CN106000093A - In-situ regenerating device for purifying air and purifier comprising same - Google Patents
In-situ regenerating device for purifying air and purifier comprising same Download PDFInfo
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- CN106000093A CN106000093A CN201610586842.9A CN201610586842A CN106000093A CN 106000093 A CN106000093 A CN 106000093A CN 201610586842 A CN201610586842 A CN 201610586842A CN 106000093 A CN106000093 A CN 106000093A
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- situ regeneration
- regeneration device
- heater
- air
- aluminium flake
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8668—Removing organic compounds not provided for in B01D53/8603 - B01D53/8665
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/2073—Manganese
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/06—Polluted air
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- Environmental & Geological Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
- Catalysts (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
The invention relates to an in-situ regenerating device for purifying air and a purifier comprising the same and belongs to the field of air purification. The in-situ regenerating device is characterized by comprising a purification module and a heating device for providing temperature conditions needed for regeneration of the purification module. The air purifier which removes indoor formaldehyde pollution efficiently and quickly is provided. The purification module can be regenerated in situ, a filter core does not need to be replaced, and the air purifier is free of secondary pollution.
Description
Technical field
The invention belongs to air purification field, specifically, belong to a kind of air purifier and cleaning module in-situ regeneration dress thereof
Put.
Background technology
Living standards of the people improve constantly, and house house fitting is increasing, but wood-based plate and goods, carpet, carpet
Liner and carpet adhesive, interior wall coating, wooden furniture, wallpaper, adhesive etc. can be to indoor release formaldehyde and VOCs (volatility
Organic substance) etc. harmful substance, serious harm human body healthy.Formaldehyde is a kind of common indoor air pollutants, and tool
The feature have slowly release, persistently polluting, has stimulation toxicity, is a kind of carcinogen, can be via sucking and contact skin
And affect health.
In recent years, indoor pollution is purified by main use air purifier, and the technology removing formaldehyde of selection mainly has work
The property technology such as charcoal absorption, catalyst oxidation Decomposition, photocatalyst catalytic decomposition.Activated carbon is the most saturated, is heated and the most outwards solves
Inhale pollutant, simultaneously with the problem of reclaiming rate variance；Catalyst typically selects noble metal and metal-oxide, noble metal
Typically select Pd, Au, Ag, Pt etc., reaction to need higher temperature, and catalyst easily inactivates, metal-oxide, as
The removal effect of the PARA FORMALDEHYDE PRILLS(91,95)s such as silver oxide, copper oxide, cobalt oxide, zinc oxide, titanium dioxide, iron sesquioxide and manganese dioxide
Really (Atmospheric Environment 2002,36,5,543 5547), find under room temperature there be manganese dioxide PARA FORMALDEHYDE PRILLS(91,95)
High removal activity.
At present it is known that air purifier because there is the problems such as saturated, the catalyst activity inactivation of adsorbent, need frequently
Replacing clean unit is to maintain clean-up effect, and the use cost of air purifier is higher, and easily causes secondary pollution.
Summary of the invention
The present invention is directed to problem of the prior art, propose a kind of situ regeneration device purifying air and the purification containing this device
Device.It is an object of the invention to provide a kind of air purifier efficient, quickly removal Formaldehyde Pollution of Indoor Air, cleaning module can
In-situ regeneration, filter element is not required to change, non-secondary pollution.
The present invention solves the technical scheme that the problems referred to above are used:
A kind of situ regeneration device purifying air, it is characterised in that this device includes cleaning module and provides cleaning module again
The heater of raw temperature required condition.
Described cleaning module is the aluminium flake of Supported Manganese oxide, and aluminium flake is the most a piece of；Or the non-woven fabrics folding of Supported Manganese oxide
The filter element built up.
Described heater is heating rod, and heating rod is interspersed in aluminium flake interlayer or is provided with hole on aluminium flake, and heating rod is interspersed in hole
In；Or the filter element that the non-woven fabrics of described Supported Manganese oxide is folded into is placed in shelf brackets, heater is under shelf brackets；
Shelf brackets is hollow, and there is one fixed width fixing support filter element at edge；Or be strip board arranged crosswise above shelf brackets.
The described heater in shelf brackets lower end is ptc heater.
Above-mentioned situ regeneration device, also includes connecting timing means on the heating for controlling the work of heater
Time.
The air purifier of a kind of situ regeneration device, 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, and the inside supporting housing is provided with draw-in groove, is used for fixing
Support and control assembly, described fan, fan power supply and air inlet are respectively positioned on below situ regeneration device, and air outlet is positioned in situ
Above regenerating unit；Described control panel is positioned at support hull outside, controls components interior circuit with fan power supply, original position the most again
The heater of generating apparatus is connected, and is provided with power supply, Wind speed switch, adds thermal timing means outside it.
Described air inlet is positioned at base and/or housing at least side, and air outlet is positioned at top cover and/or housing at least side.
Described air purifier also includes the temperature control unit being positioned at below cleaning module, and described temperature control unit includes temperature
Degree controller, temperature inductor, temperature inductor support, temperature controller internal circuit and temperature inductor and heating timing
Device is connected.
Accompanying drawing explanation
Fig. 1 is that the present invention uses Supported Manganese oxide aluminium flake and heating rod schematic diagram；
Fig. 2 is the filter element schematic diagram that the present invention uses that Supported Manganese oxide non-woven fabrics is folded into；
Fig. 3 is the embodiment of the present invention 2 shelf brackets schematic diagram, and Fig. 3 a is the signal having one fixed width in the middle of shelf brackets for empty edge
Figure；Fig. 3 b is to arrange strip board schematic diagram in the middle of shelf brackets；
Fig. 4 is the situ regeneration device schematic diagram that the present invention uses Supported Manganese oxide aluminium flake；
Fig. 5 is that the present invention contains Fig. 1 in-situ regeneration depurator structural representation；
Fig. 6 is the profile of Fig. 5；
Fig. 7 is the situ regeneration device signal of the filter element that the present invention uses load birnessite type Mn oxide non-woven fabrics to be folded into
Figure；
Fig. 8 is for using containing Fig. 7 in-situ regeneration depurator structural representation；
Fig. 9 is the profile of Fig. 8；
Figure 10 is overall appearance schematic diagram of the present invention.
Wherein:
1, base, 2, Wind speed switch, 3, temperature controller, 4, add thermal timing means, 5, switch, 6, PTC add hot charging
Put, 7, temperature inductor support, 8, temperature inductor, 9, birnessite type Mn oxide foldable filter element, 10, top cover,
11, housing, 12, fan power supply, 13, fan, 14, heating rod, 15, the aluminium flake of Supported Manganese oxide, 16, perforation,
17, shelf brackets, 18, shelf brackets edge, 19, strip board, 20, air outlet, 21, air inlet.
Detailed description of the invention
The present invention is described in further detail below in conjunction with the accompanying drawings and by embodiment, and following example are to the present invention
Explain and the invention is not limited in following example.
Embodiment 1
A kind of situ regeneration device purifying air of the present invention, as it is shown in figure 1, cleaning module and the regeneration of offer cleaning module
The heater of temperature required condition, cleaning module is the aluminium flake 15 of Supported Manganese oxide, and aluminium flake is multi-disc, at Supported Manganese oxygen
Uniformly perforation 16 on the aluminium flake 15 of compound, 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 Supported Manganese oxide.
The aluminium flake 15 of Supported Manganese oxide can be honeycomb aluminum, and heating rod is fixed in the middle of two pieces of honeycomb aluminums, and peripheral entirety adds frame
Fixed cellular aluminum and heating rod, what heating rod energising realized cleaning module is regeneration originally.
The aluminium flake 15 of Supported Manganese oxide is placed in the space of formaldehyde pollution and can carry out purifying work, then by above-mentioned adding
Thermal completes cleaning module in-situ regeneration.
Above-mentioned aluminium flake is one or more pieces, and for reaching more preferable effect, aluminium flake can be multi-disc, and heating rod is single or multiple
It is uniformly distributed and 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
Porose, heater can be heating film and the aluminium flake arranged crosswise not having hole.
Embodiment 2
The another kind of situ regeneration device purifying air of the present invention, as in figure 2 it is shown, this device includes cleaning module and offer
Cleaning module regenerates the heater of temperature required condition, and cleaning module is the load birnessite type being placed in shelf brackets 17
The filter element 9 that the non-woven fabrics of Mn oxide is folded into, the present embodiment uses PTC heater 6, power 500W, insulated type
Semiconductor-air heater (commercial), PTC heater 6 (not shown in Fig. 2) is placed under shelf brackets；During shelf brackets is
Sky, there is one fixed width fixing support filter element at shelf brackets edge 18；Or shelf brackets is the layout that strip board 19 is intersected.
This device is placed in the space of formaldehyde pollution and can carry out purifying work, PTC heater 6 energising is added when needed
Heat realizes the in-situ regeneration of cleaning module.
Embodiment 3
Containing the air purifier of embodiment 1 situ regeneration device, as in Figure 3-5.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；This
The housing 11 of embodiment is divided into upper and lower two parts, and housing uses ABS plastic material to make, and is provided with draw-in groove in the inside of housing,
Fixing each assembly supporting depurator.Have on base 1 under air inlet 21, base and pawl is installed, it is ensured that entering of air inlet
Wind space.In fan 13, fan power supply 12 are arranged on lower house, above air inlet, situ regeneration device is above fan
It is positioned at upper shell, in the perforation 16 of the aluminium flake 15 that the heating rod of situ regeneration device is interspersed in Supported Manganese oxide, aluminium flake
It is integrally attached on the draw-in groove in upper shell, top cover 10 has air outlet 20.Temperature inductor is installed below cleaning module
9 and temperature inductor support 8.Lower house has and controls the hole that parts adapt, and the operating surface of control panel is positioned at lower house
Outside, has Wind speed switch 2, temperature controller 3 on operating surface, adds the total power switch 5 of thermal timing means 4 and depurator,
The above-mentioned part of control panel is connected with lower component circuit with inside depurator respectively, Wind speed switch 2 and fan power supply 12, fan
13 are connected, and temperature controller 3 and temperature inductor 9, add thermal timing means 4 and are connected, and heating is fixed time device 4 and heats
Rod is connected, and total power switch 5 is connected with Wind speed switch 2, temperature controller 3, for controlling the running status of air purifier.
Wind speed switch is used for fan wind speed and the control of air purifier air inlet gas flow.
As desired by temperature controller 3, add thermal timing means 4 and aluminium flake is carried out electrified regulation realize the regeneration of cleaning module.
Embodiment 4
Containing the air purifier of embodiment 2 situ regeneration device, as shown in figs 6-8, increase 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；This
The housing of embodiment is divided into upper and lower two parts, is provided with draw-in groove in the inside of housing, each group of the fixing inside supporting depurator
Part.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 electricity
In source 12 is arranged on lower house, above air inlet, situ regeneration device is positioned at upper shell above fan, and clean unit is
The filter element 9 that the non-woven fabrics of the load birnessite type Mn oxide being placed in shelf brackets 17 is folded into, housing uses ABS to mould
Material material is made, and housing is designed with shelf brackets when driving grinding tool, and shelf brackets is hollow design, and shelf edges of boards edge 18 has a fixed width
Degree is fixing supports filter element；Or above shelf brackets be strip board 19 intersect layout, under shelf, have PTC heater 6, top
Air outlet 20 is had on lid 10.Temperature inductor 9 and temperature inductor support 8 are installed below regeneration module.Lower house is opened
Having and control the hole that parts adapt, the operating surface of control panel is positioned at outside lower house, has Wind speed switch 2 on operating surface,
Temperature controller 3, adds the total power switch 5 of thermal timing means 4 and device, the above-mentioned part of control panel respectively with in depurator
Portion is connected with lower component circuit, and Wind speed switch 2 is connected with fan power supply 12, fan 13, temperature controller 3 and temperature sense
Device 9, adding thermal timing means 4 and be connected, heating device 4 of fixing time is connected with PTC heater, total power switch 5 and wind speed
Switch 2, temperature controller 3 are connected, for controlling the running status of air purifier.Wind speed switch is used for fan wind speed with clean
Change the control of device air inlet gas flow.
As desired by temperature controller 3, add thermal timing means 4 and filter element is carried out electrified regulation realize the regeneration of cleaning module.
Above-described embodiment adds thermal timing means 4 and uses semicircle shaft mechanical time switch (net purchase), is used for controlling heater
Working time.Fan is used for controlling rotation speed of fan, and air purifier gas flow, during cleaning module thermal regeneration, it is ensured that
Cleaning module is heated evenly.Adding thermal timing means 4 to be controlled 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 position, can be separately provided air inlet, it is also possible to concurrently or separately exist on bottom
The side of lower section housing of situ regeneration device, both sides or three sides are provided with air inlet, and fan 13, fan power supply 12 are installed on the end
The top of seat air inlet, for disturbance air, makes air more enter into inside depurator, increases formaldehyde in air and pollutes
With contacting of cleaning module.Air outlet is arranged on top cover, it is also possible to air outlet is opened in upper shell both sides, it is ensured that contamination gas
Body is fully contacted with clean unit.
Depurator is provided with temperature control unit, and temperature control unit includes heating controller, temperature inductor, temperature sense
Device support, temperature inductor is positioned at below cleaning module, is 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 positioned at the upper of fan
Side, heating controller is for controlling the heating-up temperature of heater；Temperature sensor is used for detecting depurator interior environment temperature,
The data of temperature sensor detection are uploaded to heating controller in real time, and heating controller is made according to data results accordingly
Control instruction.
After the duty of the air purifier of the present invention is start, fan, clean unit are in running order, belong to purification
Air condition.
After the air purifier in-situ regeneration duty of the present invention is the start of described air purifier, heater, purification list
Unit, timing means in running order, belong to in-situ regeneration state.
The air purifier of the present invention passes through fan work, makes the pollutant in air enter into inside depurator through air inlet,
Through cleaning module, be fully contacted with cleaning module, after discharge through air outlet.
The non-woven fabrics filter element of the load birnessite type Mn oxide that the embodiment of the present invention uses is according to the patent No.
ZL2013101399283 patent of invention method is obtained.
The preparation method of the aluminium flake of the Supported Manganese oxide that the embodiment of the present invention uses is as follows:
The first preparation method: comprise the following steps:
(1) aluminium flake is carried out ungrease treatment, moisten water to surface completely；
(2) permanganate is soluble in water, stirring adds adjuvant ammonia or carbamide after making it fully dissolve, and is stirred until homogeneous
Mixing；
(3) the aluminium flake input that step (1) processes gained is placed in water bath with thermostatic control heating to the mixed solution of step (2) again；
(4) aluminium flake after step (3) being completed takes out, and washs and is dried；
In described mixed solution the concentration of permanganate be the concentration of 0.1-60g/L, ammonia or carbamide be 1.0-40g/L.
The described surface area of aluminum base and the concentration of permanganate are than for 0.2-28cm2:0.1-60g/L。
Ungrease treatment in described step (1) uses abluent to be carried out by the oils and fats of aluminum flake surface, then washs with clear water；Institute
Stating abluent is acid, alkalescence or the degreasing agent of organic solvent.
Permanganate in described step (2) is water solublity permanganate, in potassium permanganate, sodium permanganate, permanganic acid amine
A kind of or their any combination.
The water bath with thermostatic control heating-up temperature of described step (3) is room temperature-95 DEG C, and the time is 0.5-12 hour.
The baking temperature of described step (4) is room temperature-350 DEG C.
Detailed description of the invention
Embodiment 1:
Weigh 6g potassium permanganate, be added in 100mL pure water, ultrasonic to being completely dissolved.It is subsequently added 4mL ammonia
Solution, stirring and evenly mixing.Aluminium flake that quality is 20g is removed through defat, alkali cleaning oils and fats and the oxide layer on surface, clear with pure water
It is washed till surface the most moistening, then puts in above-mentioned potassium permanganate-ammonia water mixture.This solution is placed in water bath with thermostatic control 40 DEG C
Lower reaction 5h.Take out aluminium flake, dry at 60 DEG C, i.e. obtain the Mn oxide of aluminum base load.
Embodiment 2:
Weigh 0.1g potassium permanganate, be added in 100mL pure water, ultrasonic to being completely dissolved.It is subsequently added 1g carbamide,
Stirring and evenly mixing.Aluminium flake that quality is 0.7g is removed through defat, alkali cleaning oils and fats and the oxide layer on surface, cleans extremely with pure water
Surface is the most moistening, in potassium permanganate-urea mixed solution that rear input is above-mentioned.This solution is placed at water bath with thermostatic control 95 DEG C anti-
Answer 10h.Take out aluminium flake, dry at 105 DEG C, i.e. obtain the Mn oxide of aluminum base load.
The preparation method of the second:
Comprise the following steps:
(1) it is that 1-5:1-8:2-10 prepares catalyst pulp with catalyst, water-based adhesive, the part by weight of water；
(2) surface is processed in the slurry of the most uniformly aluminium flake immersion step (1) of profit water, uniform to aluminum base or on aluminium flake
Hanging；
(3) it is taken out to be completely dried from slurry；
The granule of described catalyst is more than 100 mesh, for birnessite manganese dioxide catalyst；The pH of described catalyst pulp
Value is 5-9.
In described step (1), the solid content of slurry is 5-50%.
Described aluminium flake carries out defoaming treatment to slurry before dipping.
Described surface processes the step of the most uniformly profit water and is the grease contamination with ethanol removing aluminum flake surface, enters with pure water
Row is washed to aluminum flake surface and the most uniformly moistens water, and keeps more than 30s in profit moisture film seriality.
The aluminium flake for Supported Manganese oxide that is dried of described step (3) is put into and is machined in baking oven be completely dried.
Detailed description of the invention
Embodiment 1
Weigh 20g potassium permanganate and 30g ammonium oxalate, add the water of 1L, ultrasonic be completely dissolved to potassium permanganate and ammonium oxalate,
The solution of gained is positioned in 90 DEG C of water-baths reaction 10 hours.The Mn oxide of generation is centrifugal, washing is placed in 105 DEG C
Oven drying, i.e. obtains manganese dioxide-catalyst.Grind, take the powder body more than 100 mesh, standby.
Weigh 20g manganese dioxide powder body catalyst, add 20g acryloid cement, 40g deionized water, mixing, obtain
Be about the slurry of 25% to solid content, regulation slurry pH is 9, then removes the foam of pulp surface.
Being 0.74g by quality, thickness is that the aluminium flake of 0.3mm is immersed in supersound washing 20min in alcoholic solution, removes surface
Oils and fats.With deionized water supersound washing to aluminum primary surface complete wetting, (profit moisture film seriality keeps more than 30s load in taking-up
Better), standby.
Being immersed by surface-treated aluminium flake in above-mentioned slurry, stirring, to aluminium flake, uniform hanging, then takes out to completely dry
Dry.For fast obtaining finished product, it is placed in 60 DEG C of oven drying 4h, obtains the purification material of the manganese oxide catalyst of aluminium flake load
Material.
Embodiment 2
Weigh 25g potassium permanganate, add the water of 1L, ultrasonic be completely dissolved to potassium permanganate, be subsequently added the first of 1.5L
Alcohol, is positioned at water-bath 45 DEG C reaction 6 hours by the solution of gained.The Mn oxide of generation is centrifugal, washing is placed in
105 DEG C of oven dryings, i.e. obtain manganese dioxide-catalyst.Grind, take more than the powder body of 100 mesh, standby.
Weigh 25g manganese dioxide powder body catalyst, add 10g polyurethane binder and 20g deionized water, mixing, obtain
Be about the slurry of 45.5% to solid content, regulation slurry pH is 7.
Being 0.74g by quality, thickness is that the aluminium flake of 0.3mm is immersed in supersound washing 20min in alcoholic solution, and taking-up spends
Ionized water supersound washing is to aluminum primary surface complete wetting (profit moisture film seriality keeps the better of more than 30s load), standby
With.
Surface-treated aluminium flake is immersed in slurry, stirs back and forth, uniform hanging to aluminium flake, after be taken out to be completely dried.
For fast obtaining finished product, it is placed in 60 DEG C of oven drying 4h, obtains the scavenging material of the manganese oxide catalyst of aluminium flake load.
Embodiment 3
Report according to (Appl.Catal.B:Environ., 2016,189,210), weigh 25g potassium permanganate, 20g
Manganous sulfate monohydrate, adds the water of 1L, ultrasonic is completely dissolved to medicine, be positioned in hydrothermal reaction kettle by the solution of gained
12h is reacted at 140 DEG C.The manganese dioxide of generation is centrifugal, washing is placed in 105 DEG C of oven dryings, i.e. obtains removing
The manganese dioxide-catalyst of ozone.Grind, take more than the powder body of 100 mesh, standby.
Weigh the manganese dioxide powder body catalyst of 10g, add 80g acryloid cement and 100g deionized water, mix,
Obtaining the slurry that solid content is about 5.3%, regulation slurry pH is 5.
Being 0.74g by quality, thickness is that the aluminium flake of 0.3mm is immersed in supersound washing 20min in alcoholic solution, and taking-up spends
Ionized water supersound washing is to aluminum flake surface complete wetting (profit moisture film seriality keeps the better of more than 30s load), standby
With.
Surface-treated aluminium flake is immersed in slurry, stirs back and forth, uniform hanging to aluminium flake, after be taken out to completely dry
Dry.For fast obtaining finished product, it is placed in 60 DEG C of oven drying 4h.After drying, then immerse slurry carries out secondary load, dry
Dry.After three dippings, until powder is completely covered the surface of aluminum base, i.e. obtain manganese oxide catalyst clean of aluminium flake load
Formed material.
Claims (8)
1. the situ regeneration device purifying air, it is characterised in that this device includes cleaning module and provides cleaning module again
The heater of raw temperature required condition.
Situ regeneration device the most according to claim 1, it is characterised in that described cleaning module is Supported Manganese oxide
Aluminium flake, aluminium flake is the most a piece of；Or the filter element that the non-woven fabrics of Supported Manganese oxide is folded into.
Situ regeneration device the most according to claim 2, it is characterised in that described heater is heating rod, heating rod
Being interspersed in aluminium flake interlayer or be provided with hole on aluminium flake, heating rod is interspersed in hole；Or the non-woven fabrics of described Supported Manganese oxide
The filter element being folded into is placed in shelf brackets, and heater is under shelf brackets；Shelf brackets is hollow, and edge has one fixed width solid
Surely filter element is supported；Or be strip board arranged crosswise above shelf brackets.
Situ regeneration device the most according to claim 3, it is characterised in that the described heater in shelf brackets lower end is
Ptc heater.
5. according to the situ regeneration device described in any one of claim 1-4, it is characterised in that also include being connected to add hot charging
The timing means put is for controlling the working time of heater.
6. the air purifier containing the situ regeneration device according to any one of claim 1 to 5, 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,
The inside supporting housing is provided with draw-in groove, is used for fixing support and control assembly, and described fan, fan power supply and air inlet are respectively positioned on
Below situ regeneration device, air outlet is positioned at above situ regeneration device；Described control panel is positioned at support hull outside, control
Components interior circuit processed is connected with the heater of fan power supply, situ regeneration device, is provided with power supply, Wind speed switch outside it,
Add thermal timing means.
Air purifier the most according to claim 6, it is characterised in that described air inlet is positioned at base and/or housing extremely
Few side, air outlet is positioned at top cover and/or housing at least side.
Air purifier the most according to claim 7, it is characterised in that described air purifier also includes being positioned at purification mould
Temperature control unit below block, described temperature control unit includes that temperature controller, temperature inductor, temperature inductor prop up
Frame, temperature controller internal circuit and temperature inductor and add thermal timing means and be connected.
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| CN201610586842.9A CN106000093B (en) | 2016-07-22 | 2016-07-22 | A kind of situ regeneration device purifying air and the clarifier containing the device |
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| CN201610586842.9A CN106000093B (en) | 2016-07-22 | 2016-07-22 | A kind of situ regeneration device purifying air and the clarifier containing the device |
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| CN106000093B CN106000093B (en) | 2019-05-17 |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106823781A (en) * | 2017-01-10 | 2017-06-13 | 清华大学 | A kind of air purifier for removing indoor VOCs and preparation method thereof |
| CN108236920A (en) * | 2016-12-26 | 2018-07-03 | 株式会社马勒滤清系统 | Honeycomb sorbent material and its manufacturing method and canister |
| CN108421367A (en) * | 2018-03-23 | 2018-08-21 | 深圳市贝优通新能源技术开发有限公司 | A kind of intelligent formaldehyde collection processing equipment based on Internet of Things |
| CN108786313A (en) * | 2018-06-21 | 2018-11-13 | 河南师范大学 | A kind of adjustable air purification instrument of intelligence |
| CN112023614A (en) * | 2020-09-03 | 2020-12-04 | 广东美的白色家电技术创新中心有限公司 | Purifying device |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101444634A (en) * | 2008-12-30 | 2009-06-03 | 中国科学院长春应用化学研究所 | Indoor air-purification device |
| CN202595246U (en) * | 2012-04-28 | 2012-12-12 | 仪征市润扬机械有限公司 | Salt-bath furnace for surface colouration machining for piston ring spiral bracing springs |
| CN103480267A (en) * | 2013-04-22 | 2014-01-01 | 清华大学 | Air cleaning material, and preparation method and application thereof |
| CN104190251A (en) * | 2014-09-09 | 2014-12-10 | 清华大学 | Air purification material and preparation method and application thereof |
| CN206103700U (en) * | 2016-07-22 | 2017-04-19 | 清华大学 | Air -purifying's normal position regenerating unit and contain device's clarifier |
-
2016
- 2016-07-22 CN CN201610586842.9A patent/CN106000093B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101444634A (en) * | 2008-12-30 | 2009-06-03 | 中国科学院长春应用化学研究所 | Indoor air-purification device |
| CN202595246U (en) * | 2012-04-28 | 2012-12-12 | 仪征市润扬机械有限公司 | Salt-bath furnace for surface colouration machining for piston ring spiral bracing springs |
| CN103480267A (en) * | 2013-04-22 | 2014-01-01 | 清华大学 | Air cleaning material, and preparation method and application thereof |
| CN104190251A (en) * | 2014-09-09 | 2014-12-10 | 清华大学 | Air purification material and preparation method and application thereof |
| CN206103700U (en) * | 2016-07-22 | 2017-04-19 | 清华大学 | Air -purifying's normal position regenerating unit and contain device's clarifier |
Cited By (6)
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| CN108236920A (en) * | 2016-12-26 | 2018-07-03 | 株式会社马勒滤清系统 | Honeycomb sorbent material and its manufacturing method and canister |
| CN108236920B (en) * | 2016-12-26 | 2022-07-19 | 株式会社马勒滤清系统 | Honeycomb adsorbent, method for producing same, and canister |
| CN106823781A (en) * | 2017-01-10 | 2017-06-13 | 清华大学 | A kind of air purifier for removing indoor VOCs and preparation method thereof |
| CN108421367A (en) * | 2018-03-23 | 2018-08-21 | 深圳市贝优通新能源技术开发有限公司 | A kind of intelligent formaldehyde collection processing equipment based on Internet of Things |
| CN108786313A (en) * | 2018-06-21 | 2018-11-13 | 河南师范大学 | A kind of adjustable air purification instrument of intelligence |
| CN112023614A (en) * | 2020-09-03 | 2020-12-04 | 广东美的白色家电技术创新中心有限公司 | Purifying device |
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