CN206291383U - A kind of twin-stage solar energy solution dehumidification system that unit is cooled down for double flash evaporation - Google Patents
A kind of twin-stage solar energy solution dehumidification system that unit is cooled down for double flash evaporation Download PDFInfo
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- CN206291383U CN206291383U CN201621282496.7U CN201621282496U CN206291383U CN 206291383 U CN206291383 U CN 206291383U CN 201621282496 U CN201621282496 U CN 201621282496U CN 206291383 U CN206291383 U CN 206291383U
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Abstract
The utility model discloses a kind of twin-stage solar energy solution dehumidification system that unit is cooled down for double flash evaporation, including internally-cooled dehumidifier, Ion-exchange device, solution preprocessor, double flash evaporation cooling unit and solar photovoltaic cell panel component etc..Weak solution groove and solution preprocessor are connected with Ion-exchange device respectively, constitute weak solution circulation canal, and the concentrated solution that will be concentrated in Ion-exchange device sends into internally-cooled dehumidifier to air dewetting；Double flash evaporation cooling unit is connected with the gas passage of internally-cooled dehumidifier.The utility model whole equipment all parts simple structure, saves initial cost, significant for improving the aspects such as air-conditioning system runnability, reduction energy resource consumption, raising indoor air quality, Optimizing City energy resource structure.
Description
Technical field
The utility model is related to double flash evaporation cooler technical group field, specifically a kind of for double flash evaporation cooling
The twin-stage solar energy solution dehumidification system of unit.
Background technology
Evaporative Cooling Air Conditioning has relatively low operation and equipment cost, can reduce the discharge capacity of greenhouse gases and CFC, therefore
It is referred to as " green air conditioner ".The ratio that the energy consumption of air-conditioning is accounted for inside building energy consumption is very big, and in the southern area of China, air-conditioning makes
With up to or so half a year, it is therefore desirable to explore a kind of new energy-saving type air conditioner.In southern area, wet-bulb depression is small, cold by evaporating
But the air humidity after air-conditioning treatment is very big, it is therefore desirable to and dehumidification system is combined together.For solution dehumidification system, due to
In improvement indoor air quality, using the aspect advantages such as low temperature exhaust heat, high efficiency energy storage, so having caused extensive pass
Note, and be gradually applied in engineering practice.But also there are some shortcomings in it.On the one hand, the regeneration of solution, the driving force of dehumidifying are
The water vapour pressure of solution surface is poor with the water vapour pressure of surrounding air, but in hot and humid area, such as Guangzhou, air
Humidity is too big, water vapour pressure subtractive is small, and regeneration and dehumidifying mass transfer effect can have a greatly reduced quality.On the other hand, although solar energy
The heat source temperature that hot dehumidification system needs is relatively low, it is possible to use the low taste energy, but is influenceed by heat source temperature is low, solution
Regeneration concentration and inefficient.However, can be very good to avoid these from lacking using the solution dehumidification system of solar-photovoltaic technology
Point, is no longer influenceed by hot and humid environment, has saved the energy, improves the efficiency of dehumidification system.This system is main by interior cold
The compositions such as type dehumidifier, Ion-exchange device, double flash evaporation cooling unit.
The early stage research of solution moisture removing device is concentrated mainly on filler and sprays on tower solution moisture removing device, because it has structure
The advantages of simple and specific surface area is big.But because the temperature of the solution during dehumidifying can be raised, prevent its dehumidification rate from
It is satisfactory.Since the nineties in 20th century, internally-cooled dehumidifier receives the common concern of people.Internally-cooled dehumidifier is using cold
Water coil or cooling air（Not with dehumidification solution directly contact）The latent heat that will be discharged in dehumidification process is taken away.Heat insulation-type is removed
Though wet device has many advantages, such as, compared with internally-cooled dehumidifier, its processed air is along stroke pressure loss is big, blower fan and molten
Liquid pump wasted work is big, mass transfer intensity is weak, and does not possess the condition of accumulation of energy.Therefore, internally-cooled dehumidifier is molten more suitable for solar energy
Liquid dehumidifier/air-conditioning system.
It is a kind of dehumidifying technology with electromotive force as driving force using the solution dehumidification system of solar-photovoltaic technology, it
Regeneration be with electrodialysis accumulation horizon as solution regenerator.Electrodialytic technique is one kind of membrane separation technique, it be by
Selective ion exchange membrane alternating parallel arrange between two electrodes, make two electrodes powered by photovoltaic power generation technology and
Electrical potential difference is formed between electrode, the zwitterion in solution is moved and positive respectively under the driving force of potential to respective direction
Amberplex and anion-exchange membrane are stopped；Concentrated solution room and diluting compartment are formed between electrode.Electrodialytic technique has energy
Consume low, easy to operate, long service life, it is pollution-free the features such as.
Utility model content
The purpose of this utility model is to overcome above-mentioned deficiency, there is provided proposed a kind of for the double of double flash evaporation cooling unit
Level solar energy solution dehumidification system, structure novelty is ingenious, can sufficiently utilize solar energy resources.
What the purpose of this utility model was realized in：A kind of twin-stage solar energy solution that unit is cooled down for double flash evaporation
Dehumidification system, including internally-cooled dehumidifier 2, weak solution groove 3, solution channel 6, solution preprocessor 7, one-level Ion-exchange device
9th, the two grades of ＇ of Ion-exchange device 9, concentrated solution groove 11, double flash evaporation cooling unit 12, rooms 13 and solar photovoltaic cell panels 5,
Internally-cooled dehumidifier 2, weak solution groove 3, solution channel 6, solution preprocessor 7,9, the two grades of electrodialysis of one-level Ion-exchange device
The ＇ of regenerator 9, concentrated solution groove 11 are sequentially connected in series, and concentrated solution groove 11 is also connected with internally-cooled dehumidifier 2 and constitutes solution recycle system, two
Level evaporation cooling unit 12 connects internally-cooled dehumidifier 2 and room 13 respectively, from double flash evaporation cooling unit 12 air out
Into after room 13, a part of return air in room 13 is evaporated cooling into double flash evaporation cooling unit 12 as Secondary Air,
Room 13 is also connected with the air inlet of internally-cooled dehumidifier 2, and solar photovoltaic cell panel 5 is arranged on solution channel 6.
Further, double flash evaporation cooling unit 12 includes direct section and indirect section, is provided between direct section and indirect section
Valve 15, indirect section connection internally-cooled dehumidifier 2, direct section connects room 13.
Further, the ＇ ＇ of valve 8 are provided between solution channel 6 and solution preprocessor 7, internally-cooled dehumidifier 2 is molten with dense
The ＇ of valve 8 is provided between liquid bath 11, valve 8 is provided between solution preprocessor 7 and one-level Ion-exchange device 9.
Further, also including battery, the input of battery connects the output end of solar photovoltaic cell panel 5, output
End connects one-level Ion-exchange device 9 and two grades of ＇ of Ion-exchange device 9 respectively.
Further, internally-cooled dehumidifier 2 is made of corrosion resistant stainless steel material, and inside is equipped with cooling tube, cold in pipe
Water supplies running water by running water pipe, and top is equipped with nozzle, and lower wall is provided with cooling water inlet 35, and upper side wall is provided with cooling water outlet
33, fog blocker is additionally provided with air outlet slit, fog blocker is PVC herringbone silk screens.
Further, one-level Ion-exchange device 9 and two grades of ＇ of Ion-exchange device 9 include battery lead plate, amberplex respectively
Group, amberplex group includes n anion-exchange membrane and n+1 cation-exchange membrane, and anion-exchange membrane and cation are handed over
Change film alternating parallel to be arranged between positive plate and negative plate, Ion-exchange device is divided into anode chamber 22, concentrated solution room 20, light
Change room 21, cathode chamber 23, concentrated solution room 20 and diluting compartment 21 are connected with solution preprocessor 7 respectively, through solution preprocessor（7）
The actified solution of first treated respectively enters one-level Ion-exchange device（9）Diluting compartment（21）With concentrated solution room（20）, afterwards
One-level Ion-exchange device（9）Weak solution after middle dilution enters the first solution tank（24）, and the solution feeding that will once concentrate
Two grades of concentrated solution rooms of Ion-exchange device (9 ＇)（20 ＇）And diluting compartment（21 ＇）, two grades of Ion-exchange devices（9 ＇）Concentrated solution room
（20 ＇）The solution of middle secondary recycling enters concentrated solution groove（11）, and diluting compartment（21 ＇）The weak solution of middle dilution flows into weak solution
Groove（3）.
Further, also including the second solution tank 25, the second solution tank 25 is built with pole liquid, the outlet point of the second solution tank 25
Not Lian Jie two grades of ＇ of anode chamber 22 and the ＇ of cathode chamber 23 of the ＇ of Ion-exchange device 9, the entrance of the second solution tank 25 connects one-level respectively
The anode chamber 22 of Ion-exchange device 9 and cathode chamber 23, the two grades of ＇ of anode chamber 22 connection one-level electrodialysis of the ＇ of Ion-exchange device 9
The anode chamber 22 of regenerator 9, two grades of cathode chambers of the ＇ of the cathode chamber 23 connection one-level Ion-exchanges device 9 of the ＇ of Ion-exchange device 9
23, the pole liquid in the second solution tank 25 is pressurizeed by the ＇ ＇ of solution pump 4 and flows into two grades of ＇ of anode chamber 22 and the moon of the ＇ of Ion-exchange device 9
The ＇ of pole room 23.
Preferably, concentrated solution groove 11 and weak solution groove 3 are made of resistant material.
Further, water pump 4 is installed, solution preprocessor 7 is with one-level electrodialysis again between weak solution groove 3 and solution channel
The ＇ of water pump 4 is installed between raw device 9.
The utility model has the advantage of：
1st, the refrigeration duty and humidity load of the utility model air are separately processed, and have efficiency of energy utilization higher, and improve
Indoor level of comfort.
2nd, the utility model uses solar energy techniques and photovoltaic technology, and solar energy is a kind of cleaning, reproducible ring
Protect the energy.
3rd, the utility model uses electrodialytic technique, electrodialytic technique have low, easy to operate energy consumption, long service life,
Pollution-free the features such as.
4th, the utility model uses calcium chloride solution, and the regeneration effect of solution is more preferable.
5th, the utility model solution dehumidification system is no longer influenceed by hot and humid environment, has saved the energy.
6th, the utility model whole equipment all parts simple structure, saves initial cost, is run for improving air-conditioning system
The aspects such as performance, reduction energy resource consumption, raising indoor air quality, Optimizing City energy resource structure are significant.
Brief description of the drawings
Fig. 1 is the Structure and Process of the twin-stage solar energy solution dehumidification system that the utility model is used for double flash evaporation cooling unit
Figure；
Fig. 2 is that the internally cooled of the twin-stage solar energy solution dehumidification system that the utility model is used for double flash evaporation cooling unit is removed
Wet device schematic diagram；
Fig. 3 be the utility model be used for double flash evaporation cooling unit twin-stage solar energy solution dehumidification system electrodialysis again
Raw device schematic diagram；
Wherein：1- outdoor fresh airs；1 ＇-return air；2- internally-cooled dehumidifiers；3- weak solution grooves；4- solution pumps；4 ＇-solution pump；
4 ＇ ＇-solution pump；5- solar photovoltaic cell panels；6- solution channels；7- solution preprocessors；8- valves；8 ＇-valve；8 ＇ ＇-valve
Door；9- Ion-exchange devices；9 ＇-Ion-exchange device；10- batteries；11- concentrated solution grooves；12- double flash evaporations cool down unit；
13- rooms；14- valves；15- valves；16- anion-exchange membranes；17- cation-exchange membranes；18- positive plates；19- minus plates；
20- concentrated solutions room；20 ＇-concentrated solution room；21- diluting compartments；21 ＇-diluting compartment；22- anode chambers；22 ＇-anode chamber；23- cathode chambers；
23 ＇-cathode chamber；The solution tanks of 24- first；The solution tanks of 25- second；30- concentrated solutions；31- nozzles；Air after 32- dehumidifying；33-
Cooling water outlet；34- cooling pipes；35- cooling water inlets；36- mixing wind；37- weak solutions；38- fog blockers.
Specific embodiment
The utility model is described in further detail below in conjunction with the accompanying drawings.
As shown in Figure 1, the utility model is a kind of twin-stage solar energy solution dehumidification that unit is cooled down for double flash evaporation
System, including internally-cooled dehumidifier 2, weak solution groove 3, solution channel 6, solution preprocessor 7, one-level Ion-exchange device 9, two
The ＇ of level Ion-exchange device 9, concentrated solution groove 11, double flash evaporation cooling unit 12, room 13 and solar photovoltaic cell panel 5, it is interior cold
Type dehumidifier 2, weak solution groove 3, solution channel 6, solution preprocessor 7,9, two grades of Ion-exchanges of one-level Ion-exchange device
The ＇ of device 9, concentrated solution groove 11 are sequentially connected in series, and concentrated solution groove 11 is also connected with internally-cooled dehumidifier 2 and constitutes solution recycle system, solar energy
Photovoltaic battery panel 5 is arranged on solution channel 6, and the output end of solar photovoltaic cell panel 5 connects the input of battery, electric power storage
The output end in pond connects one-level Ion-exchange device 9 and two grades of ＇ of Ion-exchange device 9 respectively.
Wherein concentrated solution groove 11 and weak solution groove 3, are corrosion-resistant material and are made；Double flash evaporation cooling unit 12 includes
Direct section and indirect section, are provided with valve 15, indirect section connection internally-cooled dehumidifier 2, direct section between direct section and indirect section
Connection room 13；Solution preprocessor 7 is made of corrosion resistant stainless steel material, and the top of solution preprocessor 7 is equipped with nozzle,
Inside is equipped with filler.Air feeding double flash evaporation cooling unit 12 after dehumidifying, double flash evaporation cooling unit 12 includes direct section
And indirect section, valve 15 is provided between direct section and indirect section, indirect section connection internally-cooled dehumidifier 2, direct section connects room
Between 13, after entering room 13 from double flash evaporation cooling unit 12 air out, a part of return air in room 13 steams into two-stage
The but unit 12 that feels cold is evaporated cooling as Secondary Air, and room 13 is also connected with the air inlet of internally-cooled dehumidifier 2 as return air
1 ＇ is constituted together with fresh air 1 and is mixed wind into internally-cooled dehumidifier 2.
Wherein, the ＇ ＇ of valve 8, internally-cooled dehumidifier 2 and concentrated solution are provided between solution channel 6 and solution preprocessor 7
The ＇ of valve 8 is provided between groove 11, valve 8 is provided between solution preprocessor 7 and one-level Ion-exchange device 9, valve 8 is used
Enter the liquid inventory of one-level Ion-exchange device concentrated solution room and diluting compartment in regulation, valve 14 is used to adjust return air amount, valve
Door 15 is used to adjust the air quantity from double flash evaporation cooling unit 12 indirect section out.
As shown in Figure 2, internally-cooled dehumidifier 2 is made of corrosion resistant stainless steel material, and inside is equipped with cooling pipe
And fog blocker, pipe inner cold water is running water, and internally-cooled dehumidifier inner top is equipped with nozzle 31, and lower wall is provided with cooling water inlet 35,
Upper side wall is provided with cooling water outlet 33, and the internally-cooled dehumidifier 2 is directly connected to double flash evaporation cooling unit 12, internally cooled dehumidifying
The air outlet slit of device 2 is provided with fog blocker, and fog blocker is PVC herringbone silk screens.
Internally-cooled dehumidifier 2 is realized in dehumidifying：The agent solution that dehumidified in internally-cooled dehumidifier 2 sprays from top jet nozzle 31
Enter, it is necessary to go the humid air of wet process to enter from bottom, both form adverse current, due to the water on the now surface of dehumidizer concentrated solution 30
Vapor pressure is less than the steam partial pressure of processed air, and vapor is transmitted from humid air to dehumidification solution, air humidity
Decline, the reduction of air vapor partial pressure, while solution concentration reduces, the steam partial pressure of solution surface is raised, until the two
Partial pressure is equal, completes dehumidification process, and the air after treatment cools down unit from the feeding double flash evaporation of internally-cooled dehumidifier top.Remove
Wet solution concentration reduction turns into weak solution 37, and weak solution groove 3 is flowed into from bottom.There is cooling pipe in internally-cooled dehumidifier, in pipe
It is passed through the efficiency that running water improves dehumidification solution with this.
One-level Ion-exchange device 9 and two grades of ＇ of Ion-exchange device 9 use electrodialytic technique, and accompanying drawing 3 is Ion-exchange
The schematic diagram of device, Ion-exchange device is made up of battery lead plate, amberplex, and n anion-exchange membrane is provided between both positive and negative polarity
With n+1 cation-exchange membrane, n is natural number, and anion-exchange membrane and cation-exchange membrane alternating parallel are arranged in both positive and negative polarity
Between, Ion-exchange device is divided into concentrated solution room, diluting compartment, anode chamber, cathode chamber.One-level Ion-exchange device 9 and solution
Preprocessor 7 is directly connected to.In solution reclaiming process, the actified solution of first treated is sent into one-level by solution preprocessor 7
Ion-exchange device, all the way into concentrated solution room 20, all the way into diluting compartment 21, in the diluting compartment of one-level Ion-exchange device 9
The weak solution of dilution separately uses it for anything else into the first solution tank 24, primary recycling in the concentrated solution room 20 of one-level Ion-exchange device 9
Solution afterwards is then divided into two-way and respectively enters two grades of ＇ of concentrated solution room 20 and the ＇ of diluting compartment 21 of the ＇ of Ion-exchange device 9, two grades of electric osmoses
The solution of secondary recycling is stored into concentrated solution groove in the concentrated solution room of analysis regenerator 9 ＇；And two grades of ＇ of Ion-exchange device 9
The ＇ of diluting compartment 20 in weak solution flow into weak solution groove 3, so as to constitute a closed cycle.
During Ion-exchange device actified solution, the pole liquid in the second solution tank 25 is made in the pressurization of the ＇ ＇ of solution pump 4
It is divided into the ＇ of anode chamber 22 and the ＇ of cathode chamber 23 that two-way is separately flowed into two grades of ＇ ＇ of Ion-exchange device 9 under, two grades of electrodialysis are again
Pole liquid in the ＇ of anode chamber 22 of the raw ＇ ＇ of device 9 flows into the anode chamber 22 of one-level Ion-exchange device 9, and two grades of Ion-exchange devices
Pole liquid in the ＇ of cathode chamber 23 of 9 ＇ ＇ then flows into the cathode chamber 23 of one-level Ion-exchange device 9, rear stage Ion-exchange device 9
Anode chamber 22 and cathode chamber 23 in pole liquid converge after flow into the second solution tank 25, so as to form a closed cycle.
Above-mentioned blower fan is frequency control blower fan, and water pump is circulation solution pump.
Finally it should be noted that：Obviously, above-described embodiment is only intended to clearly illustrate the application example, and simultaneously
The non-restriction to implementation method.For those of ordinary skill in the field, can also do on the basis of the above description
Go out the change or variation of other multi-forms.There is no need and unable to be exhaustive to all of implementation method.And thus drawn
Obvious change that Shen goes out or among changing still in the protection domain of the application type.
Claims (10)
1. it is a kind of for double flash evaporation cool down unit twin-stage solar energy solution dehumidification system, it is characterised in that including internally cooled
Dehumidifier (2), weak solution groove (3), solution channel（6）, solution preprocessor（7）, one-level Ion-exchange device (9), two grades of electricity
Dialysis regenerator (9 ＇), concentrated solution groove (11), double flash evaporation cool down unit (12), room（13）And solar photovoltaic cell panel
（5）, internally-cooled dehumidifier (2), weak solution groove (3), solution channel（6）, solution preprocessor（7）, one-level Ion-exchange device
(9), two grades of Ion-exchange devices (9 ＇), concentrated solution grooves (11) are sequentially connected in series, and concentrated solution groove (11) is also connected with internally-cooled dehumidifier
(2) solution recycle system is constituted, double flash evaporation cools down unit (12) and connects internally-cooled dehumidifier (2) and room respectively（13）, from
Double flash evaporation cools down unit (12) air out and enters room（13）Afterwards, room（13）A part of return air enter double flash evaporation
Cooling unit (12) is evaporated cooling, room as Secondary Air（13）It is also connected with the air inlet of internally-cooled dehumidifier (2), the sun
Can photovoltaic battery panel（5）Installed in solution channel（6）On.
2. it is according to claim 1 it is a kind of for double flash evaporation cool down unit twin-stage solar energy solution dehumidification system, its
It is characterised by, the double flash evaporation cools down unit (12) includes direct section and indirect section, is set between the direct section and indirect section
It is equipped with valve（15）, indirect section connection internally-cooled dehumidifier (2), the direct section connection room（13）.
3. it is according to claim 2 it is a kind of for double flash evaporation cool down unit twin-stage solar energy solution dehumidification system, its
It is characterised by, the solution channel（6）With solution preprocessor（7）Between be provided with valve（8 ＇ ＇）, the internally-cooled dehumidifier
(2) with concentrated solution groove（11）Between be provided with valve（8 ＇）, solution preprocessor（7）Between one-level Ion-exchange device (9)
It is provided with valve（8）.
4. it is according to claim 1 it is a kind of for double flash evaporation cool down unit twin-stage solar energy solution dehumidification system, its
It is characterised by, also including battery, the input connection solar photovoltaic cell panel of the battery（5）Output end, it is described
The output end of battery connects one-level Ion-exchange device (9) and two grades of Ion-exchange devices (9 ＇) respectively.
5. it is according to claim 1 it is a kind of for double flash evaporation cool down unit twin-stage solar energy solution dehumidification system, its
It is characterised by, internally-cooled dehumidifier (2) is made of corrosion resistant stainless steel material, inside is equipped with cooling tube, pipe inner cold water is
Running water pipe supplies running water, and internally-cooled dehumidifier (2) top is equipped with nozzle, internally-cooled dehumidifier (2) downside
Wall is provided with cooling water inlet（35）, internally-cooled dehumidifier (2) upper side wall is provided with cooling water outlet（33）.
6. it is according to claim 5 it is a kind of for double flash evaporation cool down unit twin-stage solar energy solution dehumidification system, its
It is characterised by, fog blocker is additionally provided with internally-cooled dehumidifier (2) air outlet slit, and the fog blocker is PVC herringbone silk screens.
7. it is according to claim 1 it is a kind of for double flash evaporation cool down unit twin-stage solar energy solution dehumidification system, its
It is characterised by, the one-level Ion-exchange device (9) and two grades of Ion-exchange devices (9 ＇) include battery lead plate, ion exchange respectively
Film group, the amberplex group includes n anion-exchange membrane and n+1 cation-exchange membrane, the anion-exchange membrane
And cation-exchange membrane alternating parallel is arranged between positive plate and negative plate, Ion-exchange device is divided into anode chamber（22）、
Concentrated solution room（20）, diluting compartment（21）, cathode chamber（23）, the concentrated solution room（20）And diluting compartment（21）Locate in advance with solution respectively
Reason device（7）Connection, through solution preprocessor（7）The actified solution of first treated respectively enters one-level Ion-exchange device（9）'s
Diluting compartment（21）With concentrated solution room（20）, rear stage Ion-exchange device（9）Weak solution after middle dilution enters the first solution
Groove（24）, and the solution that will once concentrate sends into two grades of concentrated solution rooms of Ion-exchange device (9 ＇)（20 ＇）And diluting compartment
（21 ＇）, two grades of Ion-exchange devices（9 ＇）Concentrated solution room（20 ＇）The solution of middle secondary recycling enters concentrated solution groove（11）, and
Diluting compartment（21 ＇）The weak solution of middle dilution flows into weak solution groove（3）.
8. it is according to claim 7 it is a kind of for double flash evaporation cool down unit twin-stage solar energy solution dehumidification system, its
It is characterised by, also including the second solution tank（25）, second solution tank（25）Built with pole liquid, second solution tank（25）
Outlet connect the anode chamber of two grades of Ion-exchange devices (9 ＇) respectively（22 ＇）And cathode chamber（23 ＇）, second solution tank
（25）Entrance connect the anode chamber of one-level Ion-exchange device (9) respectively（22）And cathode chamber（23）, two grades of electrodialysis
The anode chamber of regenerator (9 ＇)（22 ＇）The anode chamber of connection one-level Ion-exchange device (9)（22）, two grades of Ion-exchanges
The cathode chamber of device (9 ＇)（23 ＇）The cathode chamber of connection one-level Ion-exchange device (9)（23）, second solution tank（25）Interior
Pole liquid passes through solution pump（4 ＇ ＇）Pressurization flows into two grades of anode chambers of Ion-exchange device (9 ＇)（22 ＇）And cathode chamber（23 ＇）.
9. it is according to claim 1 it is a kind of for double flash evaporation cool down unit twin-stage solar energy solution dehumidification system, its
It is characterised by, the concentrated solution groove（11）With weak solution groove（3）It is made of resistant material.
10. it is according to claim 1 it is a kind of for double flash evaporation cool down unit twin-stage solar energy solution dehumidification system, its
It is characterised by, weak solution groove（3）Water pump is installed between solution channel（4）, solution preprocessor（7）With one-level electrodialysis again
Raw device（9）Between water pump is installed（4 ＇）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621282496.7U CN206291383U (en) | 2016-11-28 | 2016-11-28 | A kind of twin-stage solar energy solution dehumidification system that unit is cooled down for double flash evaporation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621282496.7U CN206291383U (en) | 2016-11-28 | 2016-11-28 | A kind of twin-stage solar energy solution dehumidification system that unit is cooled down for double flash evaporation |
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| Publication Number | Publication Date |
|---|---|
| CN206291383U true CN206291383U (en) | 2017-06-30 |
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ID=59099550
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621282496.7U Expired - Fee Related CN206291383U (en) | 2016-11-28 | 2016-11-28 | A kind of twin-stage solar energy solution dehumidification system that unit is cooled down for double flash evaporation |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108187459A (en) * | 2018-01-19 | 2018-06-22 | 东莞理工学院 | Air spiral type film dehumidifier, Ion-exchange device and its dehumidifying heating system |
-
2016
- 2016-11-28 CN CN201621282496.7U patent/CN206291383U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108187459A (en) * | 2018-01-19 | 2018-06-22 | 东莞理工学院 | Air spiral type film dehumidifier, Ion-exchange device and its dehumidifying heating system |
| CN108187459B (en) * | 2018-01-19 | 2024-01-16 | 东莞理工学院 | Air spiral type membrane dehumidifier, electrodialysis regeneration device and dehumidification heating system thereof |
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