CN206361857U - Heat reclamation type embrane method solution heat pump system - Google Patents

Heat reclamation type embrane method solution heat pump system Download PDF

Info

Publication number
CN206361857U
CN206361857U CN201621074266.1U CN201621074266U CN206361857U CN 206361857 U CN206361857 U CN 206361857U CN 201621074266 U CN201621074266 U CN 201621074266U CN 206361857 U CN206361857 U CN 206361857U
Authority
CN
China
Prior art keywords
heat
solution
exchange
heat exchanger
moisture layer
Prior art date
Application number
CN201621074266.1U
Other languages
Chinese (zh)
Inventor
王晶
薛丹
刘德昌
张立臣
胡灿
Original Assignee
青岛海尔智能技术研发有限公司
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 青岛海尔智能技术研发有限公司 filed Critical 青岛海尔智能技术研发有限公司
Priority to CN201621074266.1U priority Critical patent/CN206361857U/en
Application granted granted Critical
Publication of CN206361857U publication Critical patent/CN206361857U/en

Links

Abstract

The utility model discloses a kind of heat reclamation type embrane method solution heat pump system, including compressor, condenser, throttle part and evaporator, total-heat exchanger is set, condenser and evaporator use the heat exchanger with humidity adjusting function between condenser and evaporator;Heat exchanger includes heat exchange main body and secondary unit; the outside of heat exchange main body is provided with exchange of moisture layer; exchange of moisture layer includes diaphragm and adds based Dehumidification Membranes; diaphragm and plus based Dehumidification Membranes be successively set on heat exchange main body on; diaphragm and add and form solution flow channel between based Dehumidification Membranes, exchange of moisture layer is provided with the solution inlet port connected with solution flow channel and taphole;Secondary unit is provided with the first heat exchanger channels and the second heat exchanger channels of mutual heat exchange, the solution inlet port of first heat exchanger channels connection wherein exchange of moisture layer and the taphole of another exchange of moisture layer, the taphole of the second heat exchanger channels connection wherein exchange of moisture layer and the solution inlet port of another exchange of moisture layer.

Description

Heat reclamation type embrane method solution heat pump system

Technical field

The utility model is related to air-conditioning equipment, more particularly to a kind of heat reclamation type embrane method solution heat pump system.

Background technology

At present, air-conditioning is the household electrical appliance commonly used in people's daily life, and conventional air-conditioning generally includes compressor, condensation Device, throttle part and evaporator, air-conditioning generally have the function of dehumidifying, the main evaporating temperature using evaporator to air dew point Below so that vapor dew and dehumidify.But, in actual use, air-conditioning is generally simply possible to use in dehumidifying, and dry In dry environment, air-conditioning can not realize the function of humidification.In order to solve the above problems, using the air-conditioning with solution dehumidification function Studied exploitation, solution dehumidification is based on dissolving-diffusion mechanism, main that dehumidifying is realized using the concentration of solution and is humidified, instant Vapor when liquid concentration is big in absorption air, conversely, solution concentration hour release vapor is into air.And in the prior art In order to realize the function of solution dehumidification, generally using independent membrane type dehumidifier, membrane type dehumidifier generally includes liquor box and covered The film covered on liquor box(Organic high molecular polymer film, inoranic membrane, liquid film etc. have film of the vapor through function), in reality , it is necessary to which outside low-temperature receiver and thermal source is cooled down and regeneration treatment to solution during the use of border, humidity regulation efficiency is low, and And, extra increased membrane type dehumidifier causes the overall volume of air-conditioning to become big and manufacturing cost increase.How a kind of humidity is designed Adjust efficiency high, small volume and the low air-conditioning of manufacturing cost is technical problem to be solved in the utility model.

Utility model content

The utility model provides a kind of heat reclamation type embrane method solution heat pump system, realizes and improves heat reclamation type embrane method solution The humidity regulation efficiency high of heat pump so that the overall volume of heat pump diminishes and reduces manufacturing cost.

To reach above-mentioned technical purpose, the utility model is realized using following technical scheme:

Heat reclamation type embrane method solution heat pump system, including compressor, condenser, throttle part and the evaporation linked together Device, is provided with total-heat exchanger, the condenser and the evaporator are using tool between the condenser and the evaporator There is the heat exchanger of humidity adjusting function;The heat exchanger with humidity adjusting function includes changing for cooling matchmaker's fluid interchange Hot main body and secondary unit, the outside of the heat exchange main body are provided with exchange of moisture layer, and the exchange of moisture layer includes protecting Cuticula and plus based Dehumidification Membranes, the diaphragm and described plus based Dehumidification Membranes are successively set in the heat exchange main body, the diaphragm and Solution flow channel is formed between described plus based Dehumidification Membranes, the exchange of moisture layer is provided with what is connected with the solution flow channel Solution inlet port and taphole;The secondary unit is provided with the first heat exchanger channels of mutual heat exchange and the second heat exchange is led to Road, first heat exchanger channels connection solution inlet port of exchange of moisture layer and another exchange of moisture layer wherein described in one Taphole, the taphole and another exchange of moisture of the second heat exchanger channels connection exchange of moisture layer wherein described in one The solution inlet port of layer.

Compared with prior art, advantage of the present utility model and good effect are:By setting water in heat exchange body exterior Divide switching layer, heat exchange main body is used for cooling matchmaker's fluid interchange, when refrigerant flows through heat exchange main body, refrigerant can be with exchange of moisture layer In solution carry out heat exchange, the solution in exchange of moisture layer is freezed or heated so as to realize, the main body that exchanges heat is can While carrying out temperature adjusting, the regulation to humidity can also be together realized, refrigerant can be more quickly with exchanging heat outside main body The solution in portion carries out heat exchange, effectively raises the regulation efficiency of humidity, and heat exchanger is integrated with the function of humidification dehumidifying in itself, Importantly, the solution in the solution and outdoor heat exchanger in indoor heat exchanger carries out heat in secondary unit Exchange, realize the regeneration function of solution, so as to realize that air-conditioning need not be using extra independent membrane type dehumidifier so that heat pump Overall volume diminishes and effectively reduces manufacturing cost.In addition, by setting total-heat exchanger, indoor return air and outdoor air intake First carry out after heat exchange, then respectively enterd in evaporator and condenser in total-heat exchanger, make full use of the heat in air Or cold, to meet the requirement of indoor temperature regulation, realize the effect of reduction energy consumption.

Brief description of the drawings

, below will be to embodiment in order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art Or the accompanying drawing used required in description of the prior art is briefly described, it should be apparent that, drawings in the following description are Some embodiments of the present utility model, for those of ordinary skill in the art, are not paying the premise of creative labor Under, other accompanying drawings can also be obtained according to these accompanying drawings.

Fig. 1 is the structure principle chart of the utility model heat reclamation type embrane method solution heat pump system embodiment;

Fig. 2 is the heat exchange with humidity adjusting function in the utility model heat reclamation type embrane method solution heat pump system embodiment The structure principle chart of device;

Fig. 3 is the structural representation of heat exchange main body in the utility model heat reclamation type embrane method solution heat pump system embodiment One;

Fig. 4 is the structural representation of fin in the utility model heat reclamation type embrane method solution heat pump system embodiment;

Fig. 5 is the structural representation of heat exchange main body in the utility model heat reclamation type embrane method solution heat pump system embodiment Two;

Fig. 6 is a-quadrant close-up schematic view in Fig. 5.

Embodiment

It is new below in conjunction with this practicality to make the purpose, technical scheme and advantage of the utility model embodiment clearer Accompanying drawing in type embodiment, the technical scheme in the utility model embodiment is clearly and completely described, it is clear that retouched The embodiment stated is a part of embodiment of the utility model, rather than whole embodiments.Based on the implementation in the utility model Example, the every other embodiment that those of ordinary skill in the art are obtained under the premise of creative work is not made is belonged to The scope of the utility model protection.

As Figure 1-Figure 2, the present embodiment heat reclamation type embrane method solution heat pump system includes the compressor linked together 7th, condenser 102, throttle part 8 and evaporator 101, are provided with total-heat exchanger 6 between condenser 102 and evaporator 101;Position In indoor evaporator 101 return air and be located outside the air intake of side condenser 102 and pass through hot friendship is carried out in total-heat exchanger 6 Change, more effectively to improve operating efficiency, reduce energy consumption and improve Energy Efficiency Ratio.Wherein, condenser 102 and evaporator 101 are adopted With the heat exchanger with humidity adjusting function, the heat exchanger with humidity adjusting function includes changing for cooling matchmaker's fluid interchange The passage 10 of cooling matchmaker flowing is formed in hot main body 1, the heat exchange main body 1 and is provided with refrigerant import and refrigerant exit, it is described The outside for the main body 1 that exchanges heat is provided with exchange of moisture layer 2, and the exchange of moisture layer 2 includes diaphragm 21 and adds based Dehumidification Membranes 22, described Diaphragm 21 and described plus based Dehumidification Membranes 22 are successively set in the heat exchange main body 1, and the diaphragm 21 is attached to the heat exchange master The surface of body 1, forms solution flow channel 20, the exchange of moisture layer 2 between the diaphragm 21 and described plus based Dehumidification Membranes 22 It is provided with the solution inlet port connected with the solution flow channel 20 and taphole;And the moisture in two heat exchange main bodys 1 is handed over Change layer 2 to be connected with each other by secondary unit 3, secondary unit 3 is provided with the first heat exchanger channels 31 of mutual heat exchange With the second heat exchanger channels 32, first heat exchanger channels 31 connect the solution inlet port of the layer of exchange of moisture wherein described in one 2 and another The taphole of the exchange of moisture layer 2, the solution that second heat exchanger channels 32 connect exchange of moisture layer 2 wherein described in one goes out The solution inlet port of mouth and another exchange of moisture layer 2.

Specifically, in the present embodiment heat reclamation type embrane method solution heat pump system condenser 102 and the knot of evaporator 101 Structure uses the heat exchange main body 1 in the heat exchanger with humidity adjusting function, the heat exchanger with humidity adjusting function to be used for cooling Matchmaker's flowing carries out heat exchange, and heat exchange main body 1 will be connected to form refrigerant flow circuits with compressor in actual use, and same When, the outside of heat exchange main body 1, which is additionally provided with exchange of moisture layer 2, exchange of moisture layer 2, forms solution flow channel 20 for for molten Liquid flow, and exchange of moisture layer 2 diaphragm 21 be attached to it is described heat exchange main body 1 outer wall on, diaphragm 21 will completely cut off solution with Exchange heat main body 1 surface contact, with protect heat exchange main body 1 from solution corrosion, and exchange of moisture layer 2 plus based Dehumidification Membranes 22 protect Vapor in card air can free in and out exchange of moisture layer 2, and solution can not be by adding based Dehumidification Membranes 22.Exchange heat the side of main body 1 one Heat exchange of the face for refrigerant, on the other hand heat exchange main body 1 is using in the refrigerant of its internal flow and the exchange of moisture layer 2 of outside Solution carry out heat exchange, with as needed to exchange of moisture layer 2 in solution freeze or heat, to realize regulating environmental humidity Function, also, because refrigerant and solution can be rapidly performed by heat exchange, so as to the effective regulation effect for improving humidity Rate.Heat exchanger is also integrated with solution dehumidification function while refrigerant heat exchange is realized, the heat exchanger of integral structure makes to have leisure Adjust equipment without additionally using independent membrane type dehumidifier, the overall volume of air-conditioning equipment on the one hand can be caused to reduce, it is another Aspect can effectively reduce manufacturing cost.And in actual use, one of heat exchange main body 1 serves as condenser 102, Another heat exchange main body 1 serves as the solution exported in evaporator 101, two heat exchange main bodys 1 in different in moisture switching layer 2 will be in auxiliary Heat exchange is carried out in heat exchanger 3, to better meet the regulation requirement of indoor environment temperature and humidity.Wherein, described first Solution pump 4 and solution expansion drum 5 are connected on heat exchanger channels 31 and second heat exchanger channels 32.

Further, in order to more effectively improve humidity regulation efficiency, exchange of moisture layer 2 is wrapped in the heat exchange main body 1 Outside.Specifically, being wrapped in the outside of heat exchange main body 1 by exchange of moisture layer 2, exchange of moisture can be increased to greatest extent Heat exchange area between layer 2 and heat exchange main body 1, in the presence of refrigerant, can more effectively improve humidity regulation efficiency.It is excellent Choosing, the overlay film of diaphragm 21 formation is assembled in the outer surface of the heat exchange main body 1 in order to the processing of heat exchanger.

Wherein, the performance entity of the heat exchange main body 1 in the present embodiment can use multiple structural forms, for example:Heat exchange master Body 1 can be using structure types such as tubular radiator, gilled radiator or panel radiators, specifically, as shown in figure 3, changing Hot main body 1 is refrigerant pipe, and exchange of moisture layer 2 is wrapped on the outer wall of refrigerant pipe.And in order to improve radiating efficiency, such as Fig. 3-Fig. 4 Shown, heat exchange main body 1 is additionally provided with fin 11 on the basis of using refrigerant pipe, and fin 11 offers multiple tube expansion holes 111, cold Matchmaker's pipe 1 is arranged in the tube expansion hole 111, and the exchange of moisture layer 2 also is located in the tube expansion hole 111, the tube expansion hole 111 Edge be provided with breach 112 for passing through for the solution flow channel 20, specifically, in order to ensure solution can be in water Smoothly flowed in point switching layer 2, breach 112 is additionally provided with the tube expansion hole 111 of fin 11, the formation of breach 112 supplies solution stream The space that dynamic passage 20 is passed through, after the heat exchange tube expansion of main body 1 is arranged in tube expansion hole 111, the solution in exchange of moisture layer 2 is still Can be by the smooth outflow of solution flow channel 20 that is applied in breach 112, it is preferred that swollen in order to increase the flow of solution Pore 111 along the circumferential direction offers multiple breach 112.And in order to improve heat exchange efficiency, the heat exchange main body 1 is overall to be in Serpentine coil structure.Or, as shown in Fig. 5-Fig. 6, heat exchange main body 1, which is used, is formed with refrigerant channel 10 in heat sink, heat sink, It is preferred that, it can form empty between heat sink described in adjacent two panels as needed using the multi-disc heat sink positioned opposite Flow of air region 100.

The present embodiment heat reclamation type embrane method solution heat pump system includes air circulation, refrigerant circulation and solution circulation.

Air circulation:Indoor return air first carries out heat exchange with outdoor air intake in total-heat exchanger, respectively enters evaporator In condenser.Summer condition:Air sends into indoor, the heated row of humidification in condenser in evaporator after cooled dehumidifying Go out outdoor;Winter condition:Air, which is heated in evaporator after humidification, sends into indoor, the cooled dehumidifying discharge room in condenser Outside.

Refrigerant circulation is included:Compressor, condenser, expansion valve, evaporator, the high temperature after refrigerant is compressed by the compressor are high Compression refrigerant enters condenser, within the condenser heat release, then throttles into low-temperature low-pressure refrigerant via throttle part, into evaporation Device is absorbed heat, then flows back to compressor.

Solution circulation is included:Condenser, solution expansion drum, solution pump, secondary unit, evaporator.Concentrated solution is being steamed The vapor in absorption air in device is sent out, to reach effect on moisture extraction, while being cooled down by the refrigerant in evaporator.It is dense after dilution Solution enters solution expansion drum and solution pump, flows into secondary unit and carries out heat exchange temperature with the high temperature weak solution that condenser comes out Degree is slightly raised, and the concentrated solution after dilution, which continues to flow, to be flowed into after condenser, and by the refrigerant heat in condenser, solution is in condensation At a temperature of regenerated, the vapor in solution is discharged into air, to be humidified to air.

During summer condition, the cooled dehumidifying of air of indoor.During winter condition, the air of indoor is heated humidification.

And the operation principle of heat exchanger is as follows:

When the refrigerant in heat exchanger is in cooling condition, air is adding the flows outside of based Dehumidification Membranes 22, due to refrigerant temperature It is relatively low, the solution of liquid flow channel 20 is absorbed heat first, solution also absorbs heat to air, so that air themperature is reduced; Simultaneously as the concentration of solution is higher, moisture absorption can be carried out to air, air eventually cool-down dehumidification.

When the refrigerant in heat exchanger is in heating condition, air is adding the flows outside of based Dehumidification Membranes 22, due to refrigerant temperature Degree is higher, the solution of liquid flow channel 20 is heated first, solution is also heated to air, so that air themperature liter It is high;Simultaneously as the concentration of solution is relatively low, and refrigerant temperature reaches that the vapor in regeneration temperature, solution can be discharged to sky In gas, so as to be humidified to air, air eventually heats up humidification.

Finally it should be noted that:Above example is only to illustrate the technical solution of the utility model, rather than its limitations; Although the utility model is described in detail with reference to the foregoing embodiments, it will be understood by those within the art that: It can still modify to the technical scheme described in foregoing embodiments, or which part technical characteristic is carried out etc. With replacement;And these modifications or replacement, the essence of appropriate technical solution is departed from the utility model embodiment technology The spirit and scope of scheme.

Claims (9)

1. a kind of heat reclamation type embrane method solution heat pump system, including compressor, condenser, throttle part and the steaming linked together Send out device, it is characterised in that total-heat exchanger, the condenser and the steaming are provided between the condenser and the evaporator Device is sent out using the heat exchanger with humidity adjusting function;The heat exchanger with humidity adjusting function includes being used for cooling matchmaker The heat exchange main body and secondary unit of fluid interchange, the outside of the heat exchange main body are provided with exchange of moisture layer, the moisture Switching layer includes diaphragm and adds based Dehumidification Membranes, and the diaphragm and described plus based Dehumidification Membranes are successively set in the heat exchange main body, Solution flow channel is formed between the diaphragm and described plus based Dehumidification Membranes, the exchange of moisture layer is provided with and the solution stream The solution inlet port and taphole of dynamic passage connection;The secondary unit is provided with the first heat exchanger channels of mutual heat exchange With the second heat exchanger channels, first heat exchanger channels connection solution inlet port of exchange of moisture layer and another described wherein described in one The taphole of exchange of moisture layer, second heat exchanger channels connection taphole of exchange of moisture layer and another wherein described in one The solution inlet port of the exchange of moisture layer.
2. heat reclamation type embrane method solution heat pump system according to claim 1, it is characterised in that the exchange of moisture layer bag It is rolled in the outside of the heat exchange main body.
3. heat reclamation type embrane method solution heat pump system according to claim 1, it is characterised in that the diaphragm overlay film shape Into the outer surface in the heat exchange main body.
4. heat reclamation type embrane method solution heat pump system according to claim 1, it is characterised in that first heat exchanger channels Solution pump is connected to on second heat exchanger channels.
5. heat reclamation type embrane method solution heat pump system according to claim 1, it is characterised in that first heat exchanger channels Solution expansion drum is connected to on second heat exchanger channels.
6. heat reclamation type embrane method solution heat pump system according to claim 1, it is characterised in that the heat exchange main body is cold Matchmaker manages.
7. heat reclamation type embrane method solution heat pump system according to claim 6, it is characterised in that also set on the refrigerant pipe Fin is equipped with, the fin is provided with tube expansion hole, and the refrigerant pipe is arranged in the tube expansion hole, exchange of moisture layer also position In the tube expansion hole, the edge in the tube expansion hole is provided with the breach for being passed through for the solution flow channel.
8. heat reclamation type embrane method solution heat pump system according to claim 7, it is characterised in that the tube expansion hole is circumferentially Direction offers multiple breach.
9. heat reclamation type embrane method solution heat pump system according to claim 1, it is characterised in that the heat exchange main body is scattered Refrigerant channel is formed with hot plate, the heat sink.
CN201621074266.1U 2016-09-23 2016-09-23 Heat reclamation type embrane method solution heat pump system CN206361857U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621074266.1U CN206361857U (en) 2016-09-23 2016-09-23 Heat reclamation type embrane method solution heat pump system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621074266.1U CN206361857U (en) 2016-09-23 2016-09-23 Heat reclamation type embrane method solution heat pump system

Publications (1)

Publication Number Publication Date
CN206361857U true CN206361857U (en) 2017-07-28

Family

ID=59368564

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621074266.1U CN206361857U (en) 2016-09-23 2016-09-23 Heat reclamation type embrane method solution heat pump system

Country Status (1)

Country Link
CN (1) CN206361857U (en)

Cited By (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110762701A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762885A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762718A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762707A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762695A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762809A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762724A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762694A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762700A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762882A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762712A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762720A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762698A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762696A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762883A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762877A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762886A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762879A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762697A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762706A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762719A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762699A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762884A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762878A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762760A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762708A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762761A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762709A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762880A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762813A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762881A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762810A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762726A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner

Cited By (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110762701A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762885A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762718A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762707A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762695A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762809A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762724A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762694A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762700A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762882A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762712A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762720A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762698A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762696A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762883A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762877A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762886A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762879A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762697A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762706A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762719A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762699A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762884A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762878A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762760A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762708A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762761A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762709A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762880A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762813A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762881A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762810A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner
CN110762726A (en) * 2018-07-28 2020-02-07 青岛海尔空调器有限总公司 Self-cleaning control method for air conditioner

Similar Documents

Publication Publication Date Title
AU2017204552B2 (en) Energy exchange system for conditioning air in an enclosed structure
US10619895B1 (en) Rooftop liquid desiccant systems and methods
KR102099693B1 (en) Methods and systems for mini-split liquid desiccant air conditioning
KR100504489B1 (en) air conditioner
US7234309B2 (en) Method and apparatus for evaporative cooling of a cooling fluid
CN103062851B (en) Air-conditioning system and dehumanization method thereof
US6945065B2 (en) Cooling/heating system of air conditioner
CN104329759B (en) Temperature control dehumidification system and temperature control dehumidification method for fresh air of radiation air conditioner
CN100451468C (en) Multi-stage solution dehumidifying and regenerating fresh air set driven by heat pump
CN100476308C (en) Humidity controller
AU2006253864B2 (en) System and method for managing water content in a fluid
CN101684960B (en) Split type water-cooling air conditioner fan device and cooling method thereof
CN101846367B (en) Internally-cooled solution dehumidifying fresh air handling unit driven by heat pump
CN101634476B (en) Closed evaporation cooling high-temperature cold water unit
CN107110525A (en) Method and system for differential body liquid drier air adjustment
CN201852342U (en) Wet curtain evaporative cooling air-cooled condensing unit
JP3114447U (en) Total heat recovery cold water unit
CN201104060Y (en) Indirect evaporation type cooling/condensing unit
CN101846365B (en) Solution dehumidifying fresh air unit using indoor exhaust evaporation cooling
KR100904592B1 (en) Humidity controller
CN102297487B (en) Air conditioner and heat tube integrated machine
CN101169299A (en) Indirect evaporation type cooling/condensing device
CN201582927U (en) Coupling counterflow-type solution dehumidification fresh air system of heat pump
CN102425822A (en) Fresh air conditioner
CN101240925B (en) Solar energy absorption type liquid dehumidifying air-conditioning system

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant