CN203177376U - Novel solar liquid dehumidification air conditioning system - Google Patents

Novel solar liquid dehumidification air conditioning system Download PDF

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Publication number
CN203177376U
CN203177376U CN 201320153662 CN201320153662U CN203177376U CN 203177376 U CN203177376 U CN 203177376U CN 201320153662 CN201320153662 CN 201320153662 CN 201320153662 U CN201320153662 U CN 201320153662U CN 203177376 U CN203177376 U CN 203177376U
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China
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magnetic valve
solution
regenerating unit
fountain
heat exchanger
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Withdrawn - After Issue
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CN 201320153662
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Chinese (zh)
Inventor
徐惠斌
宋新南
葛凤华
胡自成
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Jiangsu University
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Jiangsu University
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Abstract

The utility model relates to a novel liquid dehumidification air conditioning system, in particular to a solar liquid dehumidification air conditioning system. The system comprises a solar power generation device (1), a storage battery (2), an electrical heater (3), a boiling-type regenerating device (4), a concentrated solution storage tank (5), a dilute solution storage tank (6), a dehumidifier (7), a dilute solution heating tank (8), a solar heat collection device (9), a spray-type regenerating device (10), a first electromagnetic valve (11), a second electromagnetic valve (12), a third electromagnetic valve (13), a fourth electromagnetic valve (14), a first solution pump (15), a second solution pump (16), a third solution pump (17), an energy-saving heat exchanger (18) and a concentrated solution cooling heat exchanger (19). The solar liquid dehumidification air conditioning system is characterized by also comprising a boiling-type regenerating device branch. Compared with a conventional solar solution dehumidification air conditioner, the solar liquid dehumidification air conditioning system has the following beneficial effects that only solar energy is used for a regenerating driving energy source of dehumidizer, and the regenerating driving energy source is environmentally friendly.

Description

A kind of new type solar energy liquid dehumidifying air-conditioning system
Technical field
The utility model is a kind of liquid dehumidifying air-conditioning system, relates in particular to a kind of novel solution dehumidifying air-conditioning system that utilizes Driven by Solar Energy.
Background technology
Liquid desiccant air conditioning utilizes dehumidizer strong wettability power when high concentration, directly absorbs processed airborne steam, reaches the purpose of dehumidifying.Solution dehumidifying air-conditioning system has can utilize that low-temperature heat source drives, salting liquid is to having the bactericidal purifying effect in the air, can forming a series of advantages such as humiture independence control air conditioner system, environmental friendliness, has a extensive future.
The effective regeneration of dehumidizer is the basis that dehumidification air conditioner can be kept operate as normal.Tradition solution regeneration combustion gas, fuel oil etc. heat concentrated, machine set system complexity not only, and expend a large amount of energy.Along with the rise of green building, utilize the air-conditioning system utilization of Driven by Solar Energy to receive publicity.Patent CN101900437B has provided a kind of solution dehumidification that the solar thermal collector heat dilute solution sends into regenerator and load system of productive life hot water simultaneously of utilizing.By the fountain heat-mass exchange equipment, will transfer in the regeneration air through water more than needed in the weak solution after the solar energy heating, this is the general idea and method in present air conditioner industry scientific research, the design.Patent CN1506629A has just provided a kind of solar energy dehumidification solution regenerating unit based on above thinking.
Yet it is bigger that this renovation process is influenced by the regeneration air state, and the weak solution of process ordinary solar heat collector heating is generally at 60-80 ℃, and when regeneration air humidity was big, the mass transfer driving force that spray is regenerated diminished, and dehumidification air conditioner can't normally move.When overcast and rainy, except humidity load is bigger, this contradiction is more outstanding.
Therefore, still lack at present a kind of can be under the high humility unfavorable conditions, the environmental type liquid desiccant air conditioning of efficient stable work.
The utility model content
The purpose of this utility model is: when regenerating in order to overcome the tower spray of existing solar powered fluid dehumidifier/air-conditioning system dehumidizer, be subjected to the regeneration air state to influence bigger drawback, provide a kind of under high humidity, new type solar energy that still can efficient stable work drives solution dehumidifying air-conditioning system.
The technical solution of the utility model is as follows:
A kind of new type solar energy liquid dehumidifying air-conditioning system, described system comprises device of solar generating (1), battery (2), electric heater (3), boiling type regenerating unit (4), concentrated solution holding vessel (5), weak solution holding vessel (6), dehumidifier (7), weak solution heating tank (8), solar energy heat collector (9), fountain regenerating unit (10), first magnetic valve (11), second magnetic valve (12), the 3rd magnetic valve (13), the 4th magnetic valve (14), first solution pump (15), second solution pump (16), the 3rd solution pump (17), energy-saving heat exchanger (18) and concentrated solution cooling heat exchanger (19);
Described first magnetic valve (11), the 3rd solution pump (17), fountain regenerating unit (10) and the 4th magnetic valve (14) link to each other successively, form fountain regenerating unit branch road;
It is characterized in that:
Described system also comprises a boiling type regenerating unit branch road, described boiling type regenerating unit branch road is in parallel with fountain regenerating unit branch road, comprise: second magnetic valve (12), energy-saving heat exchanger (18), boiling type regenerative device of solution (4), the 3rd magnetic valve (13), device of solar generating 1, battery (2), electric heater (3);
Described second magnetic valve (12), energy-saving heat exchanger (18) low-temperature coil, boiling type regenerative device of solution (4), energy-saving heat exchanger (18) high temperature coil pipe, the 3rd magnetic valve (13) link to each other successively; Through series circuit device of solar generating (1) is linked to each other with electric heater (3), battery (2) is connected in parallel with device of solar generating (1); Electric heater (3) is connected with boiling type regenerating unit (4), and the solution in electric heater (3) the ebuillition of heated formula regenerating unit (4) is to fluidized state, and the rapid transpiring moisture of solution is to concentrate regeneration.
Further, boiling type regenerating unit (4) the periphery parcel that uses thermal insulation material.
Implementation method according to above-mentioned air-conditioning system is characterized in that: described first magnetic valve (11), and second magnetic valve (12), the 3rd magnetic valve (13), the 4th magnetic valve (14) control two cover regenerating unit collaborative works, concrete mode of operation is as follows:
First kind of mode of operation: when regeneration air humidity reduced levels, weak solution can be finished regeneration by fountain regenerating unit (10), fountain regenerating unit (10) branch road was opened, and boiling type regenerating unit (4) branch road is closed; Open first magnetic valve (11), the 4th magnetic valve (14); Close second magnetic valve (12), the 3rd magnetic valve (13); Flow of solution in the weak solution heating tank (8) is through first magnetic valve (11), pump into fountain regenerating unit (10) through the 3rd solution pump (17), finish regeneration, become magnetic valve the 4th magnetic valve (14) of flowing through after the concentrated solution, enter concentrated solution holding vessel (5) and use for dehumidifier (7);
Second kind of mode of operation: when regeneration air humidity higher level, weak solution by fountain regenerating unit (10) change in concentration hour, fountain regenerating unit (10) branch road is closed, boiling type regenerating unit (4) branch road is opened; At this moment, open second magnetic valve (12), the 3rd magnetic valve (13); Close first magnetic valve (11), the 4th magnetic valve (14); Flow of solution in the weak solution heating tank (8) is through second magnetic valve (12), energy-saving heat exchanger (18) low-temperature coil, enter boiling type regenerating unit (4), finish explosive evaporation regeneration, become flow through after the concentrated solution energy-saving heat exchanger (18) high temperature coil pipe, the 3rd magnetic valve (13), enter concentrated solution holding vessel (5) and use for dehumidifier (7);
The third mode of operation: when regeneration air humidity is in medium level, weak solution has certain variation by fountain regenerating unit (10) concentration, but concentration still can not satisfy the operation of air conditioner requirement, then fountain regenerating unit (10) branch road, boiling type regenerating unit (4) branch road are all opened, control liquid inventory ratio on two branch roads, adjusting obtains suitable concentrated solution, enters concentrated solution holding vessel (5) and uses for dehumidifier (7); At this moment, open first magnetic valve (11), second magnetic valve (12), the 3rd magnetic valve (13), the 4th magnetic valve (14) is according to the actual concentrated effect except humidity load and fountain regenerating unit (10) of air-conditioning, control first magnetic valve (11), second magnetic valve (12) aperture is regulated the liquid inventory of two branch roads, the 3rd magnetic valve (13), the 4th magnetic valve (14) standard-sized sheet; Solution part in the weak solution heating tank (8) first magnetic valve (11) of flowing through, pump into fountain regenerating unit (10) through the 3rd solution pump (17), finish spray regeneration, become the 4th magnetic valve (14) of flowing through after the concentrated solution, enter concentrated solution holding vessel (5) and use for dehumidifier (7); Solution another part in the weak solution heating tank (8) flow through second magnetic valve (12), energy-saving heat exchanger (18) low-temperature coil, enter boiling type regenerating unit (4), finish explosive evaporation regeneration, become energy-saving heat exchanger (18) the high temperature coil pipe of flowing through after the concentrated solution, the 3rd magnetic valve (13) enters concentrated solution holding vessel (5) and uses for dehumidifier (7);
Flow of solution in the described concentrated solution holding vessel (5) is through concentrated solution heat exchanger (19) the high temperature coil pipe of lowering the temperature, concentrated solution cooling heat exchanger (19) low-temperature coil connects extraneous low-temperature receiver, concentrated solution wettability power after the cooling is improved, pump into the dehumidifying of dehumidifier (7) spray by first solution pump (15), finish circulation.
Further, in described the third mode of operation, control liquid inventory ratio on two branch roads, preferentially move fountain regenerating unit (10), auxiliary operation boiling type regenerating unit (4) is done adjusting, adapts to load variations.
The beneficial effects of the utility model are:
(1) compare with conventional solar energy liquid desiccant air conditioning, the regenerative drives energy of its dehumidizer remains and only uses solar energy, environmental protection;
(2) the new type solar energy liquid dehumidifying air conditioner has fountain regenerating unit branch road and boiling type regenerating unit branch road in parallel, two branch roads can be under the control of magnetic valve coordinate operation, solution regeneration can not be subjected to the influence of regeneration air state, and especially dehumidification air conditioner still can stability and high efficiency work under the operating mode bigger except humidity load such as overcast and rainy grade.
Description of drawings
Fig. 1 is overall structure schematic diagram of the present utility model.
Wherein, each symbology meaning is as follows: device of solar generating (1), battery (2), electric heater (3), boiling type regenerating unit (4), concentrated solution holding vessel (5), weak solution holding vessel (6), dehumidifier (7), weak solution heating tank (8), solar energy heat collector (9), fountain regenerating unit (10), first magnetic valve (11), second magnetic valve (12), the 3rd magnetic valve (3), the 4th magnetic valve (14), first solution pump (15), second solution pump (16), the 3rd solution pump (17), energy-saving heat exchanger (18) and concentrated solution cooling heat exchanger (19).
The specific embodiment
Below in conjunction with accompanying drawing, the technical solution of the utility model is further elaborated.
As shown in Figure 1, the new type solar energy solution dehumidifying air-conditioning system comprises device of solar generating 1, battery 2, electric heater 3, boiling type regenerating unit 4, concentrated solution holding vessel 5, weak solution holding vessel 6, dehumidifier 7, weak solution heating tank 8, solar energy heat collector 9, fountain regenerating unit 10, the first magnetic valves 11, the second magnetic valves 12, the 3rd magnetic valve 3, the four magnetic valves 14, the first solution pumps 15, second solution pump, 16, the three solution pumps 17, energy-saving heat exchanger 18 and concentrated solution cooling heat exchanger 19.
Described system also comprises a boiling type regenerating unit branch road, described boiling type regenerating unit branch road is in parallel with fountain regenerating unit branch road, comprise: second magnetic valve 12, energy-saving heat exchanger 18, boiling type regenerative device of solution 4, the 3rd magnetic valve 13, device of solar generating 1, battery 2, electric heater 3;
Described second magnetic valve 12, energy-saving heat exchanger 18 low-temperature coils, boiling type regenerative device of solution 4, energy-saving heat exchanger 18 high temperature coil pipes, the 3rd magnetic valve 13 link to each other successively; Through series circuit device of solar generating 1 is linked to each other with electric heater 3, battery 2 is connected in parallel with device of solar generating 1; Electric heater 3 is connected with boiling type regenerating unit 4, and the solution in the electric heater 3 ebuillition of heated formula regenerating units 4 is to fluidized state, and the rapid transpiring moisture of solution is to concentrate regeneration.
Described first magnetic valve 11, the 3rd solution pump 17, fountain regenerating unit 10 and the 4th magnetic valve 14 link to each other successively, form fountain regenerating unit branch road.
The improvements of native system are: system also comprises a boiling type regenerating unit branch road, boiling type regenerating unit branch road is in parallel with fountain regenerating unit branch road, this branch road comprises: second magnetic valve 12, energy-saving heat exchanger 18, boiling type regenerative device of solution 4, the 3rd magnetic valve 13, device of solar generating 1, battery 2, electric heater 3; Second magnetic valve 12, energy-saving heat exchanger 18 low-temperature coils, boiling type regenerative device of solution 4, energy-saving heat exchanger 18 high temperature coil pipes, the 3rd magnetic valve 13 link to each other successively; Through series circuit device of solar generating 1 is linked to each other with electric heater 3, battery 2 is connected in parallel with device of solar generating 1; Electric heater 3 is connected with boiling type regenerating unit 4, and the solution in the electric heater 3 ebuillition of heated formula regenerating units 4 is to fluidized state, and the rapid transpiring moisture of solution is to concentrate regeneration.
Solar energy heat collector 9 is connected with weak solution heating tank 8, and the heat that solar energy heat collector is obtained can pass to the solution in the weak solution heating tank.Device of solar generating 1 with the power storage that produces in battery 2, when 4 operations of boiling type regenerating unit, battery 2 is electric heater 3 power supplies, and electric heater 3 is heated to boiling temperature with weak solution, and (early-stage Study shows: dehumidizer LiBr, LiCl commonly used, CaCl 2The solution boiling temperature all between 110 ℃~150 ℃, reaches easily) after, strong evaporation takes place in the water in the weak solution, and solution is concentrated, and finishes regeneration.Battery 2 plays the effect of accumulation of energy simultaneously, can charge when sunshine enriches, and discharges energy storage during the cloudy day, makes system stable operation.Weak solution heating tank 8, the boiling type regenerating unit 4 peripheries parcel that uses thermal insulation material reduces heat and scatters and disappears.
Flow process is as follows during dehumidification system work:
Absorb the inflow of the weak solution behind steam weak solution holding vessel 6 in the humid air through dehumidifier 7, weak solution pumps into weak solution heating tank 8 through second solution pump 16, absorption is from the heat of solar energy heat collector 9, be heated to uniform temperature above (as 〉=60 ℃), selectively unlocking first magnetic valve 11, second magnetic valve 12 flows out weak solution heating tank 8.The keying of first magnetic valve, 11, the second magnetic valves 12 has following three kinds of mode of operations.
First kind of mode of operation: when regeneration air humidity reduced levels, weak solution can be finished regeneration by fountain regenerating unit 10, fountain regenerating unit 10 branch roads were opened, and boiling type regenerating unit 4 branch roads are closed; Open first magnetic valve, 11, the four magnetic valves 14; Close second magnetic valve, 12, the three magnetic valves 13; Flow of solution in the weak solution heating tank 8 is finished regeneration through first magnetic valve 11, pump into fountain regenerating unit 10 through the 3rd solution pump 17, becomes magnetic valve the 4th magnetic valve 14 of flowing through after the concentrated solution, enters concentrated solution holding vessel 5 and uses for dehumidifier 7;
Second kind of mode of operation: when regeneration air humidity higher level, weak solution by fountain regenerating unit 10 change in concentration hour, fountain regenerating unit 10 branch roads are closed, boiling type regenerating unit 4 branch roads are opened; At this moment, open second magnetic valve, 12, the three magnetic valves 13; Close first magnetic valve, 11, the four magnetic valves 14; Flow of solution in the weak solution heating tank 8 is through second magnetic valve 12, energy-saving heat exchanger 18 low-temperature coils, enter boiling type regenerating unit 4, finish explosive evaporation regeneration, become flow through after the concentrated solution energy-saving heat exchanger 18 high temperature coil pipes, the 3rd magnetic valve 13, enter concentrated solution holding vessel 5 and use for dehumidifier 7;
The third mode of operation: when regeneration air humidity is in medium level, weak solution has certain variation by fountain regenerating unit 10 concentration, but concentration still can not satisfy the operation of air conditioner requirement, then fountain regenerating unit 10 branch roads, boiling type regenerating unit 4 branch roads are all opened, control liquid inventory ratio on two branch roads, adjusting obtains suitable concentrated solution, enters concentrated solution holding vessel 5 and uses for dehumidifier 7; At this moment, open first magnetic valve 11, second magnetic valve 12, the 3rd magnetic valve 13, the four magnetic valves 14 are according to the actual concentrated effect except humidity load and fountain regenerating unit 10 of air-conditioning, control first magnetic valve 11, second magnetic valve, 12 apertures are regulated the liquid inventory of two branch roads, the 3rd magnetic valve 13, the four magnetic valves 14 standard-sized sheets; Solution parts in the weak solution heating tank 8 first magnetic valve 11 of flowing through pumps into fountain regenerating unit 10 through the 3rd solution pump 17, finishes spray regeneration, becomes the 4th magnetic valve 14 of flowing through after the concentrated solution, enters concentrated solution holding vessel 5 and uses for dehumidifier 7; Solution another part in the weak solution heating tank 8 flow through second magnetic valve 12, energy-saving heat exchanger 18 low-temperature coils, enter boiling type regenerating unit 4, finish explosive evaporation regeneration, become the energy-saving heat exchanger 18 high temperature coil pipes of flowing through after the concentrated solution, the 3rd magnetic valve 13 enters concentrated solution holding vessel 5 and uses for dehumidifier 7;
Flow of solution in the described concentrated solution holding vessel 5 is through concentrated solution cooling heat exchanger 19 high temperature coil pipes, concentrated solution cooling heat exchanger 19 low-temperature coils connect extraneous low-temperature receiver, concentrated solution wettability power after the cooling is improved, and pumps into dehumidifier 7 spray dehumidifying by first solution pump 15, finishes circulation.
The above-mentioned specific embodiment of the present utility model is just to the illustrating of the utility model patented technology scheme, and do not constitute the restriction to the utility model protection domain.The improvement of any technical scheme that produces according to the utility model spirit of the utility model, conversion, omission, substitute etc., all belong to protection domain of the present utility model.

Claims (4)

1. new type solar energy liquid dehumidifying air-conditioning system, described system comprises device of solar generating (1), battery (2), electric heater (3), boiling type regenerating unit (4), concentrated solution holding vessel (5), weak solution holding vessel (6), dehumidifier (7), weak solution heating tank (8), solar energy heat collector (9), fountain regenerating unit (10), first magnetic valve (11), second magnetic valve (12), the 3rd magnetic valve (13), the 4th magnetic valve (14), first solution pump (15), second solution pump (16), the 3rd solution pump (17), energy-saving heat exchanger (18) and concentrated solution cooling heat exchanger (19);
Described first magnetic valve (11), the 3rd solution pump (17), fountain regenerating unit (10) and the 4th magnetic valve (14) link to each other successively, form fountain regenerating unit branch road;
It is characterized in that:
Described system also comprises a boiling type regenerating unit branch road, described boiling type regenerating unit branch road is in parallel with fountain regenerating unit branch road, comprise: second magnetic valve (12), energy-saving heat exchanger (18), boiling type regenerative device of solution (4), the 3rd magnetic valve (13), device of solar generating (1), battery (2), electric heater (3);
Described second magnetic valve (12), energy-saving heat exchanger (18) low-temperature coil, boiling type regenerative device of solution (4), energy-saving heat exchanger (18) high temperature coil pipe, the 3rd magnetic valve (13) link to each other successively; Through series circuit device of solar generating (1) is linked to each other with electric heater (3), battery (2) is connected in parallel with device of solar generating (1); Electric heater (3) is connected with boiling type regenerating unit (4), and the solution in electric heater (3) the ebuillition of heated formula regenerating unit (4) is to fluidized state, and the rapid transpiring moisture of solution is to concentrate regeneration.
2. system according to claim 1 is characterized in that: described boiling type regenerating unit (4) the periphery parcel that uses thermal insulation material.
3. according to the described air-conditioning system of claim 1, it is characterized in that: described first magnetic valve (11), second magnetic valve (12), the 3rd magnetic valve (13), the 4th magnetic valve (14) control two cover regenerating unit collaborative works, concrete mode of operation is as follows:
First kind of mode of operation: when regeneration air humidity reduced levels, weak solution can be finished regeneration by fountain regenerating unit (10), fountain regenerating unit (10) branch road was opened, and boiling type regenerating unit branch road is closed; Open first magnetic valve (11), the 4th magnetic valve (14); Close second magnetic valve (12), the 3rd magnetic valve (13); Flow of solution in the weak solution heating tank (8) is through first magnetic valve (11), pump into fountain regenerating unit (10) through the 3rd solution pump (17), finish regeneration, become magnetic valve the 4th magnetic valve (14) of flowing through after the concentrated solution, enter concentrated solution holding vessel (5) and use for dehumidifier (7);
Second kind of mode of operation: when regeneration air humidity higher level, weak solution by fountain regenerating unit (10) change in concentration hour, fountain regenerating unit (10) branch road is closed, boiling type regenerating unit (4) branch road is opened; At this moment, open second magnetic valve (12), the 3rd magnetic valve (13); Close first magnetic valve (11), the 4th magnetic valve (14); Flow of solution in the weak solution heating tank (8) is through second magnetic valve (12), energy-saving heat exchanger (18) low-temperature coil, enter boiling type regenerating unit (4), finish explosive evaporation regeneration, become flow through after the concentrated solution energy-saving heat exchanger (18) high temperature coil pipe, the 3rd magnetic valve (13), enter concentrated solution holding vessel (5) and use for dehumidifier (7);
The third mode of operation: when regeneration air humidity is in medium level, weak solution has certain variation by fountain regenerating unit (10) concentration, but concentration still can not satisfy the operation of air conditioner requirement, then fountain regenerating unit (10) branch road, boiling type regenerating unit (4) branch road are all opened, control liquid inventory ratio on two branch roads, adjusting obtains suitable concentrated solution, enters concentrated solution holding vessel (5) and uses for dehumidifier (7); At this moment, open first magnetic valve (11), second magnetic valve (12), the 3rd magnetic valve (13), the 4th magnetic valve (14) is according to the actual concentrated effect except humidity load and fountain regenerating unit (10) of air-conditioning, control first magnetic valve (11), second magnetic valve (12) aperture is regulated the liquid inventory of two branch roads, the 3rd magnetic valve (13), the 4th magnetic valve (14) standard-sized sheet; Solution part in the weak solution heating tank (8) first magnetic valve (11) of flowing through, pump into fountain regenerating unit (10) through the 3rd solution pump (17), finish spray regeneration, become magnetic valve the 4th magnetic valve (14) of flowing through after the concentrated solution, enter concentrated solution holding vessel (5) and use for dehumidifier (7); Solution another part in the weak solution heating tank (8) flow through second magnetic valve (12), energy-saving heat exchanger (18) low-temperature coil, enter boiling type regenerating unit (4), finish explosive evaporation regeneration, become energy-saving heat exchanger (18) the high temperature coil pipe of flowing through after the concentrated solution, the 3rd magnetic valve (13) enters concentrated solution holding vessel (5) and uses for dehumidifier (7);
Flow of solution in the described concentrated solution holding vessel (5) is through concentrated solution heat exchanger (19) the high temperature coil pipe of lowering the temperature, concentrated solution cooling heat exchanger (19) low-temperature coil connects extraneous low-temperature receiver, concentrated solution wettability power after the cooling is improved, pump into the dehumidifying of dehumidifier (7) spray by first solution pump (15), finish circulation.
4. system according to claim 3, it is characterized in that: in described the third mode of operation, control liquid inventory ratio on two branch roads, preferentially move fountain regenerating unit (10), auxiliary operation boiling type regenerating unit (4) is done adjusting, adapts to load variations.
CN 201320153662 2013-03-29 2013-03-29 Novel solar liquid dehumidification air conditioning system Withdrawn - After Issue CN203177376U (en)

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Application Number Priority Date Filing Date Title
CN 201320153662 CN203177376U (en) 2013-03-29 2013-03-29 Novel solar liquid dehumidification air conditioning system

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103185379A (en) * 2013-03-29 2013-07-03 江苏大学 Novel solar energy liquid dehumidifying air-conditioning system and implementation method
CN107449027A (en) * 2017-07-31 2017-12-08 西安交通大学 A kind of solar energy couples hot-water heating system with air source heat pump
CN109737524A (en) * 2019-01-30 2019-05-10 山东佳鼎电气科技有限公司 A kind of air cleaning system for information machine room

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103185379A (en) * 2013-03-29 2013-07-03 江苏大学 Novel solar energy liquid dehumidifying air-conditioning system and implementation method
CN103185379B (en) * 2013-03-29 2015-01-07 江苏大学 Novel solar energy liquid dehumidifying air-conditioning system and implementation method
CN107449027A (en) * 2017-07-31 2017-12-08 西安交通大学 A kind of solar energy couples hot-water heating system with air source heat pump
CN109737524A (en) * 2019-01-30 2019-05-10 山东佳鼎电气科技有限公司 A kind of air cleaning system for information machine room

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Granted publication date: 20130904

Effective date of abandoning: 20150107

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