gmm, so that water drops can be formed conveniently.
Specifically, the distance between two adjacent hydrophilic regions 401 is 0.5-1.5mm, which is beneficial to the accumulation of small liquid drops to form large liquid drops as soon as possible and the accelerated rolling.
In this embodiment, the hydrophilic regions 401 are circular or oval in shape so that water vapor may coalesce into beads in the hydrophilic regions 401.
It should be noted that the hydrophilic region 401 is circular or elliptical to accelerate the formation and rolling of water drops and increase the condensation efficiency.
In this embodiment, a heat absorber 8 is disposed in the evaporation chamber 1 above the surface of the liquid 5.
Specifically, the evaporation of the liquid is accelerated by the heat absorber 8. The evaporation efficiency is improved.
In this embodiment, a water delivery mechanism 6 and a heat insulation layer 7 are disposed between the heat absorber 8 and the liquid surface, wherein the water delivery mechanism 6 is in contact with the liquid 5, the heat absorber 8 is used for evaporating the liquid 5 in the water delivery mechanism 6, and the heat insulation layer 7 is disposed between the water delivery mechanism 6 and the liquid surface and is used for blocking temperature transmission.
For example, the heat insulation layer 7 is arranged above the liquid surface, the water delivery device is arranged on the heat insulation layer 7, the water delivery device 6 is in contact with the liquid, the heat absorber 8 is arranged above the water delivery mechanism 7, and the heat absorber 8 heats partial surface of the water delivery mechanism 7 to evaporate the liquid in the partial surface of the water delivery mechanism 7 to form water vapor; in addition, the heat loss can be isolated, and the evaporation efficiency is improved.
Specifically, the water conveying mechanism 6 comprises water absorbing cloth.
In particular, the insulating layer 7 comprises foam.
In this embodiment, the inner wall of the condensing chamber 2 is continuously covered with the anti-convection layer 9, and the periphery of the condensing chamber 2 is provided with the heat insulation layer.
Specifically, the heat insulation layer is arranged to prevent heat loss and improve evaporation efficiency.
Specifically, a water collecting groove 10 is arranged at a water outlet of the radiation refrigeration coating 4 in the condensation chamber 2.
Specifically, the water collecting tank 10 is arranged at the water outlet of the radiation refrigeration coating 4, so that water condensed on the radiation refrigeration coating 4 slides into the water collecting tank 10 without manual water scraping.
Specifically, in this embodiment, the communication device 3 is provided with an air extraction switch.
Specifically, the communication device 3 is continuously covered with a heat insulation layer 301.
Specifically, some electronic control modules (such modules have low power consumption or can be powered by renewable energy sources such as photovoltaic energy and the like) can be additionally arranged, for example, an automatic valve is additionally arranged between the evaporation chamber 1 and the condensation chamber 2, and a pressure fine adjustment system can be additionally arranged for realizing condensation when the solar energy condensation system is used on the surface of an extraterrestrial celestial body, so that solid-gas-liquid three-phase conversion can be completed under specific conditions.
It should be understood that the above-mentioned embodiments are merely illustrative of the technical concepts and features of the present invention, which are intended to enable those skilled in the art to understand the contents of the present invention and implement the present invention, and therefore, the protection scope of the present invention is not limited thereby. All equivalent changes and modifications made according to the spirit of the present invention should be covered within the protection scope of the present invention.
Claims (10)
1. A radiation refrigeration water resource acquisition device, characterized by comprising: the water vapor condensation device comprises an evaporation chamber, a condensation chamber and a communication device, wherein the evaporation chamber is communicated with the condensation chamber through the communication device, and a radiation refrigeration coating is arranged inside the condensation chamber to accelerate the condensation of water vapor;
the radiation refrigeration coating comprises at least one high-reflectivity inorganic particle and at least one high molecular polymer, the surface of the radiation refrigeration coating comprises hydrophilic areas and hydrophobic areas, and the hydrophilic areas and the hydrophobic areas are arranged in a staggered mode.
2. The radiant cooling water resource recovery device as claimed in claim 1, wherein: the reflectivity of the radiation refrigeration coating in the visible light band is greater than 0.9, an
The emissivity of the radiation refrigeration coating in the mid-infrared atmosphere transparent window wave band is more than 0.9.
3. The radiant cooling water resource recovery device as claimed in claim 2, wherein: the radiation refrigeration coating is inclined to one side to form a height difference, and the thickness of the radiation refrigeration coating is 20-150 mu m.
4. The radiant cooling water resource recovery device as claimed in claim 1, wherein: the ratio of the inorganic particles to the high molecular polymer is not less than 3: 2; and
the particle size of the inorganic particles is 0.4-2 μm.
5. The radiant cooling water resource recovery device as claimed in claim 1, wherein: the plurality of hydrophilic areas are independently arranged, and the hydrophobic areas are intersected;
wherein the distance between two adjacent hydrophilic regions is 0.5-1.5 mm; and/or the diameter or the side length of the hydrophilic region is 0.5-1.0 mm.
6. The radiant cooling water resource recovery device as claimed in claim 5, wherein: the hydrophilic regions are rounded or oval so that water vapor coalesces into droplets in the hydrophilic regions.
7. The radiant cooling water resource recovery device as claimed in claim 1, wherein: and a heat absorber is arranged above the liquid surface in the evaporation chamber.
8. The radiant cooling water resource recovery device as claimed in claim 7 wherein: a water delivery mechanism and a heat insulation layer are arranged between the heat absorber and the liquid level, wherein the water delivery mechanism is in contact with liquid, the heat absorber is used for evaporating the liquid in the water delivery mechanism, and the heat insulation layer is arranged between the water delivery mechanism and the liquid level and is used for cutting off temperature transfer;
and/or the water conveying mechanism comprises water absorbing cloth;
and/or the insulation layer comprises foam.
9. The radiant cooling water resource recovery device as claimed in any one of claims 1 to 7 wherein: the inner wall of the condensing chamber is continuously covered with an anti-convection layer, and the periphery of the condensing chamber is provided with a heat insulation layer;
and/or a water collecting groove is arranged at the water outlet of the radiation refrigeration coating in the condensation chamber.
10. The radiant cooling water resource recovery device as claimed in any one of claims 1 to 7 wherein: an air suction switch is arranged on the communicating device; and/or the communicating device is continuously covered with a heat-insulating layer.
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| CN202111200346.2A CN113896264A (en) | 2021-10-14 | 2021-10-14 | Radiation refrigeration water resource acquisition device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114713476A (en) * | 2022-03-25 | 2022-07-08 | 湖北大学 | Preparation method of double-sided synergistic functional coating for efficient environmental water vapor capture |
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| KR20140064364A (en) * | 2012-11-20 | 2014-05-28 | 한국기계연구원 | Solar seawater distiller feeding with seawater liquid film |
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| CN114713476A (en) * | 2022-03-25 | 2022-07-08 | 湖北大学 | Preparation method of double-sided synergistic functional coating for efficient environmental water vapor capture |
| CN114713476B (en) * | 2022-03-25 | 2022-12-09 | 湖北大学 | Preparation method of double-sided synergistic functional coating for efficient environmental water vapor capture |
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