CN107456818A - A kind of automatic dust removing apparatus of high-efficient purification air - Google Patents
A kind of automatic dust removing apparatus of high-efficient purification air Download PDFInfo
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- CN107456818A CN107456818A CN201710853104.0A CN201710853104A CN107456818A CN 107456818 A CN107456818 A CN 107456818A CN 201710853104 A CN201710853104 A CN 201710853104A CN 107456818 A CN107456818 A CN 107456818A
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- air
- water tank
- air inlet
- dust removing
- gas
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- 239000000428 dust Substances 0.000 title claims abstract description 48
- 238000000746 purification Methods 0.000 title claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 87
- 238000003756 stirring Methods 0.000 claims abstract description 7
- 238000009826 distribution Methods 0.000 claims description 22
- 239000007788 liquid Substances 0.000 claims description 14
- 238000010943 off-gassing Methods 0.000 claims description 8
- 230000002209 hydrophobic effect Effects 0.000 claims description 6
- 238000005507 spraying Methods 0.000 claims description 5
- 230000001133 acceleration Effects 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims description 3
- 230000005484 gravity Effects 0.000 claims description 3
- 239000004744 fabric Substances 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 12
- 241000272517 Anseriformes Species 0.000 abstract description 4
- 239000007789 gas Substances 0.000 description 63
- 239000012535 impurity Substances 0.000 description 8
- 238000005520 cutting process Methods 0.000 description 4
- 238000005367 electrostatic precipitation Methods 0.000 description 3
- 238000007667 floating Methods 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 241000272525 Anas platyrhynchos Species 0.000 description 2
- 101100293261 Mus musculus Naa15 gene Proteins 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000004887 air purification Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000000686 essence Substances 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/02—Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath
- B01D47/021—Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath by bubbling the gas through a liquid bath
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L9/00—Disinfection, sterilisation or deodorisation of air
- A61L9/16—Disinfection, sterilisation or deodorisation of air using physical phenomena
- A61L9/18—Radiation
- A61L9/20—Ultraviolet radiation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/06—Spray cleaning
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
- F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
- F24F3/16—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by purification, e.g. by filtering; by sterilisation; by ozonisation
-
- 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
- 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
- F24F8/10—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
- F24F8/192—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 by electrical means, e.g. by applying electrostatic fields or high voltages
-
- 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
- F24F8/22—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by sterilisation using UV light
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Epidemiology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
The invention discloses a kind of automatic dust removing apparatus of high-efficient purification air, including housing, the first air inlet and the first air outlet, the hull outside is provided with controller；First air inlet is arranged on housing tip, first air inlet is provided with sensor of dust concentration, and first air inlet is connected with the first air blower, water tank, air purifier, drier, the second air blower and first air outlet successively by pipeline；The water tank top is connected by water pipe with water inlet, and the water tank bottom is connected by water pipe with delivery port；Inside the water tank unit and agitating unit are smashed including bubble；The bubble smashes unit and is used to smash air into caused air pocket in the water tank；The agitating unit is used to stir the water in the water tank, the residence time that increase gas ducks in drink.The present invention smashes unit and agitating unit by bubble strengthens dust removing effects.
Description
Technical field
The present invention relates to dust arrester technical field, more particularly to a kind of automatic dust removing apparatus of high-efficient purification air.
Background technology
In daily life or in daily production operation, modern society is increasingly tight due to the situation that ecological environment is destroyed
Weight, causes indoor sand, floating dust, Sand-Dust further frequent；In addition, in daily production operation workshop, also usually occur
Floating dust content in air improves, the problem of causing the quality of air more and more lower.Dust arrester is commonly called as deduster, be remove or
Reduce the device of fly ash content in flue gas.The species of dust arrester can be divided into biology receive film dust-arrest device, cloud and mist dust-arrest device,
Cloud and mist dust-arrest device, bag-type dust collector, cyclone dust collector, wet dust separater, electrostatic precipitation dress.But current remove
Dirt device, dedusting method is single, and dust removing effects are poor, and automaticity is low.
The content of the invention
A kind of the shortcomings that it is an object of the invention to overcome prior art, there is provided the automatic dust removing dress of high-efficient purification air
Put.
A kind of automatic dust removing apparatus of high-efficient purification air, including housing, the first air inlet and the first air outlet, the shell
External side is provided with controller；First air inlet is arranged on housing tip, and first air inlet is provided with dust concentration
Sensor, first air inlet by pipeline successively with the first air blower, water tank, air purifier, drier, the second air blast
Machine is connected with first air outlet；The water tank top is connected by water pipe with water inlet, and the water tank bottom passes through
Water pipe is connected with delivery port；Inside the water tank unit and agitating unit are smashed including bubble；The sensor of dust concentration,
First air blower, the bubble smash unit, the agitating unit, the air purifier, the drying unit and institute
The second air blower is stated to be electrically connected with the controller；The bubble is smashed unit and entered for smashing air in the water tank
Caused air pocket；The agitating unit is used to stir the water in the water tank, the residence time that increase gas ducks in drink；It is fixed
The air inlet of the justice water tank is the second air inlet, is arranged on the side wall and second air inlet and the water tank of the water tank
Side wall shape have angle ɑ, and second air inlet and the distance S of the bottom of the water tank meet：And second air inlet smashes the air line distance L of unit with the bubble, meet：Wherein, V0For gas flow rate, ρGasFor gas
Density, ρLiquidFor the density of water, g is acceleration of gravity.
It is further preferred that the air purifier from bottom to top includes air inlet, the second agitating unit, gas point successively
Layer of cloth, spraying layer and gas outlet, the gas distribution layers include first gas distribution layer and second gas distribution layer, the spray
Layer side is provided with inlet, and the air purifier bottom is provided with liquid outlet.
It is further preferred that be laid with the first gas distribution layer in annular shape, and outgassing direction is by side clockwise
To some slanted gas flow pipes clockwise, be laid with annular shape on the second gas distribution layer, and outgassing direction presses the inverse time
Some slanted gas flow pipes counterclockwise in pin direction.
It is further preferred that the bubble shredder is supersonic generator.
It is further preferred that the scope of the gas flow rate is 10m/s-30m/s.
It is further preferred that the frequency range of the supersonic generator is 70KHz~80KHz.
It is further preferred that the α, which is more than or equal to 30 °, is less than or equal to 60 °.
It is further preferred that second air inlet is further provided with network, it is two neighboring in the network
Spacing between grid is 0.2mm-0.5mm.
It is further preferred that it is further coated with hydrophobic layer in the network.
It is further preferred that the thickness of the hydrophobic layer is 0.02mm-0.08mm.
Compared with prior art, the present invention has advantages below：First, because gas by the first air blower enters water
Case can produce bubble, and the bubble for wrapping up impurity floats to liquid surface rupture, and impurity just stays in atmosphere again, and the present invention passes through setting
Bubble smashes unit and gas is smashed into caused bubble in the water tank so that and bubbles burst forms minute bubbles,
Impurity in bubble will stay in a liquid, can so strengthen dust removing effects；Second, the agitating unit is described for stirring
Water in water tank, increase the stingy residence time ducked in drink so that stingy duck in drink ruptures again, and clean gas will
Emerge, can further dedusting；Third, second air inlet is arranged at the side wall of the water tank, and institute diagonally downward
The side wall shape for stating the second air inlet and the water tank has angle ɑ, plays a part of anti-backflow, prevents the first air blower from not having work
When making, the aqueous reflux in water tank into pipeline, while with the agitating unit collective effect, can make air-flow formed arc line type fortune
It is dynamic, so as to increase the time of contact of bubble and water；Fourth, second air inlet is further provided with network, the grid
Spacing distance in structure between each small grid is 0.2mm-0.5mm, can be a plurality of by the gas column " cutting " for entering the water tank
Small gas column；Fifth, set and second gas distribution layer, two layers of air-flow provided with the first gas distribution layer in the air purifier
Slanted gas flow pipe outgassing direction on distribution layer is on the contrary, increase gas-liquid contact time, so as to improve air purification effect.
Brief description of the drawings
Accompanying drawing 1 is a kind of structural representation of the automatic dust removing apparatus of high-efficient purification air of the present invention；
Accompanying drawing 2 is a kind of automatic dust removing apparatus cisten mechanism schematic diagram of high-efficient purification air of the present invention；
Accompanying drawing 3 is a kind of automatic dust removing apparatus air purifier structural representation of high-efficient purification air of the present invention；
Accompanying drawing 4 is a kind of schematic diagram of the automatic dust removing apparatus network of high-efficient purification air of the present invention；
Accompanying drawing 5 is a kind of structural representation of the automatic dust removing apparatus second embodiment of high-efficient purification air of the present invention；
A kind of structural representation of the automatic dust removing apparatus 3rd embodiment of high-efficient purification air of the present invention of accompanying drawing 6.
Embodiment
1-4 is described in further detail with embodiment to the present invention below in conjunction with the accompanying drawings.
A kind of automatic dust removing apparatus of high-efficient purification air, including housing 1, the first air inlet 2 and the first air outlet 3, institute
State the outside of housing 1 and be provided with controller 4；First air inlet 2 is arranged on the top of housing 1, is provided with first air inlet 2
Sensor of dust concentration 5, first air inlet 2 by pipeline successively with the first air blower 6, water tank 7, air purifier 8, dry
Dry device 9, the second air blower 10 are connected with first air outlet 3；The top of water tank 7 is connected by water pipe with water inlet 11
Logical, the bottom of water tank 7 is connected by water pipe with delivery port 12；Unit 710 is smashed including bubble and is stirred in the inside of water tank 7
Mix unit 720；The sensor of dust concentration 5, first air blower 6, the bubble smash unit 710, the stirring list
Member 720, the air purifier 8, the drying unit 9 and second air blower 10 are electrically connected with the controller 4；
The bubble smashes unit 710 and is used to smash air into caused air pocket in the water tank 7；The agitating unit 720
For stirring the water in the water tank, the residence time that increase gas ducks in drink.
Fig. 2 is refer to, the air inlet for defining the water tank 7 is the second air inlet 13, in order to which increase that gas ducks in drink stops
Stay the time, it is preferred that second air inlet 13 can be arranged on diagonally downward the side wall of the water tank 7 and with the water tank
7 side wall shape has angle ɑ, under the collective effect of the agitating unit 720, air-flow can be made to form camber line as depicted
Type moves, so as to increase the time of contact of bubble and water.So, relative to bubble straight line discharge the water surface, the present invention in bubble
In impurity can have relatively long time and water contact so as to removing.Furthermore, it is contemplated that the buoyancy of gas flow rate, water (can
To control active force caused by liquid rotating speed suitable with the resistance of water, so as to cancel out each other) collective effect, can accurately obtain
Take second air inlet 13 and the distance S of the bottom of the water tank 7.
Specifically, the velocity component of the bubble of second air inlet 13 vertically downward meets：VUnder=cos α * V0；
And now bubble is substantially met by buoyancy and acceleration：FIt is floating=1/8* ρLiquid*g*VVolume=-ma=-a* ρGas*VVolume；
In addition, after the t times, bubble reaches bottom, and speed is 0 simultaneously, now, meets：cosα*V0+ at=0；
Therefore t meets：S=V againUnder*t+1/2*at2。
It can thus be concluded that second air inlet 13 and the distance S of the bottom of the water tank 7, meet：
Wherein, V0For gas flow rate, ρGasFor gas density, ρLiquidFor the density of water, g is acceleration of gravity.The gas flow rate V0By described
The power of first air blower influences, the gas flow rate V0Increase, the gas with the power increase of first air blower 6
Flow velocity V0Scope be 10m/s-30m/s.Preferably, the gas flow rate V0Scope be 15m/s-25m/s.In the present embodiment,
The gas flow rate V0Scope be about 20m/s.Additionally, it is preferred that, the α can be more than or equal to 30 ° and be less than or equal to 60 °, from
And the aqueous reflux in water tank can also be effectively prevented into pipeline, and cause distance that gas moved in water mean camber line most
It is long.It is furthermore preferred that the α, which can be more than or equal to 40 °, is less than or equal to 50 °.In the present embodiment, the α is about 45 °.
Further, since at second air inlet 13, air-flow can form gas column, and bubble has not been completed to be formed.Therefore,
Preferably, the bubble smashes unit 710 and second air inlet 13 and needs to set spaced a predetermined distance, defines described second
Air inlet 13 smashes the air line distance L of unit 710 with the bubble.It is furthermore preferred that its satisfaction of the air line distance L：
It is usually that directly air is passed through in water in the prior art, using the interaction of the impurity in water and air, from
And the pollutant in air is filtered.So the shortcomings that is：Due to the effect of the tension force of water, the air in pipeline can be direct
Larger bubble is produced into water, makes to be difficult to form effective contact between air and water, so makes the impurity in bubble difficult
Effectively to remove, the impurity in bubble can rise into downstream with bubble, reduce efficiency.Therefore in the present invention, pass through
Bubble smashes the setting of unit 710, air can be smashed into caused air pocket in the water tank 7, so as to greatly carry
Effective contact area between high air and water, make the effectively dissolving of the impurity in bubble with being removed in water.Further, will
The bubble is smashed unit 710 and set spaced a predetermined distance with second air inlet 13, so as to prevent the gas after smashing
Bubble further collects sequentially forms air pocket again.
It can be supersonic generator that the bubble, which smashes unit 710, the frequency range of the ultrasonic wave for 70KHz~
80KHz, when the frequency of the supersonic generator is high, the small range strenuous vibration around supersonic generator, when frequency is low,
Supersonic generator shakes on a large scale.The present embodiment, the frequency range of the supersonic generator is about 75KHz, described super
Sound wave can be that the center of circle forms frequency vibrations scope of the radius as 10cm-20cm using supersonic generator, and can be by this scope
Interior air pocket is smashed as a diameter of micron-sized minute bubbles.The diameter of second air inlet 13 can occur according to ultrasonic wave
The sphere of action selection of device, if the diameter of second air inlet 13 is too small, under conditions of identical flow velocity, dust arrester is in unit
Overall efficiency of dust collection in time is relatively low；If the diameter of second air inlet 13 is excessive, air-flow can largely pour into water tank,
Hinder effect of the supersonic generator to bubble.Preferably, a diameter of 2cm-6cm of second air inlet 13, so not
It can be only mutually adapted with the sphere of action of ultrasonic wave, can also protect overall efficiency of dust collection of the dust arrester within the unit interval
Hold in higher level.In the present embodiment, a diameter of 4cm of second air inlet 13.
The power of agitator of the agitating unit 720 increases with the increase of the gas flow rate.In addition, the agitating unit
720 can stir clockwise or counterclockwise along a fixed-direction, formed an eddy flow so that gas duck in drink residence time change
It is long, increase dust removing effects.
In other embodiments, second air inlet 13 is further provided with network 14, so as to enter institute
The gas column " cutting " for stating water tank 7 is a plurality of small gas column.It is appreciated that between each small grid in the network 14
Away from it is too small when, a plurality of small gas column after " cutting " easily pools together again；When between each small grid in the network 14
Spacing it is too big when, be unfavorable for the air inlet of the water tank again.It is preferred, therefore, that in the network 14 between each small grid
Spacing distance is 0.2mm-0.5mm.In the present embodiment, it is preferred that the spacing distance in the network 14 between each small grid
About 0.3mm.Further, a hydrophobic layer 15, the hydrophobic layer 15 can be further coated in the network 14
Thickness be 0.02mm-0.08mm, it is preferred that the thickness of the hydrophobic layer 15 is 0.05mm, and then can be prevented after " cutting "
A plurality of small gas column easily pool together again.
Fig. 3 is refer to, the air purifier 8 from bottom to top includes air inlet 810, the second agitating unit 820, gas successively
Body distribution layer 830, spraying layer 840 and gas outlet 850, the gas distribution layers 830 include first gas distribution layer 831 and second
Gas distribution layers 832, the side of spraying layer 840 are provided with inlet 860, and the bottom of air purifier 8 is provided with liquid outlet
870.Be laid with the first gas distribution layer 831 in annular shape, and outgassing direction in the direction of the clock it is some clockwise
Slanted gas flow pipe 833, it is laid with the second gas distribution layer 832 in annular shape, and outgassing direction is counterclockwise
Some slanted gas flow pipes 834 counterclockwise, slanted gas flow pipe upper opening obliquely, is flowed up for the ease of air-flow, and is prevented
Only the liquid at spray by gas flow tube down, the slanted gas flow pipe outgassing direction on two layers of air flow method layer is on the contrary, increase
Gas-liquid contact time, so as to improve air purification effect.Preferably, the first gas distribution layer 831 and the second gas
Slanted gas flow pipe on distribution layer 832 is evenly distributed in gas distribution layers so that gas can uniformly pass through each air-flow
Pipe rises, it is preferred that the angle of inclination of the slanted gas flow pipe is 30 ° -60 °, effectively avoids the liquid at spray from passing through gas
Flow tube down hinders air flows upwards, and in the present embodiment, the angle of inclination of the slanted gas flow pipe is 45 °.
In other embodiments, the outside of housing 1 is provided with display screen and control panel, the display screen and chain of command
Plate is electrically connected with by wire and the controller 4.
Fig. 5 is refer to, in a second embodiment, electrostatic precipitation net 16, the electrostatic precipitation net 16 can be further set
With the controller 4 by being electrically connected with, dedusting further can be carried out to air, strengthen dust removing effects.
Fig. 6 is refer to, in the third embodiment, ultraviolet sterilizer 17, the ultraviolet sterilization can be further set
After device 17 is connected to second air blower 10, the ultraviolet sterilizer 17 and the controller 4 are described by being electrically connected with
Ultraviolet sterilizer 17 is ultraviolet lamp.
In other embodiments, the top of housing 1 is provided with face water tank lookout mouths, and Tong crosses setting for Suo Shu lookout mouths
Meter, the clean-up performance of Water in Water Tanks can be observed at any time.
The foregoing is merely illustrative of the preferred embodiments of the present invention, is not intended to limit the invention, all essences in the present invention
God any modification, equivalent substitution and improvements done etc., should be included within the scope of protection of the invention with principle.
Claims (10)
- A kind of 1. automatic dust removing apparatus of high-efficient purification air, it is characterised in that：Including housing, the first air inlet and the first air-out Mouthful, the hull outside is provided with controller；First air inlet is arranged on housing tip, and first air inlet is provided with Sensor of dust concentration, first air inlet by pipeline successively with the first air blower, water tank, air purifier, drier, Second air blower is connected with first air outlet；The water tank top is connected by water pipe with water inlet, the water tank Bottom is connected by water pipe with delivery port；Inside the water tank unit and agitating unit are smashed including bubble；The dust is dense Degree sensor, first air blower, the bubble smash unit, the agitating unit, the air purifier, the drying Unit and second air blower are electrically connected with the controller；The bubble smashes unit and enters institute for smashing air State caused air pocket in water tank；The agitating unit is used to stir the water in the water tank, and what increase gas ducked in drink stops Stay the time；The air inlet for defining the water tank is the second air inlet, is arranged on the side wall of the water tank and second air inlet Had angle ɑ with the side wall shape of the water tank, and second air inlet and the distance S of the bottom of the water tank, meet：And second air inlet smashes the air line distance L of unit with the bubble, meet：Wherein, V0For gas flow rate, ρGasFor gas Density, ρLiquidFor the density of water, g is acceleration of gravity.
- 2. automatic dust removing apparatus according to claim 1, it is characterised in that：The air purifier from bottom to top wraps successively Air inlet, the second agitating unit, gas distribution layers, spraying layer and gas outlet are included, the gas distribution layers include first gas point Layer of cloth and second gas distribution layer, the spraying layer side are provided with inlet, and the air purifier bottom is provided with liquid outlet.
- 3. automatic dust removing apparatus according to claim 2, it is characterised in that：It is laid with the first gas distribution layer and is in Annular shape, and some slanted gas flow pipes clockwise of outgassing direction in the direction of the clock, lay on the second gas distribution layer Have in annular shape, and some slanted gas flow pipes counterclockwise of outgassing direction counterclockwise.
- 4. automatic dust removing apparatus according to claim 1, it is characterised in that：The bubble shredder is ultrasonic wave Device.
- 5. automatic dust removing apparatus according to claim 1, it is characterised in that：The gas flow rate V0Scope be 10m/s- 30m/s。
- 6. automatic dust removing apparatus according to claim 4, it is characterised in that：The frequency range of the supersonic generator is 70KHz~80KHz.
- 7. automatic dust removing apparatus according to claim 1, it is characterised in that：α is more than or equal to 30 ° and is less than or equal to 60 °.
- 8. automatic dust removing apparatus according to claim 1, it is characterised in that：Second air inlet is further provided with grid Structure, the spacing in the network between two neighboring grid is 0.2mm-0.5mm.
- 9. automatic dust removing apparatus according to claim 8, it is characterised in that：It is further coated with dredging in the network Water layer.
- 10. automatic dust removing apparatus according to claim 9, it is characterised in that：The thickness of the hydrophobic layer is 0.02mm- 0.08mm。
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720711528 | 2017-06-19 | ||
| CN2017207115289 | 2017-06-19 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107456818A true CN107456818A (en) | 2017-12-12 |
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ID=60551708
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| CN201710853104.0A Pending CN107456818A (en) | 2017-06-19 | 2017-09-20 | A kind of automatic dust removing apparatus of high-efficient purification air |
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| CN110107337A (en) * | 2018-02-01 | 2019-08-09 | 北京源深节能技术有限责任公司 | Underground dust removal method |
| CN111905494A (en) * | 2020-07-31 | 2020-11-10 | 马鞍山科邦生态肥有限公司 | Microbial manure is with dustless apparatus for producing |
| CN114378426A (en) * | 2021-12-17 | 2022-04-22 | 浙江奥卡耐火材料有限公司 | Fiberboard cutting device |
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| CN114378426A (en) * | 2021-12-17 | 2022-04-22 | 浙江奥卡耐火材料有限公司 | Fiberboard cutting device |
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