CN103785265A - Novel indoor air purification device - Google Patents
Novel indoor air purification device Download PDFInfo
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- CN103785265A CN103785265A CN201410063115.5A CN201410063115A CN103785265A CN 103785265 A CN103785265 A CN 103785265A CN 201410063115 A CN201410063115 A CN 201410063115A CN 103785265 A CN103785265 A CN 103785265A
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Abstract
The invention provides a novel indoor air purification device. Water or an aqueous solution is used for absorbing various types of gas and granular pollution components in air, so that the aim of purifying the air is fulfilled; a Venturi throat opening is formed in an air channel; when the gas passes through the throat opening, the speed of gas flow is obviously increased, and high shearing force is formed in the gas flow, so that liquid entering the Venturi throat opening is sheared into extremely thin fog drops; after leaving the Venturi throat opening, the gas flow is slowed down and forms strong turbulent fluctuation, so that particles in the air and the extremely thin water drops can be in full contact and collision, and the particles in the air are transferred into liquid; the water drops in a turbulent fluctuation region also collide, and the water drops are re-enlarged, so that the water drops can be removed from a gas-liquid separation chamber, and the gas pollution components in the air are dissolved in the liquid so as to be absorbed and removed.
Description
Technical field
The present patent application relates to a kind of Novel indoor air purifier, mainly utilizes venturi (Venturi) effect and cleaning solution principle of absorption to carry out washing, purifying to room air, has the features such as volume is little, efficiency is high, clean and energy-conservation.
Background technology
The pollution of room air comes from the reason of indoor and outdoors two aspects.What indoor reason discharged in coating for wall surface, furniture paint, carpet or plank binding agent, all kinds of cleaning agents etc. comprises the volatile organic matter formaldehyde and dimethylbenzene.People live in new house in the near future easy ill room syndrome (sick building syndrome) be exactly not smooth owing to ventilating in new house, in air, be full of that more these gases cause; In addition all kinds of smells that enter room in all kinds of smells, toilet water closet and the sewer ventilation shaft discharging in culinary cuisine process, (comprise H
2s, two mercaptan, the organic or inorganic gases such as indoles), gas that smoking produces etc. has also formed the important sources of indoor polluted gas; The food of the sweat gland of human body, pet and storage also can distribute a lot of gas componants in room air in addition.In room air, the source of contained dust has: the particulate pollutant discharging in smoking and kitchen fume, people and pet exuviae skin and hair, each quasi-microorganism (comprising bacterium and mould and acarid etc.) of growing on air and the surface of solids is also the important sources of dust in room air.
Outdoor reason is mainly each pollutant in outside atmosphere through ventilation or aircondition or door and window and enters indoor.Outdoor reason is subject to the impact of outside atmosphere quality and degree has larger difference.The decline of China recent years atmosphere quality, the concentration increase of airborne finely ground particles PM2.5 particle causes haze weather to increase, and the concentration of indoor PM2.5 particle is improved greatly.In addition also likely formed, the important sources of indoor particle thing by people's the entrained dust of entering house of clothes, shoes and skin.
In the face of the control of indoor environmental quality, existing many different air purifiers are available in the market.These purifiers mainly use solid filtration media that air is filtered and purified.As adopt filter course and the foamed filter material of braiding or non-woven fiber to carry out the particle in filtered air.The mechanism of filtering comprises to be held back, collide, precipitates and adsorbs.In order to increase the specific area of filtration, reduce the service time of filtration resistance and prolongation filter screen, filter screen is processed to collapsed shape conventionally.Above-mentioned filter medium generally can not effectively be removed airborne gas componant, the removal of gas componant is mainly used the natural or artificial sorbing material such as activated carbon and zeolite, the mechanism of removing is mainly physics or chemisorbed, thereby the surface that by physics or chemical action, gas molecule is adsorbed on to adsorbing medium separates gas componant from gas.
Except the indoor air-purification device of above-mentioned use adsorbing medium, United States Patent (USP) (US Pat No6,280,691, US Pat No.4,138,220, US Pat No5,447,693, US Pat No5,252,299) disclosed the air cleaning unit that uses catalytic oxidation.For catalyst (Metal Palladium or aluminium) is played a role, these purifiers all must arrange air heating apparatus, and air themperature is heated to 200-500 °F.These catalytic oxidizing equipments generally can be removed airborne CO, NOx, SOx, H well
2s, NH
3and most of organic matter, but in order to recover energy, the air of heat also must reduce temperature by heat-exchange device to get off.But it is harmful to health that catalytic oxidation process may produce a certain amount of ozone, active carbon filtration layer also must be set conventionally ozone is removed.
Also have a class airhandling equipment to press to strengthen clean-up effect with high tele-release.Under high voltage electric field, electric discharge phenomena can occur, the airborne oxygen of electron excitation producing produces anion; Anion has very high oxidability, can make the oxidized decomposition of airborne organic matter, reaches the object purifying air, and anion also likely changes the electrical of particle dust surface simultaneously, and particle dust is easily filtered.This class purifier, except needs adopt potential device, has electrion parts, also can produce ozone simultaneously, must adopt active carbon or other sorbing material to remove.
Also have a class airhandling equipment to adopt ultraviolet photooxidation reaction device, these class methods, except using ultraviolet lamp tube, also must be used catalyst (metal platinum).Metal platinum is that noble metal is expensive, and the ultraviolet ray producing is as improper in shielded, and is irradiated to human body skin and may causes and burn and cutaneum carcinoma after leakage.
Patent US Pat No5,509,946 have disclosed a kind of filter, and water and active carbon and other filter medium are purified the air of a room.Built-in water pump is extracted water out from water tank, then by a water distribution head, water is injected in air flue, and makes filter medium wetting, thereby airborne dust and water miscible gas componant are transferred to and in water, made air cleaning.But this device is limited to the removal effect of particle and gas componant, still need to rely on use fiber filter media, foamed filter medium and activated carbon adsorbent, just can reach desirable effect.The above-mentioned catalytic oxidation of this device relative usage, anion and photocatalytic oxidation, make water help absorb gas and particulate component.But the method can not be removed water-fast gas componant, receive the restriction of filter medium specific area simultaneously, very limited for the removal effect of fine particle.
In sum, existingly purifier usedly generally remove airborne dust with fiber-like or foam class medium, adopt activated carbon to remove gas pollutant.In order to reach the effect of good removal dust, especially remove fine particle (sub-micron or approach the particle of submicron order) and generally must use thickening and/or fine and close filter material layer, certainly will cause like this air to pass through the resistance of filtering layer large, often need to adopt larger filter area to reduce filtyration velocity and the pressure loss of air.After filtrate uses, must often change, otherwise not only resistance can further increase, and dust and bacterium that part is held back can come off and penetrate filter material layer, removal effect is lost completely.Often replace filtrate and can increase use cost for user.And use the wet method (US Pat No5,509,946) of shower water to filter, and the drop size causing due to spray is still larger, and assimilation effect is subject to the specific area restriction of moistening medium, little for the removal effect of molecule dust.
The existing method that removes gas pollutant with the natural or artificial sorbing material such as activated carbon or zeolite, often be subject to the restriction of indoor air cleaner volume, the use amount of sorbing material can not be too many, make the adsorption effect of device undesirable, and the surface of sorbing material is easily adsorbed saturated, as regeneration or replacing not in time, will lose effect completely.
Thereby adopt anion to make the removal of the electronegative increase of particle surface particle, although can increase to a certain extent the removal of particle, reduce filter course thickness.Produce negative electrical charge and need to use electrion, the manufacturing cost of device increases, and likely produces ozone simultaneously, active carbon filter net must be set and remove ozone.Use photochemical catalytic oxidation and the high temeperature chemistry catalytic oxidation of uviol lamp also to have similar problem, need to use uviol lamp or air heater, also need to use catalyst, manufacturing cost is higher simultaneously, also likely produce ozone, must use active carbon filter net to be removed simultaneously.
Summary of the invention
The present patent application, for the weak point in above-mentioned existing Techniques for Indoor Air Purification, provides the indoor air-purification device that a kind of main employing water or the aqueous solution are absorbing medium.Because gas and particulate component are mainly absorbed in water or the aqueous solution, therefore, can omit the use of follow-up fiber or foam filter screen and charcoal filter, or greatly extend their service life, improve air purification efficiency.And the aqueous solution can often be changed easily, thereby keep the clean of purifier inside, guarantee the effect of air cleaning.
Mentality of designing described in the present patent application is as follows: described indoor air-purification device makes water or the aqueous solution absorb airborne various gas and particle contamination composition, reaches the object purifying air.In order to reach desirable assimilation effect, venturi aditus laryngis is set in air duct, in the time that gas passes through aditus laryngis, air velocity enlarges markedly, and forms high shear force in air-flow, makes the liquid that enters venturi aditus laryngis be sheared into very thin droplet; Leave after venturi aditus laryngis, air velocity is slack-off, and forms strong turbulent fluctuation, can contact fully and collide, thereby airborne particle is transferred in liquid between airborne particle and superfine water droplet; Between turbulent fluctuation region water droplet and water droplet, also bump, and water droplet is become greatly again, thereby water droplet is removed gas-liquid separation is indoor, by it, the dissolving in liquid is absorbed and is removed airborne gaseous contamination composition.
Specifically, Novel indoor air purifier described in the present patent application, comprise air inlet and air outlet, it between air inlet and air outlet, is air flue, in air flue, be provided with successively intake chamber from air inlet to air outlet, venturi aditus laryngis, turbulent fluctuation district, gas-liquid separation chamber, air pump and absorption liquid circulating pump, air enters described indoor air-purification device from air inlet, after air inlet, establish intake chamber, in intake chamber, absorption liquid enters air duct, it after intake chamber, is venturi aditus laryngis, turbulent fluctuation district is set after venturi aditus laryngis, turbulent fluctuation is established gas-liquid separation chamber behind district, after gas-liquid separation chamber, establish the air pump for the gas after separating is extracted out by air outlet, after air pump, set out air port, have connector in gas-liquid separation chamber and be communicated to fluid reservoir, the liquid of separating can be flow back in fluid reservoir, on fluid reservoir, establishing an outlet is connected with the water inlet of absorption liquid circulating pump, the delivery port of absorption liquid circulating pump is linked in intake chamber by pipeline.
Further, the indoor dewater unit that is provided with of described gas-liquid separation, described dewater unit can adopt one or more the combination in following several form: 1, water collection device separates, adopt the gas-liquid separator of this separate mode can adopt any shape, separator inside is filled with receipts water packing, receiving water packing can be corrugated plating, ripple grid, honeycomb duct, fibrage accumulation body, or the accumulation body of the material such as particulate ceramic, water droplet is along with air enters after packing layer due to two phase flow effect, thereby water droplet bumps and leaves gas and separated with the surface of filler, 2, cyclone separator, the inner cylindrical shape that adopts of gas-liquid separator while adopting this separate mode, a certain tangential direction from turbulent fluctuation district gas out from cylindrical shape gas-liquid separator enters, the gas motion of spinning in separator inside, thus drop is subject to centrifugal action to leave air-flow and bumps and separated with cylindrical wall, 3, chemistry dehumidifying, adopt gas-liquid separation chamber while dehumidifying in this way and be provided with chemisorbed layer, the chemical dehumidizer of filling in chemisorbed layer, conventional chemical dehumidizer comprises silica gel, activated alumina, magnesium sulfate, calcium carbonate, calcium chloride, molecular sieve (crystalline aluminosilicate) etc., 4, condensation separation, condenser pipe is set while adopting this separation method in separation chamber, in the time that contacting with condenser pipe, air is cooled, the saturated vapor pressure of air reduces, under part steam just can condense on the surface of solids of contact with it, reduce airborne moisture, this method is mainly for the moisture of airborne gaseous state, but also contributes to the removal of the water droplet of graininess.
Further, between described air inlet and intake chamber, be also provided with and just consider layer, described first filter layer is for the airborne bulky grain dust of filtering, first filter layer can be made up of fiber that weave or non-woven, also can be by foamed filter material or other any medium composition that can form tiny air duct and part particle dust is filtered out.
Further, described venturi aditus laryngis is the aditus laryngis of rectangle aditus laryngis or circular aditus laryngis or any other shape, the combination of constant cross-section aditus laryngis or variable cross section aditus laryngis or constant cross-section aditus laryngis and variable cross section aditus laryngis.
Further, described variable cross section aditus laryngis is in the centre of venturi aditus laryngis or damper is set below, and the position of damping adjusting device can change shape and the size of venturi aditus laryngis.
Further, the mode of described intake chamber water inlet is spray mode or overflow mode, so that liquid can be evenly distributed to above venturi aditus laryngis.
Further, on described air inlet and/or gas outlet, be provided with shutter or grid, for adjusting the direction of air of access to plant, also can make the wind distributed uniform on admission section entering by graticule mesh is set.
Further, the connecting portion between described fluid reservoir and gas-liquid separation chamber is provided with and is connected screw socket or U-shaped or contract type draw-in groove with sealing ring.
Further, the built-in delivery port that is communicated with absorption liquid circulating pump of described intake chamber, is provided with nozzles/spray heads, dispenser or overflow pipe/groove on delivery port, and the liquid that makes to enter can be evenly distributed to and be positioned at intake chamber venturi aditus laryngis below.
Further, described venturi aditus laryngis is a slype, and at the air velocity of aditus laryngis inside, than at least exceeding one times before entering aditus laryngis, the gas flow rate in aditus laryngis is within the scope of 10-120 meter per second, more suitable in the scope of 30-100 meter per second.
The outlet of the venturi aditus laryngis turbulent fluctuation district of ining succession, turbulent fluctuation district is an empty region, between small water droplet and airborne particulate pollutant and gas pollutant and water droplet and water droplet, carry out mixing fully collision here, once entering liquid, particle and gas componant just no longer separate, after drop and droplet collision, also no longer separate, it is large that polymerization of fluid drops becomes.
Below gas-liquid separation chamber, be communicated to fluid reservoir to reclaim the absorption liquid of separating from gas-liquid separation chamber, for the liquid in fluid reservoir can be upgraded and supplement, fluid reservoir adopts spiral or card slot type design, and convenient manually taking off supplemented and cleaned.Fluid reservoir is generally placed on the below of gas-liquid separation chamber, make the liquid of gas-liquid separation chamber to flow to fluid reservoir by gravity, junction is between the two provided with sealing mechanism (as seal washer or U-shaped or contract type draw-in groove) filter this junction of when operation can not be leaked.Fluid reservoir has another opening and connects a pipeline, connects circulating pump by pipeline, and the other end of circulating pump passes to inhalant region, and is communicated with water-locator.
Further, the absorption liquid using comprises water or the aqueous solution, and the aqueous solution of indication refers to and in water, adds oxidant, reducing agent, inorganic salts, acid or alkali or metal-chelator, washing agent, organic solvent, or other water-soluble polymer.
Further, after described gas-liquid separation chamber, be provided with adsorption layer, described adsorption layer is activated carbon or other natural or artificial synthetic sorbing material (as zeolite, diatomite, molecular sieve, activated alumina, silica gel etc.) or their adsorption layer that mixture formed.
Further, after described gas-liquid separation chamber, blower fan is set, blower fan can provide enough driving forces to make air can continue to pass through inlet louver, first filter layer, intake chamber, venturi aditus laryngis, turbulent fluctuation district, gas-liquid separation chamber and active carbon adsorption floor, after blower fan, connect air port, air outlet also can be provided with shutter, to can adjust the direction of exit wind.
Further, the running status of described blower fan and absorption liquid circulating pump can be shown and be controlled by circuit board, described air inlet and/or air outlet can arrange one or more in particulate matter sensors, humidity sensor, pressure sensor, VOC sensor or temperature sensor, to detect and show air cleaning unit operation conditions and actual removal effect, and carrying out accordingly automatic or manual adjust operation operating mode.
Novel indoor air purifier described in the present patent application, principal character is to make water or the aqueous solution absorb airborne various pollutant component, reach the object purifying air, can overcome like this because mainly depending on filter medium the caused defect that purifies air, improve clean-up effect.By regularly changing absorption liquid, can make absorption liquid keep clean and clean-up effect can be kept for a long time, the dust of avoiding conventional method to bring in the time changing filter medium escapes.Owing to having used Venturi scrubbing principle, make the present invention there is the ability of stronger removal particle than other wet purifying decice, make the size of the dust that can remove reach submicron order, thereby can be used for effectively controlling PM2.5(particle diameter between 0.5-2.5 micron) particle concentration, and cannot effectively remove the particle of this magnitude range with traditional wet purifying decice.
The device of the present invention's design, except effectively removing airborne particle, can be removed airborne all kinds of gas pollutant simultaneously.For picture SO
2, formaldehyde, H
2s, NOx, toluene, benzoic acid, the gases such as phenol directly water absorb, and for picture dimethylbenzene, benzene, NO, waits gas can be absorbed by add a small amount of oxidant or solvent in water.And while using traditionally the sorbing materials such as activated carbon to remove these gas componants, must use more activated carbon in order to reach good removal effect, sorbing material is easily saturated, and regeneration difficulty.
Being different from use screen pack and active carbon filtration layer is main air cleaning unit, and the present invention can effectively remove submicron particles dust (PM2.5) and gaseous contamination composition simultaneously, does not need regularly to change filter screen or filter core.
Accompanying drawing explanation
Fig. 1 is the first embodiment schematic diagram of the Novel indoor air purifier described in the present patent application;
Fig. 2 is the second embodiment schematic diagram of the Novel indoor air purifier described in the present patent application;
Fig. 3 is the 3rd embodiment schematic diagram of the Novel indoor air purifier described in the present patent application;
Fig. 4 is the 4th embodiment schematic diagram of the Novel indoor air purifier described in the present patent application;
Fig. 5 is the 5th embodiment schematic diagram of the Novel indoor air purifier described in the present patent application;
Wherein, 1 is that air inlet, 2 is that intake chamber, 3 is that venturi aditus laryngis, 4 is that damper, 5 is that turbulent fluctuation district, 6 is that gas-liquid separation chamber, 7 is that water collection device, 8 is that blower fan, 9 is that air outlet, 10 is that shutter, 11 is that fluid reservoir, 12 is that absorption liquid circulating pump, 13 is that circulation fluid nozzle, 14 is that seal, 15 is that cyclone separator, 16 is that chemisorbed layer, 17 is that condenser, 18 is that first filter layer, 19 is activated carbon filter layer.
The specific embodiment
Below in conjunction with the drawings and specific embodiments, the Novel indoor air purifier described in the present patent application to be described without limitation, object is that the public understands described technical scheme better.
Embodiment mono-
Further illustrate the groundwork program of the embodiment of the present invention below in conjunction with Fig. 1.Contaminated air enters from air inlet 1, enter immediately intake chamber 2, in intake chamber 2, be provided with circulation cleaning nozzle for liquid 13, the cleaning solution pumping into from fluid reservoir 11 is evenly distributed to venturi aditus laryngis 3 through nozzle 13, air enters venturi aditus laryngis 3 together with cleaning solution, more than the speed of venturi aditus laryngis 3 interior air reaches 30 meter per seconds, be subject to the impact on venturi aditus laryngis 3 borders, in air-flow in venturi aditus laryngis 3, form very high velocity gradient, produce thus high shearing force, the cleaning solution that enters aditus laryngis is dispersed into evenly tiny water droplet.Be arranged at venturi aditus laryngis exit or inner damper 4 for regulating the size of air flue of venturi aditus laryngis 3, leave the rear air of venturi aditus laryngis 3 and enter turbulent fluctuation district 5, between the airborne particle in turbulent fluctuation district 5 or gas componant and water droplet, occur fully to react and be absorbed and enter in water droplet, after assembling between water droplet and water droplet, no longer separate so simultaneously, and again become large.In gas-liquid separation chamber 6, air enters in water collection device 7, and in water collection device 7, air advances in narrow sinuous passage, water droplet and parameatal surface collision and leave gas phase.Air clean after dehydration enters air outlet 9 through blower fan 8, reenters indoor.Shutter 10 can be optionally installed for air is carried out to rectification at air inlet 1 and air outlet 9, adjust the direction that air intlet confluxes and exports diffusion.
In the present embodiment, gas-liquid separation adopts water collection device 7 to carry out gas-water separation, enter in the air of water collection device 7 in gas-liquid separation chamber 6 and the narrow sinuous passage of the mixture of drop in water collection device 7 and advance, water droplet and parameatal surface collision and leave gas phase, cleaned air after dehydration enters air outlet slit 9 through blower fan 8, reenters indoor.
Embodiment bis-
In embodiment bis-, main body and the embodiment mono-of device are basic identical, difference is that gas-liquid separation adopts cyclone separator 15 to carry out gas-water separation, the drop that enters the cyclone separator 15 in gas-liquid separation chamber 6 with air is subject to centrifugal action to make centrifugal motion, and thereby air is left in the collision of the inwall of final and cyclone separator, cleaned air after dehydration enters air outlet slit 9 through blower fan 8, reenters indoor.
To the clean-up effect of room air, in table 1 and table 2, before access to plant, PM2.5 particle and the bulky grain concentration of room air are respectively 327 and 9 μ g/m
3.SO
2concentration is 200 μ g/m
3, concentration of formaldehyde is 300 μ g/m
3.
Table 1
Table 2
Embodiment tri-
In embodiment tri-, main body and the embodiment mono-of device are basic identical, difference is that gas-liquid separation adopts chemisorbed layer 16 to carry out gas-water separation, the gas-liquid mixture entering in gas-liquid separation chamber 6 enters in chemisorbed layer 16, moisture is adsorbed to the surface of chemical dehumidizer and leaves air, cleaned air after dehydration enters air outlet slit 9 through blower fan 8, reenters indoor.
Embodiment tetra-
In embodiment tetra-, main body and the embodiment mono-of device are basic identical, difference is that gas-liquid separation adopts condenser 17 to carry out gas-water separation, enter gas-liquid mixture in gas-liquid separation chamber 6 device 17 that is condensed cooling, moisture is agglomerated to the surface of condenser pipe and leaves air, cleaned air after dehydration enters air outlet slit 9 through blower fan 8, reenters indoor.
Embodiment five
In embodiment five; main body and the embodiment mono-of device are basic identical; difference is to adopt water collection device and chemical dehumidizer to mix the one design of gas-water separation; and be provided with air pre cleaner and charcoal filter simultaneously; device is suitable for the Combination Design shown in accompanying drawing 5; air inlet arrange the first filter layer 18 made from fiber remove air in larger dust; gas-liquid separator adopts the combination of water collection device 7 and chemisorbed layer 16; active carbon filtration layer 19 is also set afterwards, guarantees the quality of return air and normally work in the situation that there is no cleaning solution.
It should be understood that foregoing comprises that accompanying drawing is explanation technology contents of the present invention, and unrestricted; In fact the various modifications, made, improve, be equal to replacement, all within the present patent application technical scheme required for protection in Spirit Essence of the present invention.
Claims (10)
1. a Novel indoor air purifier, comprise air inlet and air outlet, it between air inlet and air outlet, is air flue, it is characterized in that: in air flue, be provided with successively intake chamber from air inlet to air outlet, venturi aditus laryngis, turbulent fluctuation district, gas-liquid separation chamber, air pump and absorption liquid circulating pump, air enters described indoor air-purification device from air inlet, after air inlet, establish intake chamber, in intake chamber, absorption liquid enters air duct, it after intake chamber, is venturi aditus laryngis, turbulent fluctuation district is set after venturi aditus laryngis, turbulent fluctuation is established gas-liquid separation chamber behind district, after gas-liquid separation chamber, establish the air pump for the gas after separating is extracted out by air outlet, after air pump, set out air port, have connector in gas-liquid separation chamber and be communicated to fluid reservoir, the liquid of separating can be flow back in fluid reservoir, on fluid reservoir, establishing an outlet is connected with the water inlet of absorption liquid circulating pump, the delivery port of absorption liquid circulating pump is linked in intake chamber by pipeline.
2. Novel indoor air purifier according to claim 1, it is characterized in that: the indoor dewater unit that is provided with of described gas-liquid separation, described dewater unit can adopt one or more the combination in following several form: water collection device separates, adopt the gas-liquid separator of this separate mode can adopt any shape, separator inside is filled with receipts water packing, receiving water packing can be corrugated plating, ripple grid, honeycomb duct, fibrage accumulation body, or the accumulation body of the material such as particulate ceramic, water droplet is along with air enters after packing layer due to two phase flow effect, thereby water droplet bumps and leaves gas and separated with the surface of filler, cyclone separator, the inner cylindrical shape that adopts of gas-liquid separator while adopting this separate mode, a certain tangential direction from turbulent fluctuation district gas out from cylindrical shape gas-liquid separator enters, the gas motion of spinning in separator inside, thus drop is subject to centrifugal action to leave air-flow and bumps and separated with cylindrical wall, chemistry dehumidifying, adopt the indoor chemisorbed layer that is provided with of gas-liquid separation while dehumidifying in this way, the chemical dehumidizer of filling in chemisorbed layer, conventional chemical dehumidizer comprises silica gel, activated alumina, magnesium sulfate, calcium carbonate, calcium chloride, molecular sieve (crystalline aluminosilicate) etc., condensation separation, condenser pipe is set while adopting this separation method in separation chamber, in the time that contacting with condenser pipe, air is cooled, the saturated vapor pressure of air reduces, under part steam just can condense on the surface of solids of contact with it, reduce airborne moisture, this method is mainly for the moisture of airborne gaseous state, but also contributes to the removal of the water droplet of graininess.
3. Novel indoor air purifier according to claim 1 and 2, it is characterized in that: between described air inlet and intake chamber, be also provided with and just consider layer, described first filter layer is for the airborne bulky grain dust of filtering, first filter layer can be made up of fiber that weave or non-woven, also can be by foamed filter material or other any medium composition that can form tiny air duct and part particle dust is filtered out.
4. Novel indoor air purifier according to claim 1 and 2, it is characterized in that: described venturi aditus laryngis is the aditus laryngis of rectangle aditus laryngis or circular aditus laryngis or any other shape the combination of constant cross-section aditus laryngis or variable cross section aditus laryngis or constant cross-section aditus laryngis and variable cross section aditus laryngis.
5. Novel indoor air purifier according to claim 4, is characterized in that: described variable cross section aditus laryngis is in the centre of venturi aditus laryngis or damper is set below, and the position of damping adjusting device can change shape and the size of venturi aditus laryngis.
6. Novel indoor air purifier according to claim 1 and 2, is characterized in that: the mode of described intake chamber water inlet is spray mode or overflow mode, so that liquid can be evenly distributed to above venturi aditus laryngis.
7. Novel indoor air purifier according to claim 1 and 2, it is characterized in that: on described air inlet and/or gas outlet, be provided with shutter or grid, for adjusting the direction of air of access to plant, also can make the wind distributed uniform on admission section entering by graticule mesh is set.
8. Novel indoor air purifier according to claim 1 and 2, is characterized in that: the connecting portion between described fluid reservoir and gas-liquid separation chamber is provided with and is connected screw socket or U-shaped or contract type draw-in groove with sealing ring.
9. Novel indoor air purifier according to claim 1 and 2, it is characterized in that: the delivery port of the built-in connection absorption liquid circulating pump of described intake chamber, on delivery port, be provided with nozzles/spray heads, dispenser or overflow pipe/groove, the liquid that makes to enter can be evenly distributed to and be positioned at intake chamber venturi aditus laryngis below.
10. Novel indoor air purifier according to claim 1 and 2, it is characterized in that: described venturi aditus laryngis is a slype, at the air velocity of aditus laryngis inside than at least exceeding one times before entering aditus laryngis, gas flow rate in aditus laryngis is within the scope of 10-120 meter per second, more suitable in the scope of 30-100 meter per second.Novel indoor air purifier according to claim 1 and 2, it is characterized in that: after described gas-liquid separation chamber, be provided with adsorption layer, described adsorption layer is activated carbon or other natural or artificial synthetic sorbing material (as zeolite, diatomite, molecular sieve, activated alumina, silica gel etc.) or their adsorption layer that mixture formed.Novel indoor air purifier according to claim 1 and 2, it is characterized in that: after described gas-liquid separation chamber, blower fan is set, blower fan can provide enough driving forces to make air can continue to pass through inlet louver, first filter layer, intake chamber, venturi aditus laryngis, turbulent fluctuation district, gas-liquid separation chamber and active carbon adsorption floor, after blower fan, connect air port, air outlet also can be provided with shutter, to can adjust the direction of exit wind.Novel indoor air purifier according to claim 1 and 2, it is characterized in that: the running status of described blower fan and absorption liquid circulating pump can be shown and be controlled by circuit board, described air inlet and/or air outlet can arrange one or more in particulate matter sensors, humidity sensor, pressure sensor, VOC sensor or temperature sensor, to detect and show air cleaning unit operation conditions and actual removal effect, and carrying out accordingly automatic or manual adjust operation operating mode.
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| CN106123165A (en) * | 2016-08-26 | 2016-11-16 | 陈曦 | A kind of indoor air comprehensive treatment device |
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0688595A1 (en) * | 1994-01-11 | 1995-12-27 | Eusebio Moro Franco | System for filtering residual contaminant particles for smokes and gas through atomized ultrafreezing |
| CN2458058Y (en) * | 2000-12-25 | 2001-11-07 | 武兴文 | Smoke prevention and dust control device |
| US7645432B1 (en) * | 2006-02-28 | 2010-01-12 | Hood & Motor Technology, Llc | Exhaust treatment system and method |
| US20110303594A1 (en) * | 2010-06-14 | 2011-12-15 | Glv Finance Hungary Kft, Luxembourg Branch | Flat plate membrane bioreactor with a liquid air separator |
| WO2012061068A2 (en) * | 2010-10-25 | 2012-05-10 | Diversey, Inc. | Method of using a tracer for monitoring water treatment agents in a wet air scrubber |
| CN204017604U (en) * | 2014-02-24 | 2014-12-17 | 深圳广昌达环境科学有限公司 | Novel indoor air purifier |
-
2014
- 2014-02-24 CN CN201410063115.5A patent/CN103785265A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0688595A1 (en) * | 1994-01-11 | 1995-12-27 | Eusebio Moro Franco | System for filtering residual contaminant particles for smokes and gas through atomized ultrafreezing |
| CN2458058Y (en) * | 2000-12-25 | 2001-11-07 | 武兴文 | Smoke prevention and dust control device |
| US7645432B1 (en) * | 2006-02-28 | 2010-01-12 | Hood & Motor Technology, Llc | Exhaust treatment system and method |
| US20110303594A1 (en) * | 2010-06-14 | 2011-12-15 | Glv Finance Hungary Kft, Luxembourg Branch | Flat plate membrane bioreactor with a liquid air separator |
| WO2012061068A2 (en) * | 2010-10-25 | 2012-05-10 | Diversey, Inc. | Method of using a tracer for monitoring water treatment agents in a wet air scrubber |
| CN204017604U (en) * | 2014-02-24 | 2014-12-17 | 深圳广昌达环境科学有限公司 | Novel indoor air purifier |
Non-Patent Citations (1)
| Title |
|---|
| 龚佰勋: "《环保设备设计手册-固体废物处理设备》", 1 June 2004, 化学工业出版社 * |
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