KR101946806B1 - the high efficient air pollutant eliminating device of both bad odorous material and fine dust using multi bubbles - Google Patents

Abstract

The present invention relates to an apparatus to remove fine dust and air pollutants and, more specifically, to an apparatus to remove odors, fine dust, and air pollutants by using multi-bubbles. According to the present invention, the fine dust and air pollutant removal apparatus (100) is able to be included in an air pollution removal apparatus or vehicle exhaust removal apparatus, and comprises an exhaust gas inflow pipe (110), a main tank (120), a porous panel (130), and a processing gas discharge pipe (140). Moreover, the fine dust and air pollutant removal apparatus (100) additionally includes a blower (210), an air chamber (220), and a pump (230). In addition, the fine dust and air pollutant removal apparatus (100) includes an exhaust gas guide part (111) and a bubble formation and discharge part (112) in the exhaust gas inflow pipe (110).

Description

BACKGROUND OF THE INVENTION 1. Field of the Invention [0001] The present invention relates to a high-efficiency air pollutant removing device,

The present invention relates to an apparatus for removing fine dust and air pollutants, and more particularly, to a high-performance removal apparatus for odor, fine dust, and air pollutants using multiple water films.

Due to the rapid development of industrial technology, the production scale has increased sharply, and as the scale of production increases, the pollution that follows is becoming a big social problem. The pollution includes soot, sulfur component, dust, NOx, heavy metal, garbage, etc. Some of them are recycled and used, but most of them are incinerated. Soot and dust are generated during incineration, and harmful components such as dust, odor component, acid and gas are ejected into the air in the form of smoke in the soot, and the smoke containing the pollution component is dispersed in the air, It is a fact that it gives to human being.

Recently, in a clean room system such as a semiconductor factory and a biotechnology field, a chemical filter and an air washer are used to prevent the yield of the product from being lowered due to the influence of gaseous contaminants (SOx, NOx, ammonia, To the air conditioning system.

Particularly, in recent years, there is a problem of fine dust (PM10), ultrafine dust (PM2.5) and molecular air pollutants (SOx, NOx) from automobiles and the like. Especially, Which has a noticeable adverse effect.

The dust collector separates various kinds of dust (general dust, zinc oxide, fume, wood powder, cotton, plaice, rice flour, flour, lead powder, etc.) A dust collector using a filter and a dust collector using a filter cloth as a means for filtering dust from the atmospheric air so that the atmospheric air is prevented from being contaminated by the dust.

The dust collector using the filter cloth has a basic structure in which a plurality of filter cloths made of a cylindrical filter type or an envelope filter type are installed in the housing. In operation, air containing dust is supplied to the inside of the housing And the sucked air has a flow that passes through the filter cloth and then is discharged to the outside of the housing.

Such conventional dust collecting apparatuses have been variously manufactured and used depending on the use place and use, and various techniques have already been known.

Korean Patent Laid-Open Publication No. 2000-0074807 (December 15, 2000) discloses a "rotary cleaning dust collector ". 1 is a diagram showing the overall structure of the rotary washing and dust collecting apparatus 100. FIG. As shown in the figure, the rotating cleaning dust collector 100 includes a plurality of

The support legs 103 are supported by the support legs 103, and the support legs 103 are installed vertically spaced apart from the ground.

The support legs 103 may be installed at a predetermined angle with a predetermined angle and may have a suitable number to support the rotary washing and dust collecting apparatus 100. A frame 134 for fixing and supporting the rotary cleaning dust collector 100 is provided above the support leg 103,

Or by screwing or welding. A casing 101 is installed on the frame 134. The casing 101 may have a cylindrical shape or a rectangular shape and may include a flange 128 at an intermediate portion of the casing 101 to separate the casing 101 for cleaning or repairing, Is fastened with a screw or the like.

At a substantially upper end portion of the casing 101, a sight glass 109 for viewing the inside of the casing 101 is attached. A gas inlet 107 for introducing gas into the casing 101 is provided near the upper end of the casing 101. First and second venturi portions 117 and 118 are protruded inward from the middle portion and the lower end portion of the casing 101. The venturi portion may be installed in an appropriate number as the case may be. A water tank 102 is installed at a lower end of the casing 101 and a turbo impeller 104 connected to the shaft 121 is rotatably installed at a lower portion of the casing. The shaft 121 is rotatably supported by two bearings 119 and 120. A shaft pulley 124 is installed at a lower end of the shaft 121 and a pulley 123 of the motor 125 And is connected to the impeller 104 by a belt so that the rotational force of the motor 125 is transmitted to the impeller 104. A drain port 111 is provided at a lower portion of the water tank 102 and is connected to a gas inlet port of another casing through an intermediate duct 105.

Further, Korean Utility Model Publication No. 1991-0002531 (Apr. 22, 1991) discloses "dust collecting apparatus for treating dust by high-pressure water spray ". As shown in Fig. 9, in the dust collecting apparatus using high-pressure water spray, when the dust generated in the dust generator 1 is discharged, the pump 14 The pump 13 sucks the filtered circulating water in the settling tank 5 through the supply pipe 12 and turns it into a high pressure state together with the external air to be injected into the pump so as to be supplied to the injection nozzle 3 And the high pressure is injected into the "L" -shaped bent portion 2a of the communication pipe 2 in the exhausting direction. The dust generated in the dust generator 1 due to the high-pressure spraying force is smoothly discharged and adhered to the droplets of fine droplets to be horizontally moved. In this state, when the water reaches the bent portion 2b, the contaminated water containing the dust flows down through the polluted water discharge pipe 4 connected to the lower part by the load into the settling tank 5, And is discharged to the outside. The contaminated water flowing into the settling tank 5 passes through the interstices 7 (7 ') and 7 (7' ') arranged up and down alternately with an interval therebetween while bending and moving. And is collected by the final filtration filter 8 to be filtered by the circulating water and supplied again to the pump 13. On the other hand, when dust is not generated sufficiently and dust collection is not required, the pump 13 is stopped, and only the blowing fan 14 And the exhaust gas is forcibly discharged. [0004] In the conventional art, since the spray nozzle is horizontally installed as a single large size, there is no possibility of clogging by dust, and the exhaust gas can be discharged smoothly without operating the blower fan The dust is precipitated in the sedimentation tank and collected, and the sediment is taken out and processed, so that the atmosphere and the river are not contaminated.

Korean Patent Registration No. 10-0379215 (Mar. 23, 2003) discloses a "dust collector having a cylindrical filter bag and a rectangular tubular filter bag integrally ". The present invention relates to a dust collector using a monofilament filter cloth in which a conventional cylindrical filter is combined with a square tubular filter cloth. In the dust collector, suction of mixed air is performed at the upper part of the housing, So that the dust in the mixed air sucked into the housing is of course different from that of the respective cylindrical bag filters. So that the exhausted dust is allowed to smoothly recover while freely falling in the direction of gravity without any interference.

The present invention relates to a method for extracting valuable metals from gold processing wastes such as a waste printed circuit board, a waste electrical circuit, a waste printed circuit board discharged from electronic equipment, or gold abrasion wastes, and various hydrochloric acid injection devices, nitric acid injection devices And to provide a high-performance removal device for fine dust and air pollutants using a multi-membrane to remove odor and atmospheric pollutants generated by the water.

The present invention also relates to a device for removing high-performance fine dust and air pollutants using a multi-layer membrane for removing gaseous contaminants (SOx, NOx, ammonia, organic substances) in the air provided in clean room systems such as semiconductor factories and biotechnology fields. .

The present invention also relates to a method for removing pollutants such as fine dust (PM10), ultrafine dust (PM2.5), and molecular air pollutants (SOx, NOx) from automobiles, And to provide a high-performance removal device for fine dust and air pollutants using a water film.

SUMMARY OF THE INVENTION The present invention has been made to solve the above-

An air pollution remover or an automobile exhaust gas remover,

The present invention provides a high performance removal apparatus 100 for fine dust and air pollutants using a multi-membrane including an exhaust gas inflow pipe 110, a main tank 120, a porous panel 130, and a process gas exhaust pipe 140 .

The present invention also provides a high performance removal apparatus 100 for fine dust and air pollutants using a multi-membrane, to which a blower 210, an air chamber 220 and a pump 230 are further added.

In addition, the present invention is characterized in that the exhaust gas inflow pipe (110) comprises an exhaust gas guiding portion (111) and a water film forming and discharging portion (112). The high performance removal of fine dust and air pollutants using a multi- Device 100 is provided.

The apparatus for removing fine dust and air pollutants using a multi-membrane according to the present invention extracts valuable metals from gold waste, such as waste printed circuit boards, waste electrical appliances, waste printed circuit boards discharged from electronic equipment, And 99.99% or more of odor and atmospheric pollutants generated due to various hydrochloric acid injection devices and nitric acid injection devices can be removed.

In addition, the apparatus for removing high-performance fine dust and air pollutants using a multi-membrane according to the present invention removes gaseous contaminants (SOx, NOx, ammonia, organic substances) in the air that are provided in clean room systems such as semiconductor factories and biotechnology fields. A remarkable effect appears.

The apparatus for removing high-performance fine dust and air pollutants using a multi-membrane according to the present invention is characterized in that the fine dust (PM10), ultrafine dust (PM2.5) and molecular air pollutants (SOx, NOx) %, And it is particularly effective in removing odor pollutants from industrial sites.

BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a structural view of a high-performance removal apparatus for fine dust and air pollutants using a multi-membrane according to the present invention; FIG.
1B is a structural view of another embodiment of a device for removing high-performance fine dust and air pollutants using a multi-membrane according to the present invention.
1C is a structural view of another embodiment of a device for removing high-performance fine dust and air pollutants using a multi-membrane according to the present invention (equipped with a wind power enhancing device).
FIG. 2 is a detailed structural view of an exhaust gas inflow pipe of a device for removing high-performance fine dust and air pollutants using a multi-membrane according to the present invention. FIG.
3 is a structural view of a perforated panel of an apparatus for removing high-performance fine dust and air pollutants using a multi-membrane according to the present invention.
Fig. 4 is a structural view of a device for removing a wire mesh membrane system used for removing odors in the related art. Fig.
5 is a structural view of a wind power enhancement device for a high-performance removal device for fine dust and air pollutants using a multi-membrane according to the present invention.
FIG. 5B is a view illustrating a blower air outlet structure of a wind power enhancing device for a high-performance removal device for fine dust and air pollutants using a multi-membrane according to the present invention. FIG.

Hereinafter, the present invention will be described in detail with reference to the drawings.

The present invention provides an apparatus 100 for removing high-performance fine dust and air pollutants using a multi-membrane, which can be included in an air pollution eliminating apparatus or an automobile exhaust gas removing apparatus.

The apparatus 100 for removing high-performance fine dust and air pollutants using the multi-membrane according to the present invention is installed and used as an air pollution removing apparatus or a fine dust removing apparatus for removing exhaust gas from a diesel vehicle generating a large amount of fine dust .

The present invention relates to a high performance removal apparatus 100 for fine dust and air pollutants using multiple water membranes comprising an exhaust gas inflow pipe 110, a main tank 120, a porous panel 130, and a process gas exhaust pipe 140, Lt; / RTI >

As shown in FIG. 1, the present invention is characterized in that a liquid 150 capable of forming a water film is contained in a main tank 120, and an automobile exhaust gas or an air pollution exhaust gas Etc.) into the main tank to generate a water film and apply the discharged gas to the water film to remove the liquid film.

The exhaust gas inflow pipe 110 of the present invention means an apparatus or means for allowing air or automobile exhaust gas containing air pollutants such as fine dust to flow into the main tank 120.

The exhaust gas inlet pipe 110 is connected to an air chamber 220 and the air chamber 220 is connected to a blower 210 so that a blower 220 to be treated.

The exhaust gas inflow pipe (110) of the present invention comprises an exhaust gas delivery portion (111) and a water film forming and discharging portion (112).

As shown in FIG. 2, the exhaust gas guiding portion 111 refers to a device or means for introducing the exhaust gas introduced from the air chamber 220 into the main tank 120.

The water film forming and discharging unit 112 refers to an apparatus or means connected to the discharge gas guiding unit 111 and capable of contacting the liquid 150 capable of forming a water film inside the main tank 120 do.

The liquid 150 (hereinafter referred to as "liquid") capable of forming the water film of the present invention is a concept that includes all liquids capable of forming bubbles by blowing wind or the like.

The liquid 150 capable of forming the water film of the present invention means ordinary water, acidic or basic liquid, water containing chemicals, and the like.

Preferably, the liquid of the present invention is effective to use ordinary water.

The liquid of the present invention can be a mixed liquid in which water and various explosive chemicals are mixed.

The water film of the present invention means a shape or a structure in which the liquid 150 is formed by bubbles or the like by the wind and the exhaust gas, and these droplets are formed by aggregation or dispersion to occupy space.

As shown in FIG. 2, the water film of the present invention means that the wind and exhaust gas and the liquid 150 are mixed and dispersed to form bubbles B and the like, and these droplets B are formed by aggregation or dispersion, Means the form or structure occupying

As shown in FIG. 2, the water film forming and discharging unit 112 may be in the form of a tube, and the end 113 cut in a slanting line on the horizontal plane S of the liquid 150 is formed, And the other part of the gas is brought into contact with the horizontal surface S of the liquid.

The water film forming and discharging unit 112 forms a terminal 113 cut in a slanting line on the horizontal plane S and a part of the terminal 113 cut in a slanting line on the horizontal plane S contacts the liquid 150 And the remaining part of the end 113 cut by the oblique line on the horizontal plane S is exposed to the liquid free space of the main tank so that the liquid is bubbled by the gas flowing into the main tank 120, The water film is formed as a whole in the space where there is no liquid in the main tank.

The principle in which the water film is formed as a whole in the liquid free space of the main tank is that a part of the end 113 cut by the slanting line on the horizontal plane S is in contact with the liquid 150 and the slanting line on the horizontal plane S The remaining part of the cut end 113 is exposed to the liquid-free space of the main tank, so that the exhaust gas, which is pressurized by the blower 210, is formed because the horizontal surface S of the liquid in the main tank is strongly blown.

Accordingly, the exhaust gas inlet pipe 110 is configured such that the exhaust gas introduced into the main tank 120 is primarily discharged to the outside of the main tank 120 due to the structure and function of the exhaust gas delivery portion 111 and the water film forming / (150) to adsorb and remove air pollutants such as fine dust, odor-inducing substances, NOx, and SOx contained in the exhaust gas.

In the present invention, the air pollution material that can not be removed even if it is in contact with the liquid secondarily forms a water film forming and discharging part 112, which is formed with a sloped end 113 on the horizontal plane S, Since the water film is formed as a whole in the liquid free space of the tank, the exhaust gas passes through the space where the water film is formed and the exhaust gas is discharged outside the main tank, so that the effect of adsorbing and removing the air pollutants by the water film appears.

In addition, the water film formed in the liquid-free space of the main tank adsorbs air pollutants, and then the water films coalesce with each other and fall into the liquid, so that the ability to remove air pollutants remarkably increases.

According to the present invention, the removal rate of dust such as fine dust is 99.9999% or more due to the removal of adsorption by the liquid and the removal of adsorption by the water film.

Particularly, the removal rate of vapor or liquid odor-inducing substances such as aqua regia is 99.99% or more.

Particularly, when the present invention is applied to a device for removing exhaust gas of a vehicle, the following effects as shown in Table 1 are obtained.

By Device PM10 NOx SOx HC CO Remarks  DPF 80% 0 % 0 % 80% 90% No molecular air pollutants can be removed
Non-road driving Low-speed vehicles can not be attached  p-DPF 50% 0 % 0 % 60% 60% No molecular air pollutants can be removed
Low dust removal efficiency  DOC 24% 0 % 0 % 55% 85% No molecular air pollutants can be removed
Low dust removal efficiency  Invention 85% 85% 85% 85% 85% Water-based, molecular (aqueous) removal of air pollutants is possible.

[Pollutant Removal Rate in Application to Exhaust Gas Removal Apparatus of Vehicle according to the Present Invention]

As can be seen from the above, the present diesel particulate filter (DPF), "p-DPF" and "DOC" are currently used for the diesel particulate filter. However, these devices are not only low in dust removal efficiency, There is a problem that it is impossible to remove the atmospheric pollutants (SOx, NOx) at all.

However, the present invention is capable of removing more than 85% of molecular air pollutants which can not be removed by the conventional devices, and capable of removing more than 85% of fine dust (PM10) and ultrafine dust (PM2.5).

Further, the present invention exhibits an excellent effect for removing odors such as aqua regia and mercaptane, and exhibits remarkably high economic efficiency.

As shown in FIG. 4, a conventional apparatus for removing odors uses a wire mesh membrane type removing apparatus. In the wire mesh screen removing apparatus, a wire mesh is densely installed and water is uniformly flowed through a wire mesh surface to form a water membrane. And the polluted air is permeated through the filter to remove contaminants.

The removal system of the wire mesh membrane method is only about 50% of the total volume of the membrane, and when the wire mesh bundle is passed through four stages, the water-soluble chemical gas removal performance is only 75 to 85% It will take more than 40 million won,

There is a problem in that it can not be used in a dynamic place (automobile).

In addition, this method is applied only for industrial use and the utility to be used for automobiles is remarkably low.

However, in the present invention, a vortex is continuously generated in the main tank 120 having a closed cylindrical shape to form a dense water film on the upper part of the cylinder, and polluted air is passed through the dense water film to remove contaminants. The volume is about 99% of the total volume, and it is possible to remove more than 85% by the first pass, and it takes only about 5 ~ 8% of the facility cost of the apparatus for removing the wire mesh membrane,

In addition, it can be manufactured in a small and large form, and it can be installed in a dynamic place (automobile) such as a low-speed vehicle and a high-speed car, and the effect can be obtained for both industrial use.

The main tank 120 of the present invention means a device or means for containing a liquid 150 capable of forming a water film.

 As shown in FIG. 1, the main tank 120 of the present invention may have a cylindrical or rectangular storage tank structure.

Preferably, the main tank 120 has a cylindrical shape to advantageously form a water film.

The perforated panel 130 of the present invention is mounted inside the main tank 120 and is completely immersed or partially immersed in the liquid 150 of the main tank 120.

As shown in FIG. 1, one or more perforated panels 130 are installed and are arranged in a row in the main tank 120, which is very effective in forming a water film.

As shown in FIG. 3, the perforated panel 130 of the present invention has a plurality of pores 131 formed in the panel 132, thereby forming a water film in the process of passing liquid through the pores.

The principle of the liquid passing through the pores 131 of the perforated panel 130 is that the exhaust gas or the exhaust gas flowing into the exhaust gas inflow pipe 110 is dispersed or moved by the wind force by the blower 210 This dispersion or moving liquid passes through the pores 131.

1, the perforated panel 130 may be sequentially installed from the front to the distal end of the main tank 120, and the perforated panel 130 on the front part may be arranged in the perforated panel (131, 132) are provided so that the proportion of the immersed portion of the liquid gradually becomes smaller.

The perforated panel 130 of the present invention may be made of metal, wood, chemical material, polymer material, or the like.

The technical feature of the present invention is that the porous panel 130 is made of a polymeric material and is very effective in formation of a water film (bubble formation) due to a phenomenon of clogging or fouling of the pores 131 due to a liquid.

The polymer material of the present invention is obtained by mixing 20 to 50 parts by weight of polyethylene terephthalate (PET) with 100 parts by weight of polyethylene (PE)

butyl acrylate, n-butyl acrylate, isobutyl acrylate, sec-butyl acrylate, tert-butyl acrylate, butyl acrylate, ethyl acrylate, styrene, methyl methacrylate, benzyl acrylate, And 20 to 30 parts by weight of a mixture of two or more species,

Methyl methacrylate, acrylic acid, methacrylic acid, acrylonitrile, and benzyl methacrylate, and mixing 10 to 20 parts by weight of a mixture of two or more thereof,

0.1 to 5 parts by weight of a crosslinking agent, 0.1 to 0.5 parts by weight of an emulsifier, and 0.1 to 5 parts by weight of a plasticizer.

When the porous panel is made of the above-mentioned polymer material, the strength of the porous panel is remarkably increased, and in particular, the clogging of the pores 131 due to the liquid and the phenomenon of fouling are less likely to occur, .

The crosslinking agent may be at least one selected from the group consisting of 1,2-ethanediol di (meth) acrylate, 1,3-propanediol di (meth) acrylate, 1,4-butanediol di (meth) acrylate, Acrylate, propylene glycol di (meth) acrylate, butylene glycol di (meth) acrylate, 1,6-hexanediol di (meth) acrylate, divinylbenzene, ethylene glycol di (Meth) acrylate, triethylene glycol di (meth) acrylate, polyethylene glycol di (meth) acrylate, polypropylene glycol di (meth) acrylate, polybutylene glycol di They may be used alone or in combination of two or more.

The emulsifier may be an anionic, an anionic or an amphoteric emulsifier such as sodium, ammonium or potassium salts of alkyl sulfates having 4 to 30 carbon atoms such as sodium dodecyl sulfate, sodium dioctylsulfosuccinate, sodium dodecylbenzene sulfate, Etc. may be used.

Examples of the plasticizer include phthalic acid plasticizers such as dibutyl phthalate, dioctyl phthalate, diisononyl phthalate, diisodecyl phthalate and butyl benzyl phthalate; Phosphite-based plasticizers such as tricresyl phosphate, tri-2-ethylhexyl phosphate, cresyldiphenyl phosphate, and triaryl phosphate; Di-2-ethylhexyl adipate, diisodecyl adipate, and other aliphatic plasticizers; Low-molecular-weight paraffin having 5 to 200 carbon atoms, olefin, and the like, or a mixture of two or more thereof.

In the present invention, 0.1 to 3 parts by weight of the coating additive is mixed with 100 parts by weight of polyethylene (PE) to significantly improve the bubbling function and significantly improve durability by significantly reducing the frictional force of the pores of the porous panel. do.

The coating additive may be selected from the group consisting of water glass, MMA (methylmethacrylate), BAM (Buthylacrylmonomer), AN (Acrylonitrile), MAA (Methylacrylicacid), water, alkyl sulfonate, ammonium persulfate ((NH ₄ ) ₂ S ₂ O ₈ ) soda (NaHSO ₃₎ it means that the resulting composition was mixed while heating.

The composition comprises 100 to 150 parts by weight of a monomer MMA (methylmethacrylate), 100 to 150 parts by weight of BAM (Butyllacrylonomer), 5 to 10 parts by weight of AN (Acrylonitrile), 5 to 10 parts by weight of MAA (Methylacrylicacid) 7 parts by weight,

(NH ₄ ) ₂ S ₂ O ₈ ) 0.5 to 5 parts by weight and sodium bisulfite (NaHSO ₃ ) 0.5 to 5 parts by weight based on 100 parts by weight of water, 100 to 150 parts by weight of water, 2 to 5 parts by weight of alkylsulfonate, Point.

The present invention relates to the above-mentioned polymer material by mixing 0.1 to 3 parts by weight of a natural reinforcing additive based on 100 parts by weight of polyethylene (PE) to change the polymer material environmentally, to increase the homogenization and uniformity of the porous panel, to significantly improve the acid resistance and the basicity .

It is more effective to add the above-mentioned natural reinforcing additive by using ethanol extracted as described below.

The above-mentioned natural reinforcing additive is blended with 100 parts by weight of windshield with 80 to 120 parts by weight of gossam, 80 to 120 parts by weight of the right-wing, 50 to 80 parts by weight, 30 to 55 parts by weight, 30 to 55 parts by weight, 50 to 80 parts by weight of a granule, 50 to 80 parts by weight of a granule, 100 to 150 parts by weight of a granule, 80 to 120 parts by weight of a godsend line, 80 to 120 parts by weight of a granulite, 80 to 120 parts by weight of a granule, Refers to a composition obtained by mixing and extracting 80 to 120 parts by weight of Angelica gigas Nakai, 80 to 120 parts by weight of Angelica gigas Nakai, 80 to 120 parts by weight of Angelica gigas, 80 to 120 parts by weight of crustacea, and 80 to 120 parts by weight of Angelica keiskei koidz.

As a method of extracting natural additives, 100 parts by weight of the raw material mixed with the above-mentioned weight unit may be mixed with 100 to 5,000 parts by weight of water and extracted by heating.

When 1000 parts by weight of water is mixed with 100 parts by weight of the raw material and extracted, about 800 to 1000 parts by weight of the extract is obtained.

In addition, as a method for extracting the above-mentioned natural additives, 1,000 parts by weight of 75 to 85% [mass%] ethanol is added to 100 parts by weight of the raw material mixture, refluxed for 2 to 4 hours and the filtrate is concentrated under reduced pressure , And concentrated.

Preferably, 1000 parts by weight of 80% [mass%] ethanol is added to 100 parts by weight of the raw material mixture, refluxed for 3 hours, and the filtrate is extracted with a rotary evaporator.

Such an extract may be extracted in a powder form in an amount of about 5 to 25 parts by weight based on 100 parts by weight of the mixed raw material. The extract is diluted with distilled water and diluted to about 800 to 1000 parts by weight based on 100 parts by weight of the raw material (I.e., distilled water + powdery extract) is preferably added.

The present invention exhibits the effect of exhibiting the acid resistance, the basicity and the abrasion resistance of the porous panel by mixing the above-mentioned functional substance with the functional additive.

The present invention improves the flexibility of the porous panel by mixing 0.05 to 2 parts by weight of the functional additive based on 100 parts by weight of the polyethylene (PE) with the above-mentioned polymer substance, thereby maximizing the bubble function through the pores even when the porous panel is made thin, .

The above-mentioned functional additive is characterized in that 200 to 300 parts by weight of an acrylic resin and 30 to 50 parts by weight of an isocyanate are mixed with 100 parts by weight of a mixture of acetone, methyl acetate and cellosolve acetate.

The mixing ratio of acetone, methyl acetate and cellosolve acetate is suitably adjusted to 0.1 to 1.5, and 0.1 to 1.5, based on acetone 1, of methyl acetate and cellulose sulphate.

The process gas discharge pipe 140 of the present invention means an apparatus or means through which exhaust gas or the like processed in the main tank 120 is discharged.

As shown in FIG. 1, the process gas discharge pipe 140 is preferably installed at the upper end of the main tank 120.

The present invention provides a high performance removal apparatus 100 for fine dust and air pollutants using a multiple water film having a blower 210, an air chamber 220 and a pump 230.

The blower 210 of the present invention operates the blowing force to the hood 233 into which air or automobile exhaust gas having air pollutants such as transport liquid and fine dust are carried by the pump 230, 210). ≪ / RTI >

The blower 210 may be a turbine or the like having a speed reducer, such as a conventional blower, a motor, or the like.

The present invention is characterized in that a wind power enhancing device 300 capable of improving the strength of wind power is added while significantly reducing power consumption of the blower 210 described above.

3B, the wind power enhancer 300 is installed between the blower 210 and the air chamber 220 and uses a blower 210 having a significantly low power consumption to control the noise of the blower 210, Thereby enhancing the wind pressure of the exhaust gas injected into the main tank, thereby improving the pollutant treatment efficiency of the exhaust gas.

As shown in FIG. 5, the wind power enhancer 300 includes an external wind inflow section 310 and a wind inflow section 320.

The external wind inflow section 310 may include a device or means for performing a function of mixing the wind from the blower 210 and wind from the outside of the wind power enhancer 300 into the wind inflow section 320 it means.

The external wind inflow section 310 of the present invention includes an external inflow port 311, a blower wind section 312, a blower wind outlet 313, a blower wind inlet port 314, a blower connection section 315, and a recess 316 .

The external inlet 311 functions to introduce wind from the outside of the wind power enhancer 300.

The outer inlet 311 is in the form of a hole, the cross-sectional area of the diameter of the front portion is wide, and the cross-sectional area of the diameter of the inner inlet 311 becomes narrower as it enters the interior.

The blower wind portion 312 is formed in the form of an empty hollow tube and is a space through which the air flowed from the blower 210 can be temporarily retained. Thus, the air blown from the blower 210 to the external inlet As shown in FIG.

The blower wind portion 312 of the present invention is formed by the structure of the concave portion 316 and the space forming portion 322.

The concave portion 316 is recessed inside the external wind inflow portion 310 and is coupled with the space forming portion 322 to form the blower wind portion 312.

The blower air outlet 313 refers to a structure or an apparatus that performs the function of introducing the wind during the stay of the blower fan 312 into the inflow pipe 324.

As shown in FIG. 5B, the blower air outlet 313 is composed of a tube formed by the coupling structure of the direction changing portion 313-1 and the space forming portion 322. FIG.

The direction switching unit 313-1 means an apparatus or means for performing the function of switching the wind from the blower wind unit 312 to the direction of the inflow pipe 324.

The space forming portion 322 is a device or structure that is combined with the external wind inflow portion 310 to form the blowing wind portion 312.

The blower wind inlet 314 is a structure or device that performs the function of allowing the wind from the blower 210 to flow into the blower 312.

The blower air inlet 314 is connected to the blower connection 315.

The blower connection unit 315 is a structure or apparatus that performs a function of connecting the blower pipe 211 of the blower 210 with the blower pipe 211.

The wind blowing unit 320 of the present invention means a structure or apparatus that performs a function of blowing air into the air chamber 220.

The wind blowing unit 320 includes a coupling control unit 321, a space forming unit 322, a wind outlet 323, and an inlet pipe 324.

The coupling regulator 321 performs a function of coupling the wind injecting unit 320 with the external wind inflow unit 310 and a function of controlling the size of the space of the blower wind unit 312.

The operation of adjusting the size of the space of the blower wind part 312 is performed by the screw adjusting part 321 having a screw part 321-1 so that the coupling adjusting part 321 is rotated by the rotation of the screw, As shown in FIG.

The space forming part 322 is a structure or an apparatus which is combined with the concave part 316 of the external wind inflow part 310 to form the blowing wind part 312 as described above.

The wind outlet 323 functions to allow the wind from the blower fan 312 and the external inlet 311 to mix and flow into the inlet pipe 212 of the air chamber 220.

Thus, the wind outlet 323 is connected to the inlet pipe 212 of the air chamber 220.

The wind power enhancement device 300 according to the present invention significantly increases the wind volume and wind force by introducing winds 4 to 5 times the amount of wind to be blown by the blower 210 from the outside, Significant enhancement effect appears.

The air chamber 220 of the present invention means an apparatus or means for making the concentration of the pollutants of the exhaust gas or the exhaust gas introduced by the blower 210 constant.

As shown in FIG. 1B, the air chamber 220 is connected to the blower 210 and is connected to the exhaust gas inlet pipe 110 to introduce the exhaust gas into the main tank 120.

The pump 230 of the present invention means an apparatus or means for circulating the liquid 150 in the main tank 120 and introducing the liquid 150 into the hood 233.

The pump 230 may be a conventional pump capable of circulating the liquid.

The pump 230 of the present invention allows the liquid to flow into the hood 233 through the pump tube 232 and the filter unit 231 to the pump tube 232 to filter the suspended matter of the liquid .

The pump 230 of the present invention functions to allow the liquid tank 234 to be replenished when the liquid tank 150 is short of the main tank 120 due to the connection of the liquid tank 234.

The present invention provides an apparatus (100) for removing high-performance fine dust and air pollutants using multiple water films having the above-described structure and function.

INDUSTRIAL APPLICABILITY The present invention is very useful in an industry for producing, manufacturing, selling, distributing and researching an apparatus for removing fine dust, exhaust gas and the like.

Particularly, the present invention is very useful for an industry that manufactures, manufactures, sells, distributes and researches devices for removing odorous substances such as exhaust gas, fine dust,

The exhaust gas inflow pipe 110, the main tank 120, the perforated panel 130, the process gas exhaust pipe 140,
A delivery portion 111, a water film forming and discharging portion 112,
High-performance removal equipment for odor, fine dust and air pollutants (100)
The blower 210, the air chamber 220, the pump 230,
The wind power enhancer 300, the external wind inflow section 310, the wind inflow section 320,

Claims (3)

An air pollution remover or an automobile exhaust gas remover,
An exhaust gas inflow pipe 110, a main tank 120, a perforated panel 130, and a process gas exhaust pipe 140,
A blower 210, an air chamber 220, and a pump 230 are further added,
A wind power enhancing device 300 is installed between the blower 210 and the air chamber 220,
The wind power enhancement apparatus 300 includes an external wind inflow section 310 and a wind inflow section 320,
The external wind inflow section 310 includes an external inflow port 311, a blower wind section 312, a blower wind outlet 313, a blower wind inlet port 314, a blower connection section 315, and a recess 316 Respectively,
The external inlet 311 is in the form of a hole and has a cross-sectional area of a diameter of the front part is wide and a cross-sectional area of a diameter of the inside diameter becomes narrower as it enters the inside,
The blower wind portion 312 is formed in the form of an empty hollow tube and is a space in which the air flowed from the blower 210 can be temporarily retained so that the air blown from the blower 210 to the outside inlet And the like,
The blower air outlet 313 includes a tube formed by a coupling structure of the direction changing portion 313-1 and the space forming portion 322,
And the direction switching unit 313-1 performs a function of switching the wind from the blower unit 312 to the direction of the inflow pipe 324. The multi- High performance removal device (100).
delete The method according to claim 1,
Wherein the exhaust gas inflow pipe (110) comprises an exhaust gas guiding portion (111) and a water film forming and discharging portion (112). The apparatus (100) for removing fine dust and air pollutants using a multi - .

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