CN111596575B - Condensation water taking control method for evaporator of all-working-condition air water making machine - Google Patents
Condensation water taking control method for evaporator of all-working-condition air water making machine Download PDFInfo
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- CN111596575B CN111596575B CN202010448541.6A CN202010448541A CN111596575B CN 111596575 B CN111596575 B CN 111596575B CN 202010448541 A CN202010448541 A CN 202010448541A CN 111596575 B CN111596575 B CN 111596575B
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- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05B—CONTROL OR REGULATING SYSTEMS IN GENERAL; FUNCTIONAL ELEMENTS OF SUCH SYSTEMS; MONITORING OR TESTING ARRANGEMENTS FOR SUCH SYSTEMS OR ELEMENTS
- G05B19/00—Programme-control systems
- G05B19/02—Programme-control systems electric
- G05B19/04—Programme control other than numerical control, i.e. in sequence controllers or logic controllers
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- E—FIXED CONSTRUCTIONS
- E03—WATER SUPPLY; SEWERAGE
- E03B—INSTALLATIONS OR METHODS FOR OBTAINING, COLLECTING, OR DISTRIBUTING WATER
- E03B3/00—Methods or installations for obtaining or collecting drinking water or tap water
- E03B3/28—Methods or installations for obtaining or collecting drinking water or tap water from humid air
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N25/00—Investigating or analyzing materials by the use of thermal means
- G01N25/56—Investigating or analyzing materials by the use of thermal means by investigating moisture content
- G01N25/66—Investigating or analyzing materials by the use of thermal means by investigating moisture content by investigating dew-point
Abstract
The invention discloses a condensation water taking control method for an evaporator of an all-condition air water making machine, which is a special control based on a vapor compression refrigeration principle and is used for collecting the ambient dry bulb temperature T by using a controller 1 Ambient dew point temperature T 1 dew And evaporator fin temperature T 2 And the lowest ambient dry bulb temperature T preset by the controller 1min The highest dry bulb temperature T of the environment 1max Environment minimum dew point temperature T 1 dew min Environment maximum dew point temperature T 1 Lumax First downward deviation value delta T of evaporator fin temperature 1 And a second lower deviation value delta T of the temperature of the evaporator fins 2 And comparing, and controlling the evaporator to take water by controlling the evaporation fan. According to the invention, different evaporator fin temperature control targets are obtained by detecting the environmental temperature and humidity in real time, and the evaporator is kept in a condensation state all the time within a specified temperature and humidity range.
Description
Technical Field
The invention relates to the field of control methods of air water generators, in particular to a condensation water taking control method of an evaporator of an all-working-condition air water generator.
Background
With the increasing living standard and health consciousness of people, an air water generator (also called air water taking) becomes a high-end consumer product at present and is emerging in the market continuously. At present, the mainstream air water generator adopts an evaporation compression type refrigeration principle, namely, a compressor, an evaporator, a condenser, a throttling element and the like are connected through pipelines to form a refrigerant circulation loop, the evaporator is provided with an evaporation fan, the condenser is provided with a condensation fan, air flows in from the air inlet side of the evaporator under the action of the evaporation fan, flows out from the air outlet side of the evaporator after passing through the evaporator, and low-temperature and low-pressure liquid refrigerant in the compressor is subjected to gasification phase change in a tube of the evaporator, so that the air on the outer surface of the evaporator is cooled and forms condensed water, and a water source of the air water generator is formed by collecting the condensed water. In the prior art, since an evaporator, a condenser, a compressor, etc. are solidified according to the design of a product system, the adaptability thereof is not excellent enough to face the change of complicated and severe environmental conditions.
For example, the ambient dry bulb temperature range of a common civil air water making machine is 18-43 ℃, and the ambient wet bulb temperature range is 35-95%. Meanwhile, the air water generator is different from an air conditioner in that the air conditioner has an indoor working condition and an outdoor working condition for test evaluation, but the air water generator is tested under the same environmental temperature and humidity condition, for example, some manufacturers determine that the dry bulb temperature is 27 ℃ and the relative humidity is 60% as a rated test working condition. Under the relatively stable working condition, the product design can be better carried out so as to obtain the ideal evaporation temperature and meet the condensation water outlet of the evaporator. However, the surface of the evaporator sometimes does not condense or some places do not condense any more with the change of the environmental temperature and humidity, so that the water outlet effect is poor. When the temperature range of the environment dry bulb is expanded to 5-55 ℃, the temperature range of the environment wet bulb is expanded to 10-95%, and particularly when the humidity is low, the phenomenon that the surface of an evaporator is not condensed is more and more serious, the water yield within the required range cannot be reached, and even high-temperature protection and the like are caused.
The surface temperature of the evaporator fins is a physical phenomenon that condensate water is generated as long as the surface temperature is lower than the dew point temperature of the surrounding air. Of course, if the evaporation temperature is designed to be very low (such as-10 ℃), condensation can be met under all working conditions. However, for vapor compression refrigeration, this design will cause low system energy efficiency, and cannot meet the future requirement for energy saving. In the face of different environmental humiture, under the condition that the evaporator can not change the volume or the heat exchange area, a dynamic evaporator fin temperature control method is needed to enable the evaporator to effectively condense moisture.
Disclosure of Invention
The invention aims to provide a condensation water taking control method for an evaporator of a full-working-condition air water generator, which aims to solve the problem that the surface of the evaporator in the air water generator in the prior art is easy to generate non-condensation.
In order to achieve the purpose, the technical scheme adopted by the invention is as follows:
a condensation water taking control method for an evaporator of a full-working-condition air water generator is characterized in that the evaporator is a finned heat exchanger with a refrigerating function, and the method comprises the following steps: setting temperature sensors in the air inlet direction of the evaporator to measure the environmental dew point temperature T respectively 1 distillate Ambient dry bulb temperature T 1 The surface of the evaporator fin is provided with a temperature sensor for measuring the temperature T of the evaporator fin 2 And a controller is arranged, the controller is respectively connected with the compressor and an evaporation fan configured by the evaporator in a control way, and each temperature sensor is respectively connected with the controller in a signal transmission way, the method comprises the following steps:
(1) presetting the lowest dry bulb temperature T of the environment in the controller 1min The highest dry bulb temperature T of the environment 1max Environment minimum dew point temperature T 1 dew min Environment maximum dew point temperature T 1 Lumax First downward deviation value delta T of evaporator fin temperature 1 And a second lower deviation value delta T of the temperature of the evaporator fins 2 Wherein Δ T 1 ﹤△T 2 ；
(2) The controller respectively collects the environmental dew point temperature T through each temperature sensor 1 distillate Ambient dry bulb temperature T 1 Evaporator fin temperature T 2 ；
(3) The temperature T of the ambient dry bulb in the controller 1 Respectively with the lowest dry bulb temperature T of the environment 1min The highest dry bulb temperature T of the environment 1max Comparing and simultaneously comparing the environmental dew point temperature T 1 dew And the lowest dew point temperature T of the environment 1 dew min Comparing, if the condition T is satisfied 1min ≤T 1 ≤T 1max And T 1 dew ≥T 1 dew min The controller starts the compressor and the evaporation fan to lower the temperature of the evaporator fins, so that the surface condensation of the evaporator fins realizes normal water taking;
(4) and in the water taking process in the step (3), the controller controls the ambient dew point temperature T 1 dew And the maximum dew point temperature T of the environment 1 Lumax Comparing, and adjusting the temperature T of the evaporator fins based on the comparison result 2 The temperature is maintained in a certain range, and the specific process is as follows:
if T 1 distillate ﹤T 1 Lumax Then the controller adjusts the evaporation fan to make the temperature T of the evaporator fins 2 Is maintained in the range of T 1 distillate －△T 2 ≤T 2 ≤T 1 distillate －△T 1 ；
If T 1 dew ≥T 1 Lumax The controller adjusts the evaporation fan to make the temperature T of the evaporator fins 2 Is maintained in the range of T 1 Lumax －△T 2 ≤T 2 ≤T 1 Lumax －△T 1 。
The full-working-condition air water generator evaporator condensation water taking control method is characterized by comprising the following steps of: t is 2 Not more than 0 ℃ and T 2 ﹤T 1 Lumax －△T 2 When the surface of the evaporator fin is frosted and the thickness of the frost layer meets the requirement, the evaporator enters a defrosting and water taking mode, the evaporation fan stops working when defrosting and water taking are carried out, meanwhile, one of modes of reverse defrosting of a compressor, hot gas bypass defrosting or electric heating defrosting is adopted, after defrosting and water taking are completed, the compressor, the evaporation fan and the like are in a state before recovery, namely, an intermittent water taking state is entered.
The condensation water taking control method for the evaporator of the all-working-condition air water generator is characterized by comprising the following steps of: in the step (1), the lowest dry bulb temperature T of the environment 1min Maximum dry bulb temperature T of environment 1max Environment minimum dew point temperature T 1 Lumin And the maximum ambient dew point temperature T 1 Lumax Is determined based on design input, where T 1 dew min At the lowest dry bulb temperature T in the working temperature range 1min Corresponding dew point temperature limit and maximum dry bulb temperature T 1max The lower value of the corresponding dew point temperature limit value is selected; maximum dew point temperature T of environment 1 Lumax Not only according to the highest dew point temperature met by the environment, but also considering the working capacity of the compressor, when the highest evaporation temperature which can be born by the compressor corresponds to the highest temperature T of the evaporator fins 2max ≤T 1 Lumax Time, maximum dew point temperature T of the environment 1 Lumax Press T 2max And (4) taking values.
The full-working-condition air water generator evaporator condensation water taking control method is characterized by comprising the following steps of: in the step (1), the first downward deviation value delta T of the temperature of the evaporator fins 1 And a second lower deviation value delta T of the temperature of the evaporator fins 2 Set up according to the condensation effect and fluctuation range, respectively, and Δ T 1 At 1-3 deg.C and delta T 2 Specific Δ T 1 1 to 3 ℃ in height.
The condensation water taking control method for the evaporator of the all-working-condition air water generator is characterized by comprising the following steps of: the evaporation fan is a fan capable of stepless speed regulation, such as an EC fan, a frequency conversion fan or a pressure and speed regulation fan. The controller in the step (4) performs stepless regulation on the evaporation fan to enable the temperature T of the evaporator fins 2 Maintained at a temperature range.
The full-working-condition air water generator evaporator condensation water taking control method is characterized by comprising the following steps of: the throttling element is an electronic expansion valve or a thermal expansion valve which can be controlled electrically so as to meet the superheat degree adjustment of the evaporator and ensure that the compressor is not subjected to liquid impact.
Compared with the prior art, the invention has the advantages that:
1. according to the invention, different evaporator fin temperature control targets are obtained by detecting the environmental temperature and humidity in real time, the evaporator is kept in a condensation state all the time in a specified temperature and humidity range, and the condensation and water separation effect is good.
2. The invention can divide the enthalpy wet state of air into 2 areas, the non-water taking area and the water taking area are only influenced by the lowest dew point temperature of the product, the working range is widened, and the distinction is clear.
3. The invention can be modified and upgraded on the basis of the original water making machine and has stronger popularization.
4. The invention has mature technology, clear flow and easy realization.
Drawings
Fig. 1 is a control schematic of the controller of the present invention.
Fig. 2 is a block flow diagram of the present invention.
Fig. 3 is a diagram of the enthalpy and humidity of the air during operation of the present invention.
Detailed Description
The invention is further illustrated by the following examples in conjunction with the drawings.
A method for controlling water intake of condensation from evaporator of air water generator under all working conditions is disclosed, as shown in FIG. 1, temperature sensors 1.2 and 1.1 are respectively arranged in air inlet direction of evaporator for correspondingly measuring environmental dew point temperature T 1 distillate Ambient dry bulb temperature T 1 The surface of the evaporator 4 fin is provided with a temperature sensor 1.3 for measuring the temperature T of the evaporator fin 2 And a controller 1 is arranged, the controller 1 is respectively connected with the compressor and an evaporation fan 2 configured by an evaporator 4 in a control way, and the temperature sensors 1.1, 1.2 and 1.3 are respectively connected with the controller in a signal transmission way.
As shown in fig. 2, the method of the present invention comprises the steps of:
(1) presetting the lowest dry bulb temperature T of the environment in the controller 1min Maximum dry bulb temperature T of environment 1max Environment minimum dew point temperature T 1 dew min Environment maximum dew point temperature T 1 Lumax First downward deviation value delta T of evaporator fin temperature 1 And a second lower deviation value delta T of the temperature of the evaporator fins 2 Wherein Δ T 1 ﹤△T 2 ；
In the present invention, the minimum dry bulb temperature T of the environment 1min The highest dry bulb temperature T of the environment 1max Environment minimum dew point temperature T 1 Lumin And ambient maximum dew point temperature T 1 Lumax Is determined based on design input, where T 1 dew min At the lowest dry bulb temperature T in the working temperature range 1min Corresponding dew point temperature limit and maximum dry bulb temperature T 1max The lower value of the corresponding dew point temperature limit value is selected; maximum dew point temperature T of environment 1 Lumax Not only according to the highest dew point temperature which can be met by the environment, but also considering the working capacity of the compressor, when the highest evaporation temperature which can be borne by the compressor corresponds to the highest temperature T of the evaporator fins 2max ≤T 1 Lumax Time, maximum dew point temperature T of the environment 1 Lumax According to T 2max And (4) taking values. E.g. T 2max ＝25℃，T 1 Lumax At 30 ℃, then T 1 Lumax ＝25℃。
In the invention, the first downward deviation value delta T of the temperature of the evaporator fins 1 A second lower deviation value delta T of the temperature of the evaporator fins 2 Set up according to the condensation effect and the fluctuation range, respectively, and Δ T 1 Taking the temperature of 1-3 ℃ and the delta T 2 Specific Δ T 1 1 to 3 ℃ in height.
(2) The controller respectively collects the environmental dew point temperature T through each temperature sensor 1 distillate Ambient dry bulb temperature T 1 Evaporator fin temperature T 2 ；
(3) The temperature T of the ambient dry bulb in the controller 1 Respectively with the lowest dry bulb temperature T of the environment 1min The highest dry bulb temperature T of the environment 1max Comparing and simultaneously comparing the ambient dew point temperature T 1 distillate And the lowest dew point temperature T of the environment 1 Lumin Comparing, if the condition T is satisfied 1min ≤T 1 ≤T 1max And T 1 dew ≥T 1 dew min The controller starts the compressor and the evaporation fan to reduce the temperature of the evaporator fins, so that the surface condensation of the evaporator fins realizes normal water taking;
(4) and in the water taking process in the step (3), the controller controls the ambient dew point temperature T 1 distillate And the maximum dew point temperature T of the environment 1 Lumax Comparing, and adjusting the temperature T of the evaporator fins based on the comparison result 2 The temperature is maintained in a certain range, and the specific process is as follows:
if T 1 distillate ﹤T 1 Lumax Then the controller adjusts the evaporation fan to make the temperature T of the evaporator fins 2 Is maintained in the range of T 1 dew －△T 2 ≤T 2 ≤T 1 distillate －△T 1 ；
If T 1 distillate ≥T 1 Lumax The controller adjusts the evaporation fan to make the temperature T of the evaporator fins 2 Is maintained in the range of T 1 Lumax －△T 2 ≤T 2 ≤T 1 Lumax －△T 1 。
In the invention, the evaporation fan 2 is a fan capable of stepless speed regulation, and the controller 1 steplessly regulates the evaporation fan 2 to ensure that the temperature T of the fins of the evaporator 4 is regulated steplessly 2 Maintained at a temperature range.
As shown in fig. 1, the refrigeration cycle further includes a throttling element 3, and the throttling element 3 is an electronic expansion valve or a thermal expansion valve that can be controlled electrically, so as to meet the superheat degree adjustment of the evaporator and ensure that the compressor does not have liquid slugging. Judging T in the controller 1 2 Not more than 0 ℃ and T 2 ﹤T 1 Lumax －△T 2 When the surface of the evaporator fin frosts and the thickness of a frost layer meets the requirement, the evaporator fin enters a defrosting water taking mode, an evaporation fan stops working when defrosting water taking is carried out, meanwhile, one of modes such as reverse defrosting of a compressor, hot gas bypass defrosting or electric heating defrosting is adopted, after defrosting water taking is completed, the compressor, the evaporation fan and the like recover to the previous state, and an intermittent water taking state is entered.
Specific examples are as follows:
setting an ambient minimum dry bulb temperature T in a controller 1min 5 deg.C, maximum ambient dry bulb temperature T 1max 55 deg.C, ambient minimum dew point temperature T 1 dew min At-7 deg.C, maximum dew point temperature T of environment 1 Lumax ＝25℃，△T 1 ＝2℃，△T 2 ＝3℃。
When the controller collects the temperature T of the environmental dry bulb 1 At 5 deg.C, ambient dew point temperature T 1 distillate At 4 deg.C (86% RH), T 1 distillate ﹤T 1 Lumax Then the controller implements stepless regulation on the evaporator fan to make the temperature T of the evaporator fin 2 Is maintained in the range of T 1 dew －△T 2 ≤T 2 ≤T 1 distillate －△T 1 I.e. T is not less than 1 DEG C 2 ≤2℃。
When the controller collects the temperature T of the environmental dry bulb 1 At 5 deg.C, ambient dew point temperature T 1 dew 0 ℃ (relative humidity 33%), at which time T 1 distillate ﹤T 1 Lumax The controller performs stepless regulation on the evaporation fan to ensure that the temperature T of the evaporator fins 2 Is maintained in the range of T 1 distillate －△T 2 ≤T 2 ≤T 1 distillate －△T 1 T is not less than-3 ℃ 2 Less than or equal to-2 ℃; when frost begins to be generated, the temperature T of the evaporator fins 2 Regulating to below-3 deg.C, and steamingWhen the surface of the generator fin is frosted more and the thickness of a frost layer reaches the requirement, the generator fin enters a defrosting water taking mode, an evaporation fan stops working when defrosting water is taken, meanwhile, one of modes such as reverse defrosting of a compressor, hot gas bypass defrosting or electric heating defrosting is adopted, after defrosting water taking is completed, the compressor, the evaporation fan and the like are restored to the previous state, and an intermittent water taking state is entered.
When the controller collects the temperature T of the environmental dry bulb 1 55 deg.C, ambient dew point temperature T 1 dew At 32 ℃ (30% rh), when T is reached 1 distillate ≥T 1 Lumax And the highest evaporation temperature that the compressor can bear corresponds to the highest temperature T of the evaporator fins 2max When the temperature is 25 ℃, then T 1 Lumax At 25 ℃. The controller carries out stepless regulation on the evaporation fan to ensure that the temperature T of the evaporator fins 2 Is maintained in the range of T 1 Lumax －△T 2 ≤T 2 ≤T 1 Lumax －△T 1 T is more than or equal to 22 ℃ 2 ≤23℃。
As can be seen from the case, the invention has different temperature control of the evaporator fins under different ambient temperature and humidity.
As shown in figure 3, is a schematic view of the location of the present invention on the psychrometric chart. In fig. 3, the water intake area is divided into a non-water intake area and a water intake area, and the lowest dew point temperature of the design of the water generator is taken as a boundary. Wherein the lowest dew point temperature T 1 dew min At the lowest dry bulb temperature T in the working temperature range 1min Corresponding dew point temperature limit and maximum dry bulb temperature T 1max The lower of the corresponding dew point temperature limits. If the minimum working temperature is 5 ℃ and the relative humidity limit value is 38.2% (dew point temperature-7 ℃), the maximum working temperature is 55 ℃ and the relative humidity limit value is 10% (dew point temperature 13.81 ℃), then T 1 dew min -7 ℃ as borderline value. At this time, the relative humidity can theoretically be expanded to 2.1% at an ambient temperature of 55 ℃. As can be seen from the figure, the water taking area is wider than the environmental area (18 ℃ -43 ℃) of the common air water making machine, and the water taking area has no blind area.
The above-described embodiments are only preferred embodiments of the present invention, but the present invention is not limited to the above-described embodiments, and any obvious modifications thereof without departing from the principle of the present invention will be apparent to those skilled in the art and fall within the spirit of the present invention and the scope of the appended claims.
Claims (6)
1. A full-working-condition air water generator evaporator condensation water taking control method is characterized by comprising the following steps: setting temperature sensors in the air inlet direction of the evaporator to measure the environmental dew point temperature T respectively 1 distillate Ambient dry bulb temperature T 1 The surface of the evaporator fin is provided with a temperature sensor for measuring the temperature T of the evaporator fin 2 And a controller is arranged, the controller is respectively connected with the compressor and an evaporation fan configured by the evaporator in a control way, and each temperature sensor is respectively connected with the controller in a signal transmission way, the method comprises the following steps:
(1) presetting the lowest dry bulb temperature T of the environment in the controller 1min Maximum dry bulb temperature T of environment 1max Environment minimum dew point temperature T 1 dew min Environment maximum dew point temperature T 1 Lumax First lower deviation value delta T of temperature of evaporator fin 1 And a second lower deviation value delta T of the temperature of the evaporator fins 2 Wherein Δ T 1 ﹤△T 2 ；
(2) The controller respectively collects the environmental dew point temperature T through each temperature sensor 1 dew Ambient dry bulb temperature T 1 Evaporator fin temperature T 2 ；
(3) The temperature T of the ambient dry bulb in the controller 1 Respectively with the lowest dry bulb temperature T of the environment 1min Maximum dry bulb temperature T of environment 1max Comparing and simultaneously comparing the ambient dew point temperature T 1 distillate And the lowest dew point temperature T of the environment 1 dew min Comparing, if the condition T is satisfied 1min ≤T 1 ≤T 1max And T 1 dew ≥T 1 dew min The controller starts the compressor and the evaporation fan to reduce the temperature of the evaporator fins, so that the surface condensation of the evaporator fins realizes normal water taking;
(4) and in the water taking process in the step (3), the controller controls the ambient dew point temperature T 1 distillate And the maximum dew point temperature T of the environment 1 Lumax Comparing, and adjusting the temperature T of the evaporator fins based on the comparison result 2 The temperature is maintained in a certain range, and the specific process is as follows:
if T 1 distillate ﹤T 1 Lumax The controller adjusts the evaporation fan to make the temperature T of the evaporator fins 2 Is maintained in the range of T 1 distillate －△T 2 ≤T 2 ≤T 1 distillate －△T 1 ；
If T is 1 distillate ≥T 1 Lumax The controller adjusts the evaporation fan to make the temperature T of the evaporator fins 2 Is maintained in the range of T 1 Lumax －△T 2 ≤T 2 ≤T 1 Lumax －△T 1 。
2. The method for controlling water intaking of full-working-condition air water generator evaporator condensation as claimed in claim 1, characterized in that: judging T in controller 2 Not more than 0 ℃ and T 2 ﹤T 1 Lumax －△T 2 When the surface of the evaporator fin frosts and the thickness of the frost layer meets the requirement, the evaporator enters a defrosting and water taking mode, the evaporation fan stops working when defrosting and water taking are carried out, meanwhile, one of the modes of reverse defrosting of the compressor, hot gas bypass defrosting or electric heating defrosting is adopted, and after defrosting and water taking are completed, the compressor and the evaporation fan recover to the previous state, namely, an intermittent water taking state is entered.
3. The method for controlling water intake of condensation of the evaporator of the full-working-condition air water generator according to claim 1, characterized by comprising the following steps: in the step (1), the lowest dry bulb temperature T of the environment 1min The highest dry bulb temperature T of the environment 1max Environment minimum dew point temperature T 1 Lumin And ambient maximum dew point temperature T 1 Lumax Is determined based on design input, where T 1 dew min At the lowest dry bulb temperature T in the working temperature range 1min Corresponding dew point temperature limit and maximum dry bulb temperature T 1max The lower value of the corresponding dew point temperature limit value is selected; maximum ambient dew point temperature T 1 Lumax Not only depending on the maximum dew point temperature that can be encountered by the environment, but also of the compressorWorking capacity, when the highest evaporating temperature that the compressor can bear corresponds to the highest temperature T of the evaporator fins 2max ≤T 1 Lumax Time, maximum dew point temperature T of the environment 1 Lumax Press T 2max And (4) taking values.
4. The method for controlling water intaking of full-working-condition air water generator evaporator condensation as claimed in claim 1, characterized in that: in the step (1), the first downward deviation value delta T of the temperature of the evaporator fins 1 A second lower deviation value delta T of the temperature of the evaporator fins 2 Set up according to the condensation effect and fluctuation range, respectively, and Δ T 1 Taking the temperature of 1-3 ℃ and the delta T 2 Specific Δ T 1 1 to 3 ℃ in height.
5. The method for controlling water intake of condensation of the evaporator of the full-working-condition air water generator according to claim 1, characterized by comprising the following steps: the evaporation fan is a fan capable of carrying out stepless speed regulation, and the controller in the step (4) carries out stepless regulation on the evaporation fan to ensure that the temperature T of the evaporator fins is 2 Maintained at a temperature range.
6. The method for controlling water intaking of full-working-condition air water generator evaporator condensation as claimed in claim 2, characterized in that: the throttling element is an electronic expansion valve or a thermal expansion valve which can be controlled electrically so as to meet the requirement of superheat degree adjustment of the evaporator and ensure that the compressor does not hit liquid.
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| CN110418921A (en) * | 2017-03-21 | 2019-11-05 | 三菱电机株式会社 | Dehumidifier |
| CN108800380A (en) * | 2018-02-13 | 2018-11-13 | 南京嘉涛科技有限公司 | A kind of washing oxidation air purifier from air water-intaking |
| CN109208694A (en) * | 2018-07-20 | 2019-01-15 | 西安交通大学 | It is a kind of using hydrophobe integrated structure from air water processed method and apparatus |
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