KR101382611B1 - Non contact swirl type optical composite catalytic oxidation deodorizing apparatus - Google Patents

Abstract

The present invention provides a complex oxidizing tank in a movement path of odor gas to remove odor by non-contact oxidation, and the complex oxidizing tank includes: a first casing for passing odor gas; A first demister installed at the inner front end of the first casing to remove foreign substances from the odor gas passing therethrough and to disperse the odor gas; And a plurality of first UV lamp modules installed in the first casing so as to be arranged in a direction crossing the movement direction of the malodorous gas at the rear side of the first demister, wherein each of the first UV lamp modules includes a movement direction of the malodorous gas. A plurality of first UV lamps installed at intervals along the moving direction of the malodorous gas, respectively; A plurality of first titanium dioxide catalyst plates each installed on the front side of the first UV lamp so as to be parallel to the first UV lamp and coated with titanium dioxide as a catalyst; And a plurality of second titanium dioxide catalyst plates each of which are stacked at intervals along the direction crossing the direction of movement of the malodorous gas at each rear side of the first UV lamp, the second titanium dioxide catalyst plate coated with titanium dioxide as a catalyst. A composite catalyst oxidative deodorizer.
According to the present invention, the complex oxidation method such as ultraviolet oxidation, ozone oxidation, OH radical oxidation can be increased by titanium dioxide catalyst coating plate, furthermore manganese dioxide catalyst coating plate, and the deodorization efficiency due to catalyst poisoning and foreign matter adhesion can be prevented. .

Description

Non contact swirl type optical composite catalytic oxidation deodorizing apparatus

The present invention relates to a non-contact vortex type photo-composite catalytic oxidation deodorization device, and more particularly, to effectively remove odors in industrial sites causing high concentration odors, such as wastewater treatment plants, food waste treatment plants, sewage treatment plants, manure waste treatment plants, The present invention relates to a non-contact vortex type photo-composite catalytic oxidative deodorizing device for solving complaints resulting from malodor.

In general, emissions of air pollutants are continuously increasing due to economic development and industrialization, and types of air pollutants are gradually diversifying. In particular, malodorous gases generated in the manure treatment plant, wastewater treatment plant and various plants include hydrogen sulfide (H ₂ S), mercaptan (RSH), ammonia (NH ₃ ) and amines (RNH ₂ ). Inhalation may cause headaches or discomfort.

Research is actively conducted to remove such malodorous gases from various aspects, and many malodorous treatment apparatuses are known accordingly. The techniques applied to the malodorous gas treatment apparatus currently used are largely activated carbon adsorption, chemical liquid cleaning, There are physical and chemical treatment methods such as ozone oxidation and combustion deodorization, and biological treatment methods such as soil microbial treatment, activated sludge and biofilter. Such odor gas treatment apparatus may be used alone or in combination of two or more odor treatment methods depending on the treatment environment to remove odor gas.

However, the deodorizing device for the conventional odor treatment, there is a limit to reliably remove the odor, which is a high concentration of odor is complicated and expensive equipment, including the expensive but deodorizing efficiency is not satisfactory Had a problem.

Korean Patent Application Publication No. 10-2010-0070642 "Deodorization device using ultraviolet and photocatalyst (published on June 28, 2010)"

In order to solve the conventional problems as described above, the present invention is to effectively remove the odor in industrial sites that cause high concentration odor, such as wastewater treatment plant, food waste treatment plant, sewage treatment plant, livestock waste treatment plant, resulting in complaints resulting from odor It is aimed at eliminating the problem, and furthermore, to prevent environmental pollution due to odors.

Other objects of the present invention will become readily apparent from the following description of the embodiments.

In order to achieve the object as described above, according to one aspect of the present invention, in the deodorizing device, a complex oxidation tank is installed in the movement path of the malodorous gas to remove the malodor by non-contact oxidation, the complex oxidation tank, malodorous gas A first casing for the to pass through; A first demister installed at the inner front end of the first casing to remove foreign substances from the odor gas passing therethrough and to disperse the odor gas; And a plurality of first UV lamp modules installed in the first casing so as to be arranged in a direction crossing the moving direction of the malodorous gas at the rear side of the first demister, wherein each of the first UV lamp modules is a malodorous gas. A plurality of first UV lamps, each of which is installed to intersect in a moving direction of and arranged at intervals along the moving direction of the malodorous gas; A plurality of first titanium dioxide catalyst plates disposed on the front side of the first UV lamp so as to be parallel to the first UV lamp, and coated with titanium dioxide as a catalyst; And a plurality of second titanium dioxide catalyst plates installed on the rear sides of the first UV lamps at intervals along the direction crossing the movement direction of the malodorous gas and coated with titanium dioxide as a catalyst. Non-contact vortex type photo-composite catalytic oxidation deodorizing device for filtering foreign matters from odor gas by demister and performing oxidation deodorization by the first and second titanium dioxide catalyst plates installed around the first UV lamp and Can be provided.

Further comprising a flush filter tank is provided in front of the first casing, the flush filter tank, the inlet for introducing the odor gas is provided on one side, the odor gas passing through the inside for the discharge to the first casing side Outlet is provided on the other side, the water tank is filled with the washing water in the lower portion; A first windmill installed to rotate by a non-powered by odorous gas passing through the water surface of the washing water in the tank or by a power of a motor; In order to guide the odor gas flowing through the inlet to move to the first windmill side and guide the odor gas passing through the first windmill to move in a zigzag and discharged to the outlet side, it is arranged to be arranged inside the tank A plurality of guide plates; A tank for connecting the washing water from the water tank to measure the water level in the water tank by a gauge, and a supply line for supplying the water to water to supply the water to the water tank; And a discharge line connected to the lower portion of the water tank to discharge the washing water and opened and closed by a valve.

The apparatus may further include an oxidation mixing tank in which a plurality of second windmills are installed to rotate by a non-powered by odor gas or a power by a motor passing inside the second casing provided to extend to the rear side of the first casing. Can be.

Further comprising a compound reduction tank is installed to perform a reduction action on the malodorous gas discharged from the second casing, the compound reduction tank is connected to the second casing third casing (casing) to pass through ; A second demister installed at the inner front end of the third casing and removing foreign matters from the odor gas passing therethrough and dispersing the odor gas; And a plurality of second UV lamp modules installed in the third casing such that the second UV lamp modules are arranged in a direction crossing the moving direction of the malodor gas at the rear side of the second demister. A plurality of second UV lamps each installed to intersect in a moving direction of and arranged at intervals along the moving direction of the malodorous gas; A plurality of first manganese dioxide catalyst plates each side of the second UV lamp installed side by side with the second UV lamp and coated with manganese dioxide as a catalyst; And a plurality of second manganese dioxide catalyst plates installed on the rear sides of the second UV lamps at intervals along the direction crossing the movement direction of the malodorous gas and coated with manganese dioxide as a catalyst.

A reduction mixing tank in which a plurality of third windmills installed to rotate by a non-powered by odor gas or an electric power by a motor passing inside the fourth casing provided to extend on the rear side of the third casing and the reduction mixing tank are installed. It may further include a blower tank is provided in the inner side of the fifth casing connected to the rear of the tank is provided with a blower for providing a blowing force to blow the gas after the deodorization and stabilization process from the fourth casing to the outside.

According to the non-contact vortex type photo-composite catalytic oxidation deodorizing apparatus according to the present invention, the complex oxidation method such as ultraviolet oxidation, ozone oxidation, OH radical oxidation, etc. increases the activity by titanium dioxide catalyst coating plate, and further by manganese dioxide catalyst coating plate, and ozone by windmill Increases the mixing between the odor gas and the odor gas, thereby eliminating germ sterilization as well as high concentration of odor through several steps, and preventing the reduction of deodorization efficiency due to catalyst poisoning and foreign matter adhesion, which are the biggest disadvantages of catalytic oxidation. have.

1 is a block diagram showing a non-contact vortex type photo-composite catalytic oxidation deodorizing apparatus according to an embodiment of the present invention,
2 is a block diagram showing a flush filter tank of a non-contact vortex type photo-composite catalytic oxidation deodorizing apparatus according to an embodiment of the present invention,
3 is a perspective view showing the main portion of the complex oxidation tank of the non-contact vortex type photo-composite catalytic oxidation deodorizing apparatus according to an embodiment of the present invention,
Figure 4 is a perspective view showing the main portion of the complex reduction of the non-contact vortex type photo-composite catalytic deodorization apparatus according to an embodiment of the present invention.

While the invention is susceptible to various modifications and alternative forms, specific embodiments thereof are shown by way of example in the drawings and will herein be described in detail. It is to be understood, however, that the invention is not to be limited to the specific embodiments, but is to be understood to cover all modifications, equivalents, and alternatives falling within the spirit and scope of the invention, And the scope of the present invention is not limited to the following examples.

Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings, wherein like or corresponding elements are denoted by the same reference numerals, and redundant explanations thereof will be omitted.

1 is a block diagram showing a non-contact vortex type photo-composite catalytic oxidation deodorization apparatus according to an embodiment of the present invention.

As shown in FIG. 1, the non-contact vortex type photo-composite catalytic deodorization apparatus 100 according to an embodiment of the present invention has a complex oxidation tank 120 in the movement path of the odor gas to remove odor by non-contact oxidation. Is installed.

The complex oxidizing tank 120 is installed at the first casing 121 through which the malodorous gas passes and the inner front end of the first casing 121 to remove foreign substances from the malodorous gas passing therethrough, and the malodorous gas is dispersed. A plurality of first UV lamps installed in the first casing 121 so that the first demister 122 and the first demister 122 are arranged in a direction crossing the movement direction of the malodorous gas at the rear side of the first demister 122. Module 123.

For example, the first demister 122 may have a structure in which a single or a plurality of meshes are stacked, or may have a filter structure for removing foreign matter from the odor gas.

As shown in FIG. 3, each of the first UV lamp modules 123 is provided to intersect with the moving direction of the malodorous gas, and the plurality of first UV lamps 123a are arranged at intervals along the moving direction of the malodorous gas. And a plurality of first titanium dioxide catalyst plates 123b which are installed to be parallel to the first UV lamp 123a on every front side of the first UV lamp 123a, and coated with titanium dioxide (TiO ₂ ) as a catalyst; Each of the rear side of the first UV lamp 123a is installed so as to be stacked at intervals along the direction crossing the movement direction of the malodorous gas, and includes a plurality of second titanium dioxide catalyst plates 123c coated with titanium dioxide as a catalyst. Can be. Here, the first UV lamp 123a may be formed in a bar shape so that the longitudinal direction may be coincident with the direction crossing the odor gas movement direction in the first casing 121, and simultaneously radiate UV in two wavelength bands of 185 nm and 254 nm. It can be made of a lamp. In addition, the first and second titanium dioxide catalyst plates 123b and 123c may be made of a glass substrate coated with titanium dioxide as a catalyst on its surface. In addition, the upper and lower portions of the first UV lamp module 123 may be fixed by the installation unit 124.

In front of the first casing 121, the flush filter tank 110 as shown in FIG. 2 may be installed.

The flush filter tank 110 is provided with an inlet 111a for introducing malodorous gas on one side and an outlet 111b for connecting the malodorous gas passing through the inside to the first casing 121 side. And a water tank 111 filled with a washing water, for example, city water, and a non-powered by odorous gas passing through the water surface of the washing water in the water tank 111 or a power installed by a motor. The first windmill 112 and the odor gas flowing through the inlet 111a are guided to move toward the first windmill 112, and the odor gas passing through the first windmill 112 moves in a zigzag to discharge the outlet 111b. In order to guide the discharge to the side, a plurality of guide plates 113 installed to be arranged inside the water tank 111, and the washing water from the water tank 111 is connected so that the inside of the water tank 111 by the gauge (114a) Flushing water level And a tank 114 for supplying the washing water supplied from the outside to the water tank 111 by connecting the supply line 114b for supplying the washing water to the lower portion of the water tank 111. It may be connected to, and may include a discharge line 115 that is opened and closed by the valve (115a). Meanwhile, the discharge line 115 may be connected to the first casing 121 and the second to fourth casings 131, 141, and 151, which will be described later, as well as the water tank 111, and valves may be installed as necessary. Can be.

The first windmill 112 may be rotated in a non-powered manner by the blowing force of the malodorous gas. The first windmill 112 may be forcibly rotated using the rotational force of the motor in consideration of the lack of blowing force of the malodorous gas or the mixing efficiency of the malodorous gas and the washing water. It can be configured to be powered.

The guide plate 113 is installed in two or more zigzag to filter the contaminants in the odor gas as possible to prevent the contaminants from reaching the outlet 111b located in the upper layer, and to be separated from the water tank 111, if necessary Thus disassembly and mounting are possible.

The tank 114 may be installed so that the level control valve for opening and closing the supply of the washing water by the vertical movement of the buoyancy body floating on the water surface to be connected to the supply line 114b, the discharge line (below the water tank 111) The valve 115a installed at 115 may be configured to operate in conjunction with such a water level control valve.

An oxidation mixing tank 130 may be installed at the rear side of the complex oxidation tank 120, and the oxidation mixing tank 130 passes inside the second casing 131 provided to extend to the rear side of the first casing 121. A plurality of second windmills 132 are installed to rotate by a non-powered by the blowing force of the odor gas or a power by a motor. Here, the second casing 131 may be detachably coupled to the first casing 121 or may be manufactured to be integrated as in the present embodiment. In addition, the second windmill 132 may be rotated in a non-powered manner by the blowing force of the malodorous gas. The second windmill 132 is forcibly rotated by using the rotational force of the motor in consideration of the lack of blowing force of the malodorous gas or the mixing efficiency of the malodorous gas and ozone. It can be configured to be powered.

At the rear end of the second casing 131, a complex reduction tank 140 may be installed to finish the deodorization process from the second casing 131 and to perform a reduction action on the odorous gas discharged, thereby performing stabilization of the gas. have. Here, the term odor gas discharged after the deodorization process from the second casing 131 may be a gas in which a small amount of odor is left or the odor is almost removed.

The composite reduction tank 140 is connected to the second casing 131 and is installed at a third casing 141 for allowing malodorous gas to pass therethrough, and is installed at the inner front end of the third casing 141 and passes through the malodorous gas passing therethrough. The second demister 142 which removes foreign substances and disperses malodorous gas, and the third casing 141 which is arranged in a direction crossing the movement direction of the malodorous gas at the rear side of the second demister 142. It may include a plurality of second UV lamp module 143 is installed in. Here, the second demister 142 may have a structure in which a single or a plurality of meshes are stacked, for example, or may have a filter structure to remove foreign substances from odor gas. In addition, the upper and lower portions of the second UV lamp module 143 may be fixed by the installation unit 144.

As shown in FIG. 4, each of the second UV lamp modules 143 is provided to intersect with the moving direction of the malodorous gas and is arranged at intervals along the moving direction of the malodorous gas. ) And a plurality of first manganese dioxide catalyst plates 143b, which are installed to be parallel to the second UV lamp 143a at every front side of the second UV lamp 143a, and are coated with manganese dioxide (MnO ₂ ) as a catalyst; The rear side of the UV lamp 143a may include a plurality of second manganese dioxide catalyst plates 143c installed to be stacked at intervals along the direction crossing the movement direction of the malodorous gas and coated with manganese dioxide as a catalyst. Here, the second UV lamp 143a may be configured to emit UV in the wavelength range of 254 nm, for example, and may be formed in a bar shape so that the longitudinal direction coincides with the direction in which the malodorous gas moves in the third casing 141. Can be. In addition, the first and second manganese dioxide catalyst plates 143b and 143c may be made of a glass substrate coated with manganese dioxide as a catalyst on its surface.

At the rear end of the third casing 141, a reduction mixing tank 150 and a blowing tank 160 may be installed, respectively.

The reduction mixing tank 150 is a third windmill installed to rotate by a non-powered by the odor gas or the power of the motor passing through the inside of the fourth casing 151 is provided to extend to the rear side of the third casing (141). 152 may be installed in plural. Here, the fourth casing 151 may be detachably coupled to the third casing 141 or may be manufactured to be integrated as in the present embodiment. In addition, the third windmill 152 may be rotated in a non-powered manner by the blowing force of the malodorous gas, and can be forcibly rotated by using the rotational force of the motor in consideration of the lack of blowing force of the malodorous gas or the mixing efficiency of the malodorous gas. Can be configured to be powered.

The blower 160 blows the gas after deodorization and stabilization from the fourth casing 151 inside the fifth casing 161 connected to the rear side of the fourth casing 151 of the reduction mixing tank 150 to the outside. A blower 162 may be installed to provide a blowing force so that the blower 162 of the blower tank 160 transfers the malodorous gas from the flush filter tank 110 to the reduction mixing tank 150. At this time, the required standard design static pressure may be about 80 ~ 100mmAg.

The operation of the non-contact vortex type photocomposite catalytic oxidation deodorization apparatus according to the present invention will be described.

When the high concentration of odorous gas containing moisture and oil is collected and introduced into the flush filter tank 110, the water-soluble odor is first filtered by mixing with water using the first windmill 112 using no power or power. That is, the washing tank is filled to the water tank 111 by a predetermined level, and the malodorous gas is mixed with the washing water due to the rotation of the first windmill 112, thereby primarily filtering the moisture and oil contained in the malodorous gas.

Odor gas passing through the flush filter tank 110 is introduced into the complex oxidizing tank 120, the composite oxidizing tank 120 is placed from the front end of the first casing 121 by placing the first demister 122 in the front end The first UV lamp module 123 is protected by filtering foreign substances such as dust from the odor gas supplied and dispersing the wind speed uniformly.

The first UV lamp 123a of the first lamp module 123 may maximize the ozone generation and sterilization effect by using a lamp that emits UV in two wavelengths of 185 nm and 254 nm, and may use a 40 W rated lamp. In addition, due to the first and second titanium dioxide catalyst plates 123b and 123c having layered layers arranged around the first UV lamp 123a, a combination of low temperature due to ultraviolet (photo) oxidation and ozone oxidation and OH radical generation Oxidation is carried out, and toxic poisoning and foreign matter adhesion, which are the weakest points of catalytic oxidation, are avoided.

By such a complex oxidation tank 120, a stable contactless photocatalytic oxidation is adopted, and by the oxidation mixing tank 130 at the rear end of the complex oxidation tank 120, the deodorizing ability of ozone can be exhibited to the maximum. That is, ozone is itself an unstable gas, which is converted into oxygen or the like within a few minutes or several tens of minutes in the atmosphere, but it is difficult to achieve 100% of odors and reactions in a quiet airflow, therefore, the second windmill of the oxidation mixing tank 130 ( 132), the odor gas is shaken and vortexed to mix ozone and odor gas, thereby allowing the odor gas and ozone to be properly mixed even in a small space, and to increase the retention period so that the deodorizing effect is excellent. In addition, due to the excellent mixing and deodorizing effect, ozone component that caused the oxidizing gas and the catalytic oxidation reaction disappears, and the smell of ozone disappears.

The odor gas discharged from the oxidation mixing tank 130 passes through the complex reduction tank 140 and the reduction mixing tank 150. The odor gas and ozone gas are properly mixed in the oxidation mixing tank 130, thereby reducing the complex reduction tank ( At 140), deodorization is caused by the reducing ability stably. In other words, if the odor gas flows into the composite reduction tank 140 before it is oxidized, it does not help any deodorization and reduction effect, but the oxidation is completely caused by the oxidation mixing tank 130 so that the complex reduction tank ( Reducing ability by 140) is properly exhibited to have an excellent deodorizing effect.

In addition, the odor gas introduced into the complex reduction tank 140 is passed between the second UV lamp module 143 by the third windmill 152, the contact time between the ions and the oxide gas and the unstable gases is increased, where The second UV lamp 143a generates ions of 254 nm wavelength and sterilizes the odor remaining in the odor gas. The second UV lamp 143a and the UV light of the second UV lamp 143a and the first and second manganese dioxide catalyst plates 143b are used. By the reduction reaction using manganese dioxide as a catalyst of (143c), residual ozone, peroxide gas, and unstable gases are stabilized by reduction.

In addition, by driving the blower 162 of the blower tank 160, it provides a blowing force for the odor gas to be discharged from the flush filter tank 110 to the outside through the blower tank 160, the deodorized gas to the outside To be discharged. On the other hand, the blowing force for the odor gas to move from the flush filter 110 to the composite reduction tank 140 is installed on the movement path of the odor gas, including the front end of the flush filter 110 in place of the blow tank (160). A separate blower can also be used.

As described above, according to the present invention, the complex oxidation method such as ultraviolet oxidation, ozone oxidation, OH radical oxidation, etc. is increased by titanium dioxide catalyst coating plate, and further, manganese dioxide catalyst coating plate, and the windmill increases mixing between ozone and odor gas. Due to this, bacteria can be sterilized as well as deodorized at high concentrations through a multi-step process, and the reduction of deodorization efficiency due to catalyst poisoning and foreign matter adhesion, which are the biggest disadvantages of catalytic oxidation.

In other words, the odor gas does not flow directly into the UV lamp module, but moves only between the UV lamp modules, so that the odor gas does not come into direct contact with the UV lamp and the catalyst plate in the UV lamp module. As it flows in, the dust, water, oil, and foam remaining after passing through the water tank and the destructor at the front of the deodorizing equipment can enter the UV lamp module to structurally avoid the catalyst poisoning that contaminates the UV lamp and the catalyst plate. Depending on the nature of the malodorous gas, the water tank at the front end of the deodorizing device may be excluded.

Although the present invention has been described with reference to the accompanying drawings, it is to be understood that various changes and modifications may be made without departing from the spirit of the invention. Therefore, the scope of the present invention should not be limited to the described embodiments, but should be determined by the equivalents of the claims, as well as the following claims.

110: flush filter tank 111: water tank
111a: inlet 111b: outlet
112: first windmill 113: guide plate
114 tank 114a gauge
114b: supply line 115: discharge line
115a: Valve 120: complex oxidation tank
121: first casing 122: first demister
123: first UV lamp module 123a: first UV lamp
123b: first titanium dioxide catalyst plate 123c: second titanium dioxide catalyst plate
124: installation unit 130: oxidation mixing tank
131: second casing 132: second windmill
140: complex reduction aid 141: third casing
142: second desistor 143: second UV lamp module
143a: second UV lamp 143b: first manganese dioxide catalyst plate
143c: second manganese dioxide catalyst plate 144: mounting portion
150: reduction mixing tank 151: fourth casing
152: third windmill 160: air blowing tank
161: fifth casing 162: blower

Claims (5)

In the deodorizing device,
The complex oxidation tank is installed in the movement path of the malodorous gas to remove the malodor by the non-contact oxidation,
The complex oxidation tank,
A first casing for odor gas to pass through;
A first demister installed at the inner front end of the first casing to remove foreign substances from the odor gas passing therethrough and to disperse the odor gas; And
A plurality of first UV lamp modules installed in the first casing so as to be arranged in a direction crossing the movement direction of the malodorous gas at the rear side of the first demister,
Each of the first UV lamp module,
A plurality of first UV lamps each installed to cross the moving direction of the malodorous gas and arranged at intervals along the moving direction of the malodorous gas;
A plurality of first titanium dioxide catalyst plates disposed on the front side of the first UV lamp so as to be parallel to the first UV lamp, and coated with titanium dioxide as a catalyst; And
Each of the rear side of the first UV lamp is installed so as to be stacked at intervals along the direction crossing the direction of movement of the odor gas, and comprises a plurality of second titanium dioxide catalyst plate coated with titanium dioxide as a catalyst,
Non-contact vortex type, characterized in that the foreign matter is filtered from the odor gas by the first demister, and the oxidation and deodorization by the first and second titanium dioxide catalyst plates installed around the first UV lamp and the surroundings. Photocomposite catalytic oxidation deodorizer. According to claim 1, further comprising a flush filter tank installed in front of the first casing,
The flush filter tank,
An inlet for introducing malodorous gas into one side, an outlet for discharging malodorous gas passing through the inside to the first casing side, and a washing tank filled with washing water in a lower portion thereof;
A first windmill installed to rotate by a non-powered by odorous gas passing through the water surface of the washing water in the tank or by a power of a motor;
In order to guide the odor gas flowing through the inlet to move to the first windmill side and guide the odor gas passing through the first windmill to move in a zigzag and discharged to the outlet side, it is arranged to be arranged inside the tank A plurality of guide plates;
A tank for connecting the washing water from the water tank to measure the water level in the water tank by a gauge, and a supply line for supplying the water to water to supply the water to the water tank; And
Non-contact vortex type photo-composite catalytic oxidation deodorizing device is connected to the lower portion of the water tank and comprises a discharge line which is opened and closed by a valve. The second windmill according to claim 1 or 2, wherein a plurality of second windmills are installed so as to rotate by a non-powered by odor gas or a power by a motor passing inside the second casing provided to extend to the rear side of the first casing. Non-contact vortex type photo-composite catalytic oxidation deodorizing apparatus further comprises an oxidation mixing tank installed. The method of claim 3, further comprising a complex reduction tank is installed to perform a reduction action for the malodor gas discharged from the second casing,
The complex reduction aid,
A third casing connected to the second casing to allow odor gas to pass therethrough;
A second demister installed at an inner front end of the third casing to remove foreign substances from the odor gas passing therethrough and to disperse the odor gas; And
And a plurality of second UV lamp modules installed in the third casing so as to be arranged in a direction crossing the moving direction of the malodorous gas at the rear side of the second demister,
Each of the second UV lamp module,
A plurality of second UV lamps each installed to cross the moving direction of the malodorous gas and arranged at intervals along the moving direction of the malodorous gas;
A plurality of first manganese dioxide catalyst plates each side of the second UV lamp installed side by side with the second UV lamp and coated with manganese dioxide as a catalyst; And
Non-contact vortex type, characterized in that each of the rear side of the second UV lamp is installed so as to be stacked at intervals along the direction crossing the movement direction of the malodorous gas, and a plurality of second manganese dioxide catalyst plate coated with manganese dioxide as a catalyst Photocomposite catalytic oxidation deodorizer. 5. The reduction apparatus according to claim 4, wherein a plurality of third windmills installed to rotate by a non-powered by odor gas or a power by a motor passing inside the fourth casing provided to extend on the rear side of the third casing are installed. Mixing bath; And
And a blower in which a blower is provided to blow air to the outside of the fourth casing, which is deodorized and stabilized from the fourth casing, inside the fifth casing connected to the rear side of the reduction mixing tank. Non-contact vortex type photo-composite catalytic oxidation deodorizer.

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