KR101874338B1 - Complex type odor eliminator - Google Patents

Complex type odor eliminator Download PDF

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Publication number
KR101874338B1
KR101874338B1 KR1020180026082A KR20180026082A KR101874338B1 KR 101874338 B1 KR101874338 B1 KR 101874338B1 KR 1020180026082 A KR1020180026082 A KR 1020180026082A KR 20180026082 A KR20180026082 A KR 20180026082A KR 101874338 B1 KR101874338 B1 KR 101874338B1
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South Korea
Prior art keywords
gas
water
dust
odor
storage tank
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KR1020180026082A
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Korean (ko)
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윤창진
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(주)이화에코시스템
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/02Separating 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/06Spray cleaning
    • B01D47/063Spray cleaning with two or more jets impinging against each other
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26Drying gases or vapours
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/75Multi-step processes

Abstract

The present invention relates to a complex odor removing device. More specifically, the device comprises: a body shaped into a rectangular panel; a vortex dust removing unit collecting odor through first and second demisters; a multistage chemical cleaning unit collecting fine dust and secondarily removing odor; a dust and moisture removing unit tertiarily collecting and removing remaining water particles and dust through fourth and fifth demisters; and an activated carbon adsorbing unit finally collecting and removing dust and odor, and then, discharging purified gas to the outside. As such, the present invention is capable of completely collecting and removing dust and odor contained in organic or inorganic gas.

Description

Complex type odor eliminator

More particularly, the present invention relates to a composite odor eliminating apparatus, and more particularly, to a composite odor eliminating apparatus which comprises a body having a predetermined area, a vortex type dust removing unit, a multistage chemical liquid cleaning unit, a dust and moisture removing unit, , It is passed through a vortex type dust removal unit in which various organic or inorganic gases generated in places such as a sewage treatment plant, a manure treatment plant, a food processing facility, an animal husbandry facility and the like are contained in a large amount of mixed odor and fine dust, First, the fine dust (microscopic dust) is immersed in water in a storage tank. The bad smell is collected not only in the water in the storage tank but also through a double-mounted demister. Subsequently, A multi-stage drug solution cleaning unit having a single or double deodorization tower form, And then the residual particles and dust are thirdly captured and removed through a dust and moisture removing unit, and then finally passed through the activated carbon adsorption unit and finally the odor is deodorized. The present invention relates to a complex odor eliminating apparatus which can completely deodorize and collect odor and dust contained in an inorganic gas.

Generally, in places such as sewage treatment plants, sewage treatment plants, food processing facilities, and livestock facilities, a variety of organic or inorganic gases are generated and a complex odor is generated. The odor due to this is a combination of alkaline, acidic and neutral, A single chemical liquid cleaning liquid such as an oxidizing agent (soda hypochlorite or the like) having a slower reaction rate than the reaction has a characteristic that effective treatment of the odorous gas becomes difficult.

As a method for removing the odorous gas on the basis of such characteristics, there are a method in which a plurality of nozzles are provided in the deodorization tower and water is brought into contact with the gas containing odor introduced into the deodorization tower from the deodorization tower (Adsorption method) in which an adsorbent layer such as activated carbon, silica gel and zeolite is disposed in a deodorization tower to adsorb odorous substances, or a method in which a specific microbial layer is disposed in place of the adsorbent, (Microbial contact method) and the like.

As described above, the malodor gas composed of the complex gas is purified by neutralization reaction by the 'acid and alkali' chemical liquid. In such a conventional deodorization tower, the oxidizing agent (sodium hypochlorite, etc.) , And an acid and alkaline scrubbing tower each of which is composed of a series of two deodorizing tows connected in series. This is because the deodorization efficiency of the composite gas is lowered and the complexity of the apparatus There is a problem that the installation space and the installation cost are excessively increased due to enlargement.

In order to solve such a problem, Korean Patent Registration No. 10-0820845 (entitled "Two-component simultaneous cleaning deodorization tower") filed and registered by the present applicant has been disclosed. Such a two- By providing the washing tower as an integrated deodorization tower, the washing liquid is separately circulated and the composite gas is cleaned, thereby miniaturizing the apparatus. On the other hand, even when the acid or alkali is washed alone, the jet nozzle and the pack- There is some effect that simultaneous neutralization reaction of acid and alkali improves deodorization power.

However, most deodorizing towers and deodorizers, as well as the above-described two-pack simultaneous washing and deodorizing tower, contain a large amount of complex odors and fine dusts and are generated in places such as sewage treatment plants, manure treatment facilities, food processing facilities, Various organic or inorganic gases are introduced directly without pretreatment (i.e., treatment for some complex odor and fine dust).

Therefore, in the deodorizing apparatus having most of the conventional single or double deodorization tower type, there is a problem that the deodorization efficiency is lowered due to a large pressure loss due to the mixed odor and fine dust contained in various organic or inorganic gases, There is a problem that the cleaning cost becomes high due to the high contamination rate.

On the other hand, in most deodorizing towers and deodorizers as well as the above-mentioned two-liquid simultaneous cleaning deodorization tower, various organic or inorganic gases generated in places such as sewage treatment plants, manure treatment plants, food processing facilities, livestock facilities, Deodorization treatment, and then directly transported to an activated carbon adsorption apparatus equipped with activated carbon or the like and stored.

However, since a large amount of moisture (i.e., a large amount of residue particles and dust) is contained in various organic or inorganic gases deodorized through the deodorization tower, deodorizer, etc., as well as the conventional two- It is prepared.

However, when the various deodorized organic or inorganic gases are directly transported to the activated carbon adsorption apparatus or the like for storage or the like, a large amount of moisture contained in various deodorized organic or inorganic gases has a particle shape and is introduced into the activated carbon The activated carbon in the activated carbon adsorption apparatus is largely contaminated and damaged by the moisture, so that the life span itself becomes very short. As a result, the deodorizing effect on various organic or inorganic gases stored in the dry type deodorization tower is greatly reduced, There is a problem that operation and maintenance costs are increased due to frequent replacement.

Korean Patent Registration No. 10-1816518 (Jan. 03, 2018) Korean Registered Patent No. 10-1747802 (June 09, 2017) Korean Patent Registration No. 10-1595335 (February 12, 2016) Korean Patent Registration No. 10-1005636 (December 27, 2010)

SUMMARY OF THE INVENTION The present invention has been made in order to solve the problems of the conventional art, and it is an object of the present invention to provide a vortex type dust removing unit, a multi-stage chemical liquid cleaning unit, a dust and moisture removing unit, It is equipped with a vortex type dust removal unit in which various organic or inorganic gases generated in places such as sewage treatment plants, manure treatment plants, food processing facilities, livestock facilities, etc. are contained in a large amount of mixed odor and fine dust. The fine dust is first dipped into the water in the storage tank, the odor is collected through the double-installed demister as well as the water in the storage tank, and then the single or double (two- or three- And then passed through a multistage chemical liquid cleaning unit having a deodorization tower form, And then the residual particles and the dust are thirdly captured and removed through the dust and moisture removing unit, and then finally passed through the activated carbon adsorption unit and finally the odor is deodorized. Thus, the multi-stage chemical liquid washing unit The pressure loss of the cleaning liquid can be minimized and the replacement cost of the cleaning liquids can be reduced. Also, the activated carbon and the like in the activated carbon adsorption unit can be prevented from being contaminated and damaged by moisture, It is possible to greatly increase the deodorizing effect of various organic or inorganic gases through the activated carbon adsorption unit, as well as to increase the replacement cycle of activated carbon, thereby greatly reducing the operation and maintenance costs. In particular, And odor elimination that can completely deodorize and collect dust The purpose is to provide value.

Other objects and advantages of the present invention will become apparent to those skilled in the art from the following detailed description.

According to an aspect of the present invention, there is provided a combined odor eliminating apparatus comprising: a body having a rectangular plate shape; A plurality of organic or inorganic gases supplied from the outside through a malodorous gas supply line to the inside of the storage tank through an orifice through which water is sprayed, A dust collecting unit for collecting the odor through the first and second demisters installed in the storage tank as well as the water in the storage tank; Type dust removal unit, the gas inlet being in communication with the gas outlet of the vortex-type dust removal unit, and being fixed to one side of the vortex-type dust removal unit on the upper surface of the body, A multistage chemical liquid cleaning unit for secondarily taking up the collected and odor; Stage chemical liquid cleaning unit, the gas inlet communicates with the gas outlet of the multi-stage chemical liquid cleaning unit, and is fixed to one side of the multi-stage chemical liquid cleaning unit on the upper surface of the body, and through the fourth and fifth demisters, A dust and moisture removing unit for collectively collecting and removing residual particles and dust contained in the inorganic gas; A plurality of plate type activated carbon units are arranged at predetermined intervals and a plurality of gas inlets are communicated with gas outlets of the dust and moisture removal unit, Various organic or inorganic gases fixedly installed on one side of the water removal unit and introduced into the interior thereof are passed through a plurality of plate-type activated carbon units in a staggered manner to finally collect and remove dust and odors contained in various organic or inorganic gases And an activated carbon adsorption unit for discharging the purified gas to the outside.

At this time, the vortex-type dust removal unit comprises: a main body having a rectangular tower shape with a hollow inside and having a gas outlet at one side and an open bottom; A storage tank installed at a bottom opening of the main body and containing water necessary for collecting fine dust; A malodorous gas supply line which has a cross-sectional shape and penetrates the middle portion of the main body so as to supply various organic or inorganic gases supplied from the outside toward the lower portion of the main body; A plurality of nozzles are provided inside the ring and water is supplied through the pump at a lower end of the odor gas supply line so as to be sprayed at a predetermined pressure so that various kinds of organic or inorganic gas A water injector for fine particle immersion so that the fine dust contained in the water tank is immersed in the water in the storage tank; And a gas inlet pipe having a narrow funnel shape between the funnel-shaped gas inlet pipe and the inverted funnel-shaped gas outlet pipe. The gas inlet pipe upper end is replaceably fixed to the bottom of the water injector for fine particle dipping, The flow rate of various organic or inorganic gases supplied through the gas supply pipe is instantaneously accelerated and then the flow velocity is lowered again. In addition, the water sprayed from the nozzles of the fine particle dipping water sprayer flows down to the storage tank side along the inner surface, An orifice for allowing the fine dust adsorbed by the adsorbent to flow down into the storage tank automatically; The orifice is exposed to the water surface of the storage tank, the fine dust that has absorbed the moisture is vortexed including various kinds of organic or inorganic gas including the odor passing through the orifice, And a rotating radial guide vane for swirling the storage tank by the spray pressure of various organic or inorganic gas discharged in a vortex shape; A pump installed between one side of the bottom of the storage tank and the water injector for fine dust immersion so as to continuously supply water in the storage tank to the water injector for fine particle immersion; And an odor absorbing unit for collecting odor, moisture and fine dust contaminants in various kinds of organic or inorganic gas passing through the water in the storage tank in such a manner as to block the middle portion except for the odor gas supply pipe in the main body in a horizontal direction A first demister of a chevron type; And a second demister disposed in a horizontal direction below the gas outlet in the main body to collect odor, moisture, and fine dust contaminants contained in the gas finally passing through the first demister .

The rotary radial guide vane may include a disc-shaped upper plate having a shape having a gas inlet hole formed at the center thereof and detachably fixed to the lower end of the orifice; A circular plate-shaped lower plate integrally fixed to a bottom of the upper plate through a plurality of vortex forming blades, the plate having a conical gas discharge direction guiding portion having a conical shape whose outer surface is curved in the inner direction from the center toward the upper side, ; And a variety of organic or inorganic gases contained in the form of a radial shape at a predetermined angle in a clearance between the upper plate and the lower plate and containing odors flowing through the gas inlet holes of the upper plate And a plurality of vortex forming blades for allowing the fine dust that has absorbed the moisture to flow into the water in the storage tank through the gas outlet formed along the circumference.

In addition, an automatic water supply valve for automatically supplying water when the water level in the storage tank is lowered to a predetermined level or lower is further provided at an end of the water pipe located in the storage tank, further comprising a direct water pipe penetrating through the one side of the storage tank .

The nozzles provided inside the rings of the water jet for fine dust immersion may be formed to be inclined at a predetermined angle? In one direction so that water sprayed through nozzles is sprayed in a vortex form.

In addition, a plurality of guide vanes for generating vortex are formed on the inner surface of the orifice to allow vortexing of the water in the storage tank by causing water to flow along the inner surface, as well as various organic or inorganic gases, And is formed by extrusion molding.

In addition, a drain valve for discharging contaminated water to the outside is further provided on the bottom of the storage tank.

The multistage chemical liquid cleaning unit may include: a body having a hollow interior, the body having a mist collecting portion, a gas outlet, a gas distribution chamber, and a gas inlet; A first cleaning liquid storage tank, a first cleaning liquid circulation pump, a first cleaning liquid supply pipe, a fine jet nozzle cleaning unit, and a first cleaning liquid circulation unit; A second cleaning liquid circulating pump, a second cleaning liquid spraying tube, a second cleaning bath bad part, a second cleaning liquid collecting part, and a second cleaning liquid circulating part, wherein the second cleaning liquid reservoir tank, The second cleaning liquid collecting portion is composed of a second stage cleaning separator supporting plate having a second stage cleaning gas inlet and a gas movement guide, a collision type third demister, a second stage washing liquid collecting plate and a vortex prevention plate, The gas migration guide in which the third demister is installed is extended to the upper and lower portions of the second stage cleaning separator support plate and a gas reflection preventing and gas reflecting plate is provided on the bottom of the gas migration guide in which the collision type third demister is installed Is installed.

Further, a plurality of gas pass holes for allowing a part of the odor gas to pass directly to the collision-type third demister are further formed on the moisture-trapping and gas reflecting plate at a predetermined interval, And the diameter is gradually increased by a predetermined magnification as going outward from the longitudinal center line of the reflector.

In addition, the both ends of the moisture-trapping and gas reflecting plate may be inclined upwardly or curved gas guide pieces may be further bent.

In addition, in the vertical direction in the gap between the anti-moisture discharge and gas reflection plates, various organic or inorganic gases, which are reflected by the moisture reflection preventing and gas reflecting plates and reflected by the reflection plates, are moved upward without interference with each other And an interference prevention plate is further provided.

At this time, in order to smoothly move various organic or inorganic gases, which are reflected by the moisture reflection preventing and gas reflecting plates adjacent to each other, And has a cross section of "V" shape.

The dust and moisture removal unit has a predetermined diameter and height and is provided with a gas inlet along the tangential direction at one side of the upper part, and various organic or inorganic gases introduced through the gas inlet are turned inside ; A conical portion integrally formed at a lower portion of the cylindrical portion with a drain hole having a drain valve installed at a center thereof, the diameter being gradually reduced; A lid provided with a gas outlet at a center point and coupled to an upper opening of the cylindrical portion; Water particles contained in various organic or inorganic gases which are arranged in a vertical direction so as to be perpendicular to the direction of rotation of various organic or inorganic gases in the space portion between the inner surface of the cylindrical portion and the outer surface of the fifth demodulator, And a fourth demister of a chevron type that primarily collects relatively large water particles and dust in the dust and flows it to the conical part side; A cylindrical wire mesh network having a top end fixed to a bottom surface of the lid body and a bottom end opening fixed to a disk-shaped finishing plate for preventing the fifth demister from coming off and blocking inflow of various organic or inorganic gases A frame; A plurality of organic or inorganic gases having a shape provided to surround the outer surface of the frame and passing through the fourth demister and turning the internal space of the cylindrical portion, A fifth demister of an iron wool filter type for collecting secondary particles of water particles and dust which are relatively small in water particles and dust remaining in various organic or inorganic gases and flowing them to the conical part side; A plurality of organic or inorganic gases introduced into the cylindrical portion through the gas inlet are provided in the cylindrical portion so as to block the inner side end portion of the gas inlet and the contact portion of the fourth and fifth demisters in the vertical direction, And a malodor gas backflow prevention plate that is supplied to the fourth demister side.

As described above, according to the composite odor removing apparatus of the present invention, the vortex-type dust removal unit, the multistage chemical liquid cleaning unit, the dust and moisture removing unit, and the activated carbon adsorption unit are continuously and integrally installed on the upper surface of the body having the predetermined area , It is passed through a vortex type dust removal unit in which various organic or inorganic gases generated in places such as a sewage treatment plant, a manure treatment plant, a food processing facility, an animal husbandry facility and the like are contained in a large amount of mixed odor and fine dust, The fine dust is primarily immersed in the water in the storage tank, the odor is collected through the double-installed demister as well as the water in the storage tank, and then the single or double deodorization with various cleaning solutions (for example, acid and alkali cleaning solution) And then passed through a multi-stage drug solution cleaning unit having a tower shape, And then the residual particles and dust are thirdly captured and removed through the dust and moisture removing unit, and then finally passed through the activated carbon adsorption unit and finally the odor is deodorized. Thus, the multi-stage chemical liquid cleaning unit The pressure loss can be minimized and the replacement cost of the cleaning liquids can be reduced. In addition, the activated carbon and the like in the activated carbon adsorption unit can be prevented from being contaminated and damaged by moisture, It is possible to greatly increase the deodorizing effect of various organic or inorganic gases through the adsorption unit, as well as to increase the replacement cycle of the activated carbon, thereby greatly reducing the operation and maintenance cost. In particular, Dust, etc. can be completely deodorized and collected. will be.

The effects of the present invention will be clearly understood and understood by those skilled in the art, either through the specific details described below, or during the course of practicing the present invention.

BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a front sectional view of a composite odor elimination apparatus to which the present invention is applied. Fig.
2 is an enlarged front sectional view of a vortex-type dust removal unit in the apparatus of the present invention.
FIGS. 3 and 4 are plan sectional views showing different embodiments of water injectors for fine dust immersion in the vortex-type dust removal unit of FIG. 2;
5 is a perspective view of a rotary radial guide vane in Fig. 2;
6 is a plan view of a rotary radial guide vane in Fig. 2;
7 is a front sectional view of a rotary radial guide vane in Fig. 2;
8 is an enlarged sectional front view of the multi-stage chemical liquid cleaning unit of the present invention apparatus.
FIG. 9 and FIG. 10 are enlarged sectional views of a part of the second cleaning liquid collecting portion for explaining the installation state of the moisture reflection preventing and gas reflecting plates and the malodor gas flow chart in FIG.
Fig. 11 is a plan view of the second cleaning liquid collecting portion in Fig. 8; Fig.
Fig. 12 and Fig. 13 are enlarged perspective views for explaining different embodiments of the moisture release preventing and gas reflecting plate in Fig. 8;
14 is an enlarged sectional front view of a dust and moisture removing unit of the present invention apparatus.
FIG. 15 is a partially exploded perspective view of the dust and moisture removal unit shown in FIG. 14; FIG.
16 is a plan view of the dust and moisture removal unit shown in Fig.
17 is an enlarged sectional front view of an activated carbon adsorption unit in the apparatus of the present invention.
18 is a plan sectional view of the activated carbon adsorption unit shown in Fig.

While the invention is susceptible to various modifications and alternative forms, specific embodiments thereof are shown by way of example in the drawings and are herein described in detail. It should be understood, however, that the invention is not intended to be limited to the particular forms disclosed, but includes all modifications, equivalents, and alternatives falling within the spirit and scope of the invention.

The terms first, second, etc. may be used to describe various components, but the components should not be limited by the terms. The terms are used only for the purpose of distinguishing one component from another. For example, without departing from the scope of the present invention, the first component may be referred to as a second component, and similarly, the second component may also be referred to as a first component.

The terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention. The singular expressions include plural expressions unless the context clearly dictates otherwise. In the present application, the terms "comprising" or "having ", and the like, are intended to specify the presence of stated features, integers, steps, operations, elements, parts, or combinations thereof, But do not preclude the presence or addition of one or more other features, integers, steps, operations, elements, parts, or combinations thereof.

Unless otherwise defined, all terms used herein, including technical or scientific terms, have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs.

Terms such as those defined in commonly used dictionaries are to be interpreted as having a meaning consistent with the meaning in the context of the relevant art and are to be interpreted as ideal or overly formal in meaning unless expressly defined in the present application Do not.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Reference will now be made in detail to preferred embodiments of the present invention, examples of which are illustrated in the accompanying drawings.

FIG. 1 is a front sectional view of a composite odor removing apparatus to which the present invention is applied, FIG. 2 is an enlarged front sectional view of a vortex dust removing unit of the present invention apparatus, and FIGS. 3 and 4 are cross- FIG. 5 is a perspective view of a rotary radial guide vane in FIG. 2, and FIG. 6 is a cross-sectional view of a rotary radial guide vane in FIG. And FIG. 7 is a front sectional view of the rotary radial guide vane in FIG. 2. FIG.

8 and 9 are enlarged front and sectional views of the multi-stage chemical liquid cleaning unit of the present invention. Figs. 9 and 10 are views showing a state in which the moisture release preventing and gas reflecting plates are installed and the second cleaning liquid FIG. 11 is a plan view of the second cleaning liquid collecting portion in FIG. 8, and FIGS. 12 and 13 are views for explaining different embodiments of the moisture release preventing and gas reflecting plate in FIG. FIG.

14 is an enlarged sectional front view of the dust and moisture removing unit of the present invention, FIG. 15 is a partially exploded perspective view of the dust and moisture removing unit shown in FIG. 14, and FIG. FIG. 17 is an enlarged sectional front view of the activated carbon adsorption unit in the apparatus of the present invention, and FIG. 18 is a top cross-sectional view of the activated carbon adsorption unit shown in FIG.

According to the present invention,

A body 10 having a rectangular plate shape;

Various organic or inorganic gases supplied from the outside through the odor gas supply line 23 are installed into the storage tank 22 through an orifice 25 in which water is sprayed, The fine dust contained in the various organic or inorganic gases is firstly immersed in water in the storage tank 22 and the offensive odor is stored in the water in the storage tank 22 as well as the first and second demisters 28, (20) for collecting the dust through the dust collecting unit (29);

The gas inlet 314 communicates with the gas outlet 211 of the vortex type dust removal unit 20 and is fixed to one side of the vortex type dust removal unit 20 on the upper surface of the body 10 A multistage chemical liquid cleaning unit (30) for secondarily debris the fine dust collecting and odor contained in various organic or inorganic gases through various cleaning liquid injections;

Stage chemical liquid cleaning unit 30 has a gas inlet 411 communicating with the gas outlet 312 of the multi-stage chemical liquid cleaning unit 30 and is fixed to one side of the multi-stage chemical liquid cleaning unit 30 on the upper surface of the body 10, A dust and moisture removing unit 40 for collectively collecting and removing residual particles and dust contained in various organic or inorganic gases through the fourth and fifth demisters 44 and 46, ;

A plurality of plate type activated carbon units 52 are arranged at predetermined intervals and a plurality of gas inlets 53 are provided in the gas exhaust port of the dust and moisture removal unit 40 431 and is fixed to one side of the dust and moisture removal unit 40 on the upper surface of the body 10 so that various organic or inorganic gases introduced into the inside of the body can be supplied to the plurality of plate- And an activated carbon adsorption unit (50) for collecting and removing ultimately collected dust and odor contained in various organic or inorganic gases, and then exhausting the purified gas to the outside.

At this time, the vortex-type dust removal unit (20)

A main body 21 having a hollow square shape inside and having a gas outlet 211 at one side and an open bottom;

A storage tank (22) installed at a bottom opening of the main body (21) and containing water necessary for collecting fine dust;

An odor gas supply line 23 having a cross-sectional shape of "?" Shape and provided so as to penetrate through the middle part of the main body 21 to supply various organic or inorganic gas supplied from the outside toward the lower part of the main body 21; ;

A plurality of nozzles 242 are provided inside the ring 241 and the water supplied through the pump 27 is provided at a lower end of the odor gas supply line 23 so as to be sprayed at a predetermined pressure, A fine dust immersion water injector (24) for immersing fine dust contained in various organic or inorganic gases passing through the gas supply line (23) into the water in the storage tank (22);

And a narrow fluid and gas passage hole 253 is provided between the funnel-shaped gas inlet pipe 251 and the inverted funnel-shaped gas outlet pipe 252. The upper end of the gas inlet pipe 251 is connected to the gas- The flow rate of various organic or inorganic gas supplied through the odor gas supply line 23 in a state of being fixedly installed on the bottom of the water injector 24 is instantaneously accelerated and then the flow velocity is lowered again, An orifice 25 for allowing water sprayed from the nozzles of the water sprayer 24 to flow down along the inner surface toward the storage tank 22 and allowing the fine dust adsorbed on the inner surface to automatically flow into the storage tank 22;

(25), which is exposed to the water surface of the storage tank (22), and contains various kinds of organic or inorganic gas containing odor passing through the orifice (25) And the gas is discharged from the storage tank 22 through the gas discharge port 264 formed along the circumference of the storage tank 22 directly to the water in the storage tank 22, A rotary radial guide vane (26) for making the radial guide vane (26);

A pump 27 provided between one bottom of the storage tank 22 and the water sprayer 24 for fine dust immersion so as to continuously supply the water in the storage tank 22 to the water sprayer 24 for fine dust immersion, Wow;

The odor and moisture in the various organic or inorganic gases that pass through the water in the storage tank 22 and are discharged through the water in the horizontal direction are provided in the main body 21 in an intermediate portion excluding the odor gas supply line 23, A first demister (28) of a chevron type for primarily collecting fine dust contaminants;

And secondarily collects odor, moisture and fine dust contaminants contained in the gas which is horizontally installed in the lower part of the gas outlet 211 in the main body 21 and passes through the first demister 28 and finally discharged, And a second demultiplexer (29) for demultiplexing the second demultiplexer (29).

Further, the rotary radial guide vane (26)

A disk-shaped top plate 261 having a gas inlet hole 261a formed at the center thereof and detachably fixed to the bottom of the orifice 25;

A gas discharge direction guiding protrusion 262a of a conical shape whose outer surface is curved inward in the direction from the center toward the upper side and is provided on the bottom of the upper plate 262 through a plurality of vortex forming blades 263 A disk-shaped lower plate 262 which is integrally fixed and installed;

The upper plate 261 has a shape bent in a plane ") " and is fixed radially at a predetermined angle in a clearance between the upper plate 261 and the lower plate 262, And a plurality of vortex forming blades 263 (see FIG. 4) for causing fine particles that have absorbed moisture to flow into the water in the storage tank 22 through gas outlets 264 formed along the circumference, including various organic or inorganic gases containing odors, ). ≪ / RTI >

A water pipe 221 is further provided so as to pass through one side of the upper part of the storage tank 22 and an end of the water pipe 221 located in the storage tank 22 is lowered to a water level below a predetermined water level in the storage tank 22 And an automatic water supply valve (222) for automatically supplying water is further provided.

The nozzles 242 provided inside the rings 241 of the fine particle dipping water jetting device 24 are installed or formed at an angle of a predetermined angle in one direction so as to be sprayed through the nozzles 242 Is sprayed in a vortexed form.

The orifice 25 has a shape in which various organic or inorganic gases are swirled along with the water flowing down along the inner surface of the orifice 25 and flows into the water in the storage tank 22 so that the water in the storage tank is vortexed And the guide vane 254 for generating is further protruded.

A drain valve (223) for discharging contaminated water to the outside is further provided at the bottom of the storage tank (22).

On the other hand, in the multi-stage chemical liquid cleaning unit 30,

A main body 31 provided with a mist collecting portion 311, a gas outlet 312, a gas distribution chamber 313, and a gas inlet 314 in a hollow body;

A first cleaning liquid circulation pump 322, a first cleaning liquid supply pipe 323, a fine jet nozzle cleaning unit 324 and a first cleaning liquid circulation unit 325. The first cleaning liquid circulation unit 321, the first cleaning liquid circulation pump 322, (32);

The second washing liquid dispensing tube 333, the second washing bath bad portion 334, the second washing liquid collecting portion 335 and the second washing liquid circulating pump 332, the second washing liquid circulating pump 332, the second washing liquid dispensing tube 333, And a second stepped portion (33) provided with a second portion (336)

The second washing liquid collecting portion 335 includes a second stage washing separation supporting plate 335c having a second stage cleaning gas inlet port 335a and a gas movement guide 335b, a collision type third demister 335f, Second cleaning liquid collecting plate 335d and vortex prevention plate 335e,

The gas movement guide 335b in which the collision type third demister 335f is installed is extended to the upper and lower portions of the second stage cleaning separator support plate 335c and the collision type third demister 335f is extended And a moisture reflection preventing and gas reflecting plate 337 is provided on the bottom of the gas moving guide 335b.

Further, a plurality of gas passing holes 337a are formed in the moisture reflection preventing and gas reflecting plate 337 so that a part of the odor gas is directly passed to the side of the colliding third demister 335f. The gas passing holes 337a are formed such that the diameters of the gas passing holes 337a gradually increase toward the outer side from the longitudinal center line of the moisture reflection preventing and gas reflecting plate 337 by a predetermined magnification.

Further, the both ends of the moisture-trapping and gas reflecting plate 337 are characterized in that the gas guide member 337b is inclined or bent to a predetermined angle upward.

In addition, various organic or inorganic gases, which are reflected by the moisture-trapping and gas reflecting plates 337 and reflected by the moisture-discharge preventing and gas reflecting plates 337, are changed in the vertical direction in the clearance between the moisture- And an interference prevention plate 338 is provided to move upward without interfering with each other.

At this time, the interference prevention plate 338 smoothly moves various organic or inorganic gases, which are reflected by the moisture reflection preventing and gas reflecting plates 337 adjacent to each other, The shape of the positive section is "V" shape.

On the other hand, the dust and moisture removal unit (40)

A gas inlet 411 is provided along the tangential direction on one side of the upper portion and a cylindrical portion (not shown) for circulating various organic or inorganic gases introduced through the gas inlet 411 41);

A conical portion 42 integrally formed at a lower portion of the cylindrical portion 41 and having a drain port 421 provided with a drain valve 422 at its center in a progressively smaller diameter;

A lid body 43 having a gas outlet 431 at a center point and coupled to an upper opening of the cylindrical portion 41;

Is arranged in the vertical direction so as to be perpendicular to the turning direction of various organic or inorganic gases in the space portion between the inner surface of the cylindrical portion 41 and the outer surface of the fifth demister 46 and turns inside the cylindrical portion 41 A fourth demister 44 of a chevron type that primarily collects relatively large water particles and dust among water particles and dust contained in various organic or inorganic gases and flows to the conical portion 42 side;

The upper end portion is fixed to the bottom surface of the lid body 43 and the lower end opening portion is fixed to the disk-shaped finishing plate 452 to prevent the fifth demister 46 from coming off and to block the inflow of various organic or inorganic gases A frame 45 made of a cylindrical mesh-shaped wire mesh 451;

And a plurality of organic or inorganic gases which are installed in the form of enclosing the outer surface of the frame 45 and which pass through the fourth demister 44 and turn the inner space portion of the cylindrical portion 41, The water particles and dust remaining in the various organic or inorganic gases and the relatively small water particles and dust are secondarily collected in the process of passing through the pores and moving to the gas outlet 431 side of the lid body 43, A fifth demister (46) of an iron wool-filter type which flows to the side of the second demister (42) side;

The gas inlet 411 and the fourth and fifth demisters 44 and 46 are provided in the cylindrical portion 41 so as to vertically block the inner side edge portion of the gas inlet 411 and the contact portions of the fourth and fifth demisters 44 and 46, And an odor gas backflow preventing plate 47 for supplying all the organic or inorganic gases introduced into the cylindrical portion 41 through the first and second chambers 41 and 42 to the fourth demister 44 side.

The operation and effect of the thus configured complex odor eliminating apparatus of the present invention will be described in detail with reference to the accompanying drawings.

First, as shown in FIG. 1, the composite odor removing apparatus of the present invention includes a vortex type dust removing unit 20, a multistage chemical liquid cleaning unit 30, a dust and moisture removing unit 40) and an activated carbon adsorption unit (50) are integrally installed to collect various kinds of organic or inorganic gas generated in a place such as a sewage treatment plant, a manure treatment facility, a food processing facility, an animal husbandry facility, The main technical component is to completely deodorize and collect odor, dust, and moisture.

At this time, the body 10 is formed into a rectangular plate shape by using an "H" beam or a "C" shaped steel sheet. On the upper surface thereof, a vortex type dust removing unit 20, a multistage chemical liquid cleaning unit 30, The dust and moisture removing unit 40 and the activated carbon adsorbing unit 50 are integrally provided on the bottom of the place where the inventive device is installed to perform the function of the base plate of the above units.

1 and 2, the vortex-type dust removal unit 20 includes a main body 21, a storage tank 22, a malodor gas supply line 23, a water sprayer 24 for fine dust immersion, An orifice 25, a rotating radial guide vane 26, a pump 27, a first demister 28 and a second demister 29 of a chevron type, As shown in Fig.

The vortex-type dust removal unit 20 is configured to introduce various kinds of organic or inorganic gas supplied from outside through the odor gas supply line 23 into the storage tank 22 through an orifice 25 in which water is sprayed The fine dust contained in the various organic or inorganic gases is firstly immersed in water in the storage tank 22 and the offensive odor is stored in the water in the storage tank 22 as well as the first and second demisters 28, (29).

At this time, among the constituent elements of the vortex-type dust removal unit 20, the main body 21 has a rectangular tower shape with a hollow interior, a gas outlet 211 at one side thereof, .

The storage tank 22 is provided at the bottom opening of the main body 21 to penetrate the inside of the main body 21 through the bottom opening of the main body 21 and accommodates the water required to collect the fine dust .

When the storage vessel 22 is installed in the bottom opening of the main body 21 as described above, the main body 21 and the storage vessel 22 are all sealed except for the gas discharge port 211 formed in the upper part of the main body 21, The organic or inorganic gas supplied to the inside of the main body 21 through the odor gas supply line 23 and the orifice 25 to be described later is prevented from leaking to the outside.

In the present invention, a water pipe 221 is additionally provided so as to pass through one side of the upper part of the storage tank 22, and at the end of the water pipe 221 located in the storage tank 22, The automatic water supply valve 222 for automatically supplying water is provided.

Therefore, when the water level in the storage tank 22 falls below a predetermined water level, the automatic water supply valve 222 provided in the water supply pipe 221 is automatically opened to automatically supply the water into the storage tank 22, It is possible to maintain the water level in the water level sensor 22 at a predetermined level, so that the vortex-type dust removal unit 20 can be used to prevent the shortage of water required for removing odor and fine dust contained in various organic or inorganic gases .

In the present invention, a drain valve 223 is provided near the bottom surface of the storage tank at the other side of the bottom of the storage tank 22, and a drain valve 223 is provided near the bottom surface of the storage tank 22, It is possible to further provide a sight window for visually confirming the level and the degree of contamination of water in the storage tank 22.

Accordingly, while the apparatus of the present invention is continuously operated to remove odors and fine dust contained in various organic or inorganic gases, the pollution degree and level of water in the storage tank 22 provided in the vortex-type dust removal unit 20 The drain valve 223 is opened and the contaminated water in the storage tank 22 is discharged to the outside of the storage tank 22 when the water in the storage tank 22 is judged to be highly contaminated by fine dust or the like. It is possible to automatically discharge cleanly and automatically to the outside through the direct water pipe 221, thus facilitating maintenance.

The odor gas supply line 23 is connected to the odor gas supply line 23 through the orifice 25 through the orifice 25 in the state where the odor gas supply line 23 has a " To the water in the storage tank (22) installed at the bottom of the storage tank (21).

3, a plurality of nozzles 242 are arranged at predetermined intervals on the inner side of the ring 241 having an outer diameter equal to the inner diameter of the odor gas supply duct 23 And is interchangeably provided between the bottom end of the odor gas supply line 23 and the upper end of the orifice 25 described later.

The water jetting device 24 for fine particle dipping such as this injects the water in the storage tank 22 supplied through the pump 27 at a predetermined pressure so that various kinds of organic or inorganic gas passing through the odor gas supply line 23 So that the fine particles contained in the fine particles are combined with water molecules injected through the nozzles 242 and then immersed in the water in the storage tank 22.

4, the nozzle 242 provided inside the ring 241 of the water sprayer 24 for fine dust immersion may be disposed at a position closer to the center of the ring 241 than to the central point of the ring 241, It is more preferable to arrange or form an inclination by an angle? (For example, 15 to 30 degrees) defined by?

That is, if the nozzles 242 are inclined or formed at a predetermined angle? In either direction, the water jetted through the nozzles 242 is sprayed obliquely at an angle? It is possible not only to increase the contact time with various kinds of organic or inorganic gas passing through the odor gas supply line 23 but also to vortex the various organic or inorganic gas itself, More moisture can be supplied to the fine dust, so that the amount of the water immersed in the water in the storage tank 22 can be further increased.

The orifice 25 has a funnel shape and a narrow fluid and gas passage hole 253 is provided between the gas inlet pipe 251 located at the upper portion and the gas outlet pipe 252 located at the lower portion having an inverted funnel shape The lower end of the gas discharge pipe 252 is positioned slightly higher than the water surface of the storage tank 22, and the lower end of the gas discharge pipe 252 is positioned slightly higher than the water surface of the storage tank 22. .

The orifice 25 is supplied through the odor gas supply line 23 and passes between the rings 241 of the fine particle dipping water jetting device 24 and partially discharges the water sprayed through the nozzles 242 The flow velocity of various organic or inorganic gases is passed through the narrow fluid and gas passage holes 253 and instantaneously accelerated instantaneously. The velocity of the flow of the various organic or inorganic gases through the gas outlet pipe 252 having an inverted funnel shape is lowered, To be introduced into the water.

The water injected from the nozzles 242 of the fine particle dust immersion nozzle 24 smoothly flows along the inner surface of the orifice 25 toward the rotary radial guide vane 26 and the storage tank 22, So that the fine dust that can be adsorbed on the surface of the storage tank 22 automatically flows into the storage tank 22.

Further, in the present invention, a plurality of guide vanes 254 for vortex generation are further formed on the inner surface of the orifice 25.

Therefore, not only the water flowing along the inner surface of the gas inlet pipe 251 and the gas outlet pipe 252 of the orifice 25 but also various organic or inorganic gases passing through the orifice 25 are supplied to the vortex generating guide vane The water in the storage tank 22 is vortexed, so that various organic or inorganic gases including fine dust are stored in the storage tank 22, It is possible to greatly increase the contact time between the inside water and the odor removing effect and the immersion effect on the fine dust can be further increased.

The rotary radial guide vane 26 is installed in the reservoir 22 in a state where the gas discharge ports 264 are detachably mounted on the lower end of the orifice 25 exposed to the water surface of the storage tank 22 It has a winding shape.

The rotating radial guide vane 26 includes various organic or inorganic gases containing odors that have passed through the orifice 25, so that fine dust that has absorbed the moisture is vortexed and is discharged through the gas outlet 264 formed along the circumference The water in the storage tank 22 is vortexed by the injection pressure of various organic or inorganic gas discharged in a vortex form.

5 to 7, the rotary radial guide vane 26 includes a disk-shaped upper plate 261, a disk-shaped lower plate 262, and a plurality of vortex forming blades 263 .

Among the constituent elements of the rotary radial guide vane 26, the upper plate 261 has a disk shape having a predetermined diameter, and also has a gas inflow hole 261a formed at the center thereof. The lower end 261a of the orifice 25 And a plurality of bolts and nuts.

In addition, the lower plate 262 has a disc shape having a predetermined diameter as in the case of the upper plate 261, a substantially conical gas discharge direction protruding portion 262a upward from the center, The outer surface of the discharge direction guide protrusion 262a has an inner curved shape and is integrally fixed at a predetermined interval at the bottom of the upper plate 261 through a plurality of vortex forming blades 263 described later.

At this time, the outer surface of the gas discharge direction guide protrusion 262a formed to protrude from the center of the lower plate 262 is curved in the inward direction so that the gas can flow in the vertical direction through the gas inflow hole 261a of the upper plate 261 Various organic or inorganic gases are turned to the horizontal direction along the outer surface of the substantially conical gas discharge direction guiding protrusion 262a having a curved shape toward the inside and smoothly flow to the gas discharge port 264 side so that the lower plate 262 Can be greatly reduced, and the generation of noise and vibration, which may be caused by the friction between them, can be greatly reduced.

The plurality of vortex forming blades 263 are bent to have a plane shape and are formed in a gap between the upper plate 261 and the lower plate 262 in a radial shape at a predetermined angle as shown in FIG. The fine dust that has absorbed moisture, including various organic or inorganic gases containing odors, which is fixedly installed and flows in the vertical direction through the gas inlet hole 261a of the upper plate 261, forms the vortex forming vanes 263 The upper plate 261 and the lower plate 262 are smoothly turned in the horizontal direction corresponding to the outer shape of the gas discharge direction guiding protrusion 262a of the lower plate 262 which is swirled corresponding to the installation angle and curved in the inward direction, And directly flows into the water in the storage tank 22 through the gas outlet 264 formed along the circumference of the storage tank 262.

The water in the storage tank 22 is discharged through the gas discharge port 264 formed radially along the circumference of the upper plate 261 and the lower plate 262 of the rotary radial guide vane 26, Or the injection pressure of the rotation of the inorganic gas, the contact time between various kinds of organic or inorganic gas including fine dust and the water in the storage tank 22 can be further increased, So that the immersion effect can be greatly increased.

At this time, the rotary radial guide vane 26 made up of the upper plate 261 and the vortex forming vanes 263 and the lower plate 262 can be molded integrally through the casting, A contact portion between the bottom surface of the upper plate 261 and the upper end of the vortex forming blade 263 and the lower end portion of the vortex forming vane 263 and the upper surface of the lower plate 262 are integrally fixed by welding .

The pump 27 is installed between one bottom of the storage tank 22 and the water sprayer 24 for fine particle immersion so that the water in the storage tank 22 is continuously supplied to the water sprayer 24 for fine particle immersion As shown in FIG.

Further, the first demister 28 has a chevron type in which wavy plates provided with delayed gas discharge time delay and impurity drop wings are disposed at predetermined intervals, and the odor gas supply line 23 is provided in the main body 21, The water is discharged through the water in the storage tank 22 in the form of bubbles to the outside of the water and then discharged through the sealed inner space of the main body 22 into the gas outlet 211), and collects and collects the odor, moisture, and fine dust contaminants contained in various organic or inorganic gases.

The second demister 29 is provided with a plurality of plate members arranged at predetermined intervals in the form of a wedge shape and arranged in the horizontal direction below the gas outlet 211 in the main body 21, Before passing through the mist 28 and supplying the gas to the multi-stage chemical liquid cleaning unit 30 through the gas outlet 211 of the main body 21, the odor, moisture, and fine dust contaminants contained in the gas are secondarily And performs filtering and collection.

As described above, the vortex-type dust removal unit 20 removes and filters malodorous and fine dust particles through the first and second demisters 28 and 29 to remove odor and fine dust The efficiency can be greatly increased and the pressure loss for the multi-stage chemical liquid cleaning unit 30 described later can be minimized, and the replacement cost of the cleaning liquids can be reduced.

1 and 8, the multistage chemical liquid cleaning unit 30 has a configuration mainly composed of a main body 31, a first end cleaning portion 32, and a second end cleaning portion 33 And the gas inlet 314 communicates with the gas outlet 211 of the vortex-type dust removal unit 20. The vortex-type dust removal unit 20 is provided on one side of the vortex-type dust removal unit 20, As shown in Fig.

Such a multi-stage chemical liquid cleaning unit 30 is still included in various organic or inorganic gases introduced after the deodorization and fine dust are primarily collected through the vortex type dust removal unit 20 through the injection of various cleaning liquids And also performs a function to secondarily capture the fine dust and odor.

The main body 31 of the multi-stage chemical liquid cleaning unit 30 includes a mist collecting part 311 for collecting the cleaning liquid mist contained in the purified air which is cleaned on the upper part of the hollow body, And a gas discharge port 312 for discharging the mist trapped gas to the dust and moisture removal unit 40. The gas distribution chamber 313 is formed at a lower portion of the gas distribution chamber 313, And a gas inlet 314 into which various organic or inorganic gases having passed through the vortex-type dust removal unit 20 are introduced.

In addition, the first step cleaning unit 32 may be configured such that the first cleaning liquid is circulated inside and outside the main body 31, and the odorous substances, which react with the first cleaning liquid, The first cleaning liquid circulation pump 322, the first cleaning liquid supply pipe 323, the fine jet nozzle cleaning unit 324, and the first cleaning liquid circulation unit 325. The first cleaning liquid circulation unit 321, the first cleaning liquid circulation pump 322,

The first cleaning liquid storage tank 321 of the first stage cleaning part 32 is provided on the bottom surface of the main body 31 and accommodates the first cleaning liquid as the first cleaning liquid, (322) is provided outside the first cleaning liquid storage tank (321) and transfers the received first cleaning liquid into the main body (31).

At this time, the first rinse solution circulation pump 322 transfers the first rinse solution to the first supply pipe 323 that supplies the first rinse solution to the upper portion of the fine jet nozzle cleaner 324.

In addition, the first cleaning liquid alkali supply pipe 323 is provided with a plurality of supply holes (not shown) for supplying the first cleaning liquid transferred by the first cleaning liquid circulation pump 322 downward in the main body 31 .

The fine jet nozzle cleaning unit 324 is provided between the gas distribution chamber 313 and the first cleaning liquid supply pipe 323 and is provided with a first cleaning liquid supply pipe 323, The malodorous gas is sprayed into the cleaning liquid to clean the malodorous gas, and the dust contained in the malodorous gas is simultaneously removed.

The first cleaning liquid circulating unit 325 is disposed between the fine jet nozzle cleaning unit 324 and the first cleaning liquid storage tank 321 and is provided between the first cleaning liquid circulating unit 325 and the first cleaning liquid circulating unit 325, And performs a function of circulating and transferring the cleaning liquid to the first cleaning liquid storage tank 321.

The second stage cleaning unit 33 is provided with a second cleaning liquid supply unit 32 for circulating the second cleaning liquid in and out of the main body 31 and for cleaning odorous substances reacting with the second cleaning liquid in the malodor gas flowing into the main body 31 The second cleaning liquid circulation pump 332, the second cleaning liquid dispensing tube 333, the second cleaning package bad part 334, the second cleaning liquid collection part 335, and the second cleaning liquid circulation 331, So that the odorous substances reacting with the second cleaning liquid among the odorous gas rising upward can be effectively cleaned.

At this time, the second cleaning liquid storage tank 331 is disposed adjacent to the first cleaning liquid storage tank 321 at the bottom of the main body 31 or at the bottom of the dust and moisture removal unit 40, And accommodates the second cleaning liquid.

The second rinse solution circulation pump 332 serves to transfer the second rinse solution stored in the second rinse solution storage tank 331 to the inside of the main body 31. At this time, The second cleaning liquid dispensing pipe 332 transfers the second cleaning liquid to the second cleaning liquid dispensing pipe 333 for spraying the second cleaning liquid onto the upper portion of the second cleaning package bad 334.

The second cleaning liquid spray pipe 333 is provided with a plurality of supply holes (not shown) for spraying the second acid pickling liquid transferred by the second cleaning liquid circulation pump 332 downward in the main body 31, Respectively.

In order to perform the alkali cleaning simultaneously with the second cleaning liquid contained in the second cleaning liquid storage tank 331, the second stage cleaning unit 33 has a circulation structure independent of the first stage cleaning unit 32 The first and second rinsing of the complex odor gas in the body 31 can simultaneously realize an acid and an alkali neutralization reaction.

In addition, the second cleaning pack bad part 334 is disposed under the second cleaning solution spraying pipe 333 to maximize the contact area between the malodorous gas and the cleaning liquid, thereby collecting the malodorous gas.

The second cleaning pack bad part 334 is filled with the medicament filling layer so that the odor gas passing through the packed bed layer has a sufficient thickness and a sufficient surface area to be cleaned and collected while being in contact with more washing liquid on the surface of the packed bed. And is formed to clean the odor gas.

9-11, the second cleaning liquid collecting portion 335 is spaced apart from the main body 31 in the direction of supplying the malodor gas to the main body 31 and is perpendicular to the malodor gas supply direction. A second end cleaning gas inlet 335a which is formed to be long in the lateral direction of the first end cleaning portion 32 and upwardly moves the odor gas firstly cleaned in the first end cleaning portion 32; And a gas movement guide (335b) extending upward from an outer edge of the second end cleaning gas inlet (335a) and guiding the malodor gas moved to the second end cleaning gas inlet (335a) upward, Only the washing separation part supporting plate 335c; The second end cleaning gas inlet 335a is formed inside the gas movement guide 335b and is formed to be long in the lateral direction of the main body 31 at right angles to the direction of the malodor gas flowing into the main body 31, A plurality of collision-type first demisters 335f, which are collision-type demisters, collision-type demisters 335f to collide with the first-cleaned odor gas introduced into the combustion chambers and trap the first cleaning fluid mist contained therein to suppress upward movement; Is formed to be long in the transverse direction of the main body (31) so as to be perpendicular to the supply direction of the malodor gas flowing into the main body (31), being spaced apart from the upper portion of the second stage cleaning separator supporting plate (335c) Shaped so as to collect the second cleaning liquid passing through the bad part (334) and falling down and simultaneously moving the odor gas upwardly moved to the second end cleaning gas inlet (335a) toward both sides, The second cleaning gas inlet 335a is formed to be larger than the width of the second cleaning gas inlet 335a to prevent the second cleaning solution passing through the second cleaning package 334 and falling down to the second cleaning gas inlet 335a A second-stage cleaning liquid collection plate 335d; And is disposed between one second washing liquid collecting plate 335d and the second washing liquid collecting plate 335d adjacent to the second washing liquid collecting plate 335d and perpendicular to the feeding direction of odorous gas flowing into the main body 31, And odor gas dispersed and moved by the second end cleaning liquid collection plate 335d adjacent to the odor gas dispersed and moved by one of the second end cleaning liquid collecting plates 335d upward And a vortex prevention plate 335e which is moved to the second cleaning package bad part 334.

The second cleaning liquid collecting portion 335 having such a configuration basically has a structure in which the odor gas cleaned in the first step cleaning portion 32 provided at the lower portion of the second cleaning package bad portion 334, The second washing liquid is sprayed by the second washing liquid spraying pipe 333 and passes through the second washing pack bad part 334 and falls down to the bottom, .

In addition, the second cleaning liquid collecting unit 335 also collects the second cleaning liquid falling downward so that the second cleaning liquid does not fall into the first cleaning unit 32.

The second rinsing liquid circulating unit 336 is provided between the second rinsing liquid collecting unit 335 and the second rinsing liquid storage tank 331 and is disposed in the second rinsing liquid collecting unit 335 And performs a function of circulating and transferring the second cleaning liquid to the second cleaning liquid storage tank 331.

At this time, the first cleaning liquid (acid or alkali) is used as the first cleaning liquid, and the second cleaning liquid 33 (acid or alkali) is used as the first cleaning liquid, It is needless to say that it is possible to increase the deodorization efficiency by selectively using an acid or alkaline cleaning liquid in the first stage washing section 32 and the second stage washing section 33 according to the characteristics of the complex odor.

In order to further improve the function of the second cleaning liquid collecting part 335, the present invention is characterized in that, among the components of the second cleaning liquid collecting part 335, 9 to 11 as well as the upper and lower portions of the second stage cleaning separator support plate 335c and the gas migration guide 335b having the collision type first demister 335f And a moisture release preventing and gas reflecting plate 337 having a "? "Shape or a semicircular shape at a bottom portion is provided.

That is, in the present invention, the second stage cleaning separator support plate 335c having the plurality of second stage cleaning gas inlet ports 335a punctured, the gas movement guide 335b, the collision type first demister 335f, The configuration of the gas movement guide 335b among the components of the second cleaning liquid collecting portion 335 composed of the cleaning liquid collecting plate 335d and the vortex prevention plate 335e is changed and the gas movement guide 335b 9 and 11 as shown in Figs. 9 and 11, the moisture-discharge preventing and gas reflecting plate 337 having a "? "Shape or a semicircular shape is provided at the bottom of the gas- The load is reduced to a minimum so that the mist capture efficiency and the deodorization performance can be further improved.

At this time, among the components of the second washing liquid collecting part 335, the second-stage washing and separating part supporting plate 335c is disposed inside the main body 31 in such a manner that the first-stage washing part 32 and the second- 33, and a plurality of second-stage cleaning gas inlets 335a are formed with a long interval from the front portion toward the rear portion with a predetermined interval.

The plurality of second end cleaning gas inlets 335a punctured in the second end cleaning separator support plate 335c are firstly cleaned by the first end cleaning portion 32 and then cleaned with a moisture release preventing gas So that the malodor gas transported through the reflection plate 337 can be moved to the second cleaning pack bad part 334 side.

The gas movement guide 335b has an upper and a lower molded body corresponding to the shape of the second end cleaning gas inlet port 335a and the second end of the second end washing and separating support plate 335c However, the cleaning gas inlet 335a extends upward and downward from the outer periphery of the cleaning gas inlet 335a (that is, installed so as to protrude upward and downward through welding).

That is, the gas movement guide 335b in which a collision-type first demister 335f to be described later is installed is installed outside the second-stage cleaning gas inlet port 335a formed in the second-stage cleaning separation part support plate 335c The second cleaning gas inlet 335a of the second cleaning separator supporting plate 335c is extended from the outer periphery of the second cleaning gas inlet 335a toward the upper and lower portions.

The gas movement guide 335b functions as a guide pipe to move the odor gas passing through the first stage cleaning part 32 smoothly upwardly with the second stage cleaning part 33. [

As shown in Figs. 9 and 10, the moisture release preventing and gas reflecting plate 337 has a shape formed by a metal plate or a synthetic resin so as to have a "∧" shape or a semicircular shape in a positive section, 1 through the welding or the like in the form of hanging from the bottom of the second stage cleaning separator support plate 335c through a fixing member (not shown) at the bottom of the gas migration guide 335b in which the first demister 335f is installed, It is fixedly installed.

The moisture release preventing and gas reflecting plate 337 provided in this manner is configured so that the odor gas passing through the first stage washing section 32 is supplied to the gas moving guide 335b provided with the collision type first demister 335f, A part of the moisture contained in the malodorous gas is formed in the shape of a droplet on the bottom surface of the moisture release preventing and gas reflecting plate 337, It is possible to prevent the first cleaning liquid from being neutralized by being mixed with the second cleaning liquid because the moisture can be returned to the first end cleaning portion 32 side along the inclined surface of the moisture reflection preventing and gas reflecting plate 337. As a result, Can be minimized.

In addition, the odor gas, which is reflected by the bottom of the moisture-trapping and gas-reflecting plate 337 and reflected by the both sides of the moisture-trapping and gas-reflecting plate 337, is again sandwiched between the moisture- The first collision-type demister 335f is formed through the space formed between the upper surface of the moisture release preventing and gas reflecting plate 337 and the lower surface of the second-stage washing separation supporting plate 335c, And the gas flow guide 335b is introduced into the second stage washing section 33. In this process, the moisture discharge preventing and gas reflecting plate 337 delays the flow of the odor gas to the maximum, The load on the flow is reduced to a minimum. Therefore, the trapping efficiency and the deodorizing performance of the mist trapped by the collision-type first demister 335f, which will be described later, It is good.

Further, in the present invention, as shown in Figs. 12 and 13, a plurality of gas passage holes 337a are further formed on the moisture retention and gas reflecting plate 337 at predetermined intervals.

In this case, when the diameters of the gas passage holes 337a are all the same, the pressure applied to the respective positions corresponding to the inclination angle or the curvature of the moisture reflection preventing and gas reflecting plate 337 are different from each other The amount of the odor gas passing through the gas passage holes 337a formed in the gas passage holes 337a differs from one another.

Accordingly, in consideration of this, in the present invention, when the gas passage holes 337a are drilled in the moisture reflection preventing and gas reflecting plate 337, the passage amount of the odor gas passing through the respective gas passage holes 337a is made equal The diameter of the moisture reflection preventing and gas reflecting plate 337 is gradually increased by a predetermined magnification as the distance from the longitudinal center line of the moisture reflection preventing and gas reflecting plate 337 increases.

At this time, when the gas passing holes 337a are punctured in the moisture discharge preventing and gas reflecting plate 337, the amount of gas to be directly passed through the malodorous gas, that is, the load to be reduced, The perforation rate of the gas passage holes 337a with respect to the area of the gas reflection holes 337a may be different from that of the gas reflection holes 337a with respect to the area of the gas reflection holes 337a, %. ≪ / RTI >

As described above, a plurality of gas passage holes 337a are further formed on the moisture-preventing and gas-reflecting plate 337 at predetermined intervals, and the gas-discharging holes 337a are further extended outward from the longitudinal center line of the moisture- The odor gas that has passed through the first stage washing section 32 is reflected on the bottom surface of the moisture release preventing and gas reflecting plate 337 and is reflected on both sides thereof. When the flow is changed, some odor gas (for example, 20 to 40%) flows directly through the gas passage holes 337a to the gas movement guide 335b side in which the collision-type first demister 335f is placed, The remaining odor gas (for example, 60 to 80%) is reflected by the bottom surface of the moisture reflection preventing and gas reflecting plate 337 and is reflected to both sides,The swash plate 337 and then through the gap formed between the vortex and wihoe flows toward the first collision type having Mr (335f), the said gas movement guide (335b) naeseol.

Therefore, the odor gas that has passed through the first stage washing section 32 can flow smoothly and evenly toward the second stage washing section 33 after directly and bypassing the moisture discharge preventing and gas reflecting plate 337 , The moisture discharge preventing and gas reflecting plates 337 delay the flow of the malodor gas to the maximum, while the load due to the gas flow can be minimized. Therefore, the amount of the mist trapped, It can be greatly increased.

In the present invention, at both ends of the moisture-preventing and gas reflecting plate 337, the gas guide piece 337b is inclined or bent to a predetermined angle (for example, 15 to 30 degrees) .

Therefore, the odor gas, which is reflected by the bottom surface of the moisture-trapping and gas-reflecting plate 337 adjacent to each other and reflected by the two sides, flows upward through the gap formed between the moisture-trapping and gas-reflecting plates 337 The gas guide member 337b smoothly moves along the bottom surface of the gas guide member 337b inclined or curved within a predetermined angle, so that the moisture is prevented from being reflected by the gas-reflecting and gas reflecting plates 7, It is possible to prevent the flow velocity of the malodor gas and the load from rising due to the mutual collision, thereby preventing the deodorization throughput per hour from being deteriorated with respect to the malodorous gas.

In addition, in the present invention, the gap between the moisture discharge preventing and gas reflecting plates 337 is provided with the odor gas which is reflected by the moisture discharge preventing and gas reflecting plates 337 adjacent to each other, An interference prevention plate 338 is further provided so as to be able to move smoothly upward without friction.

At this time, in the present invention, the interference prevention plate 338 is formed so that a simple cross-sectional shape is formed in a "V" shape without forming a straight plate.

Therefore, the odor gas, which is reflected by the moisture release preventing and gas reflecting plates 337 adjacent to each other and is shifted in the flow direction to both sides, changes in the direction of the interference So that the malodorous gas can be smoothly moved upward without friction with the interference prevention plate 338.

Therefore, the odor gas, which is reflected by the bottom of the moisture-preventing and gas reflecting plate 337 and reflected by both sides thereof, does not hit each other in the gap between the adjacent moisture-preventing and gas-reflecting plates 337, The first collision-type demister 335f is moved to the upper part of the clearance or the guide of the gas guide piece 337a so as to smoothly pass the gap upward. The deodorization efficiency of the odor gas can be significantly increased due to the flow rate of the odor gas due to mutual interference and the decrease in the deodorization throughput per hour of the odor gas due to the increase in load due to mutual interference .

9 and 10, the impingement first demister 335f has a wing shape so that a mist pocket can be formed in an intermediate portion bent in a substantially "" shape, Type (Chevron type) and is detachably installed in the gas movement guide 335b.

As shown by the arrows in FIGS. 9 and 10, the impinging first demister 335f having the above-described structure is configured such that the odor gas flowing in the vertical direction from the fine jet cleaner 24 passes through the moisture- 337, the moisture is removed, and the flow of the moisture is reflected and reversed to both sides. Then, the water is guided to the gas movement guide 335b through the clearance of the moisture release prevention and gas reflecting plates 337 and flows into the gas movement guide 335b. So that the mist contained in the malodorous gas is collected by the wing-shaped mist pocket and then dropped to the lower part. In addition, And functions to suppress the moving speed of the gas.

At this time, the first cleaning liquid mist, which is a primary cleaning liquid mist that carries over to the second stage cleaning unit 33 in conjunction with the first cleaned odor gas flow, strikes the collision-type first demister 335f And the first cleaning liquid mist thus dropped flows toward the first stage cleaning section 32 along the upper surface of the moisture release preventing and gas reflecting plate 337 having a "? " And is collected through the first cleaning liquid circulating unit 325.

With this configuration of the collision type first demister 335f, it is possible to minimize the carry over of the first stage cleaning liquid mist to the second stage cleaning part 33 accompanied by the malodor gas flow, This can be prevented from being neutralized and the consumption of the chemical solution due to the mixing of the cleaning liquid can be minimized

In addition, since the moving velocity of the odor gas is suppressed by the collision-type first demister 335f, it is possible to prevent the mist trapped in the wing-shaped mist pocket from being re-scattered, thereby greatly improving the collection efficiency of the secondary cleaning liquid And the deodorizing performance is greatly improved.

9 and 10, the second end cleaning liquid collecting plate 335d provided in the second end cleaning portion 33 is formed to be larger than the width and length of the second end cleaning gas inlet 335a , And is formed so as to have a substantially V-shaped cross section with a predetermined cross-section. The odor gas is supplied to the main body 31 in the odor gas supply direction And is long in the lateral direction of the main body 31 so as to be perpendicular to the main body 31.

The second cleaning liquid collecting plate 335d collects the second cleaning liquid passing through the second cleaning package bad 334 and falling down to the second cleaning liquid inlet 335a, And also functions to disperse and move the odor gas upwardly moved through the second end cleaning gas inlet 335a to both sides.

The vortex prevention plate 335e is installed in a vertical direction between the adjacent second cleaning liquid collection plates 335d. The vortex prevention plate 335e passes through the gas movement guides 335b And then the malodorous gas dispersed and moved by the second-stage cleaning-liquid collecting plates 335d is moved to the second cleaning-pack bay 334 located at the upper side without interfering with each other.

At this time, the vortex prevention plate 335e may be formed to have a simple vertical plate shape, or may be formed so as to have a "∧" -shape in the front end face. The vortex prevention plate 335e may be simply formed as a vertical plate It is more preferable to form the polygonal cross section to have a "?" Shape.

Namely, when the vortex prevention plate 335e is formed so as to have a "정" shape in its front section, the odor gas dispersed and moved by the second end cleaning liquid collection plates 335d, which are adjacent to each other, As shown by the arrow, since the vortex prevention plate 335e moves upward in a form that it collides with both inclined surfaces of the vortex prevention plate 335e having the shape of "? &Quot;, the malodorous gas is prevented from flowing into the second cleaning & It can be smoothly moved to the side of the bad part 334.

1 and 14 to 16, the dust and moisture removing unit 40 includes a cylindrical portion 41, a conical portion 42, a cover 43, a fourth demister (not shown) And the gas inlet 411 is communicated with the gas outlet 312 of the multi-stage chemical liquid cleaning unit 30. The gas inlet 411 communicates with the gas outlet 312 of the multi-stage chemical liquid cleaning unit 30, , And is integrally fixed to one side of the multi-stage chemical liquid cleaning unit (30) from the upper surface of the body (10).

The dust and moisture removing unit 40 removes residual particles and dust contained in various organic or inorganic gases introduced through the multi-stage chemical liquid cleaning unit 30 from the fourth and fifth demisters 44 and 46 ) To perform the function of collecting and removing thirdarily.

Among the components of the dust and moisture removal unit 40, the cylindrical portion 41 is manufactured to have a predetermined diameter and height, and has a shape in which a gas inlet 411 is provided along the tangential direction at one side of the upper portion , And various organic or inorganic gases introduced from the multi-stage chemical liquid cleaning unit (30) through the gas inlet (411) are rotated.

In addition, the conical portion 42 is formed in a funnel shape in which the diameter gradually decreases, and also has a drain port 421 provided with a drain valve 422 from the center toward the lower portion. The cylindrical portion 41 And collects the water separated from the odor gas by the fourth and fifth demisters 44 and 46, which will be described later, and discharges it to the outside.

The lid body 43 has a gas outlet 431 at a central point and is coupled to an upper opening of the cylindrical portion 41 through a plurality of bolts or welding. And a function of fixing a frame 45 to be described later.

In addition, the fourth demister 44 has a chevron type in which a wave-shaped plate provided with a delayed gas discharge time or a trapped water particle and a drop wing for dust is provided at a predetermined interval, and the inner surface of the cylindrical portion 41 (Not shown) so as to be perpendicular to the turning direction of the odor gas in the space between the outer surfaces of the fifth and the fifth demisters 46.

The fourth demister 44 has a function of preventing the water particles contained in the malodor gas circulating inside the cylindrical portion 41 after flowing from the multistage chemical liquid cleaning unit 30 through the gas inlet 411, And a function of collecting relatively large water particles and dust in the dust and flowing them to the conical part 42 side.

At this time, the fourth demister 44 is not limited to being installed in only one stage, and the amount of water particles and dust contained in the odor gas flowing into the cylindrical portion 41 may be large, or the size of the cylindrical portion 41 may be If it is large, it may be installed in a multi-stage such as a two-stage or three-stage corresponding to the amount or volume.

The frame 45 is formed into a cylindrical shape in the form of a wire mesh net 451. The upper end of the frame 45 is fixed to the bottom surface of the lid body 43 and the fifth demister 46 is prevented from being separated from the lower end opening. And a disk-shaped finishing plate 452 for blocking inflow of malodorous gas is fixedly installed, and the fifth demister 46, which will be described later, is installed to be replaceable.

In addition, the fifth demister 46 is fabricated in the form of a plate-like filter having a structure similar to iron wool, unlike the fourth demister 44 having a chevron shape, and is installed in the form of wrapping the outer surface of the frame 45 .

The fifth demister (46) passes through the fourth demister (44), hits the inner surface of the cylindrical portion (41), and the odor gas circulating in the inner space portion passes through the fine pores provided in the fifth demister A function of secondarily collecting relatively small water particles and dust among the water particles and dust remaining in the odor gas in the process of being moved to the purge gas outlet 431 side of the lid body 43 and flowing it to the conical part 42 side .

The malodor gas backflow prevention plate 47 is disposed on the inner side of the malodor gas inlet 411 inside the cylindrical portion 41 (ie, the opposite side of the outer side fixed in the tangential direction of the cylindrical portion 41) (In other words, the side opposite to the inflow direction of the malodor gas) so as to block the vertical end portion and the contact portion between the first and second demisters 44 and 46 In a vertical direction) of the cylindrical portion 41 of the cylinder block.

The malodor gas backflow prevention plate 47 functions to supply the malodor gas introduced into the cylindrical portion 41 through the malodor gas inlet 411 to the fourth demister 44 without backflow, do.

In the dust and moisture removal unit 40 having such a configuration, as described above, the odor gas flowing into the inside of the cylindrical portion 41 is rotated along the inner surface of the cylindrical portion 41 like the cyclone, and the fourth demister Relatively large water particles and dust are primarily collected and collected by the conical portion 42 provided at the lower portion of the cylindrical portion 41 through the fourth demister 44, Relatively small water particles and dust may be secondarily collected in the process of passing through the fifth demister 46 having a cylindrical shape and then being discharged to the outside and may be collected by the conical portion 42 and then discharged to the outside have.

Accordingly, it is possible to prevent the activated carbon and the like in the activated carbon adsorption unit 50 provided at the final stage of the apparatus of the present invention from being contaminated and damaged by moisture, It is possible to greatly increase the deodorizing effect on various organic or inorganic gases through the use of the activated carbon, and the replacement cycle of the activated carbon can be increased, thereby greatly reducing the operation and maintenance costs.

1, 17, and 18, the activated carbon adsorption unit 50 is provided with a purge gas outlet 51 at an upper portion thereof and a plurality of plate-type activated carbon units 52 at a predetermined interval And has a shape in which a plurality of gas inlets 53 are communicated with a gas outlet 431 of the dust and moisture removal unit 40 and the dust and moisture removal unit 40 is disposed on the upper surface of the body 10, As shown in Fig.

In the activated carbon adsorption unit 50, various organic or inorganic gases introduced into the interior of the activated carbon adsorption unit 40 through the dust and moisture removal unit 40 pass through the plurality of plate-type activated carbon units 52 by zigzag, And finally discharges the purified gas to the outside after collecting and removing dust and odors finally contained in the exhaust gas.

Therefore, by using the apparatus of the present invention, odor and dust contained in various organic or inorganic gases can be completely deodorized and collected.

While the present invention has been described in connection with what is presently considered to be practical and exemplary embodiments, it is to be understood that the invention is not limited to the disclosed embodiments, but, on the contrary, It will be understood by those skilled in the art that various changes in form and details may be made therein without departing from the spirit and scope of the invention as defined by the appended claims.

10: Body
20: Vortical dust removal unit
21: main body 211: gas outlet
22: storage tank 221: direct water pipe
222: Automatic water supply valve 223: Drain valve
23: Odor gas supply line
24: Water spray for fine dust immersion
241: ring 242: nozzle
25: Orifice
251: gas inlet pipe 252: gas outlet pipe
253: fluid and gas passage hole 254: guide vane for vortex generation
26: Rotating radial guide vane
261: upper plate 261a: gas inflow hole
262: lower plate 262a: gas discharge direction guide portion
263: vortex forming blade 264: gas outlet
27: pump 28, 29: first and second demister
30: Multistage chemical liquid cleaning unit
31: Body
311: mist collecting portion 312: gas outlet
313: Gas distribution chamber 314: Gas inlet
32: first-stage cleaning unit 321: first cleaning-liquid storage tank
322: first cleaning liquid circulation pump 323: first cleaning liquid supply pipe
324: fine jet nozzle cleaning section 325: first cleaning liquid circulation section
33: second-stage cleaning unit 331: second cleaning-liquid storage tank
332: second cleaning liquid circulating pump 333: second cleaning liquid spraying pipe
334: second cleaning pack bad part 335: second cleaning liquid collecting part
335a: second stage cleaning gas inlet port 335b: gas moving guide
335c: second-stage cleaning separation part support plate 335d: second-stage cleaning liquid collection plate
335e: vortex prevention plate 335f: third demister
336: second cleaning liquid circulation part
337: Damp-proof and gas reflector
337a: gas passage hole 337b: gas guide piece
338: Interference prevention plate
40: dust and moisture removal unit
41: Cylinder part 411: Gas inlet
42:
421: Drain port 422: Drain valve
43: Lid body 431: Outlet
44: fourth demister 45: frame
451: wire mesh net 452: disk-shaped finishing plate
46: second demister 47: backflow prevention plate
50: activated carbon adsorption unit 51: purge gas outlet
52: plate-type activated carbon unit 53: gas inlet

Claims (13)

A body having a rectangular plate shape;
A plurality of organic or inorganic gases supplied from the outside through a malodorous gas supply line to the inside of the storage tank through an orifice through which water is sprayed, A dust collecting unit for collecting the odor through the first and second demisters installed in the storage tank as well as the water in the storage tank;
Type dust removal unit, the gas inlet being in communication with the gas outlet of the vortex-type dust removal unit, and being fixed to one side of the vortex-type dust removal unit on the upper surface of the body, A multistage chemical liquid cleaning unit for secondarily taking up the collected and odor;
Stage chemical liquid cleaning unit, the gas inlet communicates with the gas outlet of the multi-stage chemical liquid cleaning unit, and is fixed to one side of the multi-stage chemical liquid cleaning unit on the upper surface of the body, and through the fourth and fifth demisters, A dust and moisture removing unit for collectively collecting and removing residual particles and dust contained in the inorganic gas;
A plurality of plate type activated carbon units are arranged at predetermined intervals and a plurality of gas inlets are communicated with gas outlets of the dust and moisture removal unit, Various organic or inorganic gases fixedly installed on one side of the water removal unit and introduced into the interior thereof are passed through a plurality of plate-type activated carbon units in a staggered manner, and dust and odor contained in various organic or inorganic gases are finally collected and removed And an activated carbon adsorption unit for discharging the purified gas to the outside,
The vortex-type dust removing unit includes:
A body having a hollow square shape inside and having a gas outlet at one side and an open bottom;
A storage tank installed at a bottom opening of the main body and containing water necessary for collecting fine dust;
A malodorous gas supply line installed to penetrate through an intermediate portion of the main body from the outside to supply various organic or inorganic gases supplied from the outside to water in a storage tank through an orifice and a rotary radial guide vane;
A plurality of nozzles are provided inside the ring and the water supplied through the pump is installed to be replaceable at the lower end of the odor gas supply line so that the water is jetted to a predetermined pressure on various organic or inorganic gases passing through the odor gas supply line A water injector for fine dust immersion;
The flow rate of various organic or inorganic gases supplied through the odor gas supply line is instantaneously accelerated and the flow rate is lowered again in a state in which the upper end of the gas inlet pipe is fixedly installed on the bottom surface of the water injector for micro- An orifice for allowing water sprayed from the nozzles of the water spray for fine dust immersion to flow down along the inner surface toward the storage tank and allowing fine dust adsorbed on the inner surface to automatically flow into the storage tank;
The orifice is exposed to the water surface of the storage tank, the fine dust that has absorbed the moisture is vortexed including various kinds of organic or inorganic gas including the odor passing through the orifice, And a rotating radial guide vane for swirling the storage tank by the spray pressure of various organic or inorganic gas discharged in a vortex shape;
A pump for continuously supplying water in the storage tank to the water injector for fine particle dipping;
And an odor absorbing unit for collecting odor, moisture and fine dust contaminants in various kinds of organic or inorganic gas passing through the water in the storage tank in such a manner as to block the middle portion except for the odor gas supply pipe in the main body in a horizontal direction A first demister of a chevron type;
And a second demister disposed in a horizontal direction below the gas outlet in the main body to collect odor, moisture, and fine dust contaminants contained in the gas finally passing through the first demister Wherein the odor eliminating device comprises:
delete The method according to claim 1,
Wherein the rotary radial guide vane comprises:
An upper plate having a shape in which a gas inlet hole is formed at the center and detachably fixed to a lower end of the orifice;
A lower plate integrally fixed to a bottom of the upper plate through a plurality of vortex forming blades, the lower plate having a shape having a gas discharge direction guide portion at the center thereof;
And a variety of organic or inorganic gases contained in the form of a radial shape at a predetermined angle in a clearance between the upper plate and the lower plate and containing odors flowing through the gas inlet holes of the upper plate And a plurality of vortex forming blades for allowing the fine dust that has absorbed the moisture to flow into the water in the storage tank through the gas outlet formed along the circumference.
The method according to claim 1,
And an automatic water supply valve for automatically supplying water when the water level in the storage tank falls below a predetermined water level is further provided at an end of the water pipe located in the storage tank Wherein the odor eliminating device comprises:
The method according to claim 1,
The nozzles provided on the inner side of the ring of the water jetting device for fine dust-
Wherein the water is sprayed in such a manner that water sprayed through the nozzles is vortexed by being installed or formed so as to be inclined at an angle (?) Determined in one direction.
The method according to claim 1,
A plurality of guide vanes for vortex generation which cause the water in the storage tank to vortify by causing water to flow along the inner surface of the orifice, as well as various organic or inorganic gases, Wherein the odor eliminating device comprises:
The method according to claim 1,
And a drain valve for discharging contaminated water to the outside is further provided on the bottom of the storage tank.
The method according to claim 1,
In the multi-stage drug solution cleaning unit,
A body having a hollow interior with a mist collecting portion, a gas outlet, a gas distribution chamber, and a gas inlet;
A first cleaning liquid storage tank, a first cleaning liquid circulation pump, a first cleaning liquid supply pipe, a fine jet nozzle cleaning unit, and a first cleaning liquid circulation unit;
A second washing liquid circulating pump, a second washing liquid spraying tube, a second washing bath bad part, a second washing liquid collecting part, and a second washing liquid circulating part, wherein the second washing liquid storing tank, the second washing liquid circulating pump,
The second cleaning liquid collecting part is composed of a second stage cleaning separator supporting plate having a second stage cleaning gas inlet and a gas movement guide, a collision type third demister, a second stage washing liquid collecting plate, and a vortex prevention plate,
The gas movement guide in which the collision type third demister is installed is extended to the upper and lower portions of the second stage cleaning separating portion support plate,
Characterized in that a moisture release preventing and gas reflecting plate having either a "∧" shape or a semicircular shape in its front section is provided at the bottom of the gas movement guide in which the collision type third demister is embedded. Device.
The method of claim 8,
On the moisture release preventing and gas reflecting plate,
A plurality of gas-passing holes allowing a part of the odor gas to pass directly to the side of the collision-type third demister are further punctured at regular intervals,
Wherein the gas passing holes are perforated so as to gradually increase in diameter by a predetermined magnification toward the outside from the longitudinal center line of the gas reflection plate and the gas reflection preventing plate.
The method of claim 8,
At both end portions of the moisture discharge preventing and gas reflecting plate,
Wherein the gas guide member is inclined within a predetermined angle toward the upper side or a curved gas guide member is further bent.
The method of claim 8,
In the vertical direction in the clearance between the moisture release preventing and gas reflecting plates,
Further comprising an interference prevention plate for causing the various organic or inorganic gases, which are reflected by both the moisture discharge preventing and gas reflecting plates, to be reflected and flowed to both sides, to move upward without interference with each other.
The method of claim 11,
The interference prevention plate includes:
Shape to be able to smoothly move various organic or inorganic gases, which are reflected by the moisture-preventing and gas reflecting plates adjacent to each other, Wherein the odor eliminating device comprises:
The method according to claim 1,
Wherein the dust and moisture removal unit comprises:
A cylindrical portion having a predetermined diameter and a height and having a gas inlet along the tangential direction at one side of the upper portion and for circulating various organic or inorganic gases introduced through the gas inlet;
A conical portion integrally formed at a lower portion of the cylindrical portion with a drain hole having a drain valve installed at a center thereof, the diameter being gradually reduced;
A lid provided with a gas outlet at a center point and coupled to an upper opening of the cylindrical portion;
Water particles contained in various organic or inorganic gases which are arranged in a vertical direction so as to be perpendicular to the direction of rotation of various organic or inorganic gases in the space portion between the inner surface of the cylindrical portion and the outer surface of the fifth demodulator, And a fourth demister which primarily collects relatively large water particles and dust in the dust and flows it to the conical part side;
A cylindrical wire mesh network having a top end fixed to the bottom surface of the lid body and a disk-shaped finish plate fixed to the bottom end opening to prevent the fifth demister from coming off and to block the inflow of various organic or inorganic gases A frame;
A plurality of organic or inorganic gases having a shape provided to surround the outer surface of the frame and passing through the fourth demister and turning the internal space of the cylindrical portion, A fifth demister that collects relatively small water particles and dust among the water particles and dust remaining in various organic or inorganic gases, and flows the collected water particles to the conical part side;
A plurality of organic or inorganic gases introduced into the cylindrical portion through the gas inlet are provided in the cylindrical portion so as to block the inner side end portion of the gas inlet and the contact portion of the fourth and fifth demisters in the vertical direction, And a malodor gas backflow preventing plate for supplying the malodor gas back to the fourth demister side.
KR1020180026082A 2018-03-06 2018-03-06 Complex type odor eliminator KR101874338B1 (en)

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KR101937797B1 (en) 2018-09-19 2019-01-11 한솔이엠이(주) Apparatus for removing acidic noxious gas
KR101955270B1 (en) * 2018-11-06 2019-03-08 윤창진 Complex type odor eliminator
CN110141917A (en) * 2019-05-09 2019-08-20 张波 A kind of heating of system for desulfuration and denitration disappears white equipment
KR101999595B1 (en) * 2019-04-02 2019-10-01 주식회사 일진도시환경 Fine particle collected device
KR102025024B1 (en) * 2018-12-17 2019-11-14 주식회사 창우엔바이로 Three-stage deodorizing apparatus of single absorption tower
CN112246820A (en) * 2020-10-26 2021-01-22 绍兴金诚达纺织股份有限公司 Peculiar smell device is removed to weaving equipment
KR20210052777A (en) * 2019-10-31 2021-05-11 한국생산기술연구원 A scrubber including absorption member
KR102304952B1 (en) * 2021-08-23 2021-09-24 정일교 Zigzag fog nozzle chemical cleaning deodorizer with modular vortex pore box
KR102309472B1 (en) * 2021-04-21 2021-10-06 주식회사 에코코어기술 Air flow rotary multi-stage chemical liquid cleaning device
KR102431219B1 (en) * 2021-12-09 2022-08-11 주식회사 에스엔텍솔루숀 Chemical cleaning type plasma oxidation complex deodorization device and method therefor
KR102495475B1 (en) * 2022-07-29 2023-02-06 주식회사 유진테크 Free dropping W type panel module and the method thereof
KR20230019392A (en) 2021-07-29 2023-02-08 유한회사 네오클 Physical and Chemical Deodorization System and Method using Gaseous Chlorine Dioxide Adsorption on Silica Gel and UV Irradiation as well as Adsorption-Desorption on-Shifts Process

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Publication number Priority date Publication date Assignee Title
KR101937797B1 (en) 2018-09-19 2019-01-11 한솔이엠이(주) Apparatus for removing acidic noxious gas
KR101955270B1 (en) * 2018-11-06 2019-03-08 윤창진 Complex type odor eliminator
KR102025024B1 (en) * 2018-12-17 2019-11-14 주식회사 창우엔바이로 Three-stage deodorizing apparatus of single absorption tower
KR101999595B1 (en) * 2019-04-02 2019-10-01 주식회사 일진도시환경 Fine particle collected device
CN110141917A (en) * 2019-05-09 2019-08-20 张波 A kind of heating of system for desulfuration and denitration disappears white equipment
KR20210052777A (en) * 2019-10-31 2021-05-11 한국생산기술연구원 A scrubber including absorption member
KR102376724B1 (en) 2019-10-31 2022-03-23 한국생산기술연구원 A scrubber including absorption member
CN112246820A (en) * 2020-10-26 2021-01-22 绍兴金诚达纺织股份有限公司 Peculiar smell device is removed to weaving equipment
KR102309472B1 (en) * 2021-04-21 2021-10-06 주식회사 에코코어기술 Air flow rotary multi-stage chemical liquid cleaning device
KR20230019392A (en) 2021-07-29 2023-02-08 유한회사 네오클 Physical and Chemical Deodorization System and Method using Gaseous Chlorine Dioxide Adsorption on Silica Gel and UV Irradiation as well as Adsorption-Desorption on-Shifts Process
KR102304952B1 (en) * 2021-08-23 2021-09-24 정일교 Zigzag fog nozzle chemical cleaning deodorizer with modular vortex pore box
KR102431219B1 (en) * 2021-12-09 2022-08-11 주식회사 에스엔텍솔루숀 Chemical cleaning type plasma oxidation complex deodorization device and method therefor
KR102495475B1 (en) * 2022-07-29 2023-02-06 주식회사 유진테크 Free dropping W type panel module and the method thereof

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