KR100984387B1 - Compact typed apparatus capable of removing malodor gas of animal-excretion - Google Patents

Abstract

PURPOSE: A compact device for removing bad smell gas of livestock excretions is provided to neutralize bad smell gas with a neutralizing agent of a neutralizing tank. CONSTITUTION: A compact device for removing bad smell gas of livestock excretions includes a housing, a silo(110), a neutralizing tank(120), a turbo fan(130), a scriber(140), a neutralizing agent supply tank(150), an ultraviolet ray irradiating unit(160), filtering units(170), a sensor, and a controller. The silo is connected to a bad smell gas outlet of an excretion treatment unit or excretion storage and separates the particle of the bad smell gas. The neutralizing tank neutralizes the bad smell gas from the silo with a neutralizing agent. The turbo fan is formed between the silo and the neutralizing tank. The scriber previously neutralizes the bad smell gas inputted to the neutralizing tank by bypassing the neutralizing agent. The ultraviolet ray irradiating unit dissolves the bad smell gas by irradiating the ultraviolet ray. The filtering unit discharges only neutralized gas. The sensor senses the acidity of the neutralizing agent.

Description

Compact typed apparatus capable of removing malodor gas of animal-excretion}

The present invention relates to a device for removing livestock manure odor gas, and more particularly, components for removing malodorous gas which can be discharged to the outside by purifying malodorous gas such as ammonia and hydrogen sulfide generated from livestock waste such as livestock manure. The present invention relates to a compact livestock manure odor gas removal device that can be compactly configured.

According to the Ministry of Environment (Ministry of Environment), which has been in force since February 2005, from January 1, 2006, regulations on the emission of designated odorous gases such as ammonia and hydrogen sulfide have been enforced for livestock facilities with a pig farming facility area of 50 m2 or more. . This is a law that requires the concentration of designated malodorous gas measured at the boundary of the site where livestock facilities are located to satisfy each emission limit. This is to solve the problem caused by malodorous gas in the area adjacent to pigs. Although the current odor prevention law is not applied as strictly as the wastewater management law at the beginning of implementation, there is a situation in which pig farming farms must strictly observe the odor prevention law within the next few years. Therefore, in order to satisfy the odor prevention law, there is a need for a system for removing the odor gas present in the air discharged from the pig husbandry facility.

In addition, in order to secure the competitiveness of livestock farmers as well as the odor prevention law, competitive pig livestock facilities should be equipped to produce better quality pigs. A odor gas removal system is essential to keep it clean and to eliminate related diseases.

However, as a conventional apparatus and method for removing malodorous gas, a deodorizing tower is applied to a gas containing malodors by spraying water with a plurality of nozzles to remove the malodor, and a washing apparatus and a washing method, or activated carbon in the deodorizing tower, Activated carbon adsorption system and activated carbon adsorption method for adsorbing and removing malodorous substances by placing adsorbents such as silica gel and zeolite, or microbial decomposition apparatus for decomposing and removing malodorous substances by placing specific microorganisms instead of adsorbent in deodorizing tower Method and the like.

However, the conventional odor gas removal apparatus and method as described above, all are applied to the deodorization tower, the deodorization tower as described above, the installation structure is relatively complicated and expensive to install, while difficult to maintain, in particular, In the case of activated carbon adsorption method and microbial decomposition method, it is necessary to replace the activated carbon or microorganism periodically, which makes management difficult and uneconomical.

Therefore, an object of the present invention is to inhale the odor gas generated in the manure treatment plant or the manure storage in a small silo to separate the particles in the odor gas and then neutralized through the neutralizing liquid in the neutralization tank through a plurality of filtration means It is to provide a compact livestock manure odor gas removal device that can be compactly configured to reduce the installation area and to reduce the installation cost by adsorbing the odorous substances in the discharged to the outside.

In addition, another object of the present invention is to configure a scrubber to bypass the neutralizer from the neutralization tank prior to the introduction of the odor gas into the neutralization tank so that the odor gas is preliminarily neutralized before the neutralization tank is introduced to improve the neutralization efficiency of the odor gas. It is to provide a compact livestock manure odor gas removal device that can be improved.

In addition, another object of the present invention is to allow the neutralizing agent and odor gas to flow into the neutralization tank with a high speed through a plurality of acid pipes filled with a plurality of glass beads during the preliminary neutralization of the odor gas using the scrubber It is to provide a compact livestock manure odor gas removal device that can be a large amount of odor gas neutralized by the neutralizer of the neutralization tank.

In addition, another object of the present invention is a compact type that can be easily removed to remove the odor gas without the installation of additional auxiliary facilities through the connection operation connecting the inlet extending from the silo to the existing manure treatment plant or manure storage It is to provide a livestock manure odor gas removal device.

Meanwhile, the object of the present invention is not limited to the above-mentioned objects, and other objects not mentioned can be clearly understood by those skilled in the art from the following description.

To this end, according to the present invention, a housing having a caster; A silo provided inside the housing and connected to an odor gas outlet of a manure treatment plant or a manure storage through an inlet to separate particles of the odor gas; A neutralization tank provided at one side of the silo to neutralize the malodorous gas introduced from the silo through a neutralizing agent; A turbo fan provided between the silo and the neutralization tank to allow odor gas to flow into the neutralization tank via the silo; A scrubber provided between the neutralization tank and the turbo fan to bypass the neutralizer from the neutralization tank to pre-neutralize the odor gas introduced into the neutralization tank and to allow the odor gas and the neutralizing agent to flow into the neutralization tank at a high speed; A neutralizer supply tank provided at one side of the neutralization tank to supply a neutralizer; Ultraviolet irradiation means which is provided on an upper side of the neutralization tank and irradiates ultraviolet rays inside the neutralization tank to decompose odor gas; A plurality of filtration means provided on one side of the neutralization tank to absorb odorous substances of odorous gas not neutralized by a neutralizing agent and to discharge only neutralized gas to the outside; Sensor means provided in the silo, the neutralization tank and the filtration means to detect the concentration of the malodorous gas of each component or provided in the neutralization tank to detect the acidity of the neutralizing agent; And a control means for controlling the operation of the components based on the odor gas concentration and acidity detected by the sensor means.

The neutralization tank may include a tank in which a neutralizing agent is stored and provides a space for neutralizing the malodorous gas through the generation of bubbles due to the contact of the malodorous gas and the neutralizing agent when the malodorous gas is introduced; A pump for supplying a neutralizer to the tank from the neutralizer supply tank; And a heater for maintaining a constant temperature inside the tank.

In addition, it is preferable that the said neutralizing agent is a sulfuric acid (H2SO4) phosphoric acid (P2O5) solution of pH 3 (+/- 1).

The scrubber may further include: a first diffuser located on the turbofan side; A second acid engine connected to the first acid engine and positioned inside the tank of the neutralization tank; A first bypass nozzle filtered by a filter provided in a bypass pipe connected to a tank lower end of the neutralization tank and spraying a neutralizing agent bypassed by a pump to the first acid engine; A second bypass nozzle which injects the neutralizing agent bypassed by the pump to the upper end of the tank to neutralize the odor gas remaining in the upper end without being neutralized in the tank; And a plurality of glass beads which are filled in the first acid engine and the second acid engine to allow the bypassed neutralizing agent and odor gas to flow into the tank at a high speed.

Therefore, according to the present invention, the malodorous gas generated in the manure treatment plant or the manure storage is sucked into a small silo to separate the particles in the malodorous gas, and then neutralized through the neutralizing liquid in the neutralization tank. The components that adsorb the odorous substances in and discharge them to the outside are compactly configured to reduce the installation area and reduce the installation cost.

In addition, the neutralization tank is bypassed from the neutralization tank before the odor gas is introduced into the neutralization tank so as to configure a scrubber to preliminarily neutralize the odor gas before the neutralization tank is introduced, thereby improving the neutralization efficiency of the odor gas.

In addition, during the neutralization of the odor gas using the scrubber, the neutralizer and the odor gas are introduced into the neutralization tank at a high speed through the plurality of acid pipes filled with a plurality of glass beads so that a large amount of the odor gas is neutralized. It can be neutralized by the neutralizer of the tank.

In addition, through the operation of connecting the inlet extending from the silo to the existing manure treatment plant or manure storage can be more easily removed odor gas without additional installation facilities.

On the other hand, the effects of the present invention are not limited to the effects mentioned above, and other effects not mentioned can be clearly understood by those skilled in the art from the description of the claims.

1 is a block diagram showing a compact livestock manure malodor gas removal apparatus according to a preferred embodiment of the present invention;
Figure 2 is a front view showing a compact livestock manure malodor gas removal device of Figure 1;
Figure 3 is a plan view showing a compact livestock manure malodor gas removal device of Figure 1; And
4 is a view showing a scrubber in the compact livestock manure malodor gas removal apparatus of FIG.

Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.

1 is a block diagram showing a compact livestock manure malodor gas removal apparatus according to a preferred embodiment of the present invention, Figure 2 is a front view showing a compact livestock manure malodor gas removal device of Figure 1, Figure 3 is 4 is a plan view illustrating a compact livestock manure malodor gas removal device, and FIG. 4 is a view illustrating a scrubber in the compact livestock manure malodor gas removal device of FIG. 1.

As shown in Figures 1 to 4, the compact livestock manure odor gas removal device according to a preferred embodiment of the present invention, the housing having a caster to facilitate access to a manure treatment plant or a manure storage provided in a livestock facility (H) ) Is provided in the housing (H) and is provided on one side of the silo (110) and the silo (110) for separating the particles of odor gas flowing from the manure treatment plant or the manure storage, and flows in from the silo (110). It is provided between the neutralization tank 120, the silo 110 and the neutralization tank 120 to neutralize the odor gas to be neutralized through the silo 110 to enter the neutralization tank 120 through the silo 110. It is provided between the turbo fan 130, the neutralization tank 120 and the turbo fan 130 to bypass the neutralizer from the neutralization tank 120 to neutralize the odor gas flowing into the neutralization tank 120 Clover 140, provided on one side of the neutralization tank 120, neutralizing agent supply tank 150 for supplying a neutralizing agent, is provided on the upper side of the neutralizing tank 120 irradiates ultraviolet rays inside the neutralizing tank 120 UV irradiation means 160 for decomposing malodorous gas, and the neutralization tank 120 is provided on one side to adsorb the malodorous substance of the malodorous gas which is not neutralized by the neutralizing agent, and then discharges only the neutralized gas to the outside. Two filtering means 170, the silo 110, the neutralization tank 120 and the filtering means 170 to detect the concentration of odor gas of each component or provided in the neutralization tank 120, the acidity of the neutralizing agent It includes a sensor means for detecting the 180 and the control means 190 for controlling the operation of the components based on the odor gas concentration and acidity detected by the sensor means 180.

The housing (H) has a hexahedron-shaped body having a receiving space for accommodating the components, and has a caster at a lower end thereof to move to facilitate access to a manure processing plant or a manure storage provided in a livestock facility. The compact livestock manure odor gas removal device having the configuration as described above can be more easily applied, and through this, it is possible to solve the problems of space limitation and high cost according to the installation of various facilities.

The silo 110 is provided in the housing (H) to separate the particles of odor gas flowing from the manure treatment plant or the manure storage, etc., the inlet connected to the odor gas outlet of the manure treatment plant or manure storage. It is possible to separate the malodorous gas and the particles by allowing the particles in the malodorous gas to sink to the lower portion of the space through a cylindrical or conical space having a capacity of about 20 L, including (111).

Here, it is preferable that a plurality of pre-filters or the like are further provided in the inner space of the silo 110 as a separating means for forcibly separating particles of the malodorous gas introduced through the inlet 111, in the lower portion of the inner space. Submerged particles or dirt can be vented to the outside through a vent or back to the manure treatment plant or manure storage.

Therefore, according to the silo 110, the inlet 111 is connected to the odor gas outlet of the manure treatment plant or the manure storage using a pipe such as bellows, the simple connection operation only without the additional installation facilities of the compact type The livestock manure odor gas removal device can be easily removed odor gas.

The neutralization tank 120 is provided on one side of the silo 110 to neutralize the malodorous gas flowing from the silo 110 through the neutralizer, and the neutralizing agent is stored and the malodorous gas is contacted with the neutralizing agent when the malodorous gas is introduced. Tank 121 for providing a space in which the odor gas neutralization through bubble generation according to the pump, pump 122 for supplying the neutralizing agent to the tank 121 from the neutralizing agent supply tank 150 described later and the tank 121 It includes a heater (not shown) to maintain the internal temperature constant so that the neutralizing action of the neutralizing agent is made efficiently.

Here, the neutralizing agent is widely used in the chemical industry as a basic raw material that decomposes organic substances to a colorless, odorless, strong acid and makes various chemicals. In particular, the neutralizing agent generates ammonium sulfate ((NH 4) 2 SO 4) when reacted with ammonia in odor gas. Therefore, it is preferable to produce sulfuric acid (H2SO4) or ammonium phosphate (NH4H2PO4) having a high deodorizing effect on ammonia, and a solution of phosphoric acid (P2O5) having a high deodorizing effect on ammonia, and the concentration is about ph 3 (± 1). good. On the other hand, ammonium sulfate and ammonium phosphate generated by neutralization by the neutralizing agent may be used as a liquid ratio capable of supplying nitrogen or phosphorus in the soil.

In addition, the neutralizing agent may be sodium hydroxide (NaOH) or sodium hypochlorite (NaClO) which is an alkaline solution, and the concentration may be adjusted to a concentration of pH 7-11 to remove hydrogen sulfide (H 2 S) or mercaptans. At this time, in the case of the sodium hypochlorite, the effective chlorine concentration is suitably 800ppm-900ppm.

In addition, the tank 121 may be provided with a plurality of, the vent having a neutralizing agent is stored or supplied to about 3/4 of the volume having a capacity of about 700 L and the neutralizing agent is completed at the lower end is discharged to the outside It is desirable to have a see-through window that is provided and can visually identify the interior.

Here, the tank 121, when used in a biological treatment method as well as a chemical reaction tank is used as a bioreactor to remove ammonia gas, the microorganisms that can be used at this time, Paracossus denitrificans, Pseudomonas spp. And the like can be used. On the other hand, the culture solution is completed by the microorganism in the biological treatment method, can be used as a liquid ratio that can supply nitrogen or phosphorus to the soil of environmentally friendly agriculture.

In addition, the heater (not shown), it is preferable to maximize the neutralization conditions of the neutralizer by maintaining the tank 121 at 25 ℃-30 ℃ temperature at all times.

The turbo fan 130 is provided between the silo 110 and the neutralization tank 120 to allow odor gas to flow into the neutralization tank 120 via the silo 110. It is good to have durability against acidic components.

The scrubber 140 is provided between the neutralization tank 120 and the turbo fan 130 to bypass the neutralizing agent from the neutralization tank 120 to pre-neutralize the odor gas flowing into the neutralization tank 120. The first mountain engine 141 located on the turbofan 130 side and the second mountain engine connected to the first mountain engine 141 and positioned inside the tank 121 of the neutralization tank 120 ( 142, the first acid pipe is filtered by the filter 144 provided in the bypass pipe 143 connected to the lower end of the tank 121 of the neutralization tank 120 and bypassed by the pump 145. A plurality of first bypass nozzles 146 sprayed to 141 and a neutralizer bypassed by the pump 144 are sprayed on the upper end of the tank 121 so that the upper end is not neutralized in the tank 121. Filling the inside of the second bypass nozzle 147 and the first acid engine 141 and the second acid engine 142 to neutralize the odor gas remaining in the gas. Is comprises a plurality of glass beads 148 that allows flow into the tank 121, while the bypass is the neutralizing agent and the odor gas of a high speed.

Here, the first acid pipe 141 and the second acid pipe 142 are perforated with dozens of about 2 mm size holes at the end where the malodorous gas and the neutralizing agent are discharged, respectively, so that the malodorous gas and the neutralizing agent are more easily formed. It can be diffused.

In addition, the second diffuser 142 has a double pipe structure in which a second diffuser pipe 142b having a smaller diameter is embedded in the hollow first diffuser pipe 142a, and the first diffuser pipe ( The perforation range of the first through hole 142c perforated at the lower end of 142a is longer than the perforation range of the second through hole 142d perforated at the lower end of the second diffuser pipe 142b, and the neutralizing agent is introduced at a high speed. The odor gas is introduced into the tank 121 through the second through hole 142d, and the neutralizing agent and the odor gas introduced at a slower rate are introduced into the tank 121 through the first through hole 142c. Can be neutralized.

In addition, the plurality of first bypass nozzles 146 may include the first nozzle 146a and the first nozzle 146 in the portions where the glass beads 148 are not filled and the portions filled with the first acid engine 141. Neutralizing efficiency may be improved by spraying the neutralizing agent bypassed through the two nozzles 146b.

In addition, the second bypass nozzle 147 injects the neutralizing agent bypassed to the upper end of the tank 121 to allow the tank 121 to pass through the first acid engine 121 and the second acid engine 122. Odor gas introduced into the floating through the bubbles can be prevented from remaining in the upper end of the tank 121, that is, the space not filled with the neutralizing agent.

In addition, the plurality of glass beads 148, by reducing the density of the neutralizing agent and odor gas bypassed to the first acid engine 141 to move the second acid engine 142 at high speed, Even if the second acid engine 142 is provided inside the tank 121 and has a high pressure by the neutralizing agent, the bypassed neutralizing agent and the odor gas are introduced into the tank 121 through the second acid engine 142. It can prevent the inflow.

Therefore, according to the scrubber 140, it is possible to bypass the neutralizing agent from the neutralization tank 120 to pre-neutralize the odor gas flowing into the neutralization tank 120, and also to bypass the pre-neutralized odor gas and bypass. The neutralizing agent to be introduced more easily into the tank 121 through the first and second acid pipes 141 and 142, and the odor gas suspended in the tank 121 without being neutralized by the neutralizing agent is passed through the second bypass nozzle 147. By neutralizing through), the neutralization efficiency of the malodorous gas can be improved.

The neutralizing agent supply tank 150 is provided on one side of the neutralizing tank 120 to supply the neutralizing agent to the tank 121, the tank 151 in which the neutralizing agent is stored, and the neutralizing agent in the tank 151. It includes a drive motor 153 for driving the propeller 152 to be stirred, the neutralizing agent is supplied to the neutralization tank 120 by driving the pump 122 of the neutralization tank 120.

The ultraviolet irradiation means 160 is provided on the upper side of the neutralization tank 120 to irradiate ultraviolet rays inside the neutralization tank 120 to decompose odor gas, and is provided on the upper side of the tank 121 to provide ultraviolet rays. Ultraviolet irradiation lamp 161 for irradiating and a driving means (not shown) are included.

Here, the ultraviolet irradiation lamp 161 decomposes the odor gas using a wavelength of about 253 nm.

Therefore, according to the ultraviolet irradiation means 160, by neutralizing the odor gas not neutralized in the neutralization tank 120, the neutralization efficiency can be further improved.

The plurality of filtering means 170 is provided on one side of the neutralization tank 120 to adsorb odorous substances of the odorous gas that is not neutralized by the neutralizing agent so that only the neutralized gas is discharged to the outside. And a complex call filter 171 for adsorbing odor gas which is not neutralized even through the tank 120 and the ultraviolet irradiation means 160.

Here, the plurality of filtering means 170 is connected to the upper end of the neutralization tank 120 through a line open and close by the inlet damper 172, and only the gas of the neutralized malodorous gas is opened and closed by the discharge damper 173. It can be discharged to the outside through a possible line, it is possible to determine the replacement time of the complex call filter 171 using a differential pressure gauge (not shown).

Therefore, according to the plurality of filtering means 170, by neutralizing the odorous substances of the odor gas not neutralized in the neutralization tank 120, the neutralization efficiency of the odor gas can be further improved.

The sensor means 180 is provided in the silo 110, the neutralization tank 120, and the filtering means 170, the gas sensor 181 and the neutralization tank 120 for detecting the concentration of odor gas of each component And a ph sensor 182 which detects the acidity of the neutralizing agent, and provides the control means 190 with the concentration of the malodorous gas detected by the sensors and the acidity of the neutralizing agent.

The control means 190 receives the concentration of the odor gas and the acidity information of the neutralizing agent from the sensor means 180, for example, the neutralizing agent stored in the neutralization tank 120 maintains the acidity pH 3 The neutralizing agent may be supplied from the supply tank 150 at any time, or the neutralizing tank may be compared with the odor gas concentration of the silo 110 and the odor gas concentration of the neutralization tank 120 or the odor gas discharged from the filtering means 170. The operating time of the 120 and the scrubber 140 may be controlled to improve the neutralization efficiency of the malodorous gas.

Hereinafter, the operation of the compact livestock manure malodor gas removal apparatus according to a preferred embodiment of the present invention will be described in detail.

First, the inlet 111 of the silo 110 provided in the housing H is connected to the odor gas outlet of the manure treatment plant or the manure storage by a pipe such as a bellows, according to the control of the control means 190. 130 is operated to introduce the odor gas into the silo 110 to separate the odor gas and particles.

Thereafter, only the malodorous gas from which the particles are separated by the turbofan 130 is introduced into the tank 121 of the neutralization tank 120 through the scrubber 140 and neutralized.

Thereafter, or simultaneously, the scrubber 140 bypasses the neutralizer from the neutralization tank 120 to the first acid engine 141 by using the first bypass nozzle 146, thereby neutralizing the tank 120. And preliminarily neutralizes the malodorous gas before entering, and allows the preliminary neutralized malodorous gas and the bypassed neutralizing agent to be easily introduced into the tank 121 through the second acid pipe 142, and the tank ( After being introduced into 121, the odorous gas suspended in the tank 121 without being neutralized by the neutralizing agent is neutralized by using the neutralizing agent bypassed through the second bypass nozzle 147.

Thereafter, or at the same time, the odor gas which is suspended in the upper portion of the tank 121 by the ultraviolet irradiation means 160 provided in the upper portion of the neutralization tank 120 is decomposed.

Subsequently, after the odorous substances of the odor gas which are not neutralized are adsorbed in the neutralization tank 120 by the plurality of filtering means 170, only the neutralized odor gas is discharged to the outside.

On the other hand, the control means 190, the neutralizer of the neutralization tank 120 receives the concentration information of the odor gas and the acidity of the neutralizing agent from the sensor means 180 during the operation of the components for the neutralization of the odor gas The neutralizing agent is supplied from the neutralizing agent supply tank 150 to maintain the acidity ph 3 degree from time to time, or the odor gas concentration of the silo 110 and the odor gas concentration of the neutralizing tank 120 or discharged from the filtering means 170. The operation time of the neutralization tank 120 and the scrubber 140 is controlled by comparing the odor gas concentration.

Therefore, as described above, the odor gas generated in the manure treatment plant or the manure storage inhaled into the small silo 110 to separate the particles in the odor gas and then neutralized in the neutralization tank 120 through the neutralization liquid The constituent parts for adsorbing the malodorous substances in the malodorous gas through the filtration means 170 and then discharged to the outside are compactly configured to reduce the installation area and reduce the installation cost.

In addition, a neutralizer is bypassed from the neutralization tank 120 prior to the inflow of malodorous gas into the neutralization tank 120, and the scrubber 140 is configured to preliminarily neutralize the malodorous gas before the neutralization tank 120 is introduced. The neutralization efficiency of odor gas can be improved.

In addition, during the neutralization of the malodorous gas using the scrubber 140, the neutralizing tank 120 while the neutralizing agent and the malodorous gas have a high speed through the plurality of acid pipes 141 and 142 filled with a plurality of glass beads 148. ) To be introduced into a large amount of odor gas can be neutralized by the neutralizing agent of the neutralization tank (120).

In addition, through the connecting operation connecting the inlet 111 extending from the silo 110 to the existing manure treatment plant or the manure storage more easily remove the odor gas, that is, ammonia or hydrogen hydride without the installation of additional facilities can do.

Although the present invention has been described with reference to the specific embodiments, various modifications may be made without departing from the scope of the present invention. Therefore, the scope of the invention should not be defined by the described embodiments, but should be defined by the claims and their equivalents.

Claims (5)

A housing H having a caster;
A silo (110) provided inside the housing (H) and connected to the odor gas outlet of the manure treatment plant or the manure storage through an inlet (111) to separate the particles of the odor gas;
A neutralization tank 120 provided at one side of the silo 110 to neutralize the malodorous gas introduced from the silo 110 through a neutralizing agent;
A turbo fan 130 provided between the silo 110 and the neutralization tank 120 to allow odor gas to flow into the neutralization tank 120 via the silo 110;
It is provided between the neutralization tank 120 and the turbo fan 130 to bypass the neutralizing agent from the neutralization tank 120 to neutralize the odor gas flowing into the neutralization tank 120 and at the same time to neutralize the odor gas and the neutralizing agent. Scrubber 140 to be introduced to the tank 120 with a high speed;
A neutralizer supply tank 150 provided at one side of the neutralization tank 120 to supply a neutralizer;
Ultraviolet irradiation means (160) provided at an upper portion of the neutralization tank (120) to irradiate ultraviolet rays inside the neutralization tank (120) to decompose odor gas;
A plurality of filtration means (170) provided at one side of the neutralization tank (120) to adsorb the malodorous substance of the malodorous gas not neutralized by the neutralizing agent and to discharge only the neutralized gas to the outside;
The silo 110, the neutralization tank 120 and the filtering means 170 is provided to detect the concentration of the odor gas of the silo 110, the neutralization tank 120 and the filtering means 170, or the neutralization tank 120 Sensor means for detecting the acidity of the neutralizing agent (180); And
Compact livestock manure malodor gas removal apparatus comprising a control means for controlling the operation of the components based on the odor gas concentration and acidity detected by the sensor means (180). According to claim 1, The neutralization tank 120,
A tank 121 for storing the neutralizing agent and providing a space in which the odor gas is neutralized through the generation of bubbles due to the contact of the odor gas and the neutralizing agent upon inflow of the odor gas;
A pump 122 for supplying the neutralizer from the neutralizer supply tank 150 to the tank 121; And
Compact livestock manure malodor gas removal device comprising a heater (not shown) for maintaining a constant temperature inside the tank (121). The method of claim 1, wherein the neutralizing agent,
Compact livestock manure odor gas removal device characterized in that the pH 3 (± 1) sulfuric acid (H2SO4) or phosphoric acid (P2O5) solution. The method of claim 2, wherein the scrubber 140,
A first acid engine 141 located on the turbo fan 130 side;
A second acid pipe 142 connected to the first acid pipe 141 and positioned inside the tank 121 of the neutralization tank 120;
The first acid pipe 141 is filtered by the filter 144 provided in the bypass pipe 143 connected to the lower end of the tank 121 of the neutralization tank 120 and bypassed by the pump 145. A first bypass nozzle 146 spraying the gas;
The second bypass nozzle 147 which injects the neutralizing agent bypassed by the pump 144 to the upper end of the tank 121 so that the odor gas remaining in the upper end is neutralized without being neutralized in the tank 121. ; And
The plurality of glass beads 148 are filled in the first acid pipe 141 and the second acid pipe 142 to allow the bypassed neutralizing agent and odor gas to flow into the tank 121 at a high speed. Compact livestock manure odor gas removal device comprising a. The method of claim 4, wherein the second acid engine 142,
Compact livestock manure odor gas removal device characterized in that it has a double pipe structure in which the second diffuser pipe (142b) having a smaller diameter in the hollow of the cylindrical first diffuser pipe (142a).

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