KR102619391B1 - Organic waste extinction process system - Google Patents

Abstract

The purpose of the present invention is to provide an organic waste destruction treatment device, which includes a base frame (120); a processor cylinder 130 rotatably supported on the base frame 120; A plow 150 provided inside the processor cylinder 130; Ozone deodorizer (220); It is characterized in that it includes a decomposed gas air discharge pipe 223 provided in the ozone deodorizer 220 and discharging wet air mixed with gas decomposed from organic waste in the reaction tank and moisture air.

Description

Organic waste extinction process system}

The present invention relates to an organic waste destruction treatment device, and more specifically, to maintain the optimal temperature of organic waste through the concept of revolution of the processor cylinder (destruction tank) itself and rotation of the plow (arm paddle), and also to dispose of the organic waste by maintaining the optimal temperature of the air. It can optimally match the processing conditions and environment of organic waste, such as being supplied at a sufficient capacity ratio, and destroys organic waste with a new structure that removes and drains bacteria and odor components from the humid air generated during organic waste treatment with an ozone device. It's about processing equipment.

In general, in the case of livestock farms, a large amount of livestock waste, such as livestock urine and excrement, is generated because a large amount of livestock is raised in a dense area. This livestock waste must be disposed of by an appropriate method.

In the case of fattening pigs in pig breeding facilities at livestock farms, about 5.5 kg of organic waste is emitted from each pig per day. The composition of the waste is 5.5 kg, about 4.6 kg of urine (urine), and about 900 g of excrement (poop), with liquid accounting for 84% and solid matter accounting for 16% .

As large amounts of livestock waste, such as livestock urine and manure, are generated, most livestock farms are facing great difficulties in waste disposal. Livestock farms themselves are experiencing many difficulties in processing organic livestock waste due to excessive energy consumption and high overall costs. In order to reduce treatment costs, some farms often separate food wastewater and solids using a decanter and entrust the treatment.

As a way to solve this problem, the livestock manure is pulverized, subjected to a heat treatment process, and then mixed with sawdust to make it recyclable as compost or feed. This allows the protein and nitrogen in the manure to come into contact with the carbon contained in the sawdust. There have been attempts to treat organic livestock waste by improving it to facilitate fermentation.

However, there is a problem that the quality of organic waste as compost or feed is significantly poor when processed. In other words, there is a problem that the treatment efficiency of organic waste is unsatisfactory because the organic waste and sawdust are not evenly mixed but rather clump together and the fermentation property is reduced.

In addition, the odor component contained in approximately 85% or more of the moisture (desorbed liquid, food waste water, sewage water, urine, etc.) in organic waste is due to the influence of microbial growth conditions and environmental heat in the reaction tank of the treatment equipment, and the moisture turns into vapor as soon as the waste is input. As the oxidation progresses, the odorous components contained in the moisture are often discharged to the outside along with the vaporized moisture without a chance to encounter microorganisms.

Existing organic waste destruction treatment equipment does not decompose odorous components contained in moisture and is discharged to the outside along with moisture vapor, causing odor.

The humid air emitted when processing organic waste contains gases and moisture containing bad odors, which makes it difficult to maintain a pleasant surrounding environment and causes environmental pollution.

Korean Patent No. 10-0783083 (registered on November 30, 2007) Korean Patent No. 10-1372025 (registered on March 3, 2014) Korean Patent Publication No. 10-2019-0033300 (published on March 29, 2019) Korean Patent No. 10-0433676 (registered on May 19, 2004) Korea Public Utility Model No. 20-1998-0047217 (published on September 25, 1998) Korean Patent No. 10-2080773 (registered on February 18, 2020)

The purpose of the present invention is to maintain the optimal temperature of organic waste through the concept of revolution of the processor cylinder (destruction tank) itself and rotation of the plow (arm paddle) and to maintain organic waste such that air is supplied at a rate sufficient for the treatment of organic waste. It is implemented to optimally match the waste treatment conditions and environment, and by installing a device that removes and drains bacteria and odor components mixed in the liquefied water while passing through the condenser with an ozone device, bacteria are removed from the humid air generated when processing organic waste. and odor components are removed and drained with an ozone device, and gas components other than liquefied water are removed with an additionally installed deodorizer (Blinn deodorizer) to maintain a pleasant surrounding environment. This is what I want to do.

According to the present invention to solve the above problems, a base frame 120; a processor cylinder 130 rotatably supported on the base frame 120; An organic waste destruction treatment device is provided, comprising a plow 150 provided inside the processor cylinder 130.

A cylindrical inspection chamber 132 is provided in the inner central portion of the processor cylinder 130, and the processor cylinder 130 is configured to rotate with respect to the base frame 120 by an orbital drive unit. The driving unit includes a revolving ring gear 147 rotatably coupled to the base frame 120, disposed in a horizontal direction, and having an upper surface connected to the processor cylinder 130 via a connecting rod; An idle drive motor 148 mounted on the base frame 120; An idle drive gear 149 is coaxially coupled to the motor shaft of the idle drive gear 149 and meshed with the idle ring gear 147, and the plow 150 includes a shaft disposed in a horizontal direction ( A plurality of stirring pads 156 are provided on the outer peripheral surface of the processor 152 so that the shaft 152 is rotatably coupled to the inspection chamber 132 located in the central portion of the processor cylinder 130, and at the same time, the processor is rotated by a rotation drive unit. It is configured to rotate based on the inspection chamber 132 of the cylinder 130, and the rotation drive unit includes a rotation drive motor 162 mounted on the base frame 120 and disposed at the lower part of the processor cylinder 130. ); A drive pulley 164 coaxially coupled to the motor shaft of the rotation drive motor 162; a driven pulley 166 coaxially coupled to the shaft 152 of the plow 150; It is characterized in that it includes a rotating drive belt coupled to the drive pulley 164 and the driven pulley 166.

The inside of the processor cylinder (130) is equipped with a carrier composition adsorbed with complex microorganisms, and the carrier is made of a mixture of 70 parts by weight of rubber tree sawdust and 30 parts by weight of peat moss, and the organic waste is stored in the processor cylinder (130). When put into the processor, the rotation of the processor cylinder 130 and the rotation of the plow 150 are combined with a stirring action to stir the carrier composition adsorbed with complex microorganisms and organic waste without coagulation, so that the organic material becomes a gas and disappears by more than 98%. , the remaining 2% or less is configured to be absorbed by complex microorganisms and become a carrier composition to participate in the extinction activity, and the processor cylinder 130 (cylinder processor cylinder 130) in which extinction occurs performs a deodorization operation in parallel with the role of extinction treatment. It is characterized by being a place to practice.

In addition, the present invention includes an ozone deodorizer (220); An organic waste extinction treatment device comprising a decomposition gas air discharge pipe 223 provided in the ozone deodorizer 220 and discharging wet air mixed with gas decomposed from organic waste in the reaction tank and moisture air. do.

The ozone deodorizer 220 collects water by cooling the humid air containing heat and moisture, and then treats the odor contained in the water with ozone (O3), so that the ozone is converted into odor components. Odor components are removed on the principle of destroying the molecular structure by changing radicals, and when oxygen is discharged within the ozone deodorizer 220, ozone in an unstable state is generated and acts on the pollutants to be removed, destroying them and restoring the original oxygen. It is characterized in that it is configured to remove bad odors and change vaporized gas moisture into liquid moisture to produce second-grade water or higher.

Inside the ozone deodorizer 220, a discharger that causes a discharge action is provided, and the discharger discharges oxygen within the ozone deodorizer 220 so that the pollutants to be removed and the unstable ozone react to remove bad odors. It is composed.

The organic waste destruction treatment device of the present invention maintains the optimal temperature of organic waste based on the concept of revolution of the processor cylinder (destruction tank) itself and rotation of the plow (arm paddle) and supplies air at a rate sufficient for the treatment of organic waste. As can be seen, the processing conditions and environment for organic waste can be optimally adjusted, and excessive energy consumption can be prevented when processing livestock organic waste at the livestock farm itself, resulting in a reduction in overall processing costs. Not only does it help solve situations where processing is difficult, but you can also expect satisfactory quality results when processing organic waste and using it as compost or feed.

In addition, the present invention can be expected to achieve satisfactory treatment efficiency for organic waste by preventing the organic waste and the carrier composition entering the processor cylinder from being evenly mixed and clumping together and increasing fermentation.

The organic waste extinction treatment device of the present invention collects water by cooling humid air containing high heat and a lot of moisture, and then treats odors contained in the water with ozone (O3), so that ozone Odor components are removed by changing the radicals of the odor component and destroying (decomposing) the molecular structure. The principle of deodorizing ozone is that when oxygen is discharged, ozone in an unstable state is created, and the pollutants to be removed are removed. By acting to destroy it and return it to its original oxygen, it changes vaporized gaseous water into liquid water, making it possible to produce water of second or higher grade, and has the effect of allowing it to be used as washing water, agricultural water, etc. In the case of organic food waste, more than 85% is water, so an amount of water equivalent to 85% of the treated material can be produced. In the case of pig manure from livestock farms, if one or two finishing pigs discharge per day feces: 1.6 kg, urine: 2.6 kg, excrement production: 4.2 kg, washing water: 4.4 kg, waste water production: 8.6 kg, 81% of water is discharged. , if 20 tons of raw water generated per day are destroyed as is, 3.8 tons (19%) of solids are expected to remain, or about 380 kg of 1%, and 16.2 tons of recycled water will be produced for water production.

1 is a front perspective view showing the base frame, a part of the processor cylinder, and a plow, which are the main parts of the organic waste destruction treatment device according to the present invention;
Figure 2 is a front cross-sectional view schematically showing the internal structure of the organic waste destruction treatment device according to the present invention;
Figure 3 is a perspective view schematically showing the carrier composition filled in the processor cylinder, which is the main part of the organic waste destruction treatment device according to the present invention;
Figure 4 is a perspective view schematically showing the structure of the lift and the carrier composition filled in the processor cylinder, which is the main part of the organic waste destruction treatment device according to the present invention;
Figure 5 is a perspective view showing the structure of an operation panel unit for controlling the operation of the organic waste destruction treatment device of the present invention;
Figure 6 is a front cross-sectional view showing the internal structure of the organic waste destruction treatment device according to the present invention and the front of the plow and the lift is raised;
Figure 7 is a front cross-sectional view showing the structure of the rotating drive shaft, driving pulley, driven pulley, and rotating drive belt that rotate the plow, which are the main parts of the present invention;
Figure 8 is a plan view of the organic waste destruction treatment device of the present invention;
Figure 9 is a perspective view showing the structure of a grinder installed on the upper processor panel of the processor cylinder of the present invention;
Figure 10 is a plan view showing the grinder and grinding screw shown in Figure 9;
11 is a diagram schematically showing the organic waste treatment process by the organic waste destruction treatment device according to the present invention;
Figure 12 is a perspective view of the upper divided cylinder constituting the processor cylinder, which is the main part of the organic waste destruction treatment device according to another embodiment of the present invention;
Figure 13 is a perspective view of the middle split cylinder constituting the processor cylinder, which is the main part of the organic waste destruction treatment device according to another embodiment of the present invention;
Figure 14 is a perspective view of the lower divided cylinder constituting the processor cylinder, which is the main part of the organic waste destruction treatment device according to another embodiment of the present invention;
Figure 15 is a perspective view of one half-joint support piece, which is another main part of the organic waste destruction treatment device according to another embodiment of the present invention;
Figure 16 is a perspective view of the other half-joint support piece, which is another main part of the organic waste destruction treatment device according to another embodiment of the present invention;
Figure 17 is a perspective view showing a state in which the processor cylinder, which is the main part of the organic waste destruction treatment device according to another embodiment of the present invention, is assembled by combining the upper divided cylinder, the middle divided cylinder, the lower divided cylinder, and the half-joint support piece;
Figure 18 is a longitudinal cross-sectional view of Figure 17;
Figure 19 is an enlarged longitudinal cross-sectional view showing the joint portion of the middle divided cylinder and the semi-finished joint support piece shown in Figure 18;
Figure 20 is a front cross-sectional view showing the structure of the processor cylinder, the auxiliary stirring drive motor, the auxiliary stirring shaft, and the auxiliary mixing pin, which are the main parts of the organic waste destruction treatment device according to another embodiment of the present invention;
Figure 21 is a plan cross-sectional view schematically showing the structure of the processor cylinder, auxiliary stirring shaft, and auxiliary mixing pin shown in Figure 20;
Figure 22 is a diagram schematically showing the exterior and internal structure of the ozone deodorizer, which is the main part of the organic waste destruction treatment device according to the present invention;
Figure 23 is a perspective view of the exterior of the ozone deodorizer shown in Figure 22;
Figure 24 is a diagram showing the internal structure of the ozone deodorizer and the structure of the ozone generator, which are the main parts of the organic waste destruction treatment device according to the present invention;
Figure 25 is a front cross-sectional view showing the internal structure of the treatment tank cylinder connected to the organic waste destruction treatment device according to the present invention and the state filled with the carrier composition;
Figure 26 is a perspective view of the organic waste destruction treatment device and treatment tank cylinder of the present invention;
Figure 27 is a diagram showing the internal structure of the deodorizer, which is another main part of the organic waste destruction treatment device according to the present invention;
Figure 28 is a front view showing a state in which a blowing fan is coupled to an ozone deodorizer, which is the main part of an ozone processor according to another embodiment of the present invention;
Figure 29 is a side cross-sectional view showing the state before connecting the blowing fan to the ozone deodorizer, which is the main part of the ozone processor according to another embodiment of the present invention;
Figure 30 is an enlarged side cross-sectional view showing the structure of the mounting support pin, which is the main part shown in Figure 29;
Figure 31 is an enlarged side cross-sectional view showing the structure of a split coupling support piece provided on the fan frame of the blowing fan shown in Figure 29;
Figure 32 is a side cross-sectional view showing a state in which the blowing fan is coupled to the ozone deodorizer, which is the main part of the ozone processor according to another embodiment of the present invention;
Figure 33 is an enlarged side cross-sectional view showing the part combining the ozone deodorizer and blowing fan shown in Figure 32;
Figure 34 is a perspective view of the coupling elastic ring body, the main part of which is shown in Figure 33;
Figure 35 is a side cross-sectional view schematically showing the air freshener unit installed in the blowing fan shown in Figure 33;
Figure 36 is a perspective view showing a part of the air freshener filter, which is the main part of the air freshener unit shown in Figure 35, disassembled;
Figure 37 is a perspective view of the air freshener unit shown in Figure 35.

Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the attached drawings. The purpose, features, and advantages of the present invention can be more easily understood by referring to the accompanying drawings and the following detailed description. Additionally, in describing the present invention, if it is determined that a detailed description of a related known configuration or function may obscure the gist of the present invention, the detailed description will be omitted.

Additionally, when describing the components of the present invention, terms such as first, second, A, B, (a), and (b) may be used. These terms are only used to distinguish the component from other components, and the nature, sequence, or order of the component is not limited by the term. When a component is described as being "connected," "coupled," or "connected" to another component, that component may be directly connected or connected to that other component, but there is another component between each component. It will be understood that elements may be “connected,” “combined,” or “connected.”

Figure 1 is a front perspective view showing the base frame, a part of the processor cylinder, and a plow, which are the main parts of the organic waste destruction treatment device according to the present invention, and Figure 2 is a front cross-sectional view schematically showing the internal structure of the organic waste destruction treatment device according to the present invention. , Figure 3 is a perspective view schematically showing the carrier composition filled in the processor cylinder, which is the main part of the organic waste extinction treatment device according to the present invention, and Figure 4 is a perspective view schematically showing the carrier composition filled in the processor cylinder, which is the main part of the organic waste destruction treatment device according to the present invention. A perspective view schematically showing the structure of the composition and the lift, Figure 5 is a perspective view showing the structure of an operation panel unit for controlling the operation of the organic waste destruction treatment device of the present invention, and Figure 6 is a perspective view of the organic waste destruction treatment device according to the present invention. Figure 7 is a front cross-sectional view showing the internal structure and the front of the plow and the lifted state; Figure 7 is a front cross-sectional view showing the structures of the main parts of the present invention, the rotating drive shaft, drive pulley, driven pulley, and rotating drive belt, which rotate the plow; A plan view of the organic waste destruction treatment device of the present invention, FIG. 9 is a perspective view showing the structure of a crusher installed on the upper processor panel of the processor cylinder of the present invention, and FIG. 10 is a plan view showing the crusher and crushing screw shown in FIG. 9. 11 is a diagram schematically showing the organic waste treatment process by the organic waste destruction treatment device according to the present invention, and Figure 12 is a diagram showing the upper split cylinder constituting the processor cylinder, which is the main part of the organic waste destruction treatment device according to another embodiment of the present invention. A perspective view, Figure 13 is a perspective view of the middle split cylinder constituting the processor cylinder, which is the main part of the organic waste extinction treatment apparatus according to another embodiment of the present invention, and Figure 14 is a main part of the organic waste extinction treatment apparatus according to another embodiment of the present invention. A perspective view of the lower divided cylinder constituting the processor cylinder, Figure 15 is a perspective view of a half-joint support piece on one side, which is another main part of the organic waste destruction treatment device according to another embodiment of the present invention, and Figure 16 is a perspective view of the organic waste destruction and treatment device according to another embodiment of the present invention. A perspective view of the other half-joint support piece, which is another main part of the waste destruction treatment device, is shown in Figure 17, which shows the processor cylinder, which is the main part of the organic waste destruction treatment device according to another embodiment of the present invention, into an upper divided cylinder, a middle divided cylinder, and a lower divided cylinder. and a perspective view showing the assembled state by combining the half-joint support pieces, Figure 18 is a longitudinal cross-sectional view of Figure 17, and Figure 19 is a longitudinal cross-sectional view showing an enlarged view of the joined portion of the middle split cylinder and the half-joint coupling support pieces shown in Figure 18. 20 is a front cross-sectional view showing the structure of the processor cylinder, the auxiliary stirring drive motor, the auxiliary stirring shaft, and the auxiliary mixing pin, which are the main parts of the organic waste destruction treatment device according to another embodiment of the present invention, and FIG. 21 is the processor shown in FIG. 20. Figure 22 is a cross-sectional view schematically showing the structure of the cylinder, auxiliary stirring shaft and auxiliary mixing pin, Figure 22 is a diagram schematically showing the exterior and internal structure of the ozone deodorizer, which is the main part of the organic waste destruction treatment device according to the present invention, Figure 23 is a diagram schematically showing the structure of the cylinder, auxiliary stirring shaft and auxiliary mixing pin. A perspective view of the exterior of the ozone deodorizer shown in Figure 22, Figure 24 is a diagram showing the internal structure of the ozone deodorizer and the structure of the ozone generator, which are the main parts of the organic waste extinction treatment device according to the present invention, and Figure 25 is a diagram showing the structure of the ozone generator according to the present invention. A front cross-sectional view showing the internal structure of the treatment tank cylinder connected to the waste destruction treatment device and the state in which the carrier composition is filled, Figure 26 is a perspective view of the organic waste destruction treatment device and the treatment tank cylinder according to the present invention, and Figure 27 is a perspective view of the organic waste destruction treatment device and the treatment tank cylinder according to the present invention. Figure 28 is a diagram showing the internal structure of a deodorizer, which is another main part of an organic waste extinction treatment device, and Figure 28 is a front view showing a state in which a blowing fan is coupled to an ozone deodorizer, which is a main part of an ozone processor according to another embodiment of the present invention, Figure 29 is a side cross-sectional view showing the state before combining the blowing fan with the ozone deodorizer, which is the main part of the ozone processor according to another embodiment of the present invention, and FIG. 30 is an enlarged side view showing the structure of the mounting support pin, which is the main part shown in FIG. 29. A cross-sectional view, Figure 31 is an enlarged side cross-sectional view showing the structure of the split coupling support piece provided on the fan frame of the blowing fan shown in Figure 29, and Figure 32 is a blowing to the ozone deodorizer, which is the main part of the ozone processor according to another embodiment of the present invention. A side cross-sectional view showing the state in which the fan is combined, Figure 33 is an enlarged side cross-sectional view showing the part combining the ozone deodorizer and the blowing fan shown in Figure 32, and Figure 34 is a perspective view of the main part of the coupling elastic ring body shown in Figure 33. , Figure 35 is a side cross-sectional view schematically showing the air freshener unit installed in the blowing fan shown in Figure 33, and Figure 36 is a perspective view showing a part of the air freshener filter, which is the main part of the air freshener unit shown in Figure 35, in an exploded state. 37 is a perspective view of the air freshener unit shown in FIG. 35.

Referring to the drawings, the organic waste destruction treatment apparatus of the present invention includes a base frame 120; a processor cylinder 130 rotatably supported on the base frame 120; It includes a plow 150 provided inside the processor cylinder 130.

A cylindrical inspection chamber 132 is provided in the inner central portion of the processor cylinder 130, and the processor cylinder 130 is configured to revolve around the base frame 120 by an orbital drive unit. The upper processor panel of the processor cylinder 130 is provided with a safety guard rail (SG). The decomposed air discharge pipe 223 of the ozone deodorizer 220 is connected to the space filled with the internal tint composition 10 of the processor cylinder 130, and the deodorizer 230 (Blinn) is connected to the ozone deodorizer 220. deodorizer) is configured to be connected.

At this time, the idle drive unit includes an idle ring gear 147, an idle drive motor 148, and an idle drive gear 149.

The idle ring gear 147 is configured in a disc-shaped gear shape. The center of the revolution ring gear 147 is rotatably coupled to the base frame 120. The center of the idle ring gear 147 is rotatably coupled to the center of the base frame 120. The revolution ring gear 147 is arranged in the horizontal direction. The upper surface of the revolving ring gear 147 is connected to the processor cylinder 130 via a connecting rod. The connecting bar may be composed of a connecting bar or the like in a vertical direction.

The idle drive motor 148 is mounted on the base frame 120. The motor shaft of the idle drive motor 148 is arranged in a vertical direction.

The idle drive gear 149 is coaxially coupled to the motor shaft of the idle drive gear 149. The idle drive gear is disposed in the horizontal direction and meshes with the idle ring gear 147. The gear teeth provided on the outer peripheral surface of the idle ring gear 147 are engaged with the gear teeth on the outer peripheral surface of the idle drive gear 149, so that the idle drive gear 149 has a meshed structure with the idle ring gear 147.

As the motor shaft of the idle drive motor 148 rotates, the idle drive gear 149 rotates, and as the idle drive gear 149 rotates, the idle ring gear 147 rotates, so the processor cylinder 130 It revolves around this base frame 120. At this time, since the lower processor panel of the processor cylinder 130 is rotatably coupled to the base frame 120 through a relative rotation coupling means such as a bearing, as the motor shaft of the idle drive motor 148 rotates, The idle drive gear 149 rotates, and as the idle drive gear 149 rotates, the idle ring gear 147 rotates so that the processor cylinder 130 rotates with respect to the base frame 120.

The plow 150 is provided with a plurality of stirring pads 156 on the outer peripheral surface of the shaft 152 disposed in the horizontal direction. A plurality of stirring arms 154 are disposed in a radial direction on the outer peripheral surface of the shaft 152, and a stirring pad 156 is coupled to each stirring arm 154, so that the plow 150 is arranged in the horizontal direction. (152) has a structure provided with a plurality of stirring pads (156) on the outer peripheral surface.

The shaft 152 of the plow 150 is rotatably coupled to the inspection chamber 132 located in the central portion of the processor cylinder 130. The plow 150 is configured to rotate relative to the inspection chamber 132 of the processor cylinder 130 by a rotation drive unit.

The rotation drive unit includes a rotation drive motor 162, a drive pulley 164, a driven pulley 166, and a rotation drive belt.

The rotation drive motor 162 is mounted on the base frame 120. The rotation drive motor 162 is disposed at the lower part of the processor cylinder 130.

The drive pulley 164 is coaxially coupled to the motor shaft of the rotation drive motor 162. The motor shaft of the rotation drive motor 162 is arranged in the horizontal direction, and the center of the drive pulley 164 is coaxially coupled to the motor shaft of the rotation drive motor 162, so that the drive pulley 164 is arranged in the vertical direction. .

The driven pulley 166 is coaxially coupled to the shaft 152 of the plow 150. The shaft 152 of the plow 150 is arranged in the horizontal direction, and the center of the driven pulley 166 is coaxially coupled to the shaft 152 of the plow 150, so that the driven pulley 166 is arranged in the vertical direction. . The driven pulley 166 is disposed inside the inspection chamber 132 of the processor cylinder 130, and the center of the driven pulley 166 is coaxially coupled to the shaft 152 of the plow 150.

The rotating drive belt 168 is coupled to the drive pulley 164 and the driven pulley 166. The lower processor panel of the processor cylinder 130 is provided with a belt passage hole in communication with the inside of the inspection chamber 132, so that the rotating drive belt 168 passes through the belt passage hole of the processor cylinder 130. In this state, it is coupled to the driving pulley 164 and the driven pulley 166.

As the motor shaft of the rotating drive motor 162 rotates, the plow 150 is inspected inside the processor cylinder 130 by the driving pulley 164, driven pulley 166, and rotating drive belt 168. The chamber 132 can be rotated relative to the reference.

When the plow 150 rotates based on the inspection chamber 132 of the processor cylinder 130, a plurality of stirring arms 154 stir the carrier composition and organic waste filled inside the processor cylinder 130 and simultaneously dispose of the plurality of agitating arms 154. Since the two stirring pads 156 also stir the carrier composition and the organic waste, the effect of increasing the processing efficiency of the organic waste by smoothly causing a reaction between the carrier composition and the organic waste can be expected.

In the present invention, a carrier composition on which complex microorganisms are adsorbed is installed inside the processor cylinder 130, and the carrier is made by mixing 70 parts by weight of rubber tree sawdust and 30 parts by weight of peat moss.

The present invention is based on the concept of revolution and rotation, and the temperature inside the quencher cylinder (i.e., it can be called a quencher as a processor inside the cylinder) where stirring is performed is 45 to 50 degrees during operation, and air (O2) is decomposed per 1 kg of waste. Sufficient volume of air is supplied to meet the processing capacity. In the present invention, when the temperature maintenance, weight change, and moisture change of the processor cylinder 130 are measured in real time and deviate from the extinction parameters set in the equipment, the related accessories automatically operate and supplementation is performed separately in real time. This is done automatically without manual operation. The control unit 175 may be configured to control such automatic operation.

In the present invention, the concept of revolution and rotation means that the cylinder rotates and the plow 150 rotates.

When organic waste is put into the disposal cylinder, the carrier composition on which the EM48 complex microorganisms are adsorbed and the organic waste are stirred without agglomeration through a stirring activity that combines revolution and rotation, and the organic material in 100% of the organic waste is converted into gas due to the activity of EM48. More than 98% of the remaining material is destroyed, and less than 2% of the remaining material is absorbed by EM48 and becomes a carrier composition to participate in the extinction activity.

The processor cylinder 130 (destruction tank) where extinction occurs is a place where the first deodorization operation is performed in parallel with the extinction treatment role.

The main cause of bad odor is when the decomposition process of proteins and fats contained in organic waste is incomplete. Among the 48 types of aerobic microorganisms comprised of EM48, Protease and Lipase microorganisms responsible for protein and fat decomposition are included. Protease and lipase have the most active decomposition activity at 45 to 50 degrees. This is the main reason why the temperature of the processor cylinder 130 is set to 45 to 50 degrees. At this time, the temperature of the processor cylinder 130 is determined by mounting a separate heater on the lower processor panel of the processor cylinder 130, electrically connecting the heater to the control unit 175, and operating the heater by the control unit 175. The temperature of the cylinder 130 may be set to 45 to 50 degrees.

Odor components contained in organic substances are completely deodorized by contact with microorganisms at the optimal growth temperature and by stirring with a double plow (150) (Gang Plow).

When organic waste (microorganism nutrients) is input into the processor cylinder 130 (destruction tank) where the growth temperature is maintained at a constant level of 45 to 50 degrees, external microorganisms such as Escherichia coli, salmonella, mold, and staphylococcus contained in the waste are first dominant. After annihilating 99.9% of the aerobic EM48-series adsorbed on the carrier composition, the annihilation and decomposition action of breaking the bonds in the molecular structure constituting the organic material and turning it into gas begins.

Among the 48 types of microorganisms in the EM48-series, Protease microorganisms and Lipase microorganisms, which have a growth temperature of 45 to 50 degrees, are responsible for decomposing proteins and fats that cause bad odors, and the active and complete decomposition activity of Protease microorganisms and Lipase microorganisms are responsible for the decomposition of proteins and fats that cause bad odors. The odor components generated from organic materials disappear within about 2 to 3 hours, and composting is completed within 8 hours.

Deodorization is achieved by the principle that the EM48-series decomposes by breaking the bonds between atoms in the chemical structure, and the broken atoms react with oxygen (O2) to synthesize a new, odorless chemical substance with completely different properties.

As stirring progresses, the EM48-series decomposes odor components in parallel with the disappearance of organic substances.

The carrier composition on which the organic matter extinction treatment has been completed emits a phytoncide scent.

In the present invention, effective microorganisms (EM: Effective Microorganisms) adsorbed to a carrier are complex microorganisms that are a collection of beneficial microorganisms such as photosynthetic bacteria, yeast, and lactic acid bacteria.

Therefore, in the present invention, when organic waste is input into the processor cylinder 130, the carrier composition on which complex microorganisms are adsorbed and the organic waste are mixed without agglomeration through a stirring action in which the revolution of the processor cylinder 130 and the rotation of the plow 150 are combined. When stirred, the organic material becomes a gas and annihilates more than 98%, and the remaining 2% or less is absorbed by complex microorganisms and becomes a carrier composition to participate in the annihilation activity. The processor cylinder 130 (cylinder processor cylinder 130) where extinction occurs can be said to be a place where the first deodorization operation is performed in parallel with the role of extinction treatment.

Additionally, in the present invention, an infrared sensor 172 is installed to measure temperature. The temperature inside the processor cylinder 130 is configured to be maintained at 45 to 50 degrees, and the heating method involves heating by installing an aluminum heater at the bottom of the processor cylinder (i.e., the bottom of the reaction tank) and supplying oxygen through a turbofan. The air is heated to 45 degrees and supplied. In addition, the outside of the processor cylinder 130 is constructed with an insulating material to maintain heat retention.

Real-time temperature measurement is programmed to install infrared temperature measurement sensors at two points on the upper part of the processor cylinder 130, measure the temperature during operation time, and store it in the operation panel unit 174. The temperature inside the treatment tank cylinder is sensed (measured) in real time by the infrared temperature measurement sensor, and the measured temperature inside the processor cylinder 130 is transmitted in real time to the control unit 175 provided in the operation panel unit 174. , the control unit 175 automatically controls the operation of the heater, thereby automatically setting the temperature inside the processor cylinder 130 to a range of 45 to 50 degrees.

The present invention is configured to measure the amount of change in weight by the load cell 176.

Load cells, which are load detection elements, are installed at four locations at the bottom of the processor cylinder 130, and information on the weight change measured in real time is stored. Real-time measurement of the weight change of input organic waste has the function of providing information directly related to the purpose of introducing waste treatment equipment.

Additionally, the present invention measures moisture change using a high-frequency moisture meter. The high-frequency moisture meter (MOC) is installed inside the processor cylinder 130 by being supported by a support means such as a bracket in the inspection chamber 132 inside the processor cylinder 130.

Moisture is measured by a high-frequency moisture meter in the central portion of the composition where waste and carrier composition are mixed and extinction is in progress. In the present invention, stirring is carried out with the concept of revolution and rotation as described above, and the operation method is operated in a cycle of "00 minutes of stirring operation -> 00 minutes of stirring rest," so that during the stirring rest period of the rotating stirring plow (150) High-frequency sensors are inserted into two points in the center of the composition, and are programmed to measure during the stirring pause and to position the insertion power source just before the stirring start.

Moisture measurement is an important measure of the moisture content of the carrier composition, which is an indicator that the equipment automatically stops operation according to the operation purpose of ① 98% or more of the processor operation, ② production and sale of high-quality soil conditioner with 00% residue after decay. It also serves a function.

All data measured in real time from three types of sensors is automatically saved, and various statistics according to calculation of customized extinction conditions (parameters) and equipment operation and management are recorded by day, month, and year. You can utilize it.

In the present invention, the upper processor panel of the processor cylinder 130 is provided with an organic waste inlet 145, and when the waste transport container 179 reaches the inlet through the lift 178, the inlet lid 143 is automatically opened and the waste material is disposed of. The transport container 179 is configured to automatically close when lowered through the lift 178. A lid opening and closing hydraulic cylinder 143MT is mounted on the upper processor panel of the processor cylinder 130 and is used to open and close the lid. When the waste transport container 179 reaches the inlet through the lift 178, the sensor 172 installed at the waste inlet detects the arrival of the waste transport container 179, and the waste transport container 179 is detected by the sensor 172. ) When the arrival detection signal is transmitted to the control unit 175, the control unit 175 may be configured to open the lid 143 by driving the lid opening/closing hydraulic cylinder 143MT, and the waste transport container through the lift 178. When (179) goes down from the inlet, the sensor installed in the waste inlet detects the lowering of the waste transport container 179, and when the signal for detecting the lowering of the waste transport container 179 is transmitted to the control unit 175 by the sensor, the control unit 175 ) may be configured to close the lid 143 by driving the lid opening/closing hydraulic cylinder 143MT.

Meanwhile, the waste input method can be ① Lift method, ② Screw method, ③ Pump method, and ④ Hopper method, and the lift (178) method is adopted in the present invention. Meanwhile, since the lift 178 can employ a known lift 178 device, the specific configuration of raising and lowering the waste transport container 179 by the lift 178 will be omitted.

At this time, the organic waste inlet 145 of the processor cylinder 130 is equipped with a crushing screw 146 to strongly crush food lumps, bones attached to fish, bones attached to meat, stems of food, substances that should not be input, etc. , by finely pulverizing it to increase the contact area with microorganisms, organic substances are decomposed and inorganic substances are converted into carriers and discharged when the remaining substances are discharged. The motor shaft of the crushing drive motor 146MT may be connected to the crushing screw 146, and the crushing screw 146 may be rotated by rotation of the motor shaft of the crushing drive motor 146MT. At this time, since the pulverizing screw 146 can be a known pulverizing screw used for pulverizing materials, further detailed description of the pulverizing screw 146 will be omitted. Meanwhile, the lower processor panel of the processor cylinder 130 is provided with a residue discharge pipe (DP), and a valve is installed in the residue discharge pipe DP. By opening the valve, the residue can be discharged out of the processor cylinder 130. .

The treatment process of the organic waste destruction treatment device of the present invention is one-stop and all processes are completed within 24 hours.

The EM48-series EM-series of organic waste destruction treatment equipment equipped with complex microorganisms completes the treatment of the composted waste within 8 hours after input.

Meanwhile, according to the present invention, the processor cylinder 130 in which the carrier composition 10 is embedded includes a plurality of divided cylinders 130DB; A combined support bar (130CSB) provided at the upper end of the plurality of divided cylinders (130DB); A coupling stone piece (130CSP) having a T-shaped cross-section extending in the longitudinal direction of the coupling support bar (130CSB); A lower coupling support bar (130LSB) provided at the lower end of the divided body (130DB); It includes a coupling support slit (130CSS) having a cross-sectional tee slit shape extending in the longitudinal direction of the lower coupling support bar (130LSB), and a plurality of divided cylinders (130DB) are stacked in the vertical direction to form the processor cylinder (130). In order to do this, the divided cylinders (130DB) adjacent to each other have a T-shaped coupling stone piece (130CSP) provided on the coupling support bar (130CSB) and a T-shaped slit-shaped coupling support slit provided on the lower coupling support bar (130LSB) ( It is characterized by being inserted and combined into 130CSS).

An upper flange (FL) and a lower flange (FL) are provided at the upper and lower ends of the plurality of divided cylinders (130DB), and the plurality of divided cylinders (130DB) are stacked in the vertical direction to form the processor cylinder (130). At this time, the lower flange (FL) and upper flange (FL) of the two adjacent divided cylinders (130DB) are arranged to contact each other, and the upper flange (FL) and lower flange (FL) that are in contact with each other have both ends and inner ends inside. The flange coupling hole of the half coupling support piece 131 having a flange coupling hole penetrated is inserted, and a bolt is common to the upper flange (FL), the lower flange (FL), and the half coupling support piece (131). is coupled, and a nut is fastened to the bolt to form the processor cylinder 130 in which the plurality of divided cylinders 130DB are stacked and joined in the vertical direction.

At this time, two half-joint support pieces 131 are coupled to the upper flange (FL) and the lower flange (FL) by the bolt and nut.

The uppermost divided cylinder (130DB) is provided with a coupling support bar (130CSB) at the lower end, an upper processor panel is provided at the upper end of the uppermost divided cylinder (130DB), and the upper processor panel is provided with an organic waste inlet (145). Thus, the coupling support protrusion of the coupling support bar (130CSB) provided on the split tube (130DB) immediately below is inserted into the coupling support groove formed in the coupling support bar (130CSB) at the lower end of the uppermost split tube (130DB) to be coupled. The lowermost divided cylinder (130DB) is provided with a lower processor panel at the lower end, a coupling support bar (130CSB) is provided at the upper end of the lowermost divided cylinder (130DB), and the lower processor panel is provided with a residual discharge pipe. , the coupling support protrusion on the coupling support bar (130CSB) at the upper end of the lowermost divided tube (130DB) can be inserted and coupled into the coupling support groove formed on the coupling support bar (130CSB) at the lower end of the immediately upper split tube (130DB). there is.

Of course, the lower flange (FL) at the lower end of the uppermost divided cylinder (130DB) and the upper flange (FL) at the upper end of the divided cylinder (130DB) immediately below are facing each other, and the two half-joint support pieces (131) are It is coupled to the upper flange (FL) and the lower flange (FL) by the bolt and nut, and the upper flange (FL) of the upper end of the lowermost divided cylinder (130DB) and the lower end of the divided cylinder (130DB) immediately above The lower flange (FL) of the two half-joint support pieces (131) are combined while facing each other and are coupled to the upper flange (FL) and the lower flange (FL) by the bolt and nut, forming a plurality of divided cylinders. (130DB) can be combined to form a processor cylinder 130.

Therefore, in the present invention, in order to form the processor cylinder 130, the divided cylinders 130DB adjacent to each other are provided with the T-shaped coupling protrusion piece 130CSP provided on the coupling support bar 130CSB, and the lower coupling support bar ( It is inserted into and coupled to the T-shaped slit-shaped coupling support slit (130CSS) provided in the 130LSB), and the upper flange (FL) and lower flange (FL) and lower flanges ( FL) are placed in contact with each other, and a half-joint support piece 131 is inserted into the upper flange (FL) and the lower flange (FL), and then the upper flange (FL) and the lower flange (FL) and the half-joint By fastening a nut to the bolt while the bolt is commonly coupled to the support piece 131, the effect of being able to assemble the processor cylinder 130 easily and quickly can be expected. When separating the processor cylinder 130, the bolt and Since the nut is loosened and the half-joint support piece 131 is pulled out from the upper flange (FL) and lower flange (FL) of the vertically adjacent split cylinder (130DB), the task of separating the processor cylinder (130) is also quick and easy. Effects can be expected.

Meanwhile, flanges (FL) are provided at the upper and lower ends of the cylindrical inspection chamber 132 provided at the center of the processor cylinder 130, and the flanges (FL) at the upper and lower ends of the inspection chamber 132 are connected to a plurality of flanges (FL). Since the upper plate of the uppermost divided cylinder (130DB) and the lower plate of the lowermost divided cylinder (130DB) among the divided cylinders (130DB) can be connected with bolts and nuts, when assembling and disassembling the processor cylinder (130), the inspection chamber (132) can also be easily and quickly assembled or disassembled.

In addition, in a state in which the carrier composition 10 is filled inside the processor cylinder 130, the plurality of divided cylinders 130DB are separated from top to bottom to lift the carrier composition 10 from the inside of the processor cylinder 130. Therefore, the effect of removing the carrier composition 10 from the processor cylinder 130 easily and quickly can be expected. Of course, it is natural that the carrier composition 10 can be filled into the processor cylinder 130 in which a plurality of divided cylinders 130DB are assembled and connected to the inspection chamber 132.

In addition, the present invention includes an auxiliary stirring drive motor 182 built into the inspection chamber 132 inside the processor cylinder 130; An auxiliary stirring shaft 184 connected to the motor shaft of the auxiliary stirring drive motor 182 through a rotational force transmission means and disposed in a vertical direction inside the processor cylinder 130; It is characterized in that it further includes a plurality of auxiliary mixing pins 186 protruding in a radial direction from the outer peripheral surface of the auxiliary stirring shaft 184.

The rotational force transmission means is coaxially coupled to the motor shaft of the auxiliary stirring drive motor 182 and accommodated inside the processor cylinder 130, and includes a drive gear (DG) disposed in the horizontal direction, and the auxiliary stirring shaft 184 ) is coaxially coupled to the horizontal direction and may be composed of a driven gear (SG) meshed with the driving gear (DG). A gear group connected to the motor shaft of the auxiliary stirring drive motor 182 and the auxiliary stirring shaft 184 and capable of transmitting the rotational force of the motor shaft of the auxiliary stirring drive motor 182 to the auxiliary stirring shaft 184 transmits the rotational force. It can be a means.

The auxiliary stirring shaft 184 is rotatably inserted into a coupling boss provided on the bottom of the upper processor panel and the upper surface of the lower processor panel of the processor cylinder 130, and the auxiliary stirring shaft 184 and a plurality of auxiliary mixing pins (186) may rotate within the processor cylinder (130).

A plurality of auxiliary mixing pins 186 arranged in the radial direction are arranged at regular intervals along the vertical direction of the auxiliary stirring shaft 184, and a plurality of auxiliary mixing pins 186 are arranged in multiple layers on the auxiliary stirring shaft 184. It is characterized in that it is configured to be arranged.

The auxiliary mixing pin 186 is characterized in that it is composed of a streamlined pin in which the distance between the two sides gradually decreases with respect to the center when viewed in cross section.

The auxiliary stirring shaft 184 is relatively rotatably coupled to a rotation support boss provided on the bottom of the processor cylinder 130 and a bracket boss provided on the outer peripheral surface of the inspection chamber 132, so that the auxiliary stirring shaft ( 184) and a plurality of auxiliary mixing pins 186 are rotatably coupled inside the processor cylinder 130.

An auxiliary stirring unit including the auxiliary stirring shaft 184 and a plurality of auxiliary mixing pins 186 arranged in a radial direction may be referred to as an auxiliary stirring unit.

Therefore, the auxiliary stirring unit rotates inside the processor cylinder 130 by the auxiliary stirring drive motor 182, thereby agitating more of the carrier composition 10 and organic waste filled in the processor cylinder 130. As the carrier composition 10 and organic waste are more evenly mixed inside the processor cylinder 130, the effect of further increasing the processing efficiency of organic waste due to the reaction between the carrier composition 10 and organic waste can be expected.

In addition, the auxiliary mixing pin 186 is composed of a streamlined pin in which the distance between the two sides gradually decreases based on the center when viewed in cross section, so when the auxiliary mixing pin 186 rotates and stirs the tint composition 10, the load resistance increases. Since it prevents the case from receiving too much, the effect of further increasing the reaction efficiency between the tint composition 10 and organic waste can be expected without difficulty.

The organic waste extinction treatment device of the present invention includes an ozone deodorizer (220); It includes a decomposed gas air discharge pipe 223 provided in the ozone deodorizer 220 and discharging wet air mixed with gas decomposed from organic waste in the reaction tank and moisture air.

In the present invention, the ozone deodorizer 220 is decomposed into a processor cylinder 130 containing a carrier composition in which EM complex microorganisms are adsorbed on a carrier (containing 70 parts by weight of rubber tree saws and 30 parts by weight of peat moss). It is connected via a gas discharge pipe. In the present invention, the ozone deodorizer 220 can be referred to as a cooling device and an ozone deodorization unit. A blowing fan 225 that sucks in outside air is installed in the ozone deodorizer 220, and cooling is performed by the blowing fan 225, so it also functions as a cooling function.

Humid air generated by the reaction of organic waste and carrier composition in the processor cylinder 130 flows into the ozone deodorizer 220 through the decomposition gas discharge pipe and is discharged by the discharger inside the ozone deodorizer 220. It is designed to remove odor components from humid air together with the ozone generated by the ozone generator (220GE).

The ozone deodorizer 220 cools the humid air containing heat and moisture, collects water, and then treats the odor contained in the water with ozone (O3), so that ozone is converted into odor components. Odor components are removed on the principle of destroying the molecular structure by changing radicals, and when oxygen is discharged within the ozone deodorizer 220, ozone in an unstable state is generated and acts on the pollutants to be removed, destroying them and restoring the original oxygen. It is configured to go back to remove bad odors and change vaporized gaseous moisture into liquid moisture to produce second-grade water or higher.

Inside the ozone deodorizer 220, a discharger that causes a discharge action is provided, and the discharger discharges oxygen within the ozone deodorizer 220 so that the pollutants to be removed and the unstable ozone react to remove bad odors. It is composed.

In the present invention, the discharger can generate plasma to cause oxygen discharge. In the present invention, the discharger can be an oxygen discharger. In addition to generating plasma, the discharge device may employ a known discharge device capable of generating discharge, such as generating an electronic discharge.

Meanwhile, the microorganism described in the present invention is an EM complex microorganism, and is configured to be absorbed by the carrier filled in the processor cylinder 130 and fill the processor cylinder 130 with the carrier composition.

In the first stage, the organic waste reaction tank (destruction tank), that is, the odor component contained in the organic waste in the processor cylinder 130 is deodorized within 2 to 3 hours after input due to the decomposition activity of microorganisms contained in the EM48-series. It's done.

However, the odor component contained in approximately 85% or more of the moisture (desorbed liquid, food waste water, sewage water, urine, etc.) in organic waste is caused by the heat of the microbial growth conditions and environment in the reaction tank of the treatment equipment, and the moisture is lost as soon as the waste is input. As steam progresses, odor components contained in the moisture are often discharged to the outside along with the vaporized moisture without a chance to encounter microorganisms.

Most of the odor components contained in the moisture of humid air are decomposed when they meet microorganisms, but this cannot be done and odors that are discharged to the outside along with the moisture vapor may be generated.

The second stage organic waste destruction treatment device of the present invention (i.e., humid air collection type ozone deodorizer 220) cools humid air containing high heat and moisture (blowing fan 225 provided in ozone deodorizer 220). After collecting the water, the odor contained in the water is treated with ozone (O3), and ozone changes the radicals of the odor component and destroys the molecular structure. Odor components are removed through the principle of (decomposition). The principle of deodorizing ozone is that when oxygen is transferred, ozone in an unstable state is created, which acts on the pollutants to be removed, destroying them and returning to the original oxygen.

By changing vaporized gaseous moisture into liquid moisture, second-grade water or higher can be produced. It can be used as washing water, agricultural water, etc. In the case of organic food waste, more than 85% is water, so an amount of water equivalent to 85% of the treated material can be produced. In the case of pig manure from livestock farms, if one or two finishing pigs discharge per day feces: 1.6 kg, urine: 2.6 kg, excrement production: 4.2 kg, washing water: 4.4 kg, waste water production: 8.6 kg, 81% of water is discharged. . If 20 tons of raw water generated per day are destroyed as is, 3.8 tons (19%) of solids are expected to remain, or about 380 kg of 1%, and 16.2 tons of recycled water will be produced for water production.

In the present invention, the ozone deodorizer 220 is provided with a decomposition gas air discharge pipe 223 and a dry air change gas discharge pipe 226. The decomposition gas air discharge pipe 223 is a pipe through which the steam and moisture vapor decomposed from the organic waste in the disposal cylinder (reaction tank) are mixed (wet air) in an environment of 45 to 50 degrees and discharged, and the dry air change gas discharge pipe 226 ) is a pipe through which gas changed from dry air (gas changed into dry air by the ozone deodorizer 220) moves to the deodorizer 230, which is the third stage. The deodorizer 230 is provided with a dry air passing sleeve 232 that communicates with the dry air change gas discharge pipe 226 of the ozone deodorizer 220. The third stage deodorizer 230 is the Blinn deodorizer 230.

A flow path 221 is provided inside the ozone deodorizer 220, and a water tank 221WT connected to the upper flow path 221 is built into the lower part of the ozone deodorizer 220, and the water A water spray pipe (221WSP) is disposed above the tank (221WT), collects water toward the water tank (221WT) through the water spray hole of the water spray pipe (221WSP), and moist air passes through the flow path (221). Since odor components are removed from the humid air created by the reaction of organic waste and the carrier composition in the processor cylinder 130, there is an effect of more reliably removing odor from the treated air.

As described above, the second-stage organic waste destruction treatment device (humid air collection type ozone deodorizer 220) of the present invention collects water by cooling humid air containing high heat and moisture. If the odor contained in the odor is treated with ozone (O3) generated from an ozone generator, the odor component is removed on the principle that ozone changes the radical of the odor component and destroys (decomposes) the molecular structure. , it changes vaporized gaseous moisture into liquid moisture, making it possible to produce second-grade water or higher.

Meanwhile, the present invention further includes a deodorizer 230 connected to the decomposed air discharge pipe of the ozone deodorizer 220. At this time, the deodorizer 230 is a third-stage Blinn deodorizer 230.

The deodorizer 230 includes a dry air passage sleeve 232, the interior of which is in communication with the wet air passage chamber of the ozone deodorizer 220, which is in communication with the decomposed air discharge pipe; A deodorizer casing (233) with the dry air passing sleeve (232) built into it; A cell support enclosure 234 built into the deodorizer casing 233 to be connected to the dry air passing sleeve 232; It is characterized in that it includes a blind sable cell, a zeolite save cell 244, and an activated carbon save cell 246, which are provided inside the cell support enclosure 234 and through which dry air sequentially passes. The deodorizer 230 described in the present invention is the Blinn deodorizer 230.

The Blinn Save Cell, Zeolite Save Cell 244, and Activated Carbon Save Cell 246 are built into the cell support enclosure 234, and the Blinn Save Cell 242 is built into the cell support enclosure 234. It communicates with the air passing sleeve 232, and the Blinn save cells 242 are stacked in a vertical direction in a state in which they are built into the cell support housing 234. The Blinn save cells are inside the cell support housing 234. A partition wall 247 is provided to partition the zeolite save cells 244 from the zeolite cells 242, and the partition wall 247 allows wet air passing through the blind save cells 242 to flow into the zeolite save cells 244. A connection hole is provided to allow inflow, and an activated carbon save cell 246 is disposed inside the cell support box 234 to be placed above the zeolite save cell 244, and the cell support box 234 Inside, there is a partition wall 247 that separates the zeolite save cell 244 and the activated carbon save cell 246, and the dry air that has passed through the zeolite save cell 244 is stored in the partition wall 247. It is characterized by being provided with a connection hole that allows flow into the cell 246.

Dry air passes through the dry air passage sleeve 232 in the decomposed air discharge pipe of the ozone deodorizer 220, and then third deodorization occurs as the dry air passes through the blind save cell 242, and the geol The fourth deodorization occurs as the dry air passes through the light save cell 244, and the fifth deodorization occurs as the dry air passes through the activated carbon save cell 246.

The cell support enclosure 234 is provided with a discharge connection pipe through which air from which bad odors are removed passes through the activated carbon save cell 246 and is delivered to the discharge pipe.

In the present invention, BLEAN is a non-toxic chemical synthetic material manufactured as a raw material for feed additives in fish farms (lakes, seas), etc. In the second stage, the gas deodorized in the wet air collection type ozone deodorizer (220), and the wet air converted into dry air, passes through 50 to 80 cm of the Pathway of the Blean save cell (242) filled with Blean, and Blean acts as a transition metal catalyst to decompose odor components. This is the principle of deodorization by acting as a . The third stage of Bleaning is to deodorize odorous substances contained in dry air (gas).

The zeolite save cell deodorizes by adsorbing and removing odorous substances contained in the gas using zeolite. Zeolite is an anionic mineral formed in nature by combining aluminum oxide and silicate, and is also called zeolite. Zeolite removes odors by acting as an adsorption catalyst rather than decomposing odorous substances. Adsorbs nitric acid (NOx) and sulfuric acid (SOx) series substances.

The activated carbon save cell 246 deodorizes the gas by adsorbing and removing odorous substances contained in the gas using activated carbon. Activated carbon has strong adsorption properties and most of its components are carbonaceous, so it deodorizes odorous substances by acting as an adsorption catalyst rather than decomposing them. Activated carbon made from palm or coconut shells is mainly used.

Therefore, the present invention allows the first to fifth deodorized air to be discharged to the outside, thereby increasing waste treatment efficiency and being very effective in removing bad odors.

Meanwhile, the present invention includes a blowing fan 225 installed in the ozone deodorizer 220 to force air to flow into the inlet hole with negative pressure, wherein the blowing fan 225 is installed in the ozone deodorizer 220. It is detachably installed in the inlet hole formed in by means of detachment means.

The desorption means includes a plurality of mounting support pins 252 installed on a wall around the inlet hole of the ozone deodorizer 220; A mounting support head 253 formed on the mounting support pin 252; A plurality of split coupling support pieces are provided on the fan frame 225F of the blowing fan 225 to be inserted into the outer peripheral surface of the mounting support pin 252 and are arranged in a radial direction with respect to the center of the mounting support pin 252. (255); A joint locking support piece (256) provided on the inner peripheral surface of the plurality of split coupling support pieces (255) and hooked to an inner end of the mounting support head (253); It is provided with a cutout portion (257CP) penetrating the inner and outer peripheral surfaces and is coupled to the outer peripheral surface of a plurality of split coupling support pieces 255, and when the blowing fan 225 is pushed toward the ozone deodorizer 220, the split coupling support pieces are connected to each other. It is characterized in that it includes a coupling elastic ring body (257) that pushes (255) so as to narrow it toward the mounting support pin (252).

In a state where a plurality of split coupling support pieces 255 provided on the fan frame 225F of the blowing fan 225 are aligned to meet a plurality of mounting support pins 252 provided on the ozone deodorizer 220. When the blowing fan 225 is pushed toward the ozone deodorizer 220, the plurality of split coupling support pieces 255 move forward and spread along the mounting support head of the mounting support head 253, and at the same time, the coupling elastic ring body 257 ), the mounting support head 253 is spread based on the cutout portion 257CP, and the engaging locking support piece 256 on the inner peripheral surface of the split coupling support piece 255 protrudes from the outer peripheral surface of the mounting support pin 252. Beyond this, the coupling elastic ring body 257 elastically narrows in diameter and the coupling locking support piece 256 provided on the inner peripheral surface of the plurality of split coupling support pieces 255 becomes attached to each mounting support pin 252. ), the blowing fan 225 can be maintained in a one-touch coupled state to the ozone deodorizer 220.

Meanwhile, when the blowing fan 225 is pulled from the ozone deodorizer 220 while the coupling elastic ring body 257 is separated from the plurality of split coupling support pieces 255, the plurality of split coupling support pieces ( 255) moves backwards on the long support head of the mounting support head 253 and spreads, and at the same time, the coupling elastic ring body 257 also spreads based on the notch 257CP, thereby engaging the inner peripheral surface of the split coupling support piece 255. Since the catching support piece 256 is separated from the mounting support head 253 protruding from the outer peripheral surface of the mounting support pin 252, the blowing fan 225 can be easily separated from the ozone deodorizer 220. .

Therefore, the present invention can be combined by pushing the blowing fan 225, which blows external air to cool the inside of the ozone deodorizer 220, into the ozone deodorizer 220 with one touch, and the blowing fan 225 To separate from the ozone deodorizer (220), first separate the coupling elastic ring body (257) and pull the blowing fan (225) from the ozone deodorizer (220) to easily remove the blowing fan (225) from the ozone deodorizer (220). Since it is separable, it can be expected that assembling and disassembling the blowing fan 225 from the ozone deodorizer 220 will be done quickly and easily.

In addition, the present invention is disposed at a position facing the blowing fan 225 and at the same time is disposed on the air distribution path through which the air inside the ozone deodorizer 220 is blown by the blowing fan 225, It further includes an air freshener unit 260 that removes bad odors from the humid air passing inside the furnace. The air freshener unit 260 is a structure in which a solid air freshener is built into the air freshener case 262, and is mounted on the air distribution path of the blowing fan 225 by a mounting means such as a bracket on the inner side of the blowing fan 225. It can be configured to be deployed.

Therefore, by supplying the air freshener to the inside of the ozone deodorizer 220, there is an effect in that the malodor component in the ozone deodorizer 220 can be more reliably converted into good air due to the air freshener.

Meanwhile, the air freshener unit 260 may be configured so that the air freshener filter 264 is detachably inserted into a plurality of insertion holes 262IH formed on one side wall of the air freshener case 262. The air freshener filter 264 may be configured to fill a perforated filter mesh with pores with a solid air freshener. That is, the air freshener unit 260 may be configured to have a plurality of air freshener filters 264 installed therein in a detachable manner. At this time, the other side wall facing one side wall of the air freshener case 262 does not have an insertion hole 262IH and is blocked, thereby supporting the plurality of air freshener filters 264 inserted into the insertion hole 262IH.

Accordingly, there is an effect in that the air freshener unit 260 can easily and easily separate some air freshener filters 264 that need replacement from among the plurality of air freshener filters 264 .

Above, specific embodiments of the present invention have been described in detail. However, the spirit and scope of the present invention are not limited to these specific embodiments, and it is known by common knowledge in the technical field to which the present invention pertains that various modifications and variations can be made without changing the gist of the present invention. Anyone who has it will understand.

Therefore, the embodiments described above are provided to fully inform those skilled in the art of the present invention of the scope of the invention, and should be understood as illustrative in all respects and not restrictive. The invention is defined only by the scope of the claims.

120. Base frame 130. Processor cylinder
130DB. Split whole body 130CSB. Combined support bar
130CSP. Combined stone piece 130LSB. Bottom combined support bar
130CSS. Combined support slit 131. Half-jointed support piece
132. Inspection chamber 143. Lid
144. Lid opening/closing drive motor 145. Organic waste input port
146. Crushing screw 147. Idle ring gear
148. Idle drive motor 149. Idle drive gear
150. Plow 152. Shaft
154. Stirring arm 156. Stirring pad
162. Rotating drive motor 164. Drive pulley
166. Driven pulley 168. Rotating drive belt
172. Infrared sensor 174. Control panel unit
176. Load cell 178. Lift
179. Waste transport container 182. Auxiliary stirring drive motor
184. Auxiliary stirring shaft 186. Auxiliary mixing pin
D.G. Drive gear SG. driven gear
220. Ozone deodorizer
221. Flow Pass 221WT. water tank
221WSP. Water spray pipe 223. Decomposition gas air discharge pipe
225. Blowing fan 225F. fan frame
226. Dry air change gas discharge pipe 230. Deodorizer
232. Dry air passage sleeve 233. Deodorizer casing
234. Cell support enclosure 242. Blinn save cell
244. Zeolite Save Cell 246. Activated Carbon Save Cell
247. Bulkhead 252. Mounting support pin
253. Mounting support head 255. Split joint support piece
256. Combined locking support piece 257. Combined elastic ring body
257CP. Cutout 260. Air freshener unit
262. Air freshener case 262IH. Insertion hole
264. Air freshener filter

Claims (3)

Base frame 120;
a processor cylinder 130 rotatably supported on the base frame 120;
It includes a plow 150 provided inside the processor cylinder 130,
A cylindrical inspection chamber 132 is provided at the inner center of the processor cylinder 130,
The processor cylinder 130 is configured to revolve around the base frame 120 by an orbital drive unit,
The idle driving unit,
an orbital ring gear 147 rotatably coupled to the base frame 120, disposed in a horizontal direction, and having its upper surface connected to the processor cylinder 130 via a connecting rod;
An idle drive motor 148 mounted on the base frame 120;
It includes an idle drive gear 149 coaxially coupled to the motor shaft of the idle drive motor 148 and meshed with the idle ring gear 147,
The plow 150 is provided with a plurality of stirring pads 156 on the outer peripheral surface of the shaft 152 arranged in the horizontal direction, so that the shaft 152 is placed in the inspection chamber 132 in the central portion of the processor cylinder 130. It is rotatably coupled and simultaneously rotates with respect to the inspection chamber 132 of the processor cylinder 130 by a rotation drive unit,
The rotation drive unit,
a rotation drive motor 162 mounted on the base frame 120 and disposed below the processor cylinder 130;
A drive pulley 164 coaxially coupled to the motor shaft of the rotation drive motor 162;
a driven pulley 166 coaxially coupled to the shaft 152 of the plow 150;
It is configured to include a rotating drive belt coupled to the drive pulley 164 and the driven pulley 166,
A carrier composition 10 on which complex microorganisms are adsorbed is installed inside the processor cylinder 130, and the carrier is made of a mixture of 70 parts by weight of rubber tree sawdust and 30 parts by weight of peat moss,
When organic waste is input into the processor cylinder 130, the carrier composition 10 on which complex microorganisms are adsorbed and the organic waste are stirred without agglomeration through a stirring action that combines the revolution of the processor cylinder 130 and the rotation of the plow 150. In 100% by weight of organic waste, the organic material becomes a gas and more than 98% by weight is destroyed, and the remaining 2% by weight or less is adsorbed by complex microorganisms and becomes the carrier composition 10 to participate in the extinction activity, and the above processor where extinction occurs. The cylinder 130 is a place where deodorization work is performed in parallel with the role of extinction treatment,
Ozone deodorizer (220);
It further includes a decomposition gas air discharge pipe 223 provided in the ozone deodorizer 220 and discharging wet air mixed with gas decomposed from organic waste in the reaction tank and moisture air,
The ozone deodorizer 220 collects water by cooling the humid air containing heat and moisture, and then treats the odor contained in the water with ozone, so that the ozone removes the radicals of the odor component. Odor components are removed on the principle of destroying the molecular structure by changing the ozone deodorizer 220. When oxygen is discharged within the ozone deodorizer 220, ozone in an unstable state is created, which acts on the pollutants to be removed, destroying them and returning them to the original oxygen. It is configured to remove bad odors and change vaporized gaseous moisture into liquid moisture to produce second-grade water or higher,
Inside the ozone deodorizer 220, a discharger that causes a discharge action is provided, and the discharger discharges oxygen within the ozone deodorizer 220 so that the pollutants to be removed and the unstable ozone react to remove bad odors. composed,
The decomposed air discharge pipe 223 of the ozone deodorizer 220 is connected to the space filled with the internal tint composition 10 of the processor cylinder 130, and the deodorizer 230 is connected to the ozone deodorizer 220. It is structured so that
The deodorizer 230,
A dry air passing sleeve 232 internally in communication with the wet air passing chamber of the ozone deodorizer 220, which is in communication with the decomposed air discharge pipe;
A deodorizer casing (233) with the dry air passing sleeve (232) built into it;
A cell support enclosure 234 built into the deodorizer casing 233 to be connected to the dry air passing sleeve 232;
It is configured to include a save cell 242, a zeolite save cell 244, and an activated carbon save cell 246, which are provided inside the cell support enclosure 234 and through which dry air sequentially passes,
The save cell 242, the zeolite save cell 244, and the activated carbon save cell 246 are built into the cell support box 234, and the save cell 242 is built into the cell support box 234. It is in communication with the dry air passage sleeve 232, and the save cells 242 are stacked in a plurality in the vertical direction while embedded in the cell support enclosure 234, and the inside of the cell support enclosure 234 is a save cell ( 242) and a partition wall 247 dividing the zeolite save cells 244 is provided, and the partition wall 247 allows wet air passing through the save cells 242 to flow into the zeolite save cell 244. A connection hole is provided, and an activated carbon save cell 246 is disposed inside the cell support box 234 so as to be placed above the zeolite save cell 244, and inside the cell support box 234 A partition 247 is provided that separates the zeolite save cell 244 and the activated carbon save cell 246, and the partition 247 has dry air passing through the zeolite save cell 244 into the activated carbon save cell ( A connection hole is provided to allow inflow toward 246),
Dry air passes through the dry air passage sleeve 232 in the decomposed air discharge pipe of the ozone deodorizer 220, and then third deodorization occurs as the dry air passes through the save cell 242, and the zeolite The fourth deodorization occurs as the dry air passes through the save cell 244, and the fifth deodorization occurs as the dry air passes through the activated carbon save cell 246.
The cell support enclosure 234 is provided with a discharge connection pipe through which air from which odors have been removed passes through the activated carbon save cell 246 and is delivered to the discharge pipe,
The Zeolite save cell is configured to deodorize by adsorbing and removing odorous substances contained in the gas with zeolite,
The activated carbon save cell 246 is an organic waste extinction treatment device characterized in that it is configured to deodorize by adsorbing and removing malodorous substances contained in the gas with activated carbon. delete delete