All-working-condition adsorption type air water making unit
By using an adsorption-type air-to-water generator unit that operates under all conditions, combined with a heat pump system and a low-temperature regenerative dehumidification impeller, the problems of unstable operation and high energy consumption of traditional air-to-water generator units under all conditions have been solved, achieving stable water production and energy consumption optimization in different environments.
Patent Information
- Application Number
- CN202520059027.1
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2025-01-10
- Publication Date
- 2026-01-02
- Estimated Expiration
- 2035-01-10
AI Technical Summary
Traditional air-to-water generators are unstable under all operating conditions, consume a lot of energy, and are difficult to adapt to different environmental conditions, especially with a significant drop in efficiency under low humidity or extreme climates.
The system employs a full-condition adsorption-type air-to-water generator, which includes a heat pump system, a low-temperature regeneration dehumidification rotor, and a heat recovery system. The low-temperature regeneration dehumidification rotor adsorbs moisture from the air, and the heat pump system and heat recovery system optimize regeneration temperature and energy utilization, thereby reducing energy consumption.
It can stably produce water under different operating conditions, reduce the demand for regeneration heat, improve energy utilization, reduce equipment costs, achieve a compact structure and easy maintenance, and adapt to various environmental conditions.
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Figure CN223753401U_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The utility model relates to a kind of full-condition adsorption type air water generator unit, belong to air technical field. BACKGROUND
[0002] In water making equipment, air water generator unit can realize the water in air from wet air extraction, realize the function of water from air.In traditional air water generator, it mainly relies on cooling dehumidification technology, its basic principle is to cool the cold air to dew point, so that water vapor condenses into liquid water, but traditional air water generator unit has the following defects: 1.it is provided with evaporator in the inside of traditional air water generator unit, evaporator is easy to freeze at low temperature, affect the water making effect and stability of equipment;2.when the humidity of air is low, it is difficult to obtain sufficient water from air by cooling dehumidification alone, and the water making efficiency is greatly reduced;3.the traditional system needs higher energy consumption to maintain the operation of equipment during operation, to ensure that the equipment is at lower temperature or increase the regeneration heat, and the operation cost is higher.4.The traditional air water generator performs well in single condition, for example, in high humidity, high temperature environment;In low humidity or extreme climate conditions, the efficiency is significantly reduced.The traditional system lacks the ability to flexibly respond to different air conditions, and it is difficult to meet the water making demand in full condition.
[0003] Traditional air water generator unit cannot meet the requirements of full-condition use environment, and the device has the problem of high energy consumption during operation.Therefore, an air water generator unit capable of air water making in full-condition environment and low energy consumption is needed. UTILITY MODEL CONTENT
[0004] The technical problem to be solved by the utility model lies in: provide a kind of full-condition adsorption type air water generator unit, it solves the problem that traditional air water generator unit cannot realize full-condition operation;Traditional air water generator unit has the problem of high energy consumption during use.
[0005] The technical problem to be solved by the utility model is realized by the following technical scheme: a kind of full-condition adsorption type air water generator unit, comprising
[0006] Box, heat pump system, low-temperature regenerative dehumidification runner, heat recovery system;
[0007] The heat pump system, low-temperature regenerative dehumidification runner and heat recovery system are arranged inside or on the surface of the box,
[0008] The heat pump system includes compressor, evaporator, pre-condenser, post-condenser and cooling fan;The heat pump system has two groups, which are distributed in the box, separated by a partition in the middle, and the low-temperature regenerative dehumidification runner is arranged in the middle of the partition;
[0009] The low-temperature regenerative dehumidification runner comprises a regeneration side and an adsorption side, the adsorption side can absorb moisture in air, and the regeneration side can desorb moisture absorbed by the adsorption side;
[0010] The heat recovery system comprises a heat recovery evaporator, a heat recovery condenser and a heat recovery heat dissipation fan.
[0011] The air treatment area is formed by the heat pump system, the low-temperature regenerative dehumidification runner and the partition plate in the box body, and the air treatment area comprises a runner regeneration air inlet channel, a runner regeneration air outlet and treatment air inlet combined channel and a runner treatment air outlet channel.
[0012] The runner regeneration air inlet channel is connected with the runner regeneration air outlet and treatment air inlet combined channel, and the runner treatment air outlet channel is connected with the other end of the runner regeneration air outlet and treatment air inlet combined channel.
[0013] Preferably, the runner regeneration air inlet channel is provided with an air filter, two pre-condensers and a compressor in the air flow direction.
[0014] Preferably, the runner regeneration air outlet and treatment air inlet combined channel is provided with the heat recovery evaporator, two evaporators and the compressor in the air flow direction.
[0015] Preferably, the runner treatment air outlet channel is provided with the air supply fan and the compressor.
[0016] Preferably, the surface of the box body is provided with the heat recovery condenser, the heat recovery heat dissipation fan, the rear condenser and the heat dissipation fan.
[0017] Preferably, the step of producing water by air comprises the following steps.
[0018] Step 1: the air supply fan drives air flow into the box body; the air flow in the box body passes through the air filter, is then heated by two pre-condensers, enters the regeneration side of the low-temperature regenerative dehumidification runner; the air flow then passes through the heat recovery evaporator and two evaporators in sequence, condenses and separates out liquid water from moisture in the air; the air flow flows to the adsorption side of the low-temperature regenerative dehumidification runner, adsorbs moisture onto the low-temperature regenerative dehumidification runner, further reduces the moisture content of the air flow, and the air flow rises in temperature at the same time; the air flow is discharged into the environment by the air supply fan.
[0019] Preferably, the heat pump system is connected by a pipeline, and the heat pump system is provided with refrigerant inside.
[0020] Preferably, the heat recovery system is provided with a pipeline inside, and the heat recovery system is provided with refrigerant inside.
[0021] The present application has the following advantages:
[0022] (1) Through the utility model, the heat pump system, the low-temperature regenerative dehumidification runner and the heat recovery system are arranged in the box body, the water in the air is adsorbed to the regeneration side of the low-temperature regenerative dehumidification runner by the heat pump system and the low-temperature regenerative dehumidification runner, the water content in the air is increased to the range that the heat pump system can condense, and water can be stably prepared under the low-humidity working condition of the system. The air water preparation unit can be stably used under the environment of high temperature and high humidity to low temperature and low humidity, can adapt to the air conditions of different regions and seasons, and can realize the ability of stable water preparation in each time period.
[0023] (2) Through the utility model, the regeneration temperature of the air water preparation unit is reduced to 60-70 DEG C by the low-temperature regenerative dehumidification runner, the working environment of the traditional regenerative dehumidification runner needs 120-130 DEG C, and the low-temperature regenerative dehumidification runner can greatly reduce the requirement of regenerative heat. In the air water preparation unit, the heat of regeneration is derived from the condensation waste heat of the heat pump system, electric heating or steam heating is avoided, and the energy utilization rate is improved.
[0024] (3) Through the utility model, the heat pump system, the low-temperature regenerative dehumidification runner and the heat recovery system are arranged in the box body, the heat pump system, the low-temperature regenerative dehumidification runner are arranged in the box body, the air flow is limited in the box body by the baffle, the low-temperature regenerative dehumidification runner and the heat pump system, the various units are integrated in the box body, and the heat source equipment or complex pipeline does not need to be additionally increased. The compact structure of the device is guaranteed. It is convenient to maintain. The use cost is reduced. The front condenser and the rear condenser are arranged in the heat pump system, the various condensers are matched under different air inlet conditions, the regeneration heat can be accurately controlled, the stability and reliability of the refrigeration system can be guaranteed, and water preparation under all working conditions is realized. BRIEF DESCRIPTION OF DRAWINGS
[0025] Figure 1 It is the front view internal structure schematic view of the utility model.
[0026] Figure 2 It is the plan view of the utility model.
[0027] Figure 3 It is the right side view of the utility model.
[0028] Figure 4 It is the left side view of the utility model.
[0029] Figure 5 It is the device flow schematic view of the utility model.
[0030] In the diagram: 1-box, 11-air inlet louvers, 21-compressor, 22-evaporator, 23-pre-condenser, 24-post-condenser, 25-cooling fan, 26-expansion valve, 3-low temperature regeneration dehumidification impeller, 41-heat recovery evaporator, 42-heat recovery condenser, 43-heat recovery cooling fan, 5-air filter, 6-partition plate, 7-air outlet louvers, 8-blower, 9-water inlet. Detailed Implementation
[0031] In order to make the technical means, creative features, objectives and effects of this utility model easier to understand, the present utility model will be further described below in conjunction with specific embodiments.
[0032] Example 1
[0033] like Figures 1-5 As shown, a full-condition adsorption-type air-to-water generator unit includes a housing 1, inside which a heat pump system, a low-temperature regeneration dehumidification impeller 3, and a heat recovery system are installed. The heat pump system, the low-temperature regeneration dehumidification impeller 3, and the heat recovery system are all located inside the housing 1 or on the surface of the housing 1.
[0034] The heat pump system includes a compressor 21, an evaporator 22, a pre-condenser 23, a post-condenser 24, a cooling fan 25, and an expansion valve 26. In this embodiment, there are two sets of heat pump systems, which are distributed vertically inside the housing 1 and separated by a partition 6. A low-temperature regeneration dehumidification impeller 3 is provided in the middle of the partition 6. The low-temperature regeneration dehumidification impeller covers the inside of the housing 1, and air can flow through the low-temperature regeneration dehumidification impeller 3.
[0035] The low-temperature regeneration dehumidification rotor 3 includes a regeneration side and an adsorption side. The adsorption side can absorb moisture from the air, and the regeneration side can desorb the moisture absorbed by the adsorption side.
[0036] The heat recovery system includes a heat recovery evaporator 41, a heat recovery condenser 42, and a heat recovery cooling fan 43.
[0037] Inside the housing 1, there is a partition 6. The partition 6, together with the heat pump system and the low-temperature regeneration dehumidification rotor 3, forms an air handling area. The air handling area includes a rotor regeneration air inlet channel, a rotor regeneration air outlet and a combined air handling inlet channel, and a rotor handling air outlet channel.
[0038] Reference Figure 1The heat pump system arranged inside the cabinet 1 is separated by the partition plate 6, the air from the air inlet on the top side of the partition plate 1 enters the cabinet 1, the air entering the cabinet first passes through the rotary wheel regeneration air inlet channel, the air filter 5 and the two front condensers 23 are arranged in the rotary wheel regeneration air inlet channel along the direction of the air flow; then the air flow enters the rotary wheel regeneration air outlet and the processing air inlet combined channel after passing through the low-temperature regeneration dehumidification rotary wheel 3, the heat recovery evaporator 41 and the two evaporators 22 are arranged in the rotary wheel regeneration air outlet and the processing air inlet combined channel along the direction of the air flow; the air flow is discharged from the rotary wheel regeneration air outlet and the processing air inlet combined channel and enters the rotary wheel processing air outlet channel, and the air fan 8, the compressor 21 and the auxiliary refrigeration equipment thereof are arranged in the rotary wheel processing air outlet channel. The heat recovery system condenser 42, the heat recovery heat dissipation fan 43, the rear condenser 24 and the heat dissipation fan 25 are arranged on the top of the cabinet 1, in this embodiment, the rear condenser 24 is arranged on the top of the cabinet 1 near the air filter 5, and the heat dissipation fan 25 is arranged on the top of the rear condenser 24; the heat recovery condenser 42 is arranged at one end of the cabinet 1 away from the air filter 5, and the heat recovery heat dissipation fan 43 is arranged on the top of the heat recovery condenser 42.
[0039] In this embodiment, the low-temperature regeneration dehumidification rotary wheel 3 is arranged in the middle part of the cabinet 1, the middle part of the low-temperature regeneration dehumidification rotary wheel 3 in the horizontal direction is provided with the partition plate 6, the air is guided into the cabinet 1 from the air filter 5 on the top of the partition plate 6 through the partition plate 6 in the cabinet 1, the air is guided through the partition plate, and the air extends downward in sequence through the two front condensers 23, the upper half of the low-temperature regeneration dehumidification rotary wheel 3, the heat recovery evaporator 41 and the evaporator 22, and then is discharged from the air outlet louver 7 under the guidance of the air fan 8.
[0040] In this embodiment, the upper half of the low-temperature regeneration dehumidification rotary wheel 3 is the regeneration side, and the lower half is the adsorption side, the low-temperature regeneration dehumidification rotary wheel 3 can absorb the moisture in the air on the adsorption side, and the low-temperature regeneration dehumidification rotary wheel 3 can desorb the moisture absorbed on the adsorption side on the regeneration side.
[0041] The air enters the cabinet from the side of the cabinet 1, is filtered by the air filter 5, and then is subjected to water production by various devices, and then is discharged from the air outlet louver 7 under the guidance of the air fan 8, wherein the air fan 8 is arranged inside the cabinet 1, the air outlet louver 7 is arranged on the front of the cabinet 1, the water production air is discharged from the air outlet louver 7 on the front of the cabinet 1, and there is a certain space on the side of the cabinet 1, and the compressor 21 is arranged at the space.
[0042] In the embodiment, the direction of air flow in the inside of the cabinet 1 is from right to left above the partition 6, then from left to right below the partition 6 after passing the partition 6. The specific structure is as follows:
[0043] The two front condensers 23 in the inside of the cabinet 1 are arranged in close contact, and are fixed on the upper side of the partition 6 in the inside of the cabinet 1. Then, the low-temperature regenerative dehumidification runner 3 is arranged, and the low-temperature regenerative dehumidification runner 3 passes through the partition 6 and covers the inside of the cabinet 1. The heat recovery system evaporator 41 and the evaporator 21 are arranged above the left side of the partition 1. The heat recovery system evaporator 41 is arranged in close contact with the evaporator 21. The air first passes through the heat recovery system evaporator 41 and then flows through the evaporator 21. Then, the air flows downward and passes through the partition 6.
[0044] In the lower half of the inside of the cabinet 1, the evaporator 22 is arranged at the leftmost side. Then, the air supply fan 8 is arranged after passing through the low-temperature regenerative dehumidification runner. The air outlet louver 7 is arranged on the top of the air supply fan 8, and the air outlet louver 7 is arranged on the surface of the front side of the cabinet 1.
[0045] In the embodiment, the heat dissipation cabinet is arranged on the side of the cabinet 1 away from the air filter 5. Referring to the view of Figure 4 , Figure 4 , the view is a side view of the heat dissipation cabinet. In the embodiment, another compressor 21 is arranged on the outside of the heat dissipation cabinet. The compressor 21 is connected with the heat pump system in the inside of the cabinet 1.
[0046] Referring to the view of Figure 3 , Figure 3 , the view is a right side view of the unit. The air enters the inside of the cabinet 1 from the right side of the unit. In the embodiment, the air inlet louver 11 is arranged on the surface of the cabinet 1. The air enters the cabinet 1 from the air inlet louver 11 to produce water.
[0047] Referring to the view of Figure 2 , Figure 2 , the view is a top view of the unit. The left side is the heat dissipation cabinet. The rear condenser 24 and the heat dissipation fan 25 are arranged on the top of the heat dissipation cabinet.
[0048] Referring to the view of Figure 5 , the specific process of water production of the unit in the embodiment is as follows:
[0049] Step 1: The air enters the cabinet 1 under the drive of the air supply fan 8. When entering the cabinet 1, the air flows through the air inlet louver 11.
[0050] Step 2: The air flow passes through the air filter 5 in the inside of the cabinet 1. The air filter 5 filters the air to prevent dust in the air from polluting the water quality. The air after passing through the air filter 5 flows into the regeneration side of the low-temperature regenerative dehumidification runner 3 after passing through the two front condensers 23.
[0051] Step 3: The air flow then flows through the heat recovery evaporator 41 and two evaporators 22 in sequence, and the moisture in the air is condensed to form liquid water.
[0052] Step 4: The air flow then enters the adsorption side of the low-temperature regenerative dehumidification wheel 3, and the moisture is adsorbed onto the low-temperature regenerative dehumidification wheel 3, further reducing the humidity content of the air flow, and the temperature of the air flow rises.
[0053] Step 5: The air flow is discharged from the surface of the cabinet 1 through the air supply fan 8 to the environment.
[0054] After the above steps, the liquid water produced from the air can be taken out from the water outlet 9 at the bottom of the unit.
[0055] The heat pump system can produce water during the process, and the surface of the evaporator 22 is below the freezing point of water vapor, which will cause the surface of the evaporator 22 to freeze, so it is usually difficult to achieve the dehumidification and water production function requirements of a dew point temperature below 10℃ (water vapor freezing temperature 0℃ + reasonable heat transfer temperature difference) or a humidity content less than 7.0g / kg. That is, when the inlet air humidity is low or the moisture is small, the compressor 22 alone cannot produce water from the air.
[0056] In this embodiment, cooling and dehumidification combined with low-temperature regenerative dehumidification technology is used, and the moisture that is difficult to separate in the heat pump system is adsorbed on the adsorption side of the low-temperature regenerative dehumidification wheel 3. With the continuous rotation of the low-temperature regenerative dehumidification wheel 3, the moisture can be transferred to the regeneration side of the low-temperature regenerative dehumidification wheel 3, and under the action of the regeneration air, the moisture is desorbed into the inlet air of the evaporator of the heat pump system, increasing the humidity content of the inlet air of the evaporator 22 of the heat pump system, so that the moisture can be prepared into water by the cooling and dehumidification of the heat pump system. In this embodiment, the cooling and dehumidification technology and the low-temperature regenerative dehumidification technology are combined, which can break through the ice point limitation of cooling and dehumidification, and water can be produced even when the inlet air humidity is low.
[0057] In order to ensure the regeneration desorption effect, the traditional dehumidification wheel needs to use electric heating or steam heating to provide a high-temperature regeneration temperature of 120-130℃ for the dehumidification wheel, which requires high energy consumption. In this embodiment, a low-temperature regenerative dehumidification wheel 3 is used, which only needs a medium-temperature regeneration temperature of 60-70℃, which is low in energy consumption, and can utilize the condensation waste heat generated during the operation of the heat pump system to achieve the purpose of energy saving and emission reduction.
[0058] In this embodiment, the components in the heat pump system are connected through pipelines, and a refrigerant is arranged in the pipeline, wherein:
[0059] The two front condensers 23 and the two rear condensers 24 are in series in the pipeline, the heat generated by the front condenser 23 in the heat pump system is used for the regeneration desorption of the low-temperature regeneration dehumidification runner 3, and the remaining condensing heat is discharged to the environment through the rear condenser 24. The two front condensers 23 arranged in the box 1 are attached.
[0060] In the embodiment, under the premise of ensuring the safe and stable operation of the heat pump system, in order to obtain the maximum water production, the heat pump system needs to output the maximum refrigeration capacity, and at the same time, in order to ensure the desorption effect and service life of the low-temperature regeneration dehumidification runner 3, only the temperature of the low-temperature regeneration dehumidification runner 3 needs to be raised to 60-70℃, and the temperature generated by condensation exceeds the working temperature of the low-temperature regeneration dehumidification runner 3, therefore, the excess condensing heat needs to be discharged to the atmosphere through the heat dissipation fan 25 to ensure the stability of the heat pump system, and the cooperation of each condenser can realize accurate control of the regeneration heat while ensuring the stability and reliability of the refrigeration system under different air inlet conditions. Realize water production in all working conditions.
[0061] In the embodiment, the compressor 21, the front condenser 23, the rear condenser 24, the expansion valve 26 and the evaporator 22 of the heat pump system are connected in sequence through the pipeline, and are internally provided with refrigerant. Here, the commonly used refrigerant on the market is adopted, which can ensure the safety and stability of the heat pump system while achieving a high regeneration temperature. In the embodiment, the refrigerant in the heat pump system adopts R410A or R134A medium-high temperature refrigerant.
[0062] In the embodiment, the outlet air temperature of the regeneration side of the low-temperature regeneration dehumidification runner 3 is relatively high, and there is a temperature difference with the fresh air temperature, especially when the fresh air temperature is low, the temperature difference is large. The above scheme is provided with a heat recovery system and utilizes a natural cold source to reduce the dry bulb temperature of the inlet air of the evaporator 22, so that the sensible heat handled by the heat pump system is smaller, and the cold quantity is more converted into latent heat, which is beneficial to water production.
[0063] In the embodiment, the heat recovery evaporator 41 is arranged at the front end of the evaporator 22 in the air flow direction, the heat recovery condenser 42 is arranged at the top of the unit, and the heat recovery condenser 42 is provided with a heat recovery heat dissipation fan 43 at the top; the heat recovery evaporator 41 and the heat recovery condenser 42 are connected through the pipeline. A phase-changeable refrigerant is arranged in the heat recovery system, and the refrigerant can circulate in the pipeline under the action of self-force gravity or pump driving.
[0064] Specifically, the air on the regeneration side of the low-temperature regeneration dehumidification runner 3 passes through the heat recovery evaporator 41, the internal liquid refrigerant of the heat recovery evaporator 41 can absorb the heat in the air and evaporate into a gaseous state, at this time, the inlet air temperature of the evaporator 22 can be reduced. At this time, the gaseous refrigerant enters the heat recovery condenser 42 through the pipeline, and under the driving of the heat recovery cooling fan 43, the heat in the refrigerant is released to the environment through heat exchange with the fresh air. In this process, the state of the refrigerant changes from gaseous to liquid. The liquid refrigerant flows back to the heat recovery system evaporator 41 under the action of gravity, and circulates in this way.
[0065] By setting the heat recovery system in the box body 1, the inlet air temperature of the evaporator 22 is reduced by using the natural cold source and the phase change principle of the refrigerant, under the premise of the same heat pump system input power, the cold quantity of the heat pump system can be more converted into latent heat, further improving the energy efficiency of the heat pump system and improving the water production capacity. The heat recovery system, in terms of structural arrangement, the heat recovery condenser 42 is arranged on the heat recovery evaporator 41 to form a certain height difference, which can further improve the heat recovery efficiency and energy saving effect.
[0066] The basic principle, main features and advantages of the present application are shown and described above. Those skilled in the art should understand that the present application is not limited by the above-mentioned embodiments, and various changes and improvements can be made without departing from the spirit and scope of the present application. These changes and improvements all fall within the scope of the present application. The scope of protection of the present application is defined by the appended claims and their equivalents.
Claims
1. A full-condition adsorption air water generator unit, comprising a box, a heat pump system, a low-temperature regenerative dehumidification runner, a heat recovery system; the heat pump system, the low-temperature regenerative dehumidification runner, and the heat recovery system are arranged inside or on the surface of the box, characterized in that: the heat pump system comprises a compressor, an evaporator, a pre-condenser, a post-condenser, and a heat dissipation fan; the heat pump system has two groups, which are distributed above and below in the box and separated by a partition plate, and the low-temperature regenerative dehumidification runner is arranged in the middle of the partition plate; the low-temperature regenerative dehumidification runner comprises a regeneration side and an adsorption side, the adsorption side can absorb moisture in the air, and the regeneration side can desorb the moisture absorbed by the adsorption side; the heat recovery system comprises a heat recovery evaporator, a heat recovery condenser, and a heat recovery heat dissipation fan; the inside of the box forms an air treatment area through the heat pump system, the low-temperature regenerative dehumidification runner, and the partition plate, and the air treatment area comprises a runner regeneration air inlet channel, a runner regeneration air outlet and treatment air inlet combined channel, and a runner treatment air outlet channel; the runner regeneration air inlet channel is connected with the runner regeneration air outlet and treatment air inlet combined channel, and the other end of the runner regeneration air outlet and treatment air inlet combined channel is connected with the runner treatment air outlet channel.
2. A full duty adsorption air water machine according to claim 1, characterized in that: The runner regeneration air inlet channel is provided with an air filter and two pre-condensers along the airflow direction.
3. A full duty adsorption air water generator as claimed in claim 1, wherein: The runner regeneration air outlet and treatment air inlet combined channel is provided with a heat recovery evaporator and two evaporators along the airflow direction.
4. A full duty adsorption air water machine according to claim 3, characterized in that: The bottom of the last evaporator through which the airflow flows is provided with a water outlet, and the water in the air is collected through the water outlet.
5. A full duty adsorption air water generator as set forth in claim 1, wherein: The runner treatment air outlet channel is provided with a blower and a compressor.
6. A full duty adsorption air water generator as set forth in claim 1, wherein: The surface of the box is provided with a heat recovery condenser, a heat recovery heat dissipation fan, a post-condenser, and a heat dissipation fan.
7. A full duty adsorption air water chiller as claimed in any one of claims 1 to 6, wherein: The blower drives the airflow into the box; the airflow in the box passes through the air filter, is then heated by the two pre-condensers, enters the regeneration side of the low-temperature regenerative dehumidification runner; the airflow then passes through the heat recovery evaporator and the two evaporators in sequence, condenses the moisture in the air into liquid water; the airflow flows to the adsorption side of the low-temperature regenerative dehumidification runner, adsorbs the moisture onto the low-temperature regenerative dehumidification runner, further reduces the moisture content of the airflow, and at the same time, the temperature of the airflow rises; the airflow is discharged into the environment by the blower.
8. A full duty adsorption air water generator as set forth in claim 1, characterized by: The heat pump system is connected by pipelines, and the heat pump system is provided with refrigerant inside.
9. The all-condition adsorption air water generating unit according to claim 1, characterized in that: The heat recovery system is connected by pipelines inside, and the heat recovery system is provided with refrigerant inside.