CN206637756U - Solution dehumidification unit and there is its air conditioner - Google Patents
Solution dehumidification unit and there is its air conditioner Download PDFInfo
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- CN206637756U CN206637756U CN201720340641.0U CN201720340641U CN206637756U CN 206637756 U CN206637756 U CN 206637756U CN 201720340641 U CN201720340641 U CN 201720340641U CN 206637756 U CN206637756 U CN 206637756U
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Abstract
The utility model provides a kind of solution dehumidification unit and has its air conditioner, and solution dehumidification unit includes interconnected Dehumidifying element and regeneration unit, and solution dehumidification unit also includes：First surface cooler, the first surface cooler are arranged on the air inlet side of Dehumidifying element, are cooled with the gas to Dehumidifying element air inlet side；Second surface cooler, the second surface cooler are arranged on the outlet side of Dehumidifying element, to be heated up to the gas flowed out from Dehumidifying element.Solution dehumidification unit of the present utility model solves the problems, such as that the heat pump power consumption of solution dehumidification unit of the prior art is higher.
Description
Technical field
Field of air conditioning is the utility model is related to, in particular to a kind of solution dehumidification unit and there is its air conditioner.
Background technology
The dehumidification mode of traditional air conditioner is that air themperature is down to dew point using surface cooler, the water saturation analysis in air
Go out, reach the effect of dehumidifying, relative air humidity reduces the temperature of air, dehumidifying is with dropping close to 100% while dehumidifying
Temperature is mutually coupled.In actual applications, too low wind pushing temperature also results in condensation and comfortableness problem, therefore often right
Indoor, air handling process complexity is being sent into after air reheating or mixed high temperature air after dehumidifying.
Solution dehumidification is the moisture-absorption characteristics using some solution, the moisture in absorption air, reaches effect on moisture extraction.Through solution
Treated air themperature is determined that relative humidity is determined by solution concentration by solution temperature.Solution concentration is about high, and temperature is lower,
Air humidity content is lower.Identical water capacity, relative air humidity is lower, and the dry-bulb temperature of air is higher, the temperature of corresponding solution
Degree is higher, cools down that the cold evaporating temperature of solution is higher, and system COP is higher.Therefore, solution dehumidification mode is relative to traditional table
Cold dehumidifying, not only air handling process is simpler, also has higher Energy Efficiency Ratio, is advocating today of energy-saving and emission-reduction, is having weight
Want meaning.
Conventional liquid desiccant air conditioning is divided into dehumidifying section and regenerator section two parts.The section that dehumidifies is the dehumidification solution of low temperature in sky
Sprayed in gas, the moisture in absorption air, solution concentration is thinning；Regenerator section is that the actified solution of high temperature sprays in air, solution
In moisture evaporation into air, solution concentration uprises.When operation, a part of dehumidification solution and actified solution are carried out
Exchange, both sides solution concentration is maintained, to realize the operation of continuous-stable.
The major function of solution air-conditioning is to air dewetting, therefore the relative humidity of air-out is lower, and moisture removal is bigger, required
The dehumidification solution wanted is denseer.Because dehumidification solution concentration will be less than actified solution, dehumidification solution concentration is higher, actified solution
Concentration it is also higher.Solution concentration is higher, and regeneration temperature is higher.In heat-pump-type solution air-conditioning, regeneration temperature directly affects heat
The condensation temperature of pumping system, condensation temperature is higher, and the power consumption of heat pump is higher.Therefore, air-supply relative humidity is reduced, unit can be caused
The increase of power consumption, systematic energy efficiency ratio reduce.In summer, condensation temperature is too high, easily triggers delivery temperature protection, high voltage protective etc.
Problem, influence the operation stability of system.If solution concentration is lowered, air-supply relative humidity rise, water capacity is reduced, removed
Moisture can reduce.
Utility model content
Main purpose of the present utility model is to provide a kind of solution dehumidification unit and has its air conditioner, existing to solve
There is the problem of heat pump power consumption of the solution dehumidification unit in technology is higher.
To achieve these goals, according to one side of the present utility model, there is provided a kind of solution dehumidification unit, including
Interconnected Dehumidifying element and regeneration unit, solution dehumidification unit also include：First surface cooler, the first surface cooler, which is arranged on, to be removed
The air inlet side of wet unit, cooled with the gas to Dehumidifying element air inlet side；Second surface cooler, the second surface cooler, which is arranged on, to be removed
The outlet side of wet unit, to be heated up to the gas flowed out from Dehumidifying element.
Further, solution dehumidification unit also includes：Refrigerating medium circulation line, refrigerating medium circulation line and the first surface cooler
Connect with the second surface cooler, followed so as to form refrigerating medium between refrigerating medium circulation line, the first surface cooler and the second surface cooler
Loop back path.
Further, refrigerating medium circulation line includes：First circulation pipeline, one end of first circulation pipeline and the first table are cold
Device connects, and the other end of first circulation pipeline connects with the second surface cooler.
Further, refrigerating medium circulation line also includes：Second circulation pipeline, one end of second circulation pipeline and the first table
Cooler connects, and the other end of second circulation pipeline connects with the second surface cooler.
Further, liquid reserve tank is provided with first circulation pipeline, the outlet of liquid reserve tank connects with the import of the second surface cooler
It is logical, the import of liquid reserve tank and the outlet of the first surface cooler.
Further, coolant pump is provided with first circulation pipeline, coolant pump is arranged on the outlet and of liquid reserve tank
On pipeline between two surface coolers, so that the liquid in liquid reserve tank is flowed into the second surface cooler.
Further, solution dehumidification unit also includes the 3rd circulation line, the 4th circulation line and interstage flow heat exchanger, the
Three circulation lines and the 4th circulation line are connected with interstage flow heat exchanger to be exchanged heat by interstage flow heat exchanger；Wherein, the 3rd
One end of circulation line connects with the liquid reserve tank of Dehumidifying element, and the other end of the 3rd circulation line and the liquid reserve tank of regeneration unit connect
It is logical；One end of 4th circulation line connects with the liquid reserve tank of Dehumidifying element, the other end of the 4th circulation line and regeneration unit
Liquid reserve tank connects.
Further, regeneration pump is provided with the 4th circulation line, the import of regeneration pump and the liquid reserve tank of regeneration unit connect
Logical, the outlet of regeneration pump connects with the liquid reserve tank of Dehumidifying element.
Further, dehumidifying pump is provided with the 3rd circulation line, the import for the pump that dehumidifies and the liquid reserve tank of Dehumidifying element connect
Logical, the outlet for the pump that dehumidifies connects with the liquid reserve tank of regeneration unit.
Further, solution dehumidification unit also includes：First heat exchanging pipe；Condenser, it is logical that condenser includes the first heat exchange
Road and the second heat exchanger channels, the first heat exchanger channels of condenser connect with the second spray pipeline of regeneration unit, and the of condenser
Two heat exchanger channels connect with the first heat exchanging pipe.
Further, solution dehumidification unit also includes：Second heat exchanging pipe；Evaporator, it is logical that evaporator includes the 3rd heat exchange
Road and the 4th heat exchanger channels, the 3rd heat exchanger channels of evaporator connect with the first spray pipeline of Dehumidifying element, and the of evaporator
Four heat exchanger channels connect with the second heat exchanging pipe.
According to another aspect of the present utility model, there is provided a kind of air conditioner, including solution dehumidification unit, solution dehumidifier
Group is above-mentioned solution dehumidification unit.
Solution dehumidification unit of the present utility model passes through Dehumidifying element, regeneration unit, the first surface cooler and the second surface cooler
Air dewetting is realized, wherein, Dehumidifying element and regeneration unit are interconnected, and the first surface cooler is arranged on the air inlet of Dehumidifying element
At mouthful, the second surface cooler is arranged at the gas outlet of Dehumidifying element.In specific dehumidification process, Dehumidifying element includes the first spray
Shower pipe road, the dehumidification solution that low temperature is realized by the first spray pipeline spray in atmosphere, the moisture in absorption air, so as to
Complete the dehumidifying to air and reduce the concentration of dehumidification solution, regeneration unit includes the second spray pipeline, passes through the second spray
The actified solution that shower pipe road realizes high temperature sprays in atmosphere, and the moisture evaporation in solution is into air, actified solution concentration
Uprise, be interconnected and can ensure in dehumidification process by Dehumidifying element and regeneration unit, the dehumidification solution in Dehumidifying element
Swapped with the actified solution in regeneration unit, so as to maintain both sides solution concentration balance.
In the utility model, the first surface cooler is set by the air inlet in Dehumidifying element, can make to enter dehumidifying list
The air of member first passes through the first surface cooler, realizes the cooling to inlet air, the air after cooling is removed into Dehumidifying element
Wet, the air after dehumidifying passes through the second surface cooler, and the air for flowing through the second surface cooler is heated so that the relatively wet of air-supply
Degree reduces, and meets the demand of indoor air-supply, so as to suitably reduce the dehumidification solution concentration of Dehumidifying element, reduces regeneration
The concentration of the actified solution of unit, regeneration temperature being reduced with this, the condensation temperature of heat pump declines, the lower power consumption of heat pump,
Finally solve it is of the prior art because of dehumidification solution excessive concentration in solution dehumidification unit and caused by heat pump power consumption it is higher
Problem.
Brief description of the drawings
The Figure of description for forming the part of the application is used for providing further understanding to of the present utility model, this practicality
New schematic description and description is used to explain the utility model, does not form to improper restriction of the present utility model.
In the accompanying drawings：
Fig. 1 shows the structural representation of the embodiment according to solution dehumidification unit of the present utility model.
Wherein, above-mentioned accompanying drawing marks including the following drawings：
10th, Dehumidifying element；11st, the first spray pipeline；20th, regeneration unit；21st, the second spray pipeline；30th, the first table is cold
Device；40th, the second surface cooler；50th, liquid reserve tank；60th, coolant pump；70th, condenser；80th, evaporator；90th, interstage flow heat exchanger；
100th, regeneration pump；110th, dehumidify pump；120th, first circulation pipeline；130th, second circulation pipeline；140th, the 3rd circulation line；150、
4th circulation line；160th, the first heat exchanging pipe；170th, the second heat exchanging pipe.
Embodiment
It should be noted that in the case where not conflicting, the feature in embodiment and embodiment in the application can phase
Mutually combination.Describe the utility model in detail below with reference to the accompanying drawings and in conjunction with the embodiments.
The utility model provides a kind of solution dehumidification unit, refer to Fig. 1, and solution dehumidification unit includes what is be interconnected
Dehumidifying element 10 and regeneration unit 20, solution dehumidification unit also include：First surface cooler 30, the first surface cooler 30 are arranged on dehumidifying
The air inlet side of unit 10, cooled with the gas to the air inlet side of Dehumidifying element 10；Second surface cooler 40, the second surface cooler 40 are set
Put in the outlet side of Dehumidifying element 10, to be heated up to the gas flowed out from Dehumidifying element 10.
Solution dehumidification unit of the present utility model passes through Dehumidifying element 10, regeneration unit 20, the first surface cooler 30 and second
Surface cooler 40 realizes air dewetting, wherein, Dehumidifying element 10 and regeneration unit 20 are interconnected, and the first surface cooler 30 is arranged on
At the air inlet of Dehumidifying element 10, the second surface cooler 40 is arranged at the gas outlet of Dehumidifying element 10.In specific dehumidification process
In, Dehumidifying element 10 includes the first spray pipeline 11, and the dehumidification solution of low temperature is realized in air by the first spray pipeline 11
Middle spray, the moisture in absorption air, so as to complete the dehumidifying to air and reduce the concentration of dehumidification solution, regeneration unit
20 include the second spray pipeline 21, and the actified solution that high temperature is realized by the second spray pipeline 21 sprays in atmosphere, solution
In moisture evaporation into air, actified solution concentration uprises, and being interconnected by Dehumidifying element 10 and regeneration unit 20 can be with
Ensureing in dehumidification process, the actified solution in dehumidification solution and regeneration unit 20 in Dehumidifying element 10 swaps, so as to
Maintain both sides solution concentration balance.
In the present embodiment, the first surface cooler 30 is set by the air inlet in Dehumidifying element 10, can makes to enter dehumidifying
The air of unit 10 first passes through the first surface cooler 30, realizes the cooling to inlet air, and the air after cooling enters Dehumidifying element
10 are dehumidified, and the air after dehumidifying passes through the second surface cooler 40, and the air for flowing through the second surface cooler 40 is heated so that
The relative humidity of air-supply reduces, and the demand of indoor air-supply is met, so as to suitably reduce the dehumidification solution of Dehumidifying element 10
Concentration, the concentration of the actified solution of regeneration unit 20 is reduced, regeneration temperature is reduced with this, under the condensation temperature of heat pump
Drop, the lower power consumption of heat pump, finally solve and of the prior art produced because of dehumidification solution excessive concentration in solution dehumidification unit
The problem of raw heat pump power consumption is higher.
In order to make the refrigerating medium in the first surface cooler 30 and the second surface cooler 40 realize inner loop, solution dehumidifier
Group also includes：Refrigerating medium circulation line, refrigerating medium circulation line connect with the first surface cooler 30 and the second surface cooler 40, so that
Refrigerating medium circulation loop is formed between refrigerating medium circulation line, the first surface cooler 30 and the second surface cooler 40.By in the first table
Refrigerating medium circulation line is provided between the surface cooler 40 of cooler 30 and second, refrigerating medium circulation line, the first surface cooler can be made
30 and second form refrigerating medium circulation loop between surface cooler 40, so as to ensure that refrigerating medium is cold in the first surface cooler 30 and the second table
Circulated in device 40.
In order to reduce the relative humidity of air-supply, refrigerating medium circulation pipe by the first surface cooler 30 and the second surface cooler 40
Road includes：First circulation pipeline 120, one end of first circulation pipeline 120 connect with the first surface cooler 30, first circulation pipeline
120 other end connects with the second surface cooler 40.
In the present embodiment, by being provided with first circulation pipeline 120 on solution dehumidification unit, wherein, first circulation
One end of pipeline 120 connects with the first surface cooler 30, and the other end of first circulation pipeline 120 connects with the second surface cooler 40, with
This connects the first surface cooler 30 with the second surface cooler 40.
In order to make refrigerating medium realize circulation, refrigerating medium circulation line in the first surface cooler 30 and the second surface cooler 40
Also include：Second circulation pipeline 130, one end of second circulation pipeline 130 connect with the first surface cooler 30, second circulation pipeline
130 other end connects with the second surface cooler 40.By being provided with second circulation pipeline 130 on solution dehumidification unit, second
One end of circulation line 130 connects with the first surface cooler 30, and the other end of second circulation pipeline 130 connects with the second surface cooler 40
It is logical, and by the setting of first circulation pipeline 120 and second circulation pipeline 130 can refrigerating medium in the He of the first surface cooler 30
Circulation is realized in second surface cooler 40.
In order to provide enough refrigerating mediums, first circulation pipeline in the first surface cooler 30 and the second surface cooler 40
It is provided with liquid reserve tank 50 on 120, the outlet of liquid reserve tank 50 and the inlet communication of the second surface cooler 40, the import of liquid reserve tank 50 and the
The outlet of one surface cooler 30.
In the present embodiment, by being provided with liquid reserve tank 50 on first circulation pipeline 120, wherein, liquid reserve tank 50 goes out
The inlet communication of mouth and the second surface cooler 40, the import of liquid reserve tank 50 and the outlet of the first surface cooler 30, make liquid storage with this
Refrigerating medium in case 50 is introduced into the second surface cooler 40, refrigerating medium is subcooled by the air excluded in Dehumidifying element 10, supercooling
Refrigerating medium afterwards enters the first surface cooler 30, and refrigerating medium carries out cooling processing to the air for entering Dehumidifying element.
In order to make the refrigerating medium in liquid reserve tank 50 enter the second surface cooler 40, it is provided with first circulation pipeline 120
Coolant pump 60, coolant pump 60 is arranged on the pipeline between the outlet of liquid reserve tank 50 and the second surface cooler 40, so that liquid storage
Liquid in case 50 is flowed into the second surface cooler 40.
When being swapped in order to reduce the actified solution in dehumidification solution and regeneration unit 20 in Dehumidifying element 10
Loss of refrigeration capacity, as shown in figure 1, solution dehumidification unit also include between the 3rd circulation line 140, the 4th circulation line 150 and level
Heat exchanger 90 is flowed, the 3rd circulation line 140 and the 4th circulation line 150 are connected with interstage flow heat exchanger 90 to pass through interstage flow
Heat exchanger 90 exchanges heat；Wherein, one end of the 3rd circulation line 140 connects with the liquid reserve tank of Dehumidifying element 10, the 3rd circulation line
140 other end connects with the liquid reserve tank of regeneration unit 20；One end of 4th circulation line 150 and the liquid reserve tank of Dehumidifying element 10
Connection, the other end of the 4th circulation line 150 connect with the liquid reserve tank of regeneration unit 20.
In the present embodiment, one end of the 3rd circulation line 140 connects with the liquid reserve tank of Dehumidifying element 10, the 3rd circulation pipe
The other end on road 140 connects with the liquid reserve tank of regeneration unit 20；One end of 4th circulation line 150 and the liquid storage of Dehumidifying element 10
Case connects, and the other end of the 4th circulation line 150 connects with the liquid reserve tank of regeneration unit 20, passes through the He of the 3rd circulation line 140
4th circulation line 150 can swap the actified solution in dehumidification solution and regeneration unit 20 in Dehumidifying element 10,
So as to maintain both sides solution concentration balance.By the way that the 3rd circulation line 140 and the 4th circulation line 150 are exchanged heat with interstage flow
Device 90 connects, and interstage flow heat exchanger 90 can be utilized to reduce the regeneration in dehumidification solution and regeneration unit 20 in Dehumidifying element 10
Loss of refrigeration capacity when solution swaps.
Preferably, regeneration pump 100, import and the regeneration unit 20 of regeneration pump 100 are provided with the 4th circulation line 150
Liquid reserve tank connects, and the outlet of regeneration pump 100 connects with the liquid reserve tank of Dehumidifying element 10.
Preferably, dehumidifying pump 110 is provided with the 3rd circulation line 140, import and the Dehumidifying element 10 of the pump 110 that dehumidifies
Liquid reserve tank connects, and the outlet of dehumidifying pump 110 connects with the liquid reserve tank of regeneration unit 20.
In order to also be included by the actified solution in the thermal regeneration unit 20 of condenser 70, solution dehumidification unit：The
One heat exchanging pipe 160；Condenser 70, condenser 70 include the first heat exchanger channels and the second heat exchanger channels, and the first of condenser 70
Heat exchanger channels connect with the second spray pipeline 21 of regeneration unit 20, the second heat exchanger channels and the first heat exchanging pipe of condenser 70
160 connections.
In the present embodiment, solution dehumidification unit also includes：First heat exchanging pipe 160 and condenser 70, wherein, condenser
70 include the first heat exchanger channels and the second heat exchanger channels, the first heat exchanger channels of condenser 70 and the second spray of regeneration unit 20
Pipeline 21 connects, and the second heat exchanger channels of condenser 70 connect with the first heat exchanging pipe 160, so as to so that the first heat exchanging pipe
160 and the second spray pipeline 21 of regeneration unit 20 exchanged heat by condenser 70, it is molten with the regeneration in this thermal regeneration unit 20
Liquid.
In order to realize the cooling to the dehumidification solution in Dehumidifying element 10 by evaporator 80, solution dehumidification unit is also
Including：Second heat exchanging pipe 170；Evaporator 80, evaporator 80 include the 3rd heat exchanger channels and the 4th heat exchanger channels, evaporator 80
The 3rd heat exchanger channels connected with the first spray pipeline 11 of Dehumidifying element 10, the 4th heat exchanger channels of evaporator 80 change with second
Pipe line 170 connects.
In the present embodiment, solution dehumidification unit also includes：Second heat exchanging pipe 170 and evaporator 80, wherein, evaporator
80 include the 3rd heat exchanger channels and the 4th heat exchanger channels, the 3rd heat exchanger channels of evaporator 80 and the first spray of Dehumidifying element 10
Pipeline 11 is connected, and the 4th heat exchanger channels of evaporator 80 connect with the second heat exchanging pipe 170, and the second heat exchanging pipe is realized with this
170 and the first spray pipeline 11 of Dehumidifying element 10 exchanged heat by evaporator 80, so as to realize to the dehumidifying in Dehumidifying element 10
The cooling of solution.
In the present embodiment, the first heat exchanging pipe 160 and the branch that the second heat exchanging pipe 170 is whole recuperated cycle pipeline
Pipeline.
In the present embodiment, the regeneration pump 100 on the 4th circulation line 150, outlet and the condenser 70 of regeneration pump 100
The inlet communication of first heat exchanger channels, so as to which actified solution is sent into condenser 70, actified solution is added by condenser 70
Heat.
Correspondingly, the dehumidifying pump 110 on the 3rd circulation line 140, the outlet of dehumidifying pump 110 are changed with the 3rd of evaporator 80
The inlet communication of the passage of heat, so as to which dehumidification solution is sent into evaporator 80, dehumidification solution is reduced by evaporator 80 with this
Temperature.
For the carrying out practically process of solution dehumidification unit of the present utility model：
Solution dehumidification unit of the present utility model installs precooling surface cooler (first table in the air inlet of Dehumidifying element 10
Cooler 30), air outlet installs a reheating surface cooler (the second surface cooler 40), two surface cooler pipeline series connection.Pass through a water
Pump (coolant pump 60), reheating surface cooler is squeezed into from liquid reserve tank (liquid reserve tank 50) water, gone out after air cooling into precooling
Surface cooler, air intake is cooled down, finally flows back to liquid reserve tank.
Water in liquid reserve tank can also be substituted with other refrigerating mediums.The form of surface cooler can be copper pipe aluminum fin, also may be used
To be the air-water heat exchanger of other forms.
The utility model additionally provides a kind of air conditioner, including solution dehumidification unit, and solution dehumidification unit is above-mentioned molten
Liquid dehumidifying unit.
As can be seen from the above description, the utility model the above embodiments realize following technique effect：
Solution dehumidification unit of the present utility model passes through Dehumidifying element 10, regeneration unit 20, the first surface cooler 30 and second
Surface cooler 40 realizes air dewetting, wherein, Dehumidifying element 10 and regeneration unit 20 are interconnected, and the first surface cooler 30 is arranged on
At the air inlet of Dehumidifying element 10, the second surface cooler 40 is arranged at the gas outlet of Dehumidifying element 10.In specific dehumidification process
In, Dehumidifying element 10 includes the first spray pipeline 11, and the dehumidification solution of low temperature is realized in air by the first spray pipeline 11
Middle spray, the moisture in absorption air, so as to complete the dehumidifying to air and reduce the concentration of dehumidification solution, regeneration unit
20 include the second spray pipeline 21, and the actified solution that high temperature is realized by the second spray pipeline 21 sprays in atmosphere, solution
In moisture evaporation into air, actified solution concentration uprises, and being interconnected by Dehumidifying element 10 and regeneration unit 20 can be with
Ensureing in dehumidification process, the actified solution in dehumidification solution and regeneration unit 20 in Dehumidifying element 10 swaps, so as to
Maintain both sides solution concentration balance.
In the present embodiment, the first surface cooler 30 is set by the air inlet in Dehumidifying element 10, can makes to enter dehumidifying
The air of unit 10 first passes through the first surface cooler 30, realizes the cooling to inlet air, and the air after cooling enters Dehumidifying element
10 are dehumidified, and the air after dehumidifying passes through the second surface cooler 40, and the air for flowing through the second surface cooler 40 is heated so that
The relative humidity of air-supply reduces, and the demand of indoor air-supply is met, so as to suitably reduce the dehumidification solution of Dehumidifying element 10
Concentration, the concentration of the actified solution of regeneration unit 20 is reduced, regeneration temperature is reduced with this, under the condensation temperature of heat pump
Drop, the lower power consumption of heat pump, finally solve and of the prior art produced because of dehumidification solution excessive concentration in solution dehumidification unit
The problem of raw heat pump power consumption is higher.
Solution dehumidification unit of the present utility model is by air-out reheating, reducing the relative humidity of air-out, with original system
Compare, under identical air-out relative humidity, the solution concentration of original system is higher, and regeneration temperature can be caused high, heat pump condensation
Temperature drift, power consumption is bigger than normal, and excessive discharge temperature is easily caused under bad working environments, the problems such as high voltage protective.This practicality is new
The solution dehumidification unit of type reduces solution concentration, improves wind pushing temperature, reduces air-supply relative humidity, reduces heat pump system
Unite power consumption, improve reliability while energy-conservation.
Preferred embodiment of the present utility model is the foregoing is only, is not limited to the utility model, for this
For the technical staff in field, the utility model can have various modifications and variations.It is all in the spirit and principles of the utility model
Within, any modification, equivalent substitution and improvements made etc., it should be included within the scope of protection of the utility model.
Claims (12)
1. a kind of solution dehumidification unit, including interconnected Dehumidifying element (10) and regeneration unit (20), it is characterised in that molten
Liquid dehumidifying unit also includes：
First surface cooler (30), first surface cooler (30) is arranged on the air inlet side of the Dehumidifying element (10), with to described
The gas of Dehumidifying element (10) air inlet side is cooled；
Second surface cooler (40), second surface cooler (40) are arranged on the outlet side of the Dehumidifying element (10), with to from institute
The gas for stating Dehumidifying element (10) outflow is heated up.
2. solution dehumidification unit according to claim 1, it is characterised in that the solution dehumidification unit also includes：
Refrigerating medium circulation line, the refrigerating medium circulation line and first surface cooler (30) and second surface cooler (40)
Connect, so as to be formed between the refrigerating medium circulation line, first surface cooler (30) and second surface cooler (40)
Refrigerating medium circulation loop.
3. solution dehumidification unit according to claim 2, it is characterised in that the refrigerating medium circulation line includes：
First circulation pipeline (120), one end of the first circulation pipeline (120) connect with first surface cooler (30), institute
The other end for stating first circulation pipeline (120) connects with second surface cooler (40).
4. solution dehumidification unit according to claim 2, it is characterised in that the refrigerating medium circulation line also includes：
Second circulation pipeline (130), one end of the second circulation pipeline (130) connect with first surface cooler (30), institute
The other end for stating second circulation pipeline (130) connects with second surface cooler (40).
5. solution dehumidification unit according to claim 3, it is characterised in that set on the first circulation pipeline (120)
There are liquid reserve tank (50), the outlet of the liquid reserve tank (50) and the inlet communication of second surface cooler (40), the liquid reserve tank
(50) import and the outlet of first surface cooler (30).
6. solution dehumidification unit according to claim 5, it is characterised in that set on the first circulation pipeline (120)
There is coolant pump (60), the coolant pump (60) is arranged on outlet and second surface cooler (40) of the liquid reserve tank (50)
Between pipeline on so that liquid in the liquid reserve tank (50) is flowed into second surface cooler (40).
7. solution dehumidification unit according to claim 1, it is characterised in that the solution dehumidification unit also follows including the 3rd
Endless tube road (140), the 4th circulation line (150) and interstage flow heat exchanger (90), the 3rd circulation line (140) and described
Four circulation lines (150) are connected with the interstage flow heat exchanger (90) to be exchanged heat by the interstage flow heat exchanger (90)；Its
In, one end of the 3rd circulation line (140) connects with the liquid reserve tank of the Dehumidifying element (10), the 3rd circulation line
(140) the other end connects with the liquid reserve tank of the regeneration unit (20)；One end of 4th circulation line (150) with it is described
The liquid reserve tank connection of Dehumidifying element (10), the other end of the 4th circulation line (150) and the storage of the regeneration unit (20)
Liquid case connects.
8. solution dehumidification unit according to claim 7, it is characterised in that set on the 4th circulation line (150)
There is regeneration pump (100), the import of the regeneration pump (100) connects with the liquid reserve tank of the regeneration unit (20), the regeneration pump
(100) outlet connects with the liquid reserve tank of the Dehumidifying element (10).
9. solution dehumidification unit according to claim 7, it is characterised in that set on the 3rd circulation line (140)
There is dehumidifying pump (110), the import of the dehumidifying pump (110) connects with the liquid reserve tank of the Dehumidifying element (10), the dehumidifying pump
(110) outlet connects with the liquid reserve tank of the regeneration unit (20).
10. solution dehumidification unit according to claim 1, it is characterised in that the solution dehumidification unit also includes：
First heat exchanging pipe (160)；
Condenser (70), the condenser (70) include the first heat exchanger channels and the second heat exchanger channels, the condenser (70)
First heat exchanger channels connect with the second spray pipeline (21) of the regeneration unit (20), and the second of the condenser (70)
Heat exchanger channels connect with first heat exchanging pipe (160).
11. solution dehumidification unit according to claim 1, it is characterised in that the solution dehumidification unit also includes：
Second heat exchanging pipe (170)；
Evaporator (80), the evaporator (80) include the 3rd heat exchanger channels and the 4th heat exchanger channels, the evaporator (80)
3rd heat exchanger channels connect with the first spray pipeline (11) of the Dehumidifying element (10), and the 4th of the evaporator (80) the
Heat exchanger channels connect with second heat exchanging pipe (170).
12. a kind of air conditioner, including solution dehumidification unit, it is characterised in that the solution dehumidification unit is claim 1 to 11
Any one of solution dehumidification unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720340641.0U CN206637756U (en) | 2017-03-31 | 2017-03-31 | Solution dehumidification unit and there is its air conditioner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720340641.0U CN206637756U (en) | 2017-03-31 | 2017-03-31 | Solution dehumidification unit and there is its air conditioner |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206637756U true CN206637756U (en) | 2017-11-14 |
Family
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106813326A (en) * | 2017-03-31 | 2017-06-09 | 天津华创瑞风空调设备有限公司 | Solution dehumidification unit and the air-conditioner with it |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106813326A (en) * | 2017-03-31 | 2017-06-09 | 天津华创瑞风空调设备有限公司 | Solution dehumidification unit and the air-conditioner with it |
| CN106813326B (en) * | 2017-03-31 | 2023-05-23 | 天津华创瑞风空调设备有限公司 | Solution dehumidification unit and air conditioner with same |
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