CN113959019A - Dehumidification air conditioning system based on resin drier electroosmosis regeneration - Google Patents
Dehumidification air conditioning system based on resin drier electroosmosis regeneration Download PDFInfo
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- CN113959019A CN113959019A CN202111513130.1A CN202111513130A CN113959019A CN 113959019 A CN113959019 A CN 113959019A CN 202111513130 A CN202111513130 A CN 202111513130A CN 113959019 A CN113959019 A CN 113959019A
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- 238000011069 regeneration method Methods 0.000 title claims abstract description 40
- 230000008929 regeneration Effects 0.000 title claims abstract description 38
- 238000007791 dehumidification Methods 0.000 title claims abstract description 30
- 239000011347 resin Substances 0.000 title claims abstract description 29
- 229920005989 resin Polymers 0.000 title claims abstract description 29
- 238000004378 air conditioning Methods 0.000 title claims abstract description 28
- 238000005370 electroosmosis Methods 0.000 title claims abstract description 26
- 239000002274 desiccant Substances 0.000 claims abstract description 50
- 238000005057 refrigeration Methods 0.000 claims abstract description 43
- 230000005855 radiation Effects 0.000 claims abstract description 40
- 238000001816 cooling Methods 0.000 claims abstract description 33
- 238000001704 evaporation Methods 0.000 claims abstract description 10
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- 238000000576 coating method Methods 0.000 claims description 19
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- 239000010439 graphite Substances 0.000 claims description 14
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
- F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
- F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
- F24F3/1411—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F11/00—Control or safety arrangements
- F24F11/62—Control or safety arrangements characterised by the type of control or by internal processing, e.g. using fuzzy logic, adaptive control or estimation of values
- F24F11/63—Electronic processing
- F24F11/65—Electronic processing for selecting an operating mode
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F5/00—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater
- F24F5/0007—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater cooling apparatus specially adapted for use in air-conditioning
- F24F5/0035—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater cooling apparatus specially adapted for use in air-conditioning using evaporation
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F5/00—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater
- F24F5/0046—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater using natural energy, e.g. solar energy, energy from the ground
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F5/00—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater
- F24F5/0089—Systems using radiation from walls or panels
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
- F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
- F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
- F24F2003/1458—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification using regenerators
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F5/00—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater
- F24F5/0046—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater using natural energy, e.g. solar energy, energy from the ground
- F24F2005/0064—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater using natural energy, e.g. solar energy, energy from the ground using solar energy
- F24F2005/0067—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater using natural energy, e.g. solar energy, energy from the ground using solar energy with photovoltaic panels
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Signal Processing (AREA)
- Mathematical Physics (AREA)
- Fuzzy Systems (AREA)
- Physics & Mathematics (AREA)
- Sustainable Energy (AREA)
- Drying Of Gases (AREA)
Abstract
The invention discloses a dehumidification air-conditioning system based on electroosmosis regeneration of a resin desiccant. An air supply system (1) is used for evaporating and cooling the system (3) and a desiccant dehumidification regeneration system (8). The regeneration of the desiccant after moisture absorption is realized through an electroosmosis regeneration method, the system is greatly simplified, the continuous operation can be realized, and the problems of adsorption heat, timeliness and the like generated in the thermal method regeneration process are avoided. Through the combination of direct evaporative cooling and radiation refrigeration, the independent control of temperature and humidity can be realized, the requirement of large indoor heat-humidity ratio change is met, and fresh air is processed more efficiently. For climatic environments such as high temperature and high humidity, high temperature and low humidity and the like, the air inlet position is automatically regulated and controlled through temperature and humidity feedback, so that different refrigeration modes are generated. Energy waste caused by combined control of temperature and humidity in the traditional compression air-conditioning system is avoided, low-grade energy is fully utilized, and thermal comfort is remarkably improved.
Description
Technical Field
The invention relates to a dehumidification air-conditioning system based on electroosmosis regeneration of a resin drying agent, and belongs to the field of heating ventilation air-conditioning.
Background
Along with the improvement of the living standard of people, higher requirements are put forward on the thermal comfort of the indoor environment of the building, and the total energy consumption of the building is more and more large in our country. The compression type refrigeration air-conditioning system widely used at present has strong cooling capacity and is not limited by environmental conditions, but the compression refrigeration equipment has high investment and operating cost and also has the problem of easy frosting in winter.
Evaporative cooling utilizes the characteristic that water evaporation requires latent heat absorption, and the latent heat of evaporation is absorbed from the air by the evaporation of water in the air, thereby lowering the air temperature. The equipment investment and operating cost of the evaporative cooling system are far lower than those of a compressor air conditioning system. From the perspective of comprehensive utilization of energy and environmental protection, evaporative cooling is a very potential air-conditioning cooling mode. However, the evaporative cooling effect is limited by the climate conditions, and a good cooling effect cannot be obtained in the weather with a high relative humidity. In addition, the air temperature is reduced by adopting direct evaporative cooling, and meanwhile, the humidity of the air is increased, so that the problem of high humidity of the environment is brought.
In high humidity areas and high humidity air after direct evaporative cooling, dehumidification is required. At present, the solid dehumidifying desiccant is generally adopted to absorb moisture and recover the moisture absorption capacity of the solid dehumidifying desiccant in a heating mode. However, in order to carry away the moisture in the desiccant, a large amount of latent heat of vaporization needs to be provided to evaporate the moisture, and the required regeneration equipment at least comprises a heating device, a fan for air for regeneration, an air duct and the like, so that the system is complex and difficult to miniaturize. And after the solid dehumidifying agent is heated and regenerated, the waste heat of the solid dehumidifying agent can be dissipated only after a period of cooling, so that the adsorption efficiency is influenced. Thermal regeneration using solar energy also faces the problem of unstable and discontinuous radiant energy.
Disclosure of Invention
In order to solve the technical defects, the technical scheme adopted by the invention is as follows: based on the electroosmosis regeneration principle, radiation refrigeration, direct evaporative cooling and a desiccant dehumidification regeneration system are coupled, and a dehumidification air-conditioning system based on electroosmosis regeneration of a resin desiccant is provided. The air conditioning system can realize independent temperature and humidity control, meet the requirement of large indoor heat-humidity ratio change and process fresh air more efficiently. Through temperature and humidity feedback, the air inlet position is automatically regulated and controlled, so that different refrigeration modes are generated, the air conditioner is suitable for different climatic conditions (high temperature and high humidity, high temperature and low humidity), the energy waste caused by temperature and humidity combined control in the traditional compression air conditioning system is avoided, and the thermal comfort is obviously improved.
The air conditioning system adopts the resin drying agent with high water absorbability as a dehumidifying material, can absorb water which is hundreds of times or even thousands of times higher than the self weight, adopts an electroosmosis regeneration method for regeneration, only needs a stabilized voltage power supply and electrodes for providing an electric field, has no moving parts, is simple and miniaturized in equipment and has high operation reliability. The liquid water is directly separated from the desiccant by electric field force, and the regeneration at normal temperature can be realized, so that a large amount of energy required for heating the regenerated air is saved, and the increase of cold load caused by the temperature rise of the treated air can be avoided. The regeneration process of the dehumidifying drying agent does not need to provide regeneration air, so that the treated air is prevented from contacting with the regeneration air, the cleanness of the treated air is effectively ensured, and the air quality of the treated air is improved. The electric energy required by the electroosmosis effect can adopt low-voltage direct current generated by renewable energy sources such as wind energy, solar energy and the like, and a storage battery can be adopted for supplying power in cloudy days or at night, so that continuous operation is realized.
The air conditioning system utilizes a radiation refrigeration technology to radiate the heat inside the air conditioning system and reflect the radiation energy emitted by other objects at the same time. In the evaporative cooling process, cooling of the feed water is achieved. In the dehumidification and regeneration process of the drying agent, the heat of adsorption released when the drying agent absorbs moisture is reduced. Therefore, the low-grade heat energy is used as the driving energy of the air conditioning system, and the whole air conditioning system has obvious energy-saving potential.
The technical scheme of the invention is realized by the following measures.
When the ambient air monitored by the temperature and humidity sensor 4 (6-2) positioned at the air inlet 4 (6) is in a low-temperature high-humidity state, the system firstly dehumidifies and then directly evaporates and cools the fresh air. The air valve 3 (16-1), the air valve 4 (6-1) and the air valve 1 (15-1) are opened, the air valve 2 (1) and the direct current fan (12) are started, and high-humidity air is sucked into the electric infiltration pipe. Moisture in the air is removed by the self-adsorption characteristic of the resin drying agent (8-13), so that isothermal dehumidification of high-humidity gas is realized. The air dissipates the sensible heat through the radiation refrigeration coating 2 (8-17), and weakens the adsorption heat of the resin drying agent (8-13), thereby achieving the purposes of temperature reduction and dehumidification. Meanwhile, the photovoltaic stabilized voltage power supply is switched on to carry out the regeneration process of the resin drying agent (8-13). The self-cooling of the water in the radiation refrigeration water tank (3-7) is realized through the radiation refrigeration coating 1 (3-8), and the cooling water is atomized through the ultrasonic atomizer (3-4). The dehumidified air is further introduced into an air duct 1 (2) by a direct current fan (12) to be directly contacted with liquid drops for evaporation heat exchange, and after the temperature is further reduced after isenthalpic humidification, the air is introduced into a room from an air inlet 1 (15).
When the ambient air monitored by the temperature and humidity sensors 2 (14-2) positioned at the air inlets 2 (14) is in a high-temperature low-humidity state, the system is directly subjected to evaporative cooling firstly, and then is subjected to dehumidification through the resin drying agents (8-13). The air valve 1 (15-1), the air valve 2 (14-1) and the air valve 3 (16-1) are opened, and the air valve 4 (6-1) is closed. And the direct current fan (12) is started reversely to introduce external high-temperature low-humidity air and indoor air from the air inlet 1 and the air inlet 2. And simultaneously starting the ultrasonic atomizer (3-4), wherein ambient air enters from the ambient air inlet (3-1) and is mixed with atomized liquid drops to form humid air, and the humid air is sucked into the air channel 1 (2) through the humid air inlet (13). The high-temperature low-humidity air is directly contacted with the humid air in the air duct 1 (2), the temperature of the liquid drops rises after the liquid drops absorb sensible heat of the air, the liquid drops return to the air in a gaseous state after evaporation heat exchange, and therefore the humidity of the air in the air duct 1 (2) is increased, and the air is pumped into the electroosmosis tubes (8-9) through the direct current fan (12). Moisture in the air is removed by means of self-adsorption characteristics, isothermal dehumidification of high-humidity gas is achieved, meanwhile, sensible heat of the air is dissipated out through the radiation refrigeration coating 2 (8-17), adsorption heat of the drying agent is weakened, the purposes of cooling and dehumidification are achieved, and finally the air is introduced into a room from the air inlet 4 (6).
Drawings
Fig. 1 is a schematic structural diagram of the present invention, which is used for showing the overall layout of the air conditioning system.
Fig. 2 is a schematic diagram of an evaporative cooling system of the air conditioning system of fig. 1.
Fig. 3 is a schematic cross-sectional view of a radiant cooling water tank in the evaporative cooling system of fig. 2.
Fig. 4 is a schematic structural diagram of a housing of a desiccant dehumidification and regeneration system in the air conditioning system shown in fig. 1.
Fig. 5 is a schematic cross-sectional view of the housing of fig. 4.
Fig. 6 is a schematic diagram of a desiccant dehumidification regeneration system in the air conditioning system of fig. 1.
Fig. 7 is a schematic cross-sectional view of an electroosmotic tube in the desiccant dehumidification regeneration system of fig. 6.
Fig. 8 is a schematic structural diagram of an air supply system in the air conditioning system of fig. 1.
Reference numerals are used.
1-an air supply system, 2-air channels 1, 3-an evaporative cooling system, 4-a roof, 5-a wall, 6-an air inlet 3, 7-an air channel 2, 8-a desiccant dehumidification regeneration system, 9-a photovoltaic power generation system, 12-a direct current fan, 13-a wet air inlet, 14-an air inlet 2, 15-an air inlet 1, 16-an air inlet 4.
3-1 ambient air inlet, 3-2 wet air outlet, 3-3 evaporative cooling water tank, 3-4 ultrasonic atomizer, 3-5 cooling water outlet, 3-6 stainless steel shell, 3-7 polyurethane heat insulation layer, 3-8 radiation cooling water tank, 3-9 radiation cooling coating 1, 3-10 transparent glass cover plate, and 3-11 tap water inlet.
8-1-transparent glass cover plate 2, 8-2-air inlet and outlet 1, 8-3-electroosmosis tube groove, 8-4-polyurethane heat insulation layer 2, 8-5-radiation refrigeration cavity, 8-6-air inlet and outlet 2, 8-7-air inlet, 8-8-condensate water outlet, 8-9-electroosmosis tube, 8-10 water collecting groove, 8-11-graphite anode, 8-12-plastic insulating wall 1, 8-13-resin drying agent, 8-14-graphite cathode, 8-15-metal sieve tube, 8-16-plastic insulating layer 2, 8-17-radiation refrigeration coating 2. 9-1 photovoltaic panel, 9-2 rectifier, 9-3 positive pole line, 9-4 negative pole line, 15-1 air valve 1, 14-1 air valve 2, 16-1 air valve 3, 6-1 air valve 4; 15-2-temperature and humidity sensor 1, 14-2-temperature and humidity sensor 2, 16-2-temperature and humidity sensor 3, 6-2-temperature and humidity sensor 4; 15-3-wind speed sensor 1, 14-3-wind speed sensor 2, 16-3-wind speed sensor 3, 6-3-wind speed sensor 4.
Detailed Description
The present invention will be described in detail below with reference to the accompanying drawings.
A dehumidification air-conditioning system based on electroosmosis regeneration of resin desiccant mainly comprises an evaporative cooling system (3), an air supply system (1) and a desiccant dehumidification regeneration system (8).
The air supply system (1) includes, referring to fig. 1 and 8, an air duct 1 (2), an air inlet 3 (6), an air duct 2 (7), a direct current fan (12), an air inlet 2 (14), an air inlet 1 (15), and an air inlet 4 (16). The evaporative cooling system (3) and the desiccant dehumidification system (8) are connected in series through a pipeline, the direct current fan (12) is arranged between the evaporative cooling system (3) and the desiccant dehumidification regeneration system (8), the air inlet 1 (15) and the air inlet 2 (14) are respectively positioned at two ends of the air duct 1 (2), and the air inlet 3 (6) and the air inlet 4 (16) are opposite to the two ends of the air duct 1 (2) and are positioned at the tail end of the air duct 2 (7). Automatic air valves are arranged at the four air ports, and temperature and humidity sensors and air speed measuring devices for monitoring the air temperature, humidity and air speed at the four air ports are respectively marked as an air valve 1 (15-1), an air valve 2 (14-1), an air valve 3 (16-1) and an air valve 4 (6-1); a temperature and humidity sensor 1 (15-2), a temperature and humidity sensor 2 (14-2), a temperature and humidity sensor 3 (16-2) and a temperature and humidity sensor 4 (6-2); the wind speed sensor comprises a wind speed sensor 1 (15-3), a wind speed sensor 2 (14-3), a wind speed sensor 3 (16-3) and a wind speed sensor 4 (6-3). The temperature and humidity of inlet air are fed back through the temperature and humidity sensor, and the air speed and the air inlet flow are regulated and controlled by regulating and controlling the rotating speed of the direct current fan (12) and the closing degree of each air valve, so that different refrigeration modes are realized, and different climate requirements are met.
The evaporative cooling system (3) comprises an air suction port (3-1), a wet air outlet (3-2), an evaporative cooling water tank (3-3), an ultrasonic atomizer (3-4), a cooling water outlet (3-5), a polyurethane heat-insulating layer (3-6), a radiation refrigeration water tank (3-7), a radiation refrigeration coating (3-8), a stainless steel shell (3-6), a transparent glass cover plate (3-9) and a tap water inlet (3-10). The radiation refrigeration water tank (3-7) is a cubic type made of stainless steel and is positioned in the stainless steel shell (3-6), polyurethane thermal insulation materials (3-6) are filled in gaps among the periphery, the bottom and the shell, a radiation refrigeration coating (3-8) is coated on the upper surface of the radiation refrigeration water tank, the coating emits long-wave heat radiation to the space through an infrared atmospheric window with the wavelength of 8-13 mu m, the spectral reflectivity outside the wave band of 8-13 mu m is 1, and therefore self-cooling of water in the water tank is achieved. The upper surface of the stainless steel shell (3-6) is a transparent glass cover plate (3-10), the upper right part of the radiation refrigeration water tank (3-7) is provided with a tap water inlet (3-10), and a cooling water outlet (3-5) at the lower right part is connected with the evaporation cooling water tank (3-3); the air suction port (3-1) is positioned at the upper part of the evaporative cooling water tank (3-3) and is used for introducing outside air; the ultrasonic atomizer (3-4) is arranged in the evaporative cooling water tank (3-3), and is used for crushing cooling water into micron-sized fog drops, enabling the micron-sized fog drops to enter the air supply pipeline (2) through the wet air outlet (3-2), mixing the micron-sized fog drops with air, then directly performing evaporation heat exchange, and performing equal enthalpy humidification on high-temperature and low-humidity ambient air to reduce the air temperature and achieve the refrigeration purpose.
A desiccant dehumidification regeneration system (8) refers to fig. 4, 6 and 7 and comprises a transparent glass cover plate 2 (8-1), an air inlet and outlet 1 (8-2), an electroosmosis tube groove (8-3), a polyurethane heat insulation layer 2 (8-4), a radiation refrigeration cavity (8-5), an air inlet and outlet 2 (8-6), an air inlet (9-5), a condensate water outlet (8-8), a water accumulation groove (8-10), an electroosmosis tube (8-9), a graphite anode (8-11), a plastic insulation wall (8-12), a resin desiccant (8-13), a graphite cathode (8-14), a metal sieve tube (8-15), a radiation refrigeration coating 2 (8-17), a photovoltaic electric plate (9-1) and a rectifier (9-2), a positive electrode line (9-3) and a negative electrode line (9-4). Two ends of the electroosmosis tube (8-9) are fixed in the electroosmosis tube groove (8-3) and suspended in the radiation refrigeration cavity (8-5). A polyurethane heat-insulating layer 2 (8-4) is filled between the radiation refrigeration cavity (8-5) and the shell, a radiation refrigeration coating 2 (8-17) is coated on the surface of the radiation refrigeration cavity (8-5), the outer wall of the electroosmosis tube (8-9) is composed of a graphite anode (8-11), a plastic insulating wall (8-12) and a graphite cathode ((8-14)), the radiation refrigeration coating 2 (8-17) is coated on the outer wall surface, the coating transmits long-wave heat radiation to the space through an infrared atmospheric window with the wavelength of 8-13 mu m, the spectral reflectivity outside the wave band of 8-13 mu m is 1, and therefore the adsorption heat of the resin drying agent (8-13) is reduced. The metal sieve tube (8-15) is placed in the tube, the resin drying agent (8-13) is filled in a gap between the inner wall surface of the electroosmosis tube (8-9) and the metal sieve tube (8-15), and the direct current fan (12) introduces the humid air into the electroosmosis tube (8-9) from the air inlet and outlet 1 (8-2), penetrates through the wall of the metal sieve tube (8-15), is directly contacted with the resin drying agent (8-13), and is dehumidified by the resin drying agent (8-13). The photovoltaic system (9) provides power supply for the air conditioner, direct current generated by the photovoltaic panel (9-1) is processed by the rectifier (9-2) to form stable voltage to be supplied to the direct current fan (12), the other part of the direct current is applied to the graphite anode (8-11) and the graphite cathode (8-14) through the positive electrode wire (9-3) and the negative electrode wire (9-4), and adsorbed moisture is desorbed under the action of electric field force, so that the moisture absorption and regeneration process of the resin drying agent (8-13) is realized. The two electrodes are separated by plastic insulating walls (8-12) to avoid short circuit.
The above description is only a preferred embodiment of the present invention, and the protection scope of the present invention is not limited to the above embodiments, and all technical solutions belonging to the idea of the present invention belong to the protection scope of the present invention. For those skilled in the art, several modifications and decorations can be made without departing from the inventive concept, and these modifications and decorations should also be regarded as the protection scope of the present patent.
Claims (7)
1. A dehumidification air-conditioning system based on electroosmosis regeneration of resin desiccant mainly comprises an evaporative cooling system (3), an air supply system (1) and a desiccant dehumidification regeneration system (8).
2. The dehumidification air-conditioning system based on electroosmotic regeneration of resin desiccants as claimed in claim 1, wherein the air supply system (1) comprises an air duct 1 (2), an air inlet 3 (6), an air duct 2 (7), a direct current fan (12), an air inlet 2 (14), an air inlet 1 (15), (16) an air inlet 4; the evaporative cooling system (3) and the desiccant dehumidification system (8) are connected in series through a pipeline; the direct current fan (12) is arranged between the evaporative cooling system (3) and the desiccant dehumidification regeneration system (8), the air inlet 1 (15) and the air inlet 2 (14) are respectively positioned at two ends of the air duct 1 (2), and the air inlet 3 (6) and the air inlet 4 (16) are opposite to the two ends of the air duct 1 (2) and are positioned at the tail end of the air duct 2 (7); automatic air valves are arranged at the four air ports, and temperature and humidity sensors and air speed measuring devices for monitoring the air temperature, humidity and air speed at the four air ports are respectively marked as an air valve 1 (15-1), an air valve 2 (14-1), an air valve 3 (16-1) and an air valve 4 (6-1); a temperature and humidity sensor 1 (15-2), a temperature and humidity sensor 2 (14-2), a temperature and humidity sensor 3 (16-2) and a temperature and humidity sensor 4 (6-2); the wind speed sensor comprises a wind speed sensor 1 (15-3), a wind speed sensor 2 (14-3), a wind speed sensor 3 (16-3) and a wind speed sensor 4 (6-3).
3. The dehumidification air-conditioning system based on electroosmotic regeneration of resin drying agents as claimed in claim 1, wherein the evaporative cooling system (3), referring to fig. 2, comprises an air suction port (3-1), a humid air outlet (3-2), an evaporative cooling water tank (3-3), an ultrasonic atomizer (3-4), a cooling water outlet (3-5), a polyurethane thermal insulation layer (3-6), a radiation cooling water tank (3-7), a radiation cooling coating layer (3-8), a stainless steel shell (), a transparent glass cover plate (3-9), and a tap water inlet (3-10); the radiation refrigeration water tank (3-7) is a cubic type made of stainless steel and is positioned in the stainless steel shell (3-6), polyurethane thermal insulation materials (3-6) are filled in gaps among the periphery, the bottom and the shell, a radiation refrigeration coating (3-8) is coated on the upper surface of the radiation refrigeration water tank, the coating emits long-wave thermal radiation to the space through an infrared atmospheric window with the wavelength of 8-13 mu m, the spectral reflectivity outside the wave band of 8-13 mu m is 1, and therefore self-cooling of water in the water tank is achieved; the upper surface of the stainless steel shell (3-6) is a transparent glass cover plate (3-10), the upper right part of the radiation refrigeration water tank (3-7) is provided with a tap water inlet (3-10), and a cooling water outlet (3-5) at the lower right part is connected with the evaporation cooling water tank (3-3); the air suction port (3-1) is positioned at the upper part of the evaporative cooling water tank (3-3) and is used for introducing outside air; the ultrasonic atomizer (3-4) is arranged in the evaporative cooling water tank (3-3), and is used for crushing cooling water into micron-sized fog drops, enabling the micron-sized fog drops to enter the air supply pipeline (2) through the wet air outlet (3-2), mixing the micron-sized fog drops with air, then directly performing evaporation heat exchange, and performing equal enthalpy humidification on high-temperature and low-humidity ambient air to reduce the air temperature and achieve the refrigeration purpose.
4. The dehumidifying air-conditioning system based on electroosmotic regeneration of resin desiccant as claimed in claim 1, wherein the desiccant dehumidifying regeneration system (8) comprises a transparent glass cover plate 2 (8-1), an air inlet and outlet 1 (8-2), an electroosmotic duct tank (8-3), a polyurethane insulation layer 2 (8-4), a radiation refrigeration cavity (8-5), an air inlet and outlet 2 (8-6), an air inlet (9-5), a condensed water outlet (8-8), a water collecting tank (8-10), an electroosmotic duct (8-9), a graphite anode (8-11), a plastic insulation wall (8-12), a resin desiccant (8-13), a graphite cathode (8-14), a metal sieve tube (8-15), and a radiation refrigeration coating 2 (8-17), the photovoltaic panel (9-1), the rectifier (9-2), the positive wire (9-3) and the negative wire (9-4); two ends of the electroosmosis tube (8-9) are fixed in the electroosmosis tube groove (8-3) and suspended in the radiation refrigeration cavity (8-5); a polyurethane heat-insulating layer 2 (8-4) is filled between the radiation refrigeration cavity (8-5) and the shell, and a radiation refrigeration coating 2 (8-17) is coated on the surface of the radiation refrigeration cavity (8-5); the outer wall of the electroosmosis tube (8-9) consists of a graphite anode (8-11), a plastic insulating wall (8-12) and a graphite cathode ((8-14)), and the outer wall surface is coated with a radiation refrigeration coating 2 (8-17), the coating emits long-wave heat radiation to the space through an infrared atmospheric window with the wavelength of 8-13 mu m, the spectral reflectivity outside the wave band of 8-13 mu m is 1, and thus the adsorption heat of the resin desiccant (8-13) is reduced; the metal sieve tube (8-15) is arranged in the tube, and the resin drying agent (8-13) is filled in the gap between the inner wall surface of the electroosmosis tube (8-9) and the metal sieve tube (8-15); the direct current fan (12) introduces the humid air into the infiltration pipe (8-9) from the air inlet and outlet 1 (8-2), and the humid air directly contacts the resin drying agent (8-13) through the wall of the metal sieve pipe (8-15) and is dehumidified by the resin drying agent (8-13); the photovoltaic system (9) provides power supply for an air conditioner, direct current generated by the photovoltaic panel (9-1) forms stable voltage after being processed by the rectifier (9-2) and is supplied to the direct current fan (12), the other part of the direct current is applied to the graphite anode (8-11) and the graphite cathode (8-14) through the positive electrode wire (9-3) and the negative electrode wire (9-4), and adsorbed moisture is desorbed under the action of electric field force, so that the moisture absorption and regeneration process of the resin desiccant (8-13) is realized; the two electrodes are separated by plastic insulating walls (8-12) to avoid short circuit.
5. The dehumidification air-conditioning system based on electroosmosis regeneration of the resin desiccant as claimed in claim 1, which is characterized in that two refrigeration modes are adopted, temperature and humidity changes of inlet air are fed back through a temperature and humidity sensor, and wind speed and air inlet flow are regulated and controlled by regulating and controlling the rotating speed of the direct current fan (12) and the closing degree of each air valve, so that different refrigeration modes under high-temperature and high-humidity and high-temperature and low-humidity climatic conditions are realized, and different climate requirements are met.
6. The system of claim 1, wherein the radiant refrigeration coating has a spectral reflectance of 1 outside the 8-13 μm band and an emissivity of 1 in the 8-13 μm band.
7. The system of claim 1, wherein the transparent cover has a high transmittance in the 8-13 μm band.
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| CA2454180A1 (en) * | 2001-07-19 | 2003-01-30 | Afg Industries, Inc. | Energy-free refrigeration door and method for making the same |
| RU132879U1 (en) * | 2013-04-10 | 2013-09-27 | Виктор Иванович Велюханов | RECOVERABLE REFRIGERATOR HEAT EXCHANGER |
| CN108444014A (en) * | 2018-04-20 | 2018-08-24 | 深圳瑞凌新能源科技有限公司 | A kind of radiation refrigeration water-circulating energy-saving system for building |
| CN109945363A (en) * | 2019-03-21 | 2019-06-28 | 齐鲁工业大学 | A kind of radiation refrigeration system and regulation method with temperature self-adaptation |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2454180A1 (en) * | 2001-07-19 | 2003-01-30 | Afg Industries, Inc. | Energy-free refrigeration door and method for making the same |
| RU132879U1 (en) * | 2013-04-10 | 2013-09-27 | Виктор Иванович Велюханов | RECOVERABLE REFRIGERATOR HEAT EXCHANGER |
| CN108444014A (en) * | 2018-04-20 | 2018-08-24 | 深圳瑞凌新能源科技有限公司 | A kind of radiation refrigeration water-circulating energy-saving system for building |
| CN109945363A (en) * | 2019-03-21 | 2019-06-28 | 齐鲁工业大学 | A kind of radiation refrigeration system and regulation method with temperature self-adaptation |
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