CN208032258U - Air spiral type film dehumidifier, Ion-exchange device and its dehumidifying heating system - Google Patents
Air spiral type film dehumidifier, Ion-exchange device and its dehumidifying heating system Download PDFInfo
- Publication number
- CN208032258U CN208032258U CN201820099069.8U CN201820099069U CN208032258U CN 208032258 U CN208032258 U CN 208032258U CN 201820099069 U CN201820099069 U CN 201820099069U CN 208032258 U CN208032258 U CN 208032258U
- Authority
- CN
- China
- Prior art keywords
- fluid reservoir
- air
- solution
- hollow
- chamber
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn - After Issue
Links
- 238000005342 ion exchange Methods 0.000 title claims abstract description 32
- 238000010438 heat treatment Methods 0.000 title claims abstract description 20
- 239000012530 fluid Substances 0.000 claims abstract description 102
- 238000007791 dehumidification Methods 0.000 claims abstract description 43
- 238000010521 absorption reaction Methods 0.000 claims abstract description 18
- 239000012528 membrane Substances 0.000 claims description 94
- 239000000835 fiber Substances 0.000 claims description 63
- 238000006243 chemical reaction Methods 0.000 claims description 24
- 239000003011 anion exchange membrane Substances 0.000 claims description 22
- 238000005341 cation exchange Methods 0.000 claims description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 239000006096 absorbing agent Substances 0.000 claims description 12
- 238000003491 array Methods 0.000 claims description 4
- 239000012510 hollow fiber Substances 0.000 claims description 4
- 238000003860 storage Methods 0.000 claims description 4
- 235000012489 doughnuts Nutrition 0.000 claims description 3
- 238000005349 anion exchange Methods 0.000 claims 1
- 239000007788 liquid Substances 0.000 description 14
- 230000009102 absorption Effects 0.000 description 11
- 230000008929 regeneration Effects 0.000 description 8
- 238000011069 regeneration method Methods 0.000 description 8
- 150000001768 cations Chemical class 0.000 description 7
- 238000001816 cooling Methods 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- 101700004678 SLIT3 Proteins 0.000 description 5
- 102100027339 Slit homolog 3 protein Human genes 0.000 description 5
- 239000002250 absorbent Substances 0.000 description 4
- 230000002745 absorbent Effects 0.000 description 4
- 238000004378 air conditioning Methods 0.000 description 4
- 239000002274 desiccant Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 4
- 230000006872 improvement Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 150000001450 anions Chemical class 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000000909 electrodialysis Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000003230 hygroscopic agent Substances 0.000 description 2
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M lithium chloride Chemical compound [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 230000005685 electric field effect Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 238000005213 imbibition Methods 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Abstract
The utility model provides a kind of air spiral type film dehumidifier, Ion-exchange device and its dehumidifying heating system, the dehumidifying heating system, including air spiral type film dehumidifier and Ion-exchange device；Further include the first fluid reservoir, the second fluid reservoir and absorption heat pump；It is respectively provided with dehumidification solution in first fluid reservoir and the second fluid reservoir；The solution inlet of the air spiral type film dehumidifier is connected to the first fluid reservoir, and the taphole of air spiral type film dehumidifier is connected to the second fluid reservoir, and the first fluid reservoir and the second fluid reservoir are connected to the Ion-exchange device respectively；The absorption heat pump is connected between the first fluid reservoir and the second fluid reservoir；Dehumidification solution in first fluid reservoir after air spiral type film dehumidifier and absorption heat pump, is flowed into the second fluid reservoir respectively；Dehumidification solution in second fluid reservoir is flowed into the first fluid reservoir after Ion-exchange device.The utility model meets heating and the dehumidification of people with same complete equipment simultaneously, has extensive market prospects.
Description
Technical field
The utility model is related to dehumidification device fields, and in particular to a kind of air spiral type film dehumidifier, Ion-exchange
Device and its dehumidifying heating system.
Background technology
The temperature and humidity of air is to influence two key factors of amenity degree.In hot weather, to ring
Border air themperature, which carries out cooling, can improve comfort level；However, in the weather of hot humid, especially bay-type city, dehumidifying is several
It is important with as cooling.Studies have shown that the relative humidity that human body is suitble to is 40-60%, excessively high humidity can cause human body to produce
It is raw uncomfortable.
With the development of national economy, people's lives level is continuously improved, for building the requirement of hygrothermal environment also not
Disconnected to improve, the application of air-conditioning is more and more extensive, and the requirement to air-conditioning system is also higher and higher.Energy consumption of the air-conditioning system as China
Rich and influential family accounts for 15% or so of national energy-consuming, and China's most area summer high-temperature high humidity, especially South China, dehumidify energy
The 20%~40% of duty tune total energy consumption is consumed, so humid control is to realizing that the energy saving of air-conditioning system has very great meaning.
Common air dehumidification method includes cooling method dehumidifying, solid absorbent dehumidifying and liquid desiccant dehumidifying.It is cooling
Method dehumidifying is removed from air after humid air is cooled to dew-point temperature hereinafter, the vapor in air is made to condense.This method
It is warming up to ventilation state, high energy consumption again after need to air being down to dew-point temperature hereinafter, removing moisture.Solid absorbent dehumidifying is profit
It is dehumidified with the method for certain solid absorbent moisture absorptions.The disadvantage of this method is that the regeneration of these solid absorbents is tired
Difficulty, and device is complicated, and volume is relatively large for equipment, and cost is also high.Liquid desiccant dehumidifying is that have moisture absorption using certain
The solution of property reaches dehumidifying purpose to absorb the moisture in air.Liquid dehumidifying regeneration is easy, the disadvantage is that processing air and liquid
Body hygroscopic agent is in direct contact, and is easily caused air to carry hygroscopic agent secretly, is further caused the corrosion of pipeline and equipment.
In order to settle the matter once and for all, membrane type liquid dehumidifying technology is come into being.The key of membrane type liquid dehumidifying is
Semi-permeable membrane with selective penetrated property.In membrane module dehumidifier, air and dehumidification solution are isolated by semi-permeable membrane.The film has choosing
Permeability is selected, the transmission of vapor is only allowed, and prevents the infiltration of other gases and liquid.Air stream and solution stream can pass through
Film carries out the exchange of heat and vapor, to realize dehumidifying.Membrane contactor has high efficiency, no condensation of liquid water, low energy consumption
The advantages of with by solution energy storage, it has been widely used in liquid drier air dewetting, and has obtained a very large progress and extensively
General engineer application.
Drier has very high affinity to water, can nearby absorb water vapour from it.In desiccant cooling cycle,
Drier reduces the humidity of air by absorbing the moisture in air, then such as by conventional cooling coil or other component
Devaporizer reduces air themperature.However, absorbing the dehumidification solution concentration of moisture reduces, need to concentrate in a regenerator,
Heat for desiccant regeneration represents the relevant maximum capacity demand of liquid dehumidification system.
In daily life and industrial processes, a large amount of places need to obtain hot fluid or increase environment temperature, also have
A large amount of places need to obtain dry air or gas humidity are controlled in a certain range.People will often use and have a single function
The needs of heat pump and dehumidifier are to meet heating and dehumidifying, purchase two complete equipments could meet the needs of different, there are it is of high cost,
The problem of taking up a large area, the waste for bringing inconvenience in this way and be easy to causeing on material and the energy.
Utility model content
The purpose of this utility model is that for deficiency in the prior art, provide a kind of air spiral type film dehumidifier,
Ion-exchange device and its dehumidifying heating system, heating and the dehumidification of people are met with same complete equipment simultaneously.
To achieve the above object, the utility model uses following technical scheme：
A kind of air spiral type film dehumidifier, including air dewetting chamber, the first solution cavity and the second solution cavity；The air
The chamber that dehumidifies is in hollow cylindrical shape, and first solution cavity and the second solution cavity are connected to two ends of air dewetting chamber
Outside face；In the inside of air dewetting chamber, there is multiple axially disposed hollow-fibre membrane tube banks, the multiple doughnut
Membrane tube bundle is connected between two end faces of air dewetting chamber, and the first solution cavity and the second solution cavity are connected to；
First solution cavity is equipped with solution inlet, and second solution cavity is equipped with taphole；Dehumidification solution from
The solution inlet of first solution cavity flows into, and is restrained by the multiple hollow-fibre membrane, the second solution cavity is flowed into, by the second solution
The taphole of chamber flows out；
The air dewetting chamber is equipped with air intake close to the side of the second solution cavity adjacent one end, and air dewetting chamber is close
The air outlet slit being connected to outside is equipped in the middle part of the end face of first solution cavity one end；Humid air is blown into from air intake, is passed through
After hollow-fibre membrane tube bank dehumidifying in air dewetting chamber, by the air that air outlet slit blowout is dry.
Further, the airintake direction of the air intake and the side of air dewetting chamber are tangent.
Further, the hollow-fibre membrane tube bank is arranged in order from inside to outside centered on the axle center of air dewetting chamber
At N number of regular hexagon；Wherein, the distance between two hollow-fibre membrane tube banks of arbitrary neighborhood are equal so that arbitrary three phases
Adjacent hollow-fibre membrane tube bank constitutes an equilateral triangle.
Further, multiple hollow-fibre membranes tube bank of air dewetting intracavitary is divided into N groups, each group of hollow fiber film tube
Shu Jun surrounds M circle Concentric circle arrays successively from inside to outside centered on the axle center of air dewetting chamber；The N groups hollow fiber film tube
Also arrangement forms concentric circles to beam successively from inside to outside；
In the M circle Concentric circle arrays that empty fiber membrane tube bank arrangement is formed in the same set, in arranging in each circular array
Empty fiber membrane tube bank quantity is equal, and the hollow-fibre membrane tube bank in each circular array is uniformly distributed；Wherein, two adjacent rings are hollow
Mutually be staggered certain rotation angle between fiber membrane tube bundle so that in the tube bank of any hollow-fibre membrane on outer ring and inner ring with its
Immediate two hollow-fibre membranes tube bank constitutes isosceles triangle；
In adjacent two groups of hollow-fibre membranes tube bank, the quantity that the hollow-fibre membrane positioned at outer ring is restrained is to be located at inner ring
Twice of quantity of hollow-fibre membrane tube bank.
Further, 3≤N≤8, M=4.
A kind of Ion-exchange device of dehumidification solution, the Ion-exchange device by pipeline respectively with the first liquid storage
Tank and the second fluid reservoir connect, and are respectively provided with dehumidification solution in first fluid reservoir and the second fluid reservoir, the electrodialysis is again
Generating apparatus includes power supply, positive plate and negative plate, and the positive plate is electrically connected to the anode of power supply, and the negative plate is electrically connected to
The cathode of power supply；Reaction tank is provided between the positive plate and negative plate, the reaction tank is by being parallel to positive plate and cathode
Multiple amberplexes of plate arrangement are partitioned into multiple reaction warehouses；
Wherein, the amberplex includes cation-exchange membrane and anion-exchange membrane, the cation-exchange membrane and
Anion-exchange membrane alternate intervals arrange, and are anion-exchange membrane closest to anode plate, are cation closest to cathode plate
Exchange membrane；There are one cation-exchange membranes, each adjacent two cation to exchange for setting between each adjacent two anion-exchange membrane
There are one anion-exchange membranes for setting between film；
In the multiple reaction warehouse, if the side wall close to anode plate side is cation-exchange membrane, close to cathode plate side
Side wall be anion-exchange membrane, then the reaction warehouse be concentrated solution retain storehouse；If the side wall close to anode plate side is anion
Exchange membrane, the side wall close to cathode plate side are cation-exchange membrane, then the reaction warehouse is that weak solution retains storehouse；
Each concentrated solution retains storehouse and is connected to the circulation loop to form closure with the first fluid reservoir by pipeline respectively, each dilute
Solution retains storehouse and is connected to the circulation loop to form closure with the second fluid reservoir by pipeline respectively.
Further, the power supply is solar-energy photo-voltaic cell.
A kind of dehumidifying heating system, including above-described air spiral type film dehumidifier and Ion-exchange device；
Further include the first fluid reservoir, the second fluid reservoir and absorption heat pump；In first fluid reservoir and the second fluid reservoir
It is respectively provided with dehumidification solution；
The solution inlet of the air spiral type film dehumidifier is connected to the first fluid reservoir, air spiral type film dehumidifier
Taphole is connected to the second fluid reservoir, and the first fluid reservoir and the second fluid reservoir are connected to the Ion-exchange device respectively；
The absorption heat pump is connected between the first fluid reservoir and the second fluid reservoir；
Dehumidification solution in first fluid reservoir after air spiral type film dehumidifier and absorption heat pump, is flowed into respectively
Second fluid reservoir；Dehumidification solution in second fluid reservoir is flowed into the first fluid reservoir after Ion-exchange device.
Further, the absorption heat pump includes heat pump absorber, third fluid reservoir and heat exchanger；The heat pump is inhaled
It receives device and heat exchanger is sequentially connected between the first fluid reservoir and the second fluid reservoir, heat pump absorber also connects with third fluid reservoir
It is logical to form the circulation line being closed；Water is housed in third fluid reservoir.
Further, further include air blower, the air intake that the air blower is set to air spiral type film dehumidifier goes out,
For the tangential direction along air dewetting chamber, air to be dehumidified is blown into air intake.
Air spiral type film dehumidifier provided by the utility model realizes sky using the distribution of simple and effective space structure
The dehumidification function of gas, Ion-exchange device provided by the utility model then can be in the case of not consumption of calorie to using
Dehumidification solution carry out concentration regeneration.And dehumidifying heating system provided by the utility model, then above-described air is spiraled
Type film dehumidifier and Ion-exchange device are linked into same system, in the case of not consumption of calorie, to air spiral type
The used dehumidification solution of film dehumidifier carries out circular regeneration；Further, it is also possible to generate additional heat using dehumidification solution, transport
Heating and the dehumidification for meeting people simultaneously with same complete equipment, have extensive market prospects.
Description of the drawings
Fig. 1 is a kind of structural schematic diagram for air spiral type film dehumidifier that the utility model embodiment one provides.
Fig. 2 is the first arrangement mode schematic diagram of the hollow-fibre membrane tube bank of the utility model embodiment one.
Fig. 3 is second of arrangement mode schematic diagram of the hollow-fibre membrane tube bank of the utility model embodiment one.
Fig. 4 is a kind of operation principle of the Ion-exchange device for dehumidification solution that the utility model embodiment two provides
Figure.
Fig. 5 is a kind of structural schematic diagram for dehumidifying heating system that the utility model embodiment three provides.
Reference numeral：
1 air dewetting chamber of air intake, 2 air outlet slit 3
First 41 second solution cavity of solution cavity, 42 solution inlet 5
6 negative plate of taphole, 7 first fluid reservoir 8
9 power supply of cation-exchange membrane, 10 anion-exchange membrane 11
Dehumidification solution cation 12 second fluid reservoir, 13 positive plate 14
15 concentrated solution of dehumidification solution anion retains 16 air spiral type film dehumidifier 17 of storehouse
18 heat exchanger of air blower, 19 Ion-exchange device 20
21 heat pump absorber of third fluid reservoir, 22 hollow-fibre membrane tube bank 23
Specific implementation mode
The technical solution of the utility model is described in detail below in conjunction with attached drawing and specific embodiment.
Embodiment one
As shown in Figure 1 to Figure 3, the utility model embodiment provides a kind of air spiral type film dehumidifier comprising empty
Gas dehumidifying chamber 2, the first solution cavity 41 and the second solution cavity 42；The air dewetting chamber 2 be in hollow cylindrical shape, described first
Solution cavity 41 and the second solution cavity 42 are connected to outside two end faces of air dewetting chamber 2；In air dewetting chamber 2
There are multiple axially disposed hollow-fibre membrane tube banks 23, the multiple hollow-fibre membrane tube bank 23 to be connected to air and remove in portion
Between two end faces of wet chamber 2, the first solution cavity 41 is connected to the second solution cavity 42.
Specifically, first solution cavity 41 is equipped with solution inlet 5, and second solution cavity 42 is equipped with taphole
6；Dehumidification solution is flowed into from the solution inlet 5 of the first solution cavity 41, is restrained 23 by the multiple hollow-fibre membrane, is flowed into second
Solution cavity 42 is flowed out by the taphole 6 of the second solution cavity 42.
The air dewetting chamber 2 is equipped with air intake 1, air dewetting chamber close to the side of 42 adjacent one end of the second solution cavity
2 are equipped with the air outlet slit 3 being connected to outside in the middle part of the end face of 41 one end of the first solution cavity；Humid air is from air intake 1
It is blown into, after 23 dehumidifying of hollow-fibre membrane tube bank in air dewetting chamber 2, dry air is blown out by air outlet slit 3.
As an improvement, the airintake direction of the air intake 1 and the side of air dewetting chamber 2 are tangent.
Further, two kinds of feasible hollow-fibre membrane tube bank arrangement modes are present embodiments provided, it is specific such as Fig. 2 and figure
Shown in 3.It should be noted that for the ease of clearly displaying the arranging rule of hollow-fibre membrane tube bank 23, do not have in Fig. 2 and Fig. 3
Whole tube banks are drawn, avoid information in figure excessively intensive；Meanwhile in order to enable arranging rule be more clear it is clear, in figure also
Auxiliary line is increased, related auxiliary line is used to explain the arranging rule of hollow-fibre membrane tube bank 23, and not objective reality is specific
Structure should not constitute the scope of protection of the utility model and limit.
Specifically, the first arrangement mode is as shown in Fig. 2, multiple hollow-fibre membranes in air dewetting chamber 2 restrain 23 points
At N groups, each group of hollow-fibre membrane tube bank 23 surrounds M circles successively from inside to outside centered on the axle center of air dewetting chamber 2
Concentric circle array；Also arrangement forms concentric circles successively from inside to outside for the N groups hollow-fibre membrane tube bank 23；
In the M circle Concentric circle arrays that 23 arrangement of empty fiber membrane tube bank is formed in the same set, arrange in each circular array
23 quantity of hollow-fibre membrane tube bank are equal, and the hollow-fibre membrane tube bank 23 in each circular array is uniformly distributed；Wherein, adjacent two
Mutually be staggered certain rotation angle between circle hollow-fibre membrane tube bank 23 so that any hollow-fibre membrane on outer ring restrains 23 Hes
On inner ring isosceles triangle is constituted with its immediate two hollow-fibre membranes tube bank 23；
Further, in adjacent two groups of hollow-fibre membranes tube bank 23, it is located at the hollow-fibre membrane tube bank 23 of outer ring
Quantity is twice of the quantity of the hollow-fibre membrane tube bank 23 positioned at inner ring.
In the utility model embodiment, in the group number N of hollow-fibre membrane tube bank 23 and every group of hollow-fibre membrane tube bank 23
Including number of turns M meet the following conditions：3≤N≤8, M=4.
Second of arrangement mode is as shown in figure 3, hollow-fibre membrane tube bank 23 with the axle center of air dewetting chamber 2 is
The heart is arranged in order into N number of regular hexagon from inside to outside；Wherein, the distance between two hollow-fibre membrane tube banks 23 of arbitrary neighborhood
It is equal so that arbitrary three adjacent hollow-fibre membrane tube banks 23 constitute an equilateral triangle.
What is needed to pay attention to is that in above two arrangement mode, the arrangement side with isosceles triangular structure is all used
Formula, the benefit of this arrangement mode are the flow directions that can guide air in air dewetting chamber 2, and sky is blown into conjunction with tangential direction
The mode of gas can make air plunder hollow fiber film tube 23 2 inside turn of air dewetting chamber is horizontal, more efficiently dehumidify.
When air spiral type film dehumidifier work provided in this embodiment, dehumidification solution is molten from the inflow first of solution inlet 5
Sap cavity 4 then flows through in hollow-fibre membrane tube bank 23, is absorbed outside tube wall by the selective penetrated property of hollow-fibre membrane tube bank 23
Then vapor flows into the second solution cavity 42 of lower part, is finally flowed out by taphole 6；Meanwhile pending drying process
Air is blown by air intake 1, each hollow-fibre membrane tube bank 23 is plunderred 2 inside turn of air dewetting chamber is horizontal, by the air of dehumidifying
Finally the air outlet slit 3 from central upper portion is blown out.
In the present embodiment, the dehumidification solution is water imbibition solution LiCl solution, and certain density solution equilibria water steams
The steam partial pressure of pure water flow surface is small under vapour intrinsic standoff ratio certain temperature, these solution have strong water suction as water absorbing agent
Property.The moisture in air can be quickly absorbed, is dehumidified to air.
Embodiment two
As shown in figure 4, the utility model embodiment provides a kind of Ion-exchange device of dehumidification solution.The electric osmose
Analysis regenerating unit is connect with the first fluid reservoir 8 and the second fluid reservoir 13 respectively by pipeline, and first fluid reservoir 8 and second stores up
It is respectively provided with dehumidification solution in flow container 13, it is however generally that, the dehumidification solution in the first fluid reservoir 8 is the higher solution of concentration, the
Two fluid reservoirs 13 are the lower solution of concentration after use.
Specifically, the Ion-exchange device includes power supply 10, positive plate 14 and negative plate 7,14 electricity of the positive plate
It is connected to the anode of power supply 10, the negative plate 7 is electrically connected to the cathode of power supply 10；Between the positive plate 14 and negative plate 7
Be provided with reaction tank, the reaction tank by be parallel to multiple amberplexes that positive plate 14 and negative plate 7 arrange be partitioned into it is more
A reaction warehouse.
Wherein, the amberplex includes cation-exchange membrane 9 and anion-exchange membrane 11, and cation-exchange membrane 9 is permitted
Perhaps cation permeable and prevent anion-permeable, anion-exchange membrane 11 allow anion-permeable and prevent cation permeable.
In reaction tank, the cation-exchange membrane 9 and the arrangement of 11 alternate intervals of anion-exchange membrane, wherein closest
The amberplex of anode plate 14 is anion-exchange membrane 11, and the amberplex closest to cathode plate 7 is cation-exchange membrane
9；There are one cation-exchange membrane 9, each adjacent two cation-exchange membranes 9 for setting between each adjacent two anion-exchange membrane 11
Between setting there are one anion-exchange membrane 11.
In the multiple reaction warehouse, if the side wall close to 14 side of anode plate is cation-exchange membrane 9, close to cathode plate 7
The side wall of side is anion-exchange membrane 11, then the reaction warehouse is that concentrated solution retains storehouse 16；If the side close to 14 side of anode plate
Wall is anion-exchange membrane 11, and the side wall close to 7 side of cathode plate is cation-exchange membrane 9, then the reaction warehouse is protected for weak solution
Stay storehouse.Each concentrated solution retains storehouse 16 and is connected to the circulation loop for being formed and being closed with the first fluid reservoir 8 by pipeline respectively, each dilute
Solution retains storehouse and is connected to the circulation loop for being formed and being closed with the second fluid reservoir 13 by pipeline respectively.
As an improvement, in the present embodiment, the power supply 10 is solar-energy photo-voltaic cell so that Ion-exchange device has
Standby more environmentally-friendly energy source, need not consume additional Intranet resource.
In the present embodiment, it is that driving carries out electrodialysis with solar-energy photo-voltaic cell, is under DC electric field effect, with current potential
Difference is that power is separated electrolyte from solution using the selective penetrated property of amberplex.Specifically, the present embodiment
When the Ion-exchange device work of offer, under the direct-current electrical field driving of power supply 10, deposited between positive plate 14 and negative plate 7
In potential difference, promotes weak solution to retain the dehumidification solution cation 12 in storehouse and move to 7 direction of negative plate and handed over by cation
It changes film 9 and enters concentrated solution reservation storehouse 16；Meanwhile weak solution retains the dehumidification solution anion 15 in storehouse and is transported to 14 direction of positive plate
It moves and concentrated solution is entered by anion-exchange membrane 11 and retains storehouse 16, rise to make concentrated solution retain solution concentration in storehouse 16,
Concentrated solution retains regenerated concentrated solution in storehouse 16 and is output in the first fluid reservoir 8 by pipeline, and weak solution retains diluted in storehouse
Dehumidification solution then flows back into the second fluid reservoir 13；And closest in the reaction warehouse of positive plate 14 then since reaction generates chlorine,
Closest to, then since reaction generates hydrogen, the liquid in the two reaction warehouses is not required to be recycled to first in the reaction warehouse of negative plate 7
In fluid reservoir 8 or the second fluid reservoir 13.
Embodiment three
As shown in figure 5, the utility model embodiment provides a kind of dehumidifying heating system comprising empty described in embodiment one
Ion-exchange device 20 described in gas spiral type film dehumidifier 17 and embodiment two further includes the first fluid reservoir 8, the second liquid storage
Tank 13 and absorption heat pump；It is respectively provided with dehumidification solution in first fluid reservoir, 8 and second fluid reservoir 13.
Specifically, the solution inlet 5 of the air spiral type film dehumidifier 17 is connected to the first fluid reservoir 8, and air spirals
The taphole 6 of type film dehumidifier 17 is connected to the second fluid reservoir 13, the first fluid reservoir 8 and the second fluid reservoir 13 respectively with it is described
Ion-exchange device 20 is connected to；The absorption heat pump is connected between the first fluid reservoir 8 and the second fluid reservoir 13.
The absorption heat pump includes heat pump absorber 22, third fluid reservoir 21 and heat exchanger 19；The heat pump absorbs
Device 22 and heat exchanger 19 are sequentially connected between the first fluid reservoir 8 and the second fluid reservoir 13, and heat pump absorber 22 is gone back and third
The connection of fluid reservoir 21 forms the circulation line being closed；Water is housed in third fluid reservoir 21.
As an improvement, dehumidifying heating system provided in this embodiment further includes air blower 18, the air blower 18 is set to
The air intake 1 of air spiral type film dehumidifier 17 goes out, and for the tangential direction along air dewetting chamber 2, is blown into air intake 1
Air to be dehumidified.
When work, the dehumidification solution in the first fluid reservoir 8 passes through air spiral type film dehumidifier 17 and absorption type heat respectively
After pump, it is flowed into the second fluid reservoir 13；Dehumidification solution in second fluid reservoir 13 is flowed into after Ion-exchange device 20
First fluid reservoir 8.
Specifically, at work, the concentrated solution in the first fluid reservoir 8 is pumped dehumidifying heating system provided by the utility model
Enter in air spiral type film dehumidifier 17, flows into hollow-fibre membrane tube bank 23 and dehumidify, and external environment fresh air is by air blast
Machine 17 blasts in air spiral type film dehumidifier 17, and then dry air can be input to indoor ring after the blowout of air outlet slit 3
Border.And the dehumidification solution after dehumidifying absorbs vapor so that concentration is lower, and is imported in the second fluid reservoir 13 and remains to carry out
Regeneration；When heat pump absorber 22 works, the water in third fluid reservoir 21 flows into heat pump absorber 22, while the first fluid reservoir 8
In concentrated solution enter in heat pump absorber 22, temperature increases after solution absorbs vapor, and part in heat pump absorber 22
Water evaporation heat absorption reduces to unevaporated coolant-temperature gage, pyrosol flow through heat exchanger 19 and user need the fluid heated into
To be used, the weak solution for absorbing vapor is also imported into the second fluid reservoir 13 for row heat exchange.When regeneration, the second liquid storage
Weak solution in tank 13, which flows into Ion-exchange device 20, to be regenerated, and the concentrated solution after regeneration flows into the first fluid reservoir 8
It is stored, completes the cycle of entire dehumidifying heating system.
Above-described embodiments merely represent several embodiments of the utility model, the description thereof is more specific and detailed,
But it should not be understood as limiting the scope of the patent of the utility model.It should be pointed out that for the common of this field
For technical staff, without departing from the concept of the premise utility, various modifications and improvements can be made, these all belong to
In the scope of protection of the utility model.Therefore, the protection domain of the utility model patent should be determined by the appended claims.
Claims (10)
1. a kind of air spiral type film dehumidifier, which is characterized in that including air dewetting chamber, the first solution cavity and the second solution
Chamber；The air dewetting chamber is in hollow cylindrical shape, and first solution cavity and the second solution cavity are connected to air and remove
Outside two end faces of wet chamber；In the inside of air dewetting chamber, there are multiple axially disposed hollow-fibre membrane tube banks, it is described
Multiple hollow-fibre membrane tube banks are connected between two end faces of air dewetting chamber, and the first solution cavity and the second solution cavity are connected
It is logical；
First solution cavity is equipped with solution inlet, and second solution cavity is equipped with taphole；Dehumidification solution is from first
The solution inlet of solution cavity flows into, and is restrained by the multiple hollow-fibre membrane, the second solution cavity is flowed into, by the second solution cavity
Taphole flows out；
The air dewetting chamber is equipped with air intake close to the side of the second solution cavity adjacent one end, and air dewetting chamber is close to first
The air outlet slit being connected to outside is equipped in the middle part of the end face of solution cavity one end；Humid air is blown into from air intake, by air
After hollow-fibre membrane tube bank dehumidifying in dehumidifying chamber, by the air that air outlet slit blowout is dry.
2. air spiral type film dehumidifier according to claim 1, which is characterized in that the airintake direction of the air intake
It is tangent with the side of air dewetting chamber.
3. air spiral type film dehumidifier according to claim 1, which is characterized in that the hollow-fibre membrane tube bank is with sky
Centered on the axle center of gas dehumidifying chamber, it is arranged in order into N number of regular hexagon from inside to outside；Wherein, two doughnuts of arbitrary neighborhood
The distance between membrane tube bundle is equal so that arbitrary three adjacent hollow-fibre membrane tube banks constitute an equilateral triangle.
4. air spiral type film dehumidifier according to claim 1, which is characterized in that air dewetting intracavitary it is multiple hollow
Fiber membrane tube bundle is divided into N groups, each group of hollow-fibre membrane restrain centered on the axle center of air dewetting chamber from inside to outside according to
It is secondary to surround M circle Concentric circle arrays；Also arrangement forms concentric circles successively from inside to outside for the N groups hollow-fibre membrane tube bank；
The M that empty fiber membrane tube bank arrangement is formed in the same set is enclosed in Concentric circle array, the hollow fibre arranged in each circular array
Dimension membrane tube bundle quantity is equal, and the hollow-fibre membrane tube bank in each circular array is uniformly distributed；Wherein, two adjacent rings doughnut
Mutually be staggered certain rotation angle between membrane tube bundle so that is most connect with it in the tube bank of any hollow-fibre membrane and inner ring on outer ring
Close two hollow-fibre membranes tube bank constitutes isosceles triangle；
In adjacent two groups of hollow-fibre membranes tube bank, the quantity that the hollow-fibre membrane positioned at outer ring is restrained is located in inner ring
Twice of the quantity of empty fiber membrane tube bank.
5. air spiral type film dehumidifier according to claim 4, which is characterized in that 3≤N≤8, M=4.
6. a kind of Ion-exchange device of dehumidification solution, the Ion-exchange device by pipeline respectively with the first fluid reservoir
It is connected with the second fluid reservoir, is respectively provided with dehumidification solution in first fluid reservoir and the second fluid reservoir, which is characterized in that described
Ion-exchange device includes power supply, positive plate and negative plate, and the positive plate is electrically connected to the anode of power supply, the negative plate
It is electrically connected to the cathode of power supply；Reaction tank is provided between the positive plate and negative plate, the reaction tank is by being parallel to anode
Plate and multiple amberplexes of negative plate arrangement are partitioned into multiple reaction warehouses；
Wherein, the amberplex includes cation-exchange membrane and anion-exchange membrane, the cation-exchange membrane and it is cloudy from
Proton exchange alternate intervals arrange, and are anion-exchange membrane closest to anode plate, are that cation exchanges closest to cathode plate
Film；Setting is there are one cation-exchange membrane between each adjacent two anion-exchange membrane, each adjacent two cation-exchange membrane it
Between setting there are one anion-exchange membrane；
In the multiple reaction warehouse, if the side wall close to anode plate side is cation-exchange membrane, the side close to cathode plate side
Wall is anion-exchange membrane, then the reaction warehouse is that concentrated solution retains storehouse；If the side wall close to anode plate side is anion exchange
Film, the side wall close to cathode plate side are cation-exchange membrane, then the reaction warehouse is that weak solution retains storehouse；
Each concentrated solution retains storehouse and is connected to the circulation loop to form closure, each weak solution with the first fluid reservoir by pipeline respectively
Retain storehouse and is connected to the circulation loop to form closure with the second fluid reservoir by pipeline respectively.
7. Ion-exchange device according to claim 6, which is characterized in that the power supply is solar-energy photo-voltaic cell.
8. a kind of dehumidifying heating system, which is characterized in that including any air spiral type film dehumidifying of claim 1 to 5
Device further includes any Ion-exchange device of claim 6 to 7；
Further include the first fluid reservoir, the second fluid reservoir and absorption heat pump；In first fluid reservoir and the second fluid reservoir respectively
Equipped with dehumidification solution；
The solution inlet of the air spiral type film dehumidifier is connected to the first fluid reservoir, the solution of air spiral type film dehumidifier
Outlet is connected to the second fluid reservoir, and the first fluid reservoir and the second fluid reservoir are connected to the Ion-exchange device respectively；It is described
Absorption heat pump is connected between the first fluid reservoir and the second fluid reservoir；
Dehumidification solution in first fluid reservoir after air spiral type film dehumidifier and absorption heat pump, is flowed into second respectively
Fluid reservoir；Dehumidification solution in second fluid reservoir is flowed into the first fluid reservoir after Ion-exchange device.
9. dehumidifying heating system according to claim 8, which is characterized in that the absorption heat pump includes that heat pump absorbs
Device, third fluid reservoir and heat exchanger；The heat pump absorber and heat exchanger are sequentially connected to the first fluid reservoir and the second storage
Between flow container, heat pump absorber is also connected to the circulation line to form closure with third fluid reservoir；Water is housed in third fluid reservoir.
10. dehumidifying heating system according to claim 8, which is characterized in that further include air blower, the air blower setting
Go out in the air intake of air spiral type film dehumidifier, for the tangential direction along air dewetting chamber, is blown into and waits for air intake
The air of dehumidifying.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820099069.8U CN208032258U (en) | 2018-01-19 | 2018-01-19 | Air spiral type film dehumidifier, Ion-exchange device and its dehumidifying heating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820099069.8U CN208032258U (en) | 2018-01-19 | 2018-01-19 | Air spiral type film dehumidifier, Ion-exchange device and its dehumidifying heating system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208032258U true CN208032258U (en) | 2018-11-02 |
Family
ID=63953817
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820099069.8U Withdrawn - After Issue CN208032258U (en) | 2018-01-19 | 2018-01-19 | Air spiral type film dehumidifier, Ion-exchange device and its dehumidifying heating system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208032258U (en) |
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 |
-
2018
- 2018-01-19 CN CN201820099069.8U patent/CN208032258U/en not_active Withdrawn - After Issue
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 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108187459A (en) | Air spiral type film dehumidifier, Ion-exchange device and its dehumidifying heating system | |
| CN106906874B (en) | Island air water fetching device and its method for fetching water | |
| Cheng et al. | Review of solar regeneration methods for liquid desiccant air-conditioning system | |
| CN206055832U (en) | The solar energy solution dehumidification system of unit is cooled down for double flash evaporation | |
| WO2014181898A1 (en) | Large-capacity electric power storage system using thermal energy/chemical potential | |
| CN106935886A (en) | A kind of gases humidification apparatus | |
| CN102149980A (en) | Liquid desiccant dehumidification system and heat /mass exchanger therefor | |
| CN205351583U (en) | Heat pump driven hollow fiber membrane liquid dehydrating unit | |
| CN104083994A (en) | High-voltage discharge air dehumidification device based on electrodialysis | |
| CN208032258U (en) | Air spiral type film dehumidifier, Ion-exchange device and its dehumidifying heating system | |
| CN111473431A (en) | Solar dehumidification system for underground space | |
| CN212832916U (en) | High-salinity wastewater purification device | |
| CN105299783A (en) | Solar-driven solution membrane concentration and solution dehumidification device and dehumidification method | |
| CN103316569B (en) | The method and apparatus of a kind of magnetic field-intensification solid dehumidifying and regeneration | |
| CN113526598A (en) | Interface evaporation device and method for strong brine | |
| CN203400623U (en) | Magnetic field enhanced solid dehumidification and regeneration device | |
| CN207277427U (en) | Island air water fetching device | |
| CN105174338B (en) | Optically focused heats multiple-effect backheat matrix form air wetting dehumidification type solar energy sea water desalination apparatus | |
| CN206560796U (en) | A kind of hollow fiber film assembly | |
| CN206291383U (en) | A kind of twin-stage solar energy solution dehumidification system that unit is cooled down for double flash evaporation | |
| CN205676175U (en) | A kind of device for preparing drinking water | |
| CN104949544B (en) | A kind of electric osmose formula total-heat exchanger | |
| CN106895507A (en) | A kind of control device directly dehumidified based on graphene oxide EDBM air | |
| CN203990266U (en) | A kind of based on electrodialytic electrion air dehumidifier | |
| CN102757102B (en) | Method and device for desalting seawater or brackish water |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20181102 Effective date of abandoning: 20240116 |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20181102 Effective date of abandoning: 20240116 |
|
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |