CN105890057A - Multi-phase exchange purification treatment module - Google Patents
Multi-phase exchange purification treatment module Download PDFInfo
- Publication number
- CN105890057A CN105890057A CN201610303830.0A CN201610303830A CN105890057A CN 105890057 A CN105890057 A CN 105890057A CN 201610303830 A CN201610303830 A CN 201610303830A CN 105890057 A CN105890057 A CN 105890057A
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- Prior art keywords
- sieve plate
- plate
- shell
- air
- treatment module
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- 238000000746 purification Methods 0.000 title claims abstract description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000007921 spray Substances 0.000 claims abstract description 17
- 238000000034 method Methods 0.000 claims description 21
- 230000008569 process Effects 0.000 claims description 17
- 239000000463 material Substances 0.000 claims description 15
- 230000001857 anti-mycotic effect Effects 0.000 claims description 8
- 230000002421 anti-septic effect Effects 0.000 claims description 8
- 239000002543 antimycotic Substances 0.000 claims description 8
- 238000006555 catalytic reaction Methods 0.000 claims description 8
- 238000005245 sintering Methods 0.000 claims description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- 230000003647 oxidation Effects 0.000 claims description 6
- 238000007254 oxidation reaction Methods 0.000 claims description 6
- 239000011248 coating agent Substances 0.000 claims description 5
- 238000000576 coating method Methods 0.000 claims description 5
- 229910052581 Si3N4 Inorganic materials 0.000 claims description 4
- 239000003973 paint Substances 0.000 claims description 4
- 229920002635 polyurethane Polymers 0.000 claims description 4
- 239000004814 polyurethane Substances 0.000 claims description 4
- 229910010271 silicon carbide Inorganic materials 0.000 claims description 4
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 claims description 4
- 238000005507 spraying Methods 0.000 claims description 4
- 239000004575 stone Substances 0.000 claims description 4
- 239000000377 silicon dioxide Substances 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims 1
- 229910052782 aluminium Inorganic materials 0.000 claims 1
- 239000004411 aluminium Substances 0.000 claims 1
- 238000007598 dipping method Methods 0.000 claims 1
- 238000004887 air purification Methods 0.000 abstract description 4
- 241000490025 Schefflera digitata Species 0.000 abstract 1
- 235000015250 liver sausages Nutrition 0.000 abstract 1
- 230000001105 regulatory effect Effects 0.000 abstract 1
- 238000004140 cleaning Methods 0.000 description 16
- 239000007789 gas Substances 0.000 description 11
- 239000007788 liquid Substances 0.000 description 7
- 239000000843 powder Substances 0.000 description 6
- 238000010521 absorption reaction Methods 0.000 description 5
- 238000001802 infusion Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 4
- 239000004088 foaming agent Substances 0.000 description 4
- 230000001788 irregular Effects 0.000 description 4
- 238000012546 transfer Methods 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- 229910003460 diamond Inorganic materials 0.000 description 3
- 239000010432 diamond Substances 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical group O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 230000001954 sterilising effect Effects 0.000 description 3
- FOIXSVOLVBLSDH-UHFFFAOYSA-N Silver ion Chemical compound [Ag+] FOIXSVOLVBLSDH-UHFFFAOYSA-N 0.000 description 2
- 230000005587 bubbling Effects 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000005213 imbibition Methods 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 239000011941 photocatalyst Substances 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000004080 punching Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000001778 solid-state sintering Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 241000209140 Triticum Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 239000000443 aerosol Substances 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 238000005034 decoration Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F8/00—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
- F24F8/10—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F13/00—Details common to, or for air-conditioning, air-humidification, ventilation or use of air currents for screening
- F24F13/28—Arrangement or mounting of filters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F8/00—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
- F24F8/10—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering
- F24F8/117—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering using wet filtering
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F8/00—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
- F24F8/20—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by sterilisation
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
Abstract
A multi-phase exchange purification treatment module comprises a shell, screen plates and a water spray device. An air inlet and an air outlet are formed in the left end and the right end of the shell correspondingly, the water spray device is arranged on a top plate of the shell, and a water outlet is formed in a bottom plate of the shell. The screen plates are arranged between the air inlet and the air outlet and each provided with a three-dimensional through hole network structure or a porous structure with part of holes connected. The screen pates and the shell are fixedly connected, each screen plate and the bottom plate of the shell are arranged by an angle, and the angle is larger than 0 degree and smaller than and equal to 90 degrees. In the purification process, air passes through the screen plates from left to right, water flows through the screen plates from top to bottom, and each screen plate and the bottom plate of the shell are arranged by the angle; and by means of the multiple screen plates, multi-stage purification is achieved, the size of the module is compressed, and purification efficiency can be regulated and controlled. The module can be made into a complete air purification machine in cooperation with HEPA, a primary filter plate and other purification devices and is suitable for air purification of homes, office places, industrial environments and other places.
Description
Technical field
The present invention relates to air purification field, be specifically related to a kind of be applied to air cleaning be exchanged purified treatment mould more
Block.
Background technology
Due to industrialized fast development, various heavy motor vehicles and the increase of family expenses vehicle, China becomes in the world
Atmosphere pollution increases the weight of the country that degree is the fastest, air pollution particularly indoor pollution, has caused the continuous of various disease incidence
Rise, had a strong impact on work and the life health of people.
Time at least over half in life of people is spent in indoor, the most always, the weak group such as young, sick, residual
Body, vulnerable, outdoor activities are less, and the time spent in indoor is even as high as more than 90%.But the interior space is limited, itself
Not only there is no natural purifying ability, and due to the universal use of indoor decoration, air-conditioning etc., constantly to indoor exhaust emission
The harmful substances such as thing, the most mainly solid-state suspended particulate substance, volatile organic matter and aerosol.
At present, the cleaning principle of air purifier market sold is roughly divided into passive type adsorption filtration and purifies and active
Formula air cleaning.Passive adsorption formula typically uses HEPA filter screen+active carbon filter screen+photocatalyst+ultraviolet+Electrostatic Absorption net etc.
Reason room air, active air purifies the active such as the technology that typically uses silver ion, anion, low-temperature plasma and photocatalyst
The purifying and sterilizing factor is discharged in air.Although these modes can reach certain purification purpose, but corresponding every kind of device pin
Strong to property.Such as HEPA filter screen energy filtration of particulate matters but can not be sterilized, silver ion technology can realize sterilizing function, but can not filter solid
Body pollution thing.Therefore purification efficiency is low, in order to reach the purpose of comprehensive decontamination, needs to be applied in combination, accordingly various devices
The difficult problem that cost is high, be difficult to universal use can be produced.
It is the volatile contaminant in place's process gases and the typical process of dust using liquid as the absorption tower of dense medium purifica tion.
It is broadly divided into the liquid spray regime injected liquid in gas phase and the gas injecting operations that gas is ejected into liquid phase, mesh
Before, improve the main direction of studying that gas liquid contacting efficiency is absorption tower.The operation principle on JBR formula absorption tower is, processed
Gas is imported in the closing space being made up of upper and lower plate by playpipe and forms gas-bearing formation, and from liquid, bubbling rises, through gas
After dispersion plate or rectification tedge, the liquid that gas is carried secretly forms one by a large amount of gas constantly being formed and crushing on plate top
The continuous print bubble level of bubble composition.The mass transfer rate on JBR formula absorption tower is high, can effectively absorb in removal gas contained
Volatile contaminant, and the fine particles such as dust are also removed after contact liquid film.
CN204159341U discloses a kind of fine ga(u)ge screen plate bubble tower, and column plate is microchannel pore sieve plate, sets below column plate
Having imbibition gas-permeable nets, liquid phase is transported to imbibition gas-permeable nets, is carried secretly the microchannel pore entering column plate by air-flow from bottom to top,
Form a large amount of bubble and constantly rupture and update, trapping dust in bubbling area.The column plate limited amount can placed in this bubble tower,
It is difficult to multistage purification, in order to improve purification efficiency, it is necessary to increase effective contact area of column plate, and bubble level entirety is relatively
Greatly, cause this bubble tower volume bigger, it is impossible to be applied in the air purifier in the place such as household, office.
Summary of the invention
In order to solve the purification efficiency of heterogeneous exchange processing module in prior art and can not regulate and control, bulky problem, this
Invention provides one and is exchanged purified treatment module more, can also regulate and control purification efficiency while improving purification efficiency, pressure
The volume of contracting module, technical scheme is as follows:
Two ends, described shell left and right are respectively air inlet and air outlet, and described sheath top plate arranges water injector, described shell
Base plate arranges delivery port；
Described air inlet arranges sieve plate to air outlet, and described sieve plate has three-dimensional through hole network structure or some perforations is connected with each other
Loose structure, described sieve plate and shell are fixing to be connected and setting angled with shell bottom plate, and described angle is more than 0 ° and is less than
In 90 °.
Air enters from described air inlet, and by described sieve plate, water soaks sieve plate from described water injector, and air flows through institute
The micropore stated in sieve plate contacts with water, formed bubble and constantly rupture update thus carry out multistage purification.
Further, the longitudinal thickness of described sieve plate is 10-400mm.
Further, the distance between described sieve plate at least two, and described adjacent two sieve plates is 0-200mm.
Further, each described sieve plate has identical aperture.
Further, each described sieve plate has different apertures, and the described sieve plate of arrangement from air inlet to air outlet
Aperture is gradually reduced.Be conducive to reducing windage, improve air purification efficiency.
Further, the hole shape of same described sieve plate is irregular, and same position aperture is different, and the hole shape of sieve plate can be
Circular hole, slotted hole, square hole, delthyrium, projecting apertures, diamond hole, hexagon ring, cross bore.
Preferably, during the material of described sieve plate is aluminum oxide, silica, silicon nitride, carborundum, polyurethane, medical stone
One or more.Described sieve plate can prepare, by solid-state sintering, the irregular structure of shape of portalling, and uses aluminum oxide, oxidation
One or more powder in silicon, silicon nitride, carborundum, polyurethane make raw material, through compressing after mixing with foaming agent, whole
In individual process, powder remains solid state, and under high temperature sintering, foaming agent decomposes precipitation, causes powder expansion, burns
Loose structure is obtained after knot.
Further, described sieve plate passes through infusion process, spraying process or sintering process in its surface coating catalysis material, mildew-resistant
Sterilization material, catalysis oxidation coating, anticorrosive paint in one or more, make described sieve plate while carrying out air cleaning,
Antimycotic antiseptic and the Corrosion Protection of sieve plate can also be improved, extend the service life of sieve plate.
Further, described water injector includes spray head, and described spray head is arranged at the surface of each sieve plate.
Particularly, what the present invention provided is exchanged purified treatment module more, can coordinate HEPA, first filter plate, uviol lamp, low temperature
Other cleaning module such as plasma makes air purifier.
What the present invention provided is exchanged having the beneficial effect that of purified treatment module more:
1) in purification process, air is from left to right by sieve plate, and water flows through sieve plate, described sieve plate and shell bottom plate from top to down
Angled setting, arranges different angles according to air force, thus regulates and controls purification efficiency.
2) achieve multistage purification by the setting of multiple sieve plates, and have compressed the volume of module, be greatly enhanced heterogeneous
Exchange purification efficiency, and can according to service condition increase and decrease sieve plate number thus regulate and control purification efficiency further.
3) described that to be exchanged purified treatment module higher compared to traditional bubble tower mass-transfer efficiency is more, and volume is less, can
Coordinate other cleaning modules such as HEPA, first filter plate, uviol lamp, low temperature plasma to make air cleaning complete machine, be suitable for application in
In the air cleaning in the places such as household, office space, industrial environment.
Accompanying drawing explanation
Fig. 1 is the schematic diagram being exchanged purified treatment module of embodiment 1 more.
Fig. 2 is the front view being exchanged purified treatment module of embodiment 1 more.
Fig. 3 be embodiment 1 be exchanged sieve plate and shell bottom plate engaging fixing structure schematic diagram in purified treatment module more.
Fig. 4 is the front view being exchanged purified treatment module of embodiment 2 more.
Reference: 1 shell, 2 air inlets, 3 air outlets, 4 sheath top plate, 5 shell bottom plates, 6 delivery ports, 7 sieve plates, 8
A junction, 9 second connecting portions, 10 the 3rd connecting portions, 11 the 4th connecting portions.
Detailed description of the invention
Below by way of being specifically embodied as embodiments of the present invention are described, those skilled in the art can be by this specification
Disclosed content understands further advantage and effect of the present invention easily.
Embodiment one
One is exchanged purified treatment module, as it is shown in figure 1, include that shell 1, sieve plate 7 and water injector (are drawn the most in the drawings more
Go out).
Shell 1 left end is air inlet 2, and shell 1 right-hand member is air outlet 3, sheath top plate 4 arranges water injector, at the bottom of shell
Plate 5 arranges delivery port 6.
The internal setting with shell bottom plate of shell 1 is 90 degree of sieve plates 7 arranged, and sieve plate 7 has three-dimensional through hole network structure.As
Shown in Fig. 2, the top of sieve plate 7 and bottom are connected by snap-in structure with sheath top plate 4 and shell bottom plate 5 respectively.Concrete, as
Fig. 3 shows, sieve plate 7 bottom be one fall " convex " type the first connecting portion 8, have second connecting portion 9 of " recessed " type at shell bottom plate 5,
Together with described first connecting portion 8 is fixed with the shape complementarity of described second connecting portion 9；As in figure 2 it is shown, sieve plate 7 top
Having the 3rd connecting portion 10 of " convex " type, described sheath top plate 4 to be down the 4th connecting portion 11 of " recessed " type, the described 3rd even
Connect together with portion 10 is fixed with the shape complementarity of described 4th connecting portion 11, can freely dismantle sieve plate.
As in figure 2 it is shown, described sieve plate 7 has 4, the longitudinal thickness of sieve plate is 10mm, and described adjacent two sieve plates it
Between distance be 200mm.Sieve plate number can also be increased and decreased according to air quantity and actual conditions.The material of described sieve plate 7 is aluminum oxide,
Described sieve plate 7 prepares, by solid-state sintering, the irregular structure of shape of portalling, and uses alumina powder to make raw material, mixes with foaming agent
Through compressing after conjunction, in whole process, powder remains solid state, and under high temperature sintering, foaming agent decomposes analysis
Go out, cause powder expansion, after sintering, obtain that there is the loose structure that some perforations is connected with each other.The material of described sieve plate is all right
It is one or more in silica, silicon nitride, carborundum, polyurethane, medical stone.
The structure of 4 sieve plates is identical in the present embodiment, is three-dimensional through hole network structure, and hole shape is irregular, and same
Aperture, position is different.As the deformation of the present embodiment, it is identical that sieve plate can also prepare aperture by the method for punching press, Kong Xinggui
Then, the structure such as such as circular hole, slotted hole, square hole, delthyrium, projecting apertures, diamond hole, hexagon ring, cross bore, it is also possible to be aperture not
With, the sieve plate of hole shape rule is arranged in order.
Sieve plate 7 coats antimycotic antiseptic material by infusion process on its surface, makes described sieve plate carry out the same of air cleaning
Time, moreover it is possible to improve the antimycotic antiseptic performance of sieve plate, extend the service life of sieve plate.Sieve plate 7 surface can also by infusion process or
Spraying process or sintering process coat the one or several in catalysis material, antimycotic antiseptic material, catalysis oxidation coating, anticorrosive paint
Kind, to reach the multiple performance such as mildew-resistant, anticorrosion.
Water injector includes spray head (being not drawn in figure), and described spray head quantity can be consistent with described sieve plate 7 quantity,
Can also be inconsistent, as long as reaching to purify institute's water requirement, and described spray head is positioned at the top of each sieve plate 7, and water is from spray
Drench head to flow out through sieve plate again from the delivery port outflow 3 of shell bottom plate.
Embodiment 1 provide the course of work being exchanged purified treatment module more as follows: air under the drive of blower fan from
Described air inlet 2 enters, and enters shell 1 internal, passes sequentially through described sieve plate 7, and water is sprayed by spray head from water injector 5 simultaneously
Going out, soak sieve plate 7, the micropore that air flows through in described sieve plate 7 contacts with water, forms bubble and constantly ruptures renewal, thus real
The multistage purification of existing air, the air after purification flows out from air outlet 3.
What the present embodiment provided be exchanged purified treatment module more can coordinate HEPA, first filter plate, uviol lamp etc. other purify
Module is made air purifier and is applied in household air cleaner.
What above example provided is exchanged the sieve plate that purified treatment module includes having three-dimensional through hole network structure more,
In purification process, air is from left to right by sieve plate, and water flows through sieve plate from top to down, and described sieve plate is angled with shell bottom plate to be set
Put, different angles is set according to air force, thus regulates and controls purification efficiency.Multistage purifying is achieved by the setting of multiple sieve plates
Change, and have compressed the volume of module, be greatly enhanced and be exchanged purification efficiency more, and sieve plate can be increased and decreased according to service condition
Number thus regulate and control purification efficiency further.Being exchanged purified treatment module compared to traditional bubble tower mass-transfer efficiency described more
Higher, volume is less, and other cleaning modules such as HEPA, first filter plate, uviol lamp, low temperature plasma can be coordinated to make air cleaning
Complete machine, is suitable for application in the air cleaning in the places such as household, office space, industrial environment.
Embodiment two
One is exchanged purified treatment module more, as shown in Figure 4, (draws the most in the drawings including shell 1, sieve plate 7 and water injector
Go out).
Shell 1 left end is air inlet 2, and shell 1 right-hand member is air outlet 3, sheath top plate 4 arranges water injector, at the bottom of shell
Plate 5 arranges delivery port 6.
Being 60 degree of sieve plates 7 arranged from internal the setting with shell bottom plate of the shell 1 of air inlet 2 to air outlet 3, sieve plate 7 has
There is the loose structure that some perforations is connected with each other.The top of sieve plate 7 and bottom are fixed with sheath top plate 4 and shell bottom plate 5 respectively
Connect.
As in figure 2 it is shown, described sieve plate 7 has 2, the longitudinal thickness of sieve plate is between 400mm, and said two sieve plate
Distance is 0mm.Fit together between two sieve plates and do not affect the purification efficiency that module is overall.The material of described sieve plate 7 is wheat
Meal stone.
The structure of 2 sieve plates is identical in the present embodiment, but is the loose structure that some perforations is connected with each other, and hole shape is not
Rule.As the deformation of the present embodiment, it is identical that sieve plate can also prepare aperture by the method for punching press, hole shape rule, such as
The structures such as circular hole, slotted hole, square hole, delthyrium, projecting apertures, diamond hole, hexagon ring, cross bore, it is also possible to be that aperture is different, hole shape
The sieve plate of rule is arranged in order.
Sieve plate 7 coats antimycotic antiseptic material by infusion process on its surface, makes described sieve plate carry out the same of air cleaning
Time, moreover it is possible to improve the antimycotic antiseptic performance of sieve plate, extend the service life of sieve plate.Sieve plate 7 surface can also by infusion process or
Spraying process or sintering process coat the one or several in catalysis material, antimycotic antiseptic material, catalysis oxidation coating, anticorrosive paint
Kind, to reach the multiple performance such as mildew-resistant, anticorrosion.
Water injector includes spray head (being not drawn in figure), and described spray head quantity can be consistent with described sieve plate 7 quantity,
Can also be inconsistent, as long as reaching to purify institute water requirement, and described spray head is positioned at the surface of each sieve plate 7, water from
Spray head flows out and flows out 3 from the delivery port of shell bottom plate again through sieve plate.
Embodiment 1 provide the course of work being exchanged purified treatment module more as follows: air under the drive of blower fan from
Described air inlet 2 enters, and enters shell 1 internal, passes sequentially through described sieve plate 7, and water is sprayed by spray head from water injector 5 simultaneously
Going out, soak sieve plate 7, the micropore that air flows through in described sieve plate 7 contacts with water, forms bubble and constantly ruptures renewal, thus real
The multistage purification of existing air, the air after purification flows out from air outlet 3.
What the present embodiment provided be exchanged purified treatment module more can coordinate HEPA, first filter plate, uviol lamp etc. other purify
Module is made air purifier and is applied in household air cleaner.
The loose structure that purified treatment module that what above example provided be exchanged more includes that some perforations is connected with each other
Sieve plate, in purification process, air is from left to right by sieve plate, and water flows through sieve plate, described sieve plate and shell bottom plate from top to down
Angled setting, arranges different angles according to air force, thus regulates and controls purification efficiency.By multiple sieve plates, realization is set
Multistage purification, and have compressed the volume of module, it is greatly enhanced and is exchanged purification efficiency more, and can according to service condition
Increase and decrease sieve plate number thus regulate and control purification efficiency further.Being exchanged purified treatment module compared to traditional bubble tower described more
Mass-transfer efficiency is higher, and volume is less, and other cleaning modules such as HEPA, first filter plate, uviol lamp, low temperature plasma can be coordinated to make
Air cleaning complete machine, is suitable for application in the air cleaning in the places such as household, office space, industrial environment.
The above, only presently preferred embodiments of the present invention, the principle of above-described embodiment only illustrative present invention and
Its effect, and not any formal and substantial to present invention restriction, it is noted that for the common skill of the art
Art personnel, on the premise of without departing from the inventive method, also can make some improvement and supplement, and these improve and supplement also
Should be regarded as protection scope of the present invention.All those skilled in the art, in the feelings without departing from the spirit and scope of the present invention
Under condition, a little change of making when available disclosed above technology contents, the equivalent variations modified and develop, it is this
The Equivalent embodiments of invention；Meanwhile, all foundation present invention obtain any equivalent variations that above-described embodiment is made by substantial technological
Change, modify and develop, all still fall within the scope of technical scheme.
Claims (10)
1. it is exchanged purified treatment module one kind, it is characterised in that include shell, sieve plate and water injector more；
Two ends, described shell left and right are respectively air inlet and air outlet, and described sheath top plate arranges water injector, described shell
Base plate arranges delivery port；
Described air inlet arranges sieve plate to air outlet, and described sieve plate has three-dimensional through hole network structure or some perforations is connected with each other
Loose structure, described sieve plate and shell are fixing to be connected and setting angled with shell bottom plate, and described angle is more than 0 ° and is less than
In 90 °；
Air enters from described air inlet, and by described sieve plate, water soaks sieve plate from described water injector, and air flows through described sieve
Micropore in plate contacts with water, formed bubble and constantly rupture update thus carry out multistage purification.
2. it is exchanged purified treatment module as claimed in claim 1, it is characterised in that the longitudinal thickness of described sieve plate is more
10-400mm。
3. it is exchanged purified treatment module as claimed in claim 1, it is characterised in that described sieve plate at least two, and institute more
Stating the distance between adjacent sieve plate is 0-200mm.
4. it is exchanged purified treatment module as claimed in claim 3, it is characterised in that each described sieve plate has identical more
Aperture.
5. it is exchanged purified treatment module as claimed in claim 3, it is characterised in that each described sieve plate has different more
Aperture, and the aperture of the described sieve plate of arrangement is gradually reduced from air inlet to air outlet.
6. it is exchanged purified treatment module as claimed in claim 3, it is characterised in that the hole shape of same described sieve plate is not advised more
Then, and same position aperture is different.
7. it is exchanged purified treatment module as claimed in claim 1, it is characterised in that the material of described sieve plate is oxidation more
One or more in aluminium, silica, silicon nitride, carborundum, polyurethane, medical stone.
8. as described in claim 1-7 is arbitrary, it is exchanged purified treatment module, it is characterised in that described sieve plate is by dipping more
Method, spraying process or sintering process are in its surface coats catalysis material, antimycotic antiseptic material, catalysis oxidation coating, anticorrosive paint
One or more.
9. it is exchanged purified treatment module as claimed in claim 1, it is characterised in that described water injector includes spray more
Head, and described spray head is arranged at the top of each sieve plate.
10. an air purifier, it is characterised in that comprise and be exchanged purified treatment more as described in claim 1-9 is arbitrary
Module.
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| CN201610303830.0A CN105890057A (en) | 2016-05-10 | 2016-05-10 | Multi-phase exchange purification treatment module |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201610303830.0A CN105890057A (en) | 2016-05-10 | 2016-05-10 | Multi-phase exchange purification treatment module |
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| CN105890057A true CN105890057A (en) | 2016-08-24 |
Family
ID=56702586
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| CN201610303830.0A Pending CN105890057A (en) | 2016-05-10 | 2016-05-10 | Multi-phase exchange purification treatment module |
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Cited By (1)
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| CN109174451A (en) * | 2018-08-15 | 2019-01-11 | 郑州莉迪亚医药科技有限公司 | A kind of Printing ink producing filter device |
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| US20110139005A1 (en) * | 2009-02-23 | 2011-06-16 | Yong Joon Kwon | Air Purifier Employing A Water Jet-Type Fan System, and Purification Method Thereof |
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