CN206103700U - Air -purifying's normal position regenerating unit and contain device's clarifier - Google Patents
Air -purifying's normal position regenerating unit and contain device's clarifier Download PDFInfo
- Publication number
- CN206103700U CN206103700U CN201620783373.5U CN201620783373U CN206103700U CN 206103700 U CN206103700 U CN 206103700U CN 201620783373 U CN201620783373 U CN 201620783373U CN 206103700 U CN206103700 U CN 206103700U
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- air
- heater
- aluminium flake
- temperature
- oxide
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Links
- 230000001172 regenerating effect Effects 0.000 title abstract description 6
- 230000008929 regeneration Effects 0.000 claims abstract description 37
- 238000011069 regeneration method Methods 0.000 claims abstract description 37
- 238000010438 heat treatment Methods 0.000 claims abstract description 33
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 62
- 238000004140 cleaning Methods 0.000 claims description 28
- 238000000746 purification Methods 0.000 claims description 10
- 239000004745 nonwoven fabric Substances 0.000 claims description 8
- 238000011068 loading method Methods 0.000 claims description 4
- 239000011229 interlayer Substances 0.000 claims description 2
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 abstract description 26
- 238000004887 air purification Methods 0.000 abstract description 2
- 239000011572 manganese Substances 0.000 description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 24
- 239000003054 catalyst Substances 0.000 description 19
- 239000002585 base Substances 0.000 description 17
- 235000010210 aluminium Nutrition 0.000 description 14
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 description 14
- 239000002002 slurry Substances 0.000 description 14
- 229910052782 aluminium Inorganic materials 0.000 description 13
- 238000011065 in-situ storage Methods 0.000 description 10
- 238000005406 washing Methods 0.000 description 9
- 239000004411 aluminium Substances 0.000 description 8
- 239000000463 material Substances 0.000 description 8
- 239000012286 potassium permanganate Substances 0.000 description 8
- 239000000243 solution Substances 0.000 description 8
- 238000010586 diagram Methods 0.000 description 7
- 239000000843 powder Substances 0.000 description 7
- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 239000004519 grease Substances 0.000 description 5
- 238000002604 ultrasonography Methods 0.000 description 5
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 4
- 239000004202 carbamide Substances 0.000 description 4
- 238000000227 grinding Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 238000000643 oven drying Methods 0.000 description 4
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 3
- 239000000853 adhesive Substances 0.000 description 3
- 230000001070 adhesive effect Effects 0.000 description 3
- 230000001476 alcoholic effect Effects 0.000 description 3
- 235000011114 ammonium hydroxide Nutrition 0.000 description 3
- 238000005119 centrifugation Methods 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 229910052748 manganese Inorganic materials 0.000 description 3
- 239000011259 mixed solution Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000003643 water by type Substances 0.000 description 3
- 238000009736 wetting Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- QPLDLSVMHZLSFG-UHFFFAOYSA-N Copper oxide Chemical compound [Cu]=O QPLDLSVMHZLSFG-UHFFFAOYSA-N 0.000 description 2
- 229930040373 Paraformaldehyde Natural products 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- VBIXEXWLHSRNKB-UHFFFAOYSA-N ammonium oxalate Chemical compound [NH4+].[NH4+].[O-]C(=O)C([O-])=O VBIXEXWLHSRNKB-UHFFFAOYSA-N 0.000 description 2
- 239000004568 cement Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000012459 cleaning agent Substances 0.000 description 2
- 238000005238 degreasing Methods 0.000 description 2
- 238000007598 dipping method Methods 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 150000004706 metal oxides Chemical class 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229910000510 noble metal Inorganic materials 0.000 description 2
- 229920002866 paraformaldehyde Polymers 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- 229910052709 silver Inorganic materials 0.000 description 2
- 238000004381 surface treatment Methods 0.000 description 2
- 230000036413 temperature sense Effects 0.000 description 2
- 239000004408 titanium dioxide Substances 0.000 description 2
- JYLNVJYYQQXNEK-UHFFFAOYSA-N 3-amino-2-(4-chlorophenyl)-1-propanesulfonic acid Chemical compound OS(=O)(=O)CC(CN)C1=CC=C(Cl)C=C1 JYLNVJYYQQXNEK-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- DQMUQFUTDWISTM-UHFFFAOYSA-N O.[O-2].[Fe+2].[Fe+2].[O-2] Chemical compound O.[O-2].[Fe+2].[Fe+2].[O-2] DQMUQFUTDWISTM-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002671 adjuvant Substances 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 239000000809 air pollutant Substances 0.000 description 1
- 231100001243 air pollutant Toxicity 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000357 carcinogen Toxicity 0.000 description 1
- 239000003183 carcinogenic agent Substances 0.000 description 1
- 238000003421 catalytic decomposition reaction Methods 0.000 description 1
- 230000001413 cellular effect Effects 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 229910000428 cobalt oxide Inorganic materials 0.000 description 1
- IVMYJDGYRUAWML-UHFFFAOYSA-N cobalt(ii) oxide Chemical compound [Co]=O IVMYJDGYRUAWML-UHFFFAOYSA-N 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 229960004643 cupric oxide Drugs 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000013527 degreasing agent Substances 0.000 description 1
- 238000005237 degreasing agent Methods 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 238000001727 in vivo Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- SQQMAOCOWKFBNP-UHFFFAOYSA-L manganese(II) sulfate Chemical compound [Mn+2].[O-]S([O-])(=O)=O SQQMAOCOWKFBNP-UHFFFAOYSA-L 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
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- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 239000012855 volatile organic compound Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
Landscapes
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
Abstract
The utility model relates to an air -purifying's normal position regenerating unit and contain device's clarifier belongs to the air purification field, its characterized in that, the device is including purifying the module and providing the heating device who purifies module regeneration the desired temperature condition. Providing a high efficiency, the indoor formaldehyde pollution's of rapid removal air purifier, but purifying the regeneration of module normal position, the filter core need not changed, no secondary pollution.
Description
Technical field
The utility model belongs to air purification field, specifically, belongs to a kind of air purifier and its cleaning module is former
Position regenerating unit.
Background technology
Living standards of the people are improved constantly, and house house fitting is increasing, however wood-based plate and its product, carpet,
Blanket liner and carpet adhesive, interior wall coating, wooden furniture, wallpaper, adhesive etc. can be to indoor release formaldehyde and VOCs (volatility
Organic matter) etc. harmful substance, serious harm human body it is healthy.Formaldehyde is a kind of common indoor air pollutants, and is had
The characteristics of having slow release, persistently pollute, is a kind of carcinogen with toxicity is stimulated, can be via suction and skin contact
Affect health.
In recent years, mainly indoor pollution is purified using air purifier, the technology of the removal formaldehyde of selection is main
The technology such as active charcoal absorption, catalyst oxidation Decomposition, photochemical catalyst catalytic decomposition.The easy saturation of activated carbon, is heated easily outwards
Desorbed contaminants, while with the problem of coefficient of recovery difference；Catalyst is typically from noble metal and metal oxide, noble metal
Typically from Pd, Au, Ag, Pt etc., reaction needs higher temperature, and catalyst easily to inactivate, and metal oxide is such as aoxidized
The removal effect of the PARA FORMALDEHYDE PRILLS(91,95)s such as silver, cupric oxide, cobalt oxide, zinc oxide, titanium dioxide, di-iron trioxide and manganese dioxide
(Atmospheric Environment 2002,36,5543-5547), it is found that manganese dioxide PARA FORMALDEHYDE PRILLS(91,95) has highest under normal temperature
Remove activity.
At present it is known that air purifier because there is adsorbent adsorption saturation, catalyst activity, need frequency
, to maintain clean-up effect, the use cost of air purifier is higher, and easily causes secondary pollution for numerous replacing clean unit.
Utility model content
The utility model is directed to problem of the prior art, proposes a kind of situ regeneration device of purify air and containing the dress
The clarifier put.The purpose of this utility model is to provide a kind of air purifier for efficiently, quickly removing Formaldehyde Pollution of Indoor Air,
Cleaning module can in-situ regeneration, filter core be not required to change, non-secondary pollution.
The technical scheme in the invention for solving the above technical problem：
A kind of situ regeneration device of purify air, it is characterised in that the device includes cleaning module and provides purification mould
Block regenerates the heater of temperature required condition.
The cleaning module is the aluminium flake for loading Mn oxide, and aluminium flake is at least a piece of；Or the nonwoven of load Mn oxide
The filter core that cloth is folded into.
The heater is heating rod, and heating rod is interspersed in aluminium flake interlayer or hole is provided with aluminium flake, and heating rod interts
In hole；Or the filter core that the non-woven fabrics of the load Mn oxide is folded into is placed in shelf brackets, heater is in shelf
Under frame；Shelf brackets are hollow, and edge has one fixed width to fix support filter core；Or above shelf brackets be strip board arranged crosswise.
The heater in shelf brackets lower end is ptc heater.
Above-mentioned situ regeneration device, the also timing means including connection on the heating are used to control heater
Working time.
A kind of air purifier of situ regeneration device, it is characterised in that also including casing, into and out of air port, chain of command
Plate, fan, fan power supply；Casing includes base, supports housing and top cover, and the inside for supporting housing is provided with draw-in groove, for fixing
Support and control component, the fan, fan power supply and air inlet are respectively positioned on situ regeneration device lower section, and air outlet is located at original position again
Generating apparatus top；The control panel is located at and supports hull outside, and control unit internal circuit is filled with fan power supply, in-situ regeneration
The heater put is connected, and power supply, Wind speed switch, plus thermal timing means are provided with outside it.
The air inlet is located at base and/or housing at least side, and air outlet is located at top cover and/or housing at least side.
The air purifier also includes being located at the temperature control unit below cleaning module, the temperature control unit bag
Temperature controller, temperature inductor, temperature inductor support are included, temperature controller internal circuit is fixed with temperature inductor and heating
When device be connected.
Description of the drawings
Fig. 1 is the utility model using load Mn oxide aluminium flake and heating rod schematic diagram；
Fig. 2 is the filter core schematic diagram that the utility model is folded into using load Mn oxide non-woven fabrics；
Fig. 3 is the shelf brackets schematic diagram of the utility model embodiment 2, and Fig. 3 a are have one fixed width for empty edge in the middle of shelf brackets
Schematic diagram；Fig. 3 b are shelf brackets middle setting strip board schematic diagram；
Fig. 4 is situ regeneration device schematic diagram of the utility model using load Mn oxide aluminium flake；
Fig. 5 contains Fig. 1 in-situ regeneration clarifier structural representations for the utility model；
Fig. 6 is the profile of Fig. 5；
Fig. 7 is the in-situ regeneration of the filter core that the utility model is folded into using load birnessite type Mn oxide non-woven fabrics
Schematic device；
Fig. 8 is using containing Fig. 7 in-situ regeneration clarifier structural representations；
Fig. 9 is the profile of Fig. 8；
Figure 10 is the utility model overall appearance schematic diagram.
Wherein：
1. the temperature controller 4. of 2. Wind speed switch of base 3. plus thermal timing means 5. switch 6.PTC heaters 7.
The housing 12. of 8. temperature inductor of temperature inductor support, 9. 10. top cover of birnessite type Mn oxide foldable filter element 11.
The perforation shelf brackets of 17. shelf brackets 18. of aluminium flake 16. of the load Mn oxide of 13. fan of fan power supply, 14. heating rod 15.
The air inlet of 20. air outlet of edge 19. strip board 21..
Specific embodiment
Below in conjunction with the accompanying drawings and by embodiment the utility model is described in further detail, and following examples are right
It is of the present utility model explanation and the utility model is not limited to following examples.
Embodiment 1
The situ regeneration device of a kind of purify air of the present utility model, as shown in figure 1, cleaning module and offer purification mould
Block regenerates the heater of temperature required condition, and cleaning module is the aluminium flake 15 for loading Mn oxide, and aluminium flake is multi-disc, in load
Uniform perforation 16 on the aluminium flake 15 of Mn oxide, heating rod 14 is interspersed in perforation 16.The present embodiment uses power 100W,
Single-end electric-heating tube (net purchase), heating rod electrified regulation realizes the regeneration of the aluminium flake of load Mn oxide.
The aluminium flake 15 of load Mn oxide can be honeycomb aluminum, and heating rod is fixed in the middle of two pieces of honeycomb aluminums, and periphery is overall
Plus frame fixed cellular aluminium and heating rod, what cleaning module was realized in heating rod energization is regeneration originally.
The aluminium flake 15 of load Mn oxide carries out purification work by being placed in the space of formaldehyde pollution, then by above-mentioned
Heater complete cleaning module in-situ regeneration.
Above-mentioned aluminium flake is one or more pieces, and to reach more preferable effect, aluminium flake can be multi-disc, and heating rod is single or many
Individual being uniformly distributed is interspersed in perforation.Aluminium flake can be the single hole of middle part, and heating rod is punctured in hole.Aluminium flake can also not have
There is hole, heater can be heating film and the aluminium flake arranged crosswise without hole.
Embodiment 2
The situ regeneration device of another kind of purify air of the present utility model, as shown in Fig. 2 the device includes cleaning module
With the heater for providing the temperature required condition of cleaning module regeneration, cleaning module is the water load sodium being placed in shelf brackets 17
The filter core 9 that the non-woven fabrics of manganese ore type Mn oxide is folded into, the present embodiment uses PTC heaters 6, power 500W, absolutely
Edge type semiconductor-air heater (commercial), under PTC heaters 6 (not shown in Fig. 2) are placed on shelf brackets；During shelf brackets are
Sky, as shown in Fig. 3 a in Fig. 3, shelf brackets edge 18 has one fixed width to fix support filter core；Or shelf brackets are that strip board 19 is handed over
The arrangement of fork, as shown in Fig. 3 b in Fig. 3.
The device carries out purification work by being placed in the space of formaldehyde pollution, and PTC heaters 6 are powered when needed
The in-situ regeneration of cleaning module is realized in heating.
Embodiment 3
Air purifier containing the situ regeneration device of embodiment 1, as Figure 4-Figure 6.Increase on the basis of embodiment 1
Housing 11, base 1, top cover 10, air inlet 21, air outlet 20, control panel, fan 13, fan power supply 12；The shell of the present embodiment
11 points of body is upper and lower two parts, and housing is made using ABS plastic material, and in the inside of housing draw-in groove is provided with, fixed to support purification
Each component of device.Have on base 1 under air inlet 21, base and pawl is installed, it is ensured that the air intake space of air inlet.Fan 13,
Fan power supply 12 is arranged in lower casing body, air inlet top, and situ regeneration device is located in upper shell in the top of fan, in situ
The heating rod of regenerating unit is interspersed in the perforation 16 of the aluminium flake 15 of load Mn oxide, and aluminium flake is integrally attached in upper casing body
On draw-in groove, there is air outlet 20 on top cover 10.Temperature inductor 9 and temperature inductor support 8 are installed below cleaning module.Under
Housing is provided with the hole being adapted with control unit, and the operating surface of control panel is located at outside lower house, there is wind speed on operating surface
Switch 2, temperature controller 3, plus the total power switch 5 of thermal timing means 4 and clarifier, the above-mentioned part of control panel respectively with only
Change and be connected with lower component circuit inside device, Wind speed switch 2 is connected with fan power supply 12, fan 13, temperature controller 3 and temperature sense
Answer device 9, plus thermal timing means 4 be connected, heating device 4 of fixing time is connected with heating rod, total power switch 5 and Wind speed switch 2, warm
Degree controller 3 is connected, for controlling the running status of air purifier.Wind speed switch is used for fan wind speed and air purifier enters
The control of air port gas flow.
As desired by temperature controller 3, plus thermal timing means 4 electrified regulation carried out to aluminium flake realize cleaning module
Regeneration.Embodiment 4
Air purifier containing the situ regeneration device of embodiment 2, as Figure 7-9, increases on the basis of embodiment 2
Housing 11, base 1, top cover 10, air inlet 21, air outlet 20, control panel, fan 13, fan power supply 12；The shell of the present embodiment
Body is divided into upper and lower two parts, and in the inside of housing draw-in groove, each component of the inside of fixed support clarifier are provided with.On base 1
Have under air inlet 21, base and pawl is installed, it is ensured that the air intake space of air inlet.Fan 13, fan power supply 12 are arranged on lower casing
In vivo, air inlet top, situ regeneration device is located in upper shell above fan, and clean unit is located in shelf brackets 17
Load birnessite type Mn oxide the filter core 9 that is folded into of non-woven fabrics, housing made using ABS plastic material, and housing exists
Shelf brackets are designed with when driving grinding tool, shelf brackets are hollow design, and shelf edges of boards edge 18 has one fixed width to fix support filter core；Or put
It is the arrangement of the intersection of strip board 19 above grillage, there are PTC heaters 6 under shelf, there is air outlet 20 on top cover 10.In regeneration
Module lower section is provided with temperature inductor 9 and temperature inductor support 8.Lower house is provided with the hole being adapted with control unit, control
The operating surface of panel processed is located at outside lower house, there is Wind speed switch 2, temperature controller 3, plus thermal timing means 4 on operating surface
With the total power switch 5 of device, the above-mentioned part of control panel is connected respectively with inside clarifier with lower component circuit, Wind speed switch
2 are connected with fan power supply 12, fan 13, temperature controller 3 and temperature inductor 9, plus thermal timing means 4 be connected, heating is regularly
Between device 4 be connected with PTC heaters, total power switch 5 is connected with Wind speed switch 2, temperature controller 3, for controlling air
The running status of clarifier.Wind speed switch is used for the control of fan wind speed and clarifier air inlet gas flow.
As desired by temperature controller 3, plus thermal timing means 4 electrified regulation carried out to filter core realize cleaning module
Regeneration.
Above-described embodiment adds thermal timing means 4 to use semicircle shaft mechanical time switch (net purchase), for controlling heating
The working time of device.Fan is used to control rotation speed of fan, and air purifier gas flow during cleaning module thermal regeneration, is protected
Card cleaning module is heated evenly.Plus thermal timing means 4 is controlled to the time of heating devices heat, temperature inductor sensing adds
Thermal is applied to the temperature near cleaning module, feeds back to temperature controller, maintains certain heating-up temperature.
The lower section of air inlet regenerating unit in the original location, can be separately provided air inlet on bottom, it is also possible to while or single
Solely in the original location the side of the lower section housing of regenerating unit, both sides or three sides are provided with air inlet, and fan 13, fan power supply 12 are installed on
The top of base air inlet, for disturbing air, makes air more enter into inside clarifier, increases formaldehyde in air pollution
Contact with cleaning module.Air outlet is arranged on top cover, it is also possible to air outlet is opened in into upper shell both sides, it is ensured that dusty gas
It is fully contacted with clean unit.
Clarifier is provided with temperature control unit, and temperature control unit includes heating controller, temperature inductor, temperature sense
Device support, temperature inductor is answered to be located at cleaning module lower section, be fixed on temperature inductor support, by binding post and heating
Controller is connected, and has temperature control unit display screen and temperature operating knob outside control panel.Heater is located at the upper of fan
Side, heating controller is used to control the heating-up temperature of heater；Temperature sensor be used for detect clarifier interior environment temperature,
The data of temperature sensor detection are uploaded in real time heating controller, and heating controller is made accordingly according to data results
Control instruction.
The working condition of air purifier of the present utility model is that fan, clean unit are in running order after start, category
In purify air state.
Air purifier in-situ regeneration working condition of the present utility model is after air purifier start, plus hot charging
Put, clean unit, timing means it is in running order, belong to in-situ regeneration state.
Air purifier of the present utility model makes the pollutant Jing air inlets in air enter into purification by fan work
Inside device, through cleaning module, be fully contacted with cleaning module, most after Jing air outlets discharge.
The non-woven fabrics filter core of the load birnessite type Mn oxide that the utility model embodiment is adopted is according to the patent No.
ZL2013101399283 patent of invention methods are obtained.
The preparation method of the aluminium flake of the load Mn oxide that the utility model embodiment is adopted is as follows：
The first preparation method：Comprise the following steps：
(1) aluminium flake is carried out into ungrease treatment, to surface water is moistened completely；
(2) permanganate is soluble in water, stirring adds adjuvant ammoniacal liquor or urea after it is fully dissolved, and stirs to equal
Even mixing；
(3) aluminium flake obtained by step (1) process is put into and is placed in water bath with thermostatic control again into the mixed solution of step (2) and adds
Heat；
(4) aluminium flake after the completion of step (3) is taken out, washs and be dried；
The concentration of permanganate is 1.0-40g/L for the concentration of 0.1-60g/L, ammoniacal liquor or urea in the mixed solution.
The surface area of the aluminium base is 0.2-28cm with the concentration ratio of permanganate2:0.1-60g/L。
Ungrease treatment in the step (1) is cleaned the grease of aluminum flake surface using cleaning agent, then is washed with clear water
Wash；The cleaning agent is the degreasing agent of acid, alkalescence or organic solvent.
Permanganate in the step (2) is water-soluble permanganate, is potassium permanganate, sodium permanganate, permanganic acid amine
In one kind or their any combination.
The water bath with thermostatic control heating-up temperature of the step (3) is -95 DEG C of room temperature, and the time is 0.5-12 hours.
The baking temperature of the step (4) is -350 DEG C of room temperature.
Specific embodiment
Embodiment 1：
6g potassium permanganate is weighed, in being added into 100mL pure water, ultrasound is to being completely dissolved.It is subsequently added 4mL ammoniacal liquor molten
Liquid, stirs and evenly mixs.By aluminium flake Jing degreasings, the grease on alkali cleaning removal surface and oxide layer that quality is 20g, cleaned to table with pure water
Face moistens completely, in then putting into above-mentioned potassium permanganate-ammonia water mixture.This solution is placed at 40 DEG C of water bath with thermostatic control and is reacted
5h.Aluminium flake is taken out, is dried at 60 DEG C, that is, obtain the Mn oxide of aluminium base load.
Embodiment 2：
0.1g potassium permanganate is weighed, in being added into 100mL pure water, ultrasound is to being completely dissolved.1g urea is subsequently added, is stirred
Mix mixing.By aluminium flake Jing degreasings, the grease on alkali cleaning removal surface and oxide layer that quality is 0.7g, clean complete to surface with pure water
Full moistening, during above-mentioned potassium permanganate-urea mixed solution is put into afterwards.This solution is placed at 95 DEG C of water bath with thermostatic control and reacts 10h.Take
Go out aluminium flake, dry at 105 DEG C, that is, obtain the Mn oxide of aluminium base load.
Second of preparation method：
Comprise the following steps：
(1) it is 1-5 with the part by weight of catalyst, water-based adhesive, water:1-8:2-10 prepares catalyst pulp；
(2) aluminium flake of surface treatment substantially uniformity profit water is immersed in the slurry of step (1), to aluminium base or on aluminium flake
Even hanging；
(3) it is taken out to from slurry and is completely dried；
The particle of the catalyst is more than 100 mesh, for birnessite manganese dioxide catalyst；The catalyst pulp
PH value is 5-9.
The solid content of slurry is 5-50% in the step (1).
The aluminium flake carries out defoaming treatment to slurry before dipping.
The step of surface treatment substantially uniformity profit water be remove the grease contamination of aluminum flake surface with alcohol, again with pure
Water carries out being washed to aluminum flake surface substantially uniformity profit water, and keeps more than 30s in profit moisture film continuity.
The drying of the step (3) is that the aluminium flake for loading Mn oxide is put in baking oven and is machined to be completely dried.
Specific embodiment
Embodiment 1
20g potassium permanganate and 30g ammonium oxalate are weighed, add the water of 1L, ultrasound to potassium permanganate and ammonium oxalate to be completely dissolved,
The solution of gained is positioned in 90 DEG C of water-baths and is reacted 10 hours.The Mn oxide centrifugation of generation, washing are placed in into 105 DEG C of bakings
Case is dried, that is, obtain manganese dioxide-catalyst.Grinding, takes the powder more than 100 mesh, standby.
20g manganese dioxide powder body catalysts are weighed, adds 20g acryloid cements, 40g deionized waters to mix, consolidate
Content is about 25% slurry, and it is 9 to adjust slurry pH, then removes the foam of pulp surface.
It is 0.74g by quality, thickness is immersed in supersound washing 20min in alcoholic solution for the aluminium flake of 0.3mm, removes surface
Grease.(profit moisture film continuity keeps more than 30s loads to aluminium base surface complete wetting to take out deionized water supersound washing
It is better), it is standby.
Surface-treated aluminium flake is immersed in above-mentioned slurry, stirring, the uniform hanging to aluminium flake, then taken out to complete
White drying.Finished product is obtained for quick, 60 DEG C of oven drying 4h are placed in, the purification material of the manganese oxide catalyst of aluminium flake load is obtained
Material.
Embodiment 2
25g potassium permanganate is weighed, adds the water of 1L, ultrasound to be completely dissolved to potassium permanganate, be subsequently added the methyl alcohol of 1.5L,
The solution of gained is positioned at 45 DEG C of water-bath and is reacted 6 hours.The Mn oxide centrifugation of generation, washing are placed in into 105 DEG C of bakings
Case is dried, that is, obtain manganese dioxide-catalyst.Grinding, takes powder more than 100 mesh, standby.
25g manganese dioxide powder body catalysts are weighed, adds 10g polyurethane binder and 20g deionized waters, mixing to obtain
Solid content is about 45.5% slurry, and it is 7 to adjust slurry pH.
It is 0.74g by quality, thickness is immersed in supersound washing 20min in alcoholic solution for the aluminium flake of 0.3mm, and taking-up spends
Ionized water supersound washing is standby to aluminium base surface complete wetting (profit moisture film continuity keeps the better of more than 30s loads).
By in surface-treated aluminium flake immersion slurry, stir back and forth, the uniform hanging to aluminium flake, after be taken out to it is complete
It is dried.Finished product is obtained for quick, 60 DEG C of oven drying 4h are placed in, the purification material of the manganese oxide catalyst of aluminium flake load is obtained
Material.Embodiment 3
According to (Appl.Catal.B:Environ., 2016,189,210) report, weigh 25g potassium permanganate, the water of 20g mono-
Manganese sulfate is closed, adds the water of 1L, ultrasound to be completely dissolved to medicine, the solution of gained is positioned in hydrothermal reaction kettle at 140 DEG C
Reaction 12h.The manganese dioxide centrifugation of generation, washing are placed in into 105 DEG C of oven dryings, that is, obtain that the titanium dioxide of ozone can be removed
Mn catalyst.Grinding, takes powder more than 100 mesh, standby.
The manganese dioxide powder body catalyst of 10g is weighed, adds 80g acryloid cements and 100g deionized waters, mixing to obtain
It is about 5.3% slurry to solid content, it is 5 to adjust slurry pH.
It is 0.74g by quality, thickness is immersed in supersound washing 20min in alcoholic solution for the aluminium flake of 0.3mm, and taking-up spends
Ionized water supersound washing is standby to aluminum flake surface complete wetting (profit moisture film continuity keeps the better of more than 30s loads).
By in surface-treated aluminium flake immersion slurry, stir back and forth, the uniform hanging to aluminium flake, after be taken out to it is complete
It is dried.Finished product is obtained for quick, 60 DEG C of oven drying 4h are placed in.After drying, then immerse in slurry and carry out secondary load, be dried.
After three dippings, until powder is completely covered the surface of aluminium base, that is, the purification material of the manganese oxide catalyst of aluminium flake load is obtained
Material.
Claims (6)
1. a kind of situ regeneration device of purify air, it is characterised in that the device includes cleaning module and provides cleaning module
Regenerate the heater of temperature required condition；The cleaning module is the aluminium flake for loading Mn oxide, and aluminium flake is at least a piece of；Or
The filter core that the non-woven fabrics of load Mn oxide is folded into；The heater be heating rod, heating rod be interspersed in aluminium flake interlayer or
Hole is provided with aluminium flake, heating rod is interspersed in hole；Or the filter core that the non-woven fabrics of the load Mn oxide is folded into is placed
In shelf brackets, heater is under shelf brackets；Shelf brackets are hollow, and edge has one fixed width to fix support filter core；Or shelf
It is strip board arranged crosswise above frame.
2. situ regeneration device according to claim 1, it is characterised in that the heater in shelf brackets lower end is
Ptc heater.
3. situ regeneration device according to claim 1, it is characterised in that the timing also including connection on the heating
Device is used to control the working time of heater.
4. a kind of air purifier of the situ regeneration device containing any one of claims 1 to 3, it is characterised in that
Also include casing, into and out of air port, control panel, fan, fan power supply；Casing includes base, supports housing and top cover, supports
The inside of housing is provided with draw-in groove, and for fixing support and control component, the fan, fan power supply and air inlet are respectively positioned on original position again
Generating apparatus lower section, air outlet is located at situ regeneration device top；The control panel is located at and supports hull outside, in control unit
Portion's circuit is connected with the heater of fan power supply, situ regeneration device, and power supply, Wind speed switch, heating timing are provided with outside it
Device.
5. air purifier according to claim 4, it is characterised in that the air inlet is located at base and/or housing extremely
Few side, air outlet is located at top cover and/or housing at least side.
6. air purifier according to claim 5, it is characterised in that the air purifier also includes being located at purification mould
Temperature control unit below block, the temperature control unit includes temperature controller, temperature inductor, temperature inductor
Frame, temperature controller internal circuit and temperature inductor and adds thermal timing means to be connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620783373.5U CN206103700U (en) | 2016-07-22 | 2016-07-22 | Air -purifying's normal position regenerating unit and contain device's clarifier |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620783373.5U CN206103700U (en) | 2016-07-22 | 2016-07-22 | Air -purifying's normal position regenerating unit and contain device's clarifier |
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| Publication Number | Publication Date |
|---|---|
| CN206103700U true CN206103700U (en) | 2017-04-19 |
Family
ID=58511985
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620783373.5U Expired - Fee Related CN206103700U (en) | 2016-07-22 | 2016-07-22 | Air -purifying's normal position regenerating unit and contain device's clarifier |
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| CN (1) | CN206103700U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106000093A (en) * | 2016-07-22 | 2016-10-12 | 清华大学 | In-situ regenerating device for purifying air and purifier comprising same |
-
2016
- 2016-07-22 CN CN201620783373.5U patent/CN206103700U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106000093A (en) * | 2016-07-22 | 2016-10-12 | 清华大学 | In-situ regenerating device for purifying air and purifier comprising same |
| CN106000093B (en) * | 2016-07-22 | 2019-05-17 | 清华大学 | A kind of situ regeneration device purifying air and the clarifier containing the device |
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