JP2961280B2 - Batch fermentation treatment method for organic waste and its treatment system - Google Patents

Description

DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for rapidly fermenting an organic waste rich in fibrous material such as cut grass and defoliated leaves to use as a fertilizer or a soil conditioner. The present invention relates to a batch fermentation treatment method and a treatment system for continuously performing the method.

[Prior art] In the processing of turf and the like cut at a golf course,
The cut grass is discarded as it is in a valley. However, such a method causes dead grass and the like to rot and emit a bad smell, thereby deteriorating the surrounding environment.

For this reason, the method of depositing cut grass and defoliation and making it into a natural compost and using it as a fertilizer or soil conditioner is also used. In order to fully mature fiber such as lignin and cellulose contained in plant waste such as 1
In addition to the extremely long period of one year to one and a half years, there is also a problem that the switching operation must be frequently performed in order to properly supply air to the sedimentary layer.

Therefore, recently, in order to reduce the time required for natural composting treatment, a method of sufficiently fermenting organic waste in a fermentation tank before the composting treatment has been disclosed in Japanese Patent Laid-Open No. Sho 62-62.
It has been developed and proposed as shown in 52194, etc., but this proposed method promotes the fermentation of cut grass and defoliated leaves in fermentation tanks, so that organic waste such as cut grass is removed. Must be once crushed by a crusher,
After fermentation treatment in the fermenter, it was necessary to uniformly grind using a raikai machine or the like.

[Problem to be solved by the invention] The present invention has been made in view of such circumstances,
The batch fermentation treatment method for organic wastes, which can process organic waste that is generally difficult to ferment due to its high fiber content in a short time and efficiently without deteriorating the environment, and this fermentation method continuously and efficiently It is an object of the present invention to provide a fermentation treatment system that can be performed.

[Means for Solving the Problems] The batch-type fermentation treatment method for waste of the present invention proposed to achieve the above object reinforces fresh water into fibrous organic waste such as cut grass and defoliated leaves. While keeping the moisture content constant, put it into the fermentation tank together with the fermentation accelerator and fermentation bacterium and heat it up to the optimal fermentation temperature while mixing and stirring, then stop mixing, stirring and heating, and mix the fermentation tank. The product is kept in a state where it does not come into contact with the outside air, and the fermentation bacterium is left for a certain period of time to perform logarithmic growth, and then the mixture is subjected to mulling treatment. ,
Fermentation is performed for a predetermined time while maintaining the fermentation optimum temperature, and finally, the mixed treatment discharged from the fermenter is subjected to composting by subjecting the mixed treatment to forced aeration and switching over for a certain period of time to obtain a fermentation treatment.

In the method of the present invention, the pre-fermentation process is completed in which the water content is adjusted by adding fresh water to the organic waste, and the fermentation accelerator and the fermenting bacterium are put into a fermentation tank and heated to a fermentation optimum temperature while mixing and stirring. After that, the mixing and stirring are stopped for a certain period of time to stop the contact with the outside air, and the muroidizing process is performed. Fermentative bacteria active in the process are growing rapidly.

In this mulling process, the fermentation bacteria are maintained at the optimal temperature for the fermentation activity and are cut off from contact with the outside air, so that they can grow logarithmically. The fermentation of the product will take place quickly and evenly.

In addition, in this mulling treatment step, there is also an effect of suppressing the growth of anaerobic fermentation bacteria that cause malodor and increasing only the anaerobic fermentation bacteria that are beneficial to the fermentation treatment. Because it can be performed, there is no adverse effect on the surrounding environment.

In such an inventive method, the organic waste to be fermented is always subjected to optimal fermentation conditions (moisture 50-75%, temperature around 40 ° C).
Fresh water is appropriately replenished in order to maintain the fermentation. However, in the fermentation treatment of the fibrous rich plant waste, it is desirable to mix the fermentation promoter with the animal waste that has been fermented. Further, since plant wastes contain a large amount of fibrous materials such as lignin and cellulose, even after the constant temperature fermentation treatment according to the present invention, natural composting treatment is performed to fully mature these fibrous materials. When the fermentation process is performed, it is desirable that the moisture content is about 50% to 70% when the fermentation process is performed. Has been stopped.

In addition, the present inventors have referred to the fermentation treatment in the method of the present invention as such because fermentation proceeds while maintaining a constant temperature lower than the temperature range that rises during natural composting treatment.

In the method of the present invention, microorganisms such as Bacillus which are suitable for fibrous fermentation are used. However, the fermentation efficiency can be reduced by adding an appropriate amount of Hanaoka porphyry during the fermentation process. The present inventors have also confirmed that they are particularly desirable in terms of improvement.

The waste fermentation treatment method of the present invention proposed in claim 2 is characterized in that the fermentation treatment product obtained by the method of the present invention is reduced and used as a fermentation promoter. The fermentation process can be made faster and more effective by mixing the produced fermentation product with the waste organic matter to be processed.

Claim 4 proposes a fermentation treatment system that is used when the method of the present invention is continuously performed on a large scale at a waste treatment plant or the like.
A first transfer means for transferring organic waste such as fallen leaves,
A cross section U constituted by attaching a paddle-type stirring blade to a horizontal rotating shaft so as to rotate along a bottom curved surface of the processing tank.
Above the letter-shaped fermentation treatment tank, a mudification chamber for storing carbon dioxide generated during the fermentation treatment of organic waste is formed, and the upper part is moved by the first transfer means. A fermentation treatment device having a material input port for inputting incoming organic waste and a material discharge port at the bottom,
A fertilizer-treated organic waste discharged from the outlet of the fermentation treatment apparatus is stored, and a composting treatment tank having an aeration unit that blows air to the stored fermented organic waste stored at the bottom. It is provided with a configuration.

[Action] According to the method of the present invention, organic wastes such as cut grass and defoliated leaves rich in fibrous materials are left unattended for a certain period of time to cause a bad smell, and crushing treatment by a troublesome crusher is not performed. The fermentation treatment can be carried out by directly charging the fermentation tank.

Further, in the method of the present invention, in the constant temperature fermentation treatment step, fermentation treatment is performed in the fermentation treatment tank while the fermentation bacterium is maintained in the environmental condition in which the fermentation bacterium is most easily activated. The processing time of the composting process performed can be significantly reduced.

Generally speaking, the lag phase of the fermentative bacterium growth phase is the time when the protein synthesis required for division is carried out. If a rapid change occurs in the outside world at this time, the fermentation bacteria may be killed.

Therefore, in the method of the present invention, the mixing and heating of the mixture are temporarily stopped by the mulling step, and the carbon dioxide generated by the fermentation action of the fermenting bacteria is stored in the tank and left for a certain period of time in a state of being in contact with the mixture. The method employs a method of cutting off the contact with the outside air and creating a favorable lag phase environment for the fermentation bacteria to efficiently perform logarithmic growth.

The contact of carbon dioxide required in such a mashing step may be carried out from a separately prepared tank into the tank in addition to storing what is generated during fermentation. Further, when contacting with carbon dioxide, it is desirable to mix an appropriate amount of oxygen, and the oxygen in the mixed gas can suppress the growth of obligate anaerobic bacteria which cause a bad odor, so that the odor can be further reduced.

Further, when Hanaoka porphyry was added to the mixture during the constant temperature fermentation treatment, the fermentation was further promoted, and the fermentation treatment time could be further shortened. This is thought to be because the physical properties of Hanaoka porphyry are porous and polyhedral, exhibiting filterability, containing trace elements dissolve out and ionize the solution of the treated product, promoting the enzymatic reaction in fermentation. It is.

In the method of the present invention described in claim 2, the fermented product obtained by the method of the present invention is reduced and used. Such a fermented product contains nutrients such as amino acids obtained by fermentation that are easily used by fermentation bacteria, so that the fermentation process can be further accelerated and the processing time can be reduced.

Further, in the method of the present invention, since organic waste required to maintain a constant moisture content is fermented, fresh water is appropriately supplied during the pre-fermentation process or the constant temperature fermentation process to maintain the moisture content constant. ing.

In the system according to the third aspect of the present invention, the fermentation can be accelerated more quickly by applying an appropriate vibration to the fermentation tank during the fermentation treatment.

Furthermore, in the system of the present invention described in claim 4, since the above-described method of the present invention can be continuously and efficiently performed, if it is installed in a waste disposal site or the like, it can be used as a non-polluting organic waste treatment plant.

Examples Examples of the present invention will be described below.

FIG. 1 is a flow chart showing a processing procedure when the method of the present invention is applied to the fermentation treatment of cut grass, and in the first pre-fermentation treatment step, a fermentation accelerator, a cut grass to be treated, a fermentation bacterium, etc. Is fed into the fermentation tank together with fresh water for adjusting the moisture content, and heated to the optimum fermentation temperature while being mixed and stirred in the fermentation tank.

After the fermentation pretreatment step has been completed in this way, the fermentation step is started, in which the mixing and stirring are stopped and the fermentation bacteria are mixed in order to logarithmically grow the fermentation bacteria mixed in the fermentation treatment tank. The mixed product is kept for a predetermined time in a state where it is cut off from the outside air.

Then, when entering the constant temperature fermentation treatment step, the mixed treatment in the fermentation treatment tank is again maintained at the optimum fermentation temperature, the mixing and stirring is performed while replenishing fresh water, and the fermentation treatment is performed. Continue mixing and stirring until the optimum conditions for the composting process are reached. After completion of the fermentation process, natural composting is performed to decompose fibers such as lignin and cellulose.

The fermented product obtained by this composting process is sieved without being subjected to any crushing treatment, and is used as a fertilizer or a soil conditioner after removing impurities.

(Experimental example) (1) Pre-fermentation process Along with the fermentation accelerator, fresh water from which the calcium component at room temperature was removed was put into a 150 fermentation tank to adjust the water content and stirred. Add the fermentation bacteria together and heat the panel heater of the fermentation tank while mixing and stirring. About 1 hour until the actual temperature of the mixed product in the fermentation tank reaches the optimum fermentation temperature of 42 ° C while watching the temperature sensor Mixing and stirring were performed.

 Each material put into the fermenter is as follows.

B) Cut grass turf (rough) 9.5Kg (30cm length after cutting), 30.5Kg in total of bent grass and Koryo grass (3mm after cutting)
Length) b) Fermentation accelerator Bio Gold Meal manufactured by Gold Co., Ltd. (waste chicken is mixed with a water regulator such as bran and fusuma and fermenting bacteria) and fermented. 14kg C) Fermenting bacteria Gold Co., Ltd. 200g Gold 8 (manufactured mainly by fermenting bacteria such as Bacillus) d) Shimizu (water 24 with chlorine chlorine removed for sterilization) (2) Muro treatment process The substance of the mixture in the fermenter Temperature is optimal fermentation temperature 42 ℃
At that time, the mixing and stirring were stopped, and the blow-off port and the discharge port of the blower of the mulling chamber formed above the fermentation treatment tank were closed.

Thus, carbon dioxide generated during the fermentation process from the mixed processed product in the fermentation processing tank is filled in the mulling chamber, thereby blocking the mixed processed product from contacting the outside air, and maintaining the temperature by the fermentation heat. It was left for 2 hours.

(3) Constant temperature fermentation process While controlling the actual temperature of the mixed product in the fermentation tank with the temperature sensor again, it controls the ON / OFF of the panel heater provided in the fermentation tank and blows an error into the mulling chamber. The on / off control of the fermentation tank keeps the actual temperature of the mixed product in the fermentation processing tank at the optimum fermentation temperature of 42 ° C, performs the fermentation process by stirring, and replenishes fresh water from which calcium has been removed. This condition was maintained for about 48 hours until the mixed product became in a condition necessary for moving to the next composting process while keeping the temperature constant.

As a result, a fine mulch-like fermented material (a long one, which is crushed without touching with a finger at about 3 cm) with a small amount of fine thread-like lawn grass remaining in the powdered processed material, The outlet of the tank was opened and discharged.

(4) Composting treatment The fermented product obtained by the fermentation treatment step was transferred to a composting treatment tank, and was naturally turned over for about two months while appropriately turning over and supplying air.

At the time of natural fermentation at this time, the fermented product further continued fermentation and temporarily increased the temperature by about 75 ° C., but thereafter the temperature gradually decreased and finally reached room temperature.

The fermented product thus obtained did not require any crushing treatment, and was sieved as it was to remove impurities. As a result, a fine powdery fermented product that could be used as it was as a fertilizer or soil conditioner could be obtained.

As shown in FIGS. 2 (a) to 2 (c), FIGS. 3 and 4, a fermentation treatment apparatus constituting a main part of the fermentation treatment system of the present invention A processing tank 1 provided with a processing chamber 9 and a machine chamber 2 are integrally formed. The processing tank 1 is made of a metal plate and has a bottom formed in a U-shaped cross section as shown in FIG. A paddle type stirring blade 3 is pivotally supported inside 1, and a mixing chamber 4 is connected above the stirring blade 3. On the outer periphery of the processing tank 1,
A panel heater 11 is provided.

A motor (not shown) for rotating the stirring blade and a blower (not shown) are disposed in one machine room 2.
A control panel 6 is attached to an outer wall of the control panel.

As shown in FIG. 3, the paddle-type stirring blade 3 has a pair of vertical blades 32, 32 attached to two square-shaped horizontal blades 31, 31 parallel to the horizontal rotation axis 5. The processing tank 1 is rotated along the bottom curved surface by the rotation of a motor connected to the horizontal rotation shaft 5.

U-shaped bottom curved surface of processing tank 1 and horizontal blade 31 of stirring blade 3
As shown in FIGS. 5 and 6, a gap S (10 to 15 mm) for preventing the killing of the fermentation bacteria is formed between the horizontal blades 31 of the stirring blade 3 by the gap S. By doing so, it is prevented from being crushed and crushed to the curved surface at the bottom of the processing tank.

As shown in FIG. 4 and FIG. 5, the mudification chamber 4 is generated when a mixed product obtained by mixing the waste in the fermentation treatment tank 1, the moisture regulator, and the fermenter is performing fermentation. It is provided for retaining carbon dioxide, by storing the carbon dioxide as it is above the mixed product tank,
For a certain period of time, it is configured to keep the contact with the outside air shut off and keep the temperature by fermentation heat.

An air outlet 71 and an exhaust port 81 connected to the blower are arranged on the partition wall 7 between the processing tank 1 and the machine room 2 so as to be positioned above the mulling chamber 4 and diagonally. A temperature sensor 72 for measuring the actual temperature of the mixed product is provided below the horizontal rotation axis 5 in the fermentation tank 1.
Is disposed so as to be directly embedded in the mixed processed product layer in the fermentation processing tank. Reference numeral 82 denotes a viewing window for visually checking the fermentation state of the mixed product in the fermentation tank.

Further, a processing material input port 14 closed by an upper lid 13 is formed in a top plate 12 of the processing tank 1, and a material input hopper 9 which is freely moved by a rail 91 is provided at an upper portion thereof.
As shown in FIG. 6, the bottom curved plate 15 of the processing tank 1 is provided with a discharge port 17 closed by a lower lid 16. Here, the lower lid 16 has a structure in which a lid plate 16e is attached to a lower lid main body 16a, and an inner plate 16c corresponding to the curvature of the bottom curved plate 15 is provided.
Outside plate 16d having a larger area than its inner plate 16c
The lower lid body 16a formed by polymerizing and integrating is bent to the same curvature as the bottom curved surface of the processing tank 1.

In such a structure, a groove is formed between both ends of the inner plate 16c and the edge of the bottom curved plate 15 when the lower lid 16 is closed, and the groove is formed at the bottom of the treatment tank 1 during the fermentation treatment. The accumulated oil and moisture are removed from the groove b by the bottom curved plate 15 and the outer plate 16 as shown by the arrows in the figure.
Oil can be drained or drained by reaching the trough 16b through the contact surface with d, and when the lower lid 16 is removed, the opening can be used as it is as a material discharge port.

In the fermentation treatment of the present invention, the panel heater 11, the blower, and the stirring blade 3 are program-controlled by operating the operation switch of the control panel 6, so that the fermentation treatment can be performed fully automatically. I have.

Next, the operation of the fermentation treatment apparatus of the present invention will be described in detail.

In the pretreatment step, organic waste such as grass clippings is put into the treatment tank 1 together with fresh water and fermentation bacteria as a moisture content adjusting agent, and the stirring blade 3 is rotated by driving a motor, and the panel heater 11 is operated. While monitoring the detection signal of the temperature sensor 72, the heating is performed to the optimum fermentation temperature according to the processed material.

When the detection signal of the temperature sensor 72 reaches the optimum fermentation temperature, the rotation of the stirring blade 3 is stopped, and the air outlet 71 and the exhaust port 81 are closed to perform the mulling process.

In this mulling treatment, the emission of carbon dioxide generated from the mixed product in the fermentation treatment tank 1 is prevented, so that carbon dioxide having a higher specific gravity than air is stored above the mixed product layer and becomes a heat insulating layer. The mixture can be kept warm while being shielded from contact with outside air.

The release of carbon dioxide from the fermenter can be made to function as a simple leak valve by connecting a hose of an appropriate length downward at the end of the exhaust port 81. In such a leak valve, the property of carbon dioxide heavier than air can be used, and if the amount of generated carbon dioxide increases and the storage pressure exceeds a certain limit, it will be naturally discharged from the end of the hose, so It is always possible to store an appropriate amount.

In this state, if the mixed processed product is shielded from the outside air and maintained at a certain optimal fermentation temperature by the mulling process, the fermentation bacteria mixed in the mixed processed product will be placed in an environment where it is most likely to proliferate. And can be dramatically increased by so-called logarithmic multiplication. In addition, since the anaerobic bacterium increases and the aerobic bacterium dies if the mulling time is long, the leaving time is set to about 2 hours. In this mudification process, the temperature of the mixture can be kept at 37 ° C. to 40 ° C. by the heat of fermentation, so the panel heater 11 is stopped.

After logarithmic growth of the fermentation bacterium in this manner, the panel heater 11 and the blower are turned on and off while monitoring the detection signal of the temperature sensor 72 by rotating the stirring blade to ferment the actual temperature of the mixed product. Maintain the optimum temperature and continue the fermentation process.

That is, when the detection signal of the temperature sensor 72 falls below the optimum fermentation temperature, the blower is turned off and the panel heater 11 is turned on, and when the detection signal of the temperature sensor 72 rises above the optimum fermentation temperature, the blower is turned on. With the control to turn off the panel heater 11,
Such control is continuously performed until the mixed product reaches the optimum condition for the next composting process.

During the fermentation process, the stirring blade 2 is rotated forward and backward with a stop operation interposed therebetween. In the experimental example, the forward and reverse rotation times at this time were 15 minutes each, the stop time was 1 minute, and the rotation speed was 1 RPM.

At this time, air necessary for fermentation is simultaneously supplied to the mixed processed product by supplying air into the processing tank 1 from the air outlet 71 and discharging the air from the exhaust port 81 by the blower. The fermentation may be promoted by applying vibrations to the vibrating means.

After terminating the fermentation treatment in this way, the mixed treatment product is discharged from the discharge port, transferred to a composting treatment tank, and cut back as appropriate to supply fresh oxygen and contained in organic waste. After the fibers such as lignin and cellulose are fully ripened, and the fibers are completely ripened, they are sieved to remove impurities, and then used as a fertilizer or a soil conditioner.

FIG. 7 shows another example of a fermentation treatment apparatus constituting a main part of the system of the present invention.

In this embodiment, since one of the horizontal blades 31a disposed in the fermentation treatment layer 1 is disposed obliquely with respect to the other horizontal blade 31, the inclined horizontal blade 31a and the horizontal horizontal blade 31 In both cases, the mixture can be alternately stirred, and the stirring efficiency is further improved.

Further, after the fermentation of the mixed processed product, there is an excellent effect that the mixed processed product in the fermentation processing layer 1 can be discharged in a short time only by removing the lower lid (indicated by 16 in FIG. 6).

FIG. 8 and FIG. 9 show a schematic configuration diagram of the system of the present invention together with work procedures.

Organic waste m0, such as cut grass, is stored in a waste storage layer 101, and is input into a material input hopper 104 of a first transport means 105 constituted by a belt conveyor or the like by a loader 102 having a shovel 103 or the like. Then, the first transport unit 105
Transports the transported organic waste m0 and puts it through a material inlet formed in the upper part of the fermentation treatment apparatus A. During this process, foreign substances such as iron pieces and wires mixed by the metal sorting device 106 are removed by magnetic force.

Mixed processed product m1 fermented by fermentation processing device A
Is a second conveyor 10 constituted by a belt conveyor or the like.
By 7, it is sent to a box-shaped composting tank 108. As shown in FIG. 10, this composting treatment tank 108
The aeration pipe 109a is connected to an air source 109 such as a blower, and is configured to blow air from an injection hole 109b by controlling the opening and closing of a valve 110.

The mixed product m1 discharged from the discharge port of the fermentation treatment device A and transferred into the composting treatment tank 108 by the second transport means 107 is supplied from the one tank 108a of the treatment tank 108 to the other tank 108b. After being cut back by being transferred to a fermentation product, it is taken out as a fermented product m2 and used as a fertilizer or a soil conditioner.

[Effects] According to the method of the present invention proposed in claims 1 to 3, the organic wastes such as cut grass and defoliated leaves are efficiently pulverized by simply putting them into the fermentation treatment tank and stirring them. Fermentation can be carried out, and if the mixed processed product thus fermented is transported to a composting tank and matured, it can be matured in a very short period of about two months.

In addition, compared to the conventional fermentation treatment method, there is no cause of environmental deterioration such as emitting a bad smell, the fermentation treatment can be performed easily and quickly, and a high-quality fertilizer or soil conditioner can be easily obtained.

In particular, according to the method of the present invention proposed in claim 3, the fermentation treatment in the fermentation treatment step described in claim 1 can be performed evenly and more quickly.

Furthermore, according to the system of the present invention proposed in claim 4, since the fermentation treatment method proposed in claim 1 can be continuously and efficiently performed, a pollution-free waste treatment plant can be provided.

[Brief description of the drawings]

FIG. 1 is a flow chart showing a process procedure in the method of the present invention,
2 (a), 2 (b) and 2 (c) are a front view, a side view and a rear view showing the appearance of a fermentation treatment apparatus constituting a main part of the system of the present invention, and FIG. 3 is a transparent view of the fermentation treatment tank. FIG. 4 is a perspective view showing the appearance, FIG. 4 is a view showing the shape of the fermentation treatment tank, and FIG.
The figure is a longitudinal sectional view showing the inside of the fermentation tank, FIG. 6 is a longitudinal sectional view of the fermentation tank showing the structure of the discharge port, and FIG. 7 shows the internal structure of another example of the fermentation tank. FIG. 8 is a view for explaining the schematic configuration of the system of the present invention together with work procedures, FIG. 9 is an external view of a fermentation treatment apparatus used in the system of the present invention, and FIG. It is a top view. (Explanation of symbols) A: Fermentation treatment apparatus 1: Fermentation treatment tank 11: Heating means (panel heater) 3: Stirring blade 31, 31a Horizontal blade 32 Vertical blade 4: Muro chamber 5 ... Horizontal rotation axis 9 Material input hopper 14 Material input port S Material gap S First transport means 107 Second transport means 108 Composting tank

Continued on the front page (72) Inventor Mikio Mihara 354-48 Matsuodera-cho, Izumi-shi, Osaka (72) Inventor Jun Yamada 579-1 Kidoyamacho, Tondabayashi-shi, Osaka Remains K Heights 202 No. 56 (56) References JP-A-63-95186 (JP, A) JP-A-2-51485 (JP, A) JP-A-64-69585 (JP, A) JP-A-61-281091 (JP, A) JP-A-1-145388 (JP, A) JP-A-62-52194 (JP, A) JP-A-60-71584 (JP, A) JP-A-58-3695 (JP, A)

Claims (4)

(57) [Claims] 1. A batch fermentation treatment method in which an organic waste is charged into a fermenter, a series of fermentation treatments are performed, and then discharged from the fermentation tank to perform a composting treatment. Inject fermentation-rich organic waste into the fermenter, add fresh water and maintain a constant water content, mix with fermentation accelerators and fermentation bacteria, and heat to the optimal fermentation temperature while mixing and stirring. Then, stop mixing, stirring and heating, leave the mixed product in the fermenter in a state where it does not come into contact with the outside air for a certain period of time, perform mulling treatment, and logarithmically grow fermentative bacteria. After discharging the filled carbon dioxide, through oxygen, replenish fresh water to adjust the moisture content, mix and stir the mixed product, maintain the fermentation optimal temperature, and ferment for a predetermined time. Discharge the mixed processed product from the fermenter, and strengthen the discharged mixed processed product. A batch fermentation treatment method for organic waste, wherein a fermentation treatment product is obtained by performing composting treatment by performing ventilation and turning over for a certain period. 2. The method according to claim 1, wherein the fermentation product obtained by the batch-type fermentation treatment method for organic waste according to claim 1 is added to the fermentation tank as a fermentation promoter. Batch fermentation treatment method for waste. 3. The batch-type fermentation treatment method for organic waste according to claim 1, wherein the fermenter is vibrated when the mixed product is fermented for a predetermined time while maintaining the fermentation optimum temperature. 4. A first transfer means for transferring organic wastes rich in fibrous materials such as cut grass, defoliated leaves and the like, and a paddle type stirring blade is horizontally rotated so as to rotate along the bottom curved surface of the processing tank. Section U attached to the rotating shaft
Above the letter-shaped fermentation tank, a mudification chamber for storing carbon dioxide generated during the fermentation treatment of the organic waste is formed, and the upper part is transferred by the first transfer means. The fermentation treatment device has a material input port for inputting incoming organic waste, a material discharge port at the bottom, and an aeration pipe means for blowing air at the bottom. And a fertilizer treatment tank for storing the mixed treated material. The first transfer means removes fibrous organic waste such as cut grass and defoliated leaves together with a fermentation promoter and a fermentative bacterium. After the series and the processing steps described in claim 1 are executed, the mixed processed material discharged from the fermentation tank is transferred to the composting processing tank, and forced aeration and turning over for a certain period are performed. By doing Batch fermentation system of the organic waste and performing Koeka process.