JP2005298292A - Apparatus for treating organic waste - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To compost an organic material or organic waste having high water content such as garbage by quickly treating without producing odor or sewage. <P>SOLUTION: The organic material or the organic waste is treated to be decomposed by fermenting the organic material or the organic waste with actinomyces while ventilating air in a stirring fermentor formed of a porous material, cooling the gas producing odor, moisture or the like, returning the hot air with the condensed water separated to the stirring fermentor to remove the odor and repeating the process. The decomposed material is used as a high quality compost. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

  The present invention relates to an organic waste processing technique, and can provide a technique for rapidly composting organic waste such as garbage.

  According to the present invention, organic waste can be processed efficiently and quickly, for example, composting of garbage can be performed quickly and compactly, and the generation of malodor is suppressed, so a small factory In addition to hotels, restaurants, homes, hospitals, schools, etc., compost production and / or waste disposal can be carried out in relatively small facilities such as farmers, greengrocers, fish shops, supermarkets, etc. ing.

  Composting is known as one of the methods for treating organic waste, but compost has traditionally been manufactured by depositing compost raw materials such as straw and livestock excrement and turning it back as necessary. . Therefore, the production of compost not only took a long time, but also the generation of bad odor and fly was unavoidable, causing secondary pollution.

Therefore, the present inventor succeeded in controlling fly by spraying actinomycetes or actinomycete cultures on the fly generation area as a result of examination and research from various directions (see Patent Document 1). There have been no reports of successful treatment of garbage or other organic waste quickly and efficiently, for example in composting, in a processing device rather than in the open outdoors while suppressing the generation of malodors. .
Japanese Patent No. 3075857

  The present invention has been made in view of the current state of the art, and treats various organic wastes including organic wastes with high water content such as garbage in a short period of time without generating malodors. This was made for the purpose of developing a new technology for efficiently producing compost and the like.

  The present invention has been made in order to achieve the above-mentioned object, and since garbage and the like have a high water content, incineration treatment is not suitable. Actinomycetes were selected from among the microorganisms. And after depositing garbage in the open air according to the usual method of compost production, inoculating actinomycetes on it and fermenting it, not only generated a lot of bad odor with a lot of steam, but also sewage leaked out The occurrence of secondary pollution was confirmed, and it was confirmed that implementation in urban areas was particularly inappropriate.

  However, since a large amount of garbage is discharged from hotels, restaurants, supermarkets, etc., it is strongly desired to process this in the facility, and since secondary pollution occurs, processing in urban areas is not In spite of being unsuitable, the present inventors dared to develop an organic waste treatment system using actinomycetes that can be carried out in urban areas.

  And as a result of investigations from various directions, the present inventors housed garbage and actinomycetes in a cylindrical body with a net, and stirred, aerobic fermentation accompanied by fever by actinomycetes was performed abundantly, Not only composting is possible in a short time of only 4-5 days, but a large amount of steam and odor are generated by the heat of fermentation, but by cooling these gases, moisture is separated as condensed water, When the dehumidified gas was returned to the cylindrical body again, it was confirmed for the first time that it was deodorized unexpectedly.

The present invention has been made on the basis of these useful new findings, in which organic waste is aerobically fermented with actinomycetes in a stirred fermenter having a vent, and at this time, decomposition of organic substances by actinomycetes is performed. Steam and odor are also generated due to fermentation heat, and deodorized by returning the gas after cooling and dehumidifying it to the stirrer-fermenting tank containing actinomycetes, thereby efficiently treating organic waste for a short period of time By repeating this cycle more than once if necessary, it can be complicated in a compact device without causing pollution in facilities such as hotels and restaurants or in the vicinity of the facility. It is possible to efficiently process without requiring an operation.
Hereinafter, the present invention will be described in detail.

  An example of an apparatus for carrying out the present invention is shown in the accompanying drawings, and garbage is taken as a representative example as organic waste, and the present invention will be described in detail below.

  The organic waste treatment apparatus according to the present invention is mainly composed of an organic waste crushing inoculum inoculation apparatus A, an agitation fermenter B made of a material having an aeration part, and a dehumidification deodorization apparatus C (FIG. 2). Each of these devices may be provided integrally or detachably, and a moving means such as a caster may be attached. FIG. 1 shows an overall view of assembling these devices.

First, the organic waste crushing inoculum inoculation apparatus A will be described.
This device crushes organic waste such as garbage and adds and mixes actinomycetes, and includes all devices having such actions. One example is shown in FIG. In the drawing, (A-1) is a top view, (A-2) is a side sectional view, and (A-3) is an end view.

  Organic waste crushing inoculum inoculation device A has an inlet (hopper) H for feeding organic waste such as garbage and actinomycetes (including broadly including actinomycete cultures, reusable inoculum and other actinomycetes-containing materials), The pulverizing and inoculating device S for crushing, mixing, and inoculating the inoculum, and a power M such as a motor for driving the inoculating device S. These are attached to the frame F, and the frame F is provided with moving means W such as casters (wheels). The frame F can be a box.

  The pulverizing and inoculating device S is composed of two screws rotating in opposite directions, and moves the raw material charged from the hopper H to the outlet while pulverizing and mixing it. The height is continuously increased from the lower part of the hopper H according to the direction of the outlet D (that is, the gap between the screw blade and the inner wall of the pulverization inoculation apparatus S is narrowed) to enhance the effect. I have to.

  Further, as the pulverizing and inoculating device S, a rotating shaft is rotatably provided instead of a screw, and a cutting blade having a sharp edge and a breaking blade having a blunt edge are respectively provided from the hopper H side to the outlet D side. And one or more discharge plates for discharging from the outlet D to the outside may be provided on the side closest to the outlet.

  The attachment angle of these blades can be appropriately changed according to the purpose. In addition, the size of the blade edge can be changed as appropriate, but generally, in the case of a sharp cut blade, the blade edge should be 1.0 mm or less, preferably 0.5 mm or less. The blunt edge is 0.1 mm or more, preferably 0.5 mm or more. In addition, the mounting state of these rotary blades may be three, four, or five, two, or six or more if desired. The mounting of these rotary blades may be firmly fixed so that the rotary blades do not vibrate, but the mounting portion is installed so that the tip of each blade swings about 1 to 8 cm, preferably about 2 to 5 cm, The impact may be reduced as much as possible.

  In the present invention, it is preferable to use a cutting blade and a crushing blade in combination. For example, when cutting organic (waste) sharply with only the cutting blade, it is shredded, but it becomes anaerobic and cut to some extent. If it crushes with the crushing blade which has a blunt edge later, it will be shredded and will contain air, and it will become an environment suitable for growth of the inoculum which is an aerobic microbe (actinomycetes). As a result, the growth of inoculum is promoted and composting progresses, and high-quality compost is obtained.

  In addition to the above, any device that can crush and mix organic waste (and actinomycetes) and inoculate the inoculum can be used, for example, chopper, crusher, mixer, mince, chopping machine, Disposers, extruders, etc. can be used.

Next, the stirred fermenter B will be described.
The stirred fermenter B has a cylindrical body 1 made of a material having an aeration part installed in a horizontal shape, a stirring device 2 provided therein, and the whole is accommodated in a housing 3 if desired. .

  The cylindrical body is a cylindrical body having a triangular to polygonal cross section, and a cylindrical body having a circular cross section is illustrated in the drawing. The cylindrical body is made of a material having a ventilation part, and any material having a hole (a ventilation part) through which air and various gases can pass without allowing crushed organic waste to pass through. For example, a net, a perforated plate, or the like can be used. The pore diameter is usually 5 to 100 mesh, preferably 10 to 75 mesh, and more preferably about 10 to 50 mesh.

  The material having these ventilation portions (hereinafter also referred to as a breathable material) may form a cylindrical shape only with this material, or the frame (1-1, 1- 1) to be a cylindrical body in advance. 2, 1-3, etc.) may be provided in an appropriate number, and a breathable material may be stretched thereon. In addition to a single breathable material, it may be double or more as desired, and the same material may be used, and different materials may be used to create a hybrid structure. You can also In this example, a double-equipped net-stirring fermenter with double nets was used. As the material of the breathable material, plastic, stainless steel, various metals, and other appropriate materials can be used.

  The entire cylindrical body may be made of a breathable material. However, even if the entire cylindrical body is filled with organic waste without providing a gap, the stirring is sufficiently performed. In addition, since aeration is not sufficient, fermentation by actinomycetes may not be performed sufficiently, so that organic waste is not filled densely over the entire cylindrical body, and is left in a space. Is preferred. It is preferable that at least the lower half of the cylindrical body is made of a gas permeable material and the upper part has an open structure. In this embodiment, an air-permeable material is not used for the upper part of about 1/3, and an open structure is used (FIGS. 1 and 4). The cylindrical body 1 is provided with a supply port 4 for disrupting actinomycetes-containing crushed organic waste supplied from the outlet D of the disrupted inoculum A in the upper part on the upstream side (in the case of an open structure, the supply port The discharge outlet 5 is provided in the lower part on the downstream side thereof. W is a caster.

  The stirring device 2 is provided with stirring claws 7-1, 7-2, 7-3,... Around a rotating shaft 6 driven by power M such as a motor. The stirring claw may be a normal stirring blade, but may have a propeller structure with a pitch so that the contents can be moved downstream.

  The cylindrical body is accommodated in the housing 3 as desired. The housing 3 is provided with an opening for the outlet D communicating with the supply port 4, a gas outlet 8, and an opening 9 for the blower of the dehumidifying and deodorizing device C. Although both end views of the housing 3 are shown in FIG. 4, as shown in the drawing, a part of the housing 3 may be opened and closed for the purpose of dehumidification or the like when the temperature in the housing 3 is increased by fermentation heat. Moreover, if the housing 3 is made of transparent plastic or the like, not only the inside can be observed, but also solar heat can be used when installed outdoors, and the fermenter can be heated. it can.

And the dehumidification deodorizing apparatus C is demonstrated.
The dehumidifying and deodorizing device includes a connection pipe 51 connected to the gas outlet 8 of the stirred fermenter B, a hot air blower device 52 provided at the lower portion thereof, and a fermentation drying device (or actinomycetes deodorizing device) 53 if desired. To do. The connection pipe 51 takes out the gas (including moisture and odor) generated in the stirred fermenter B, returns it to the stirred fermenter B, and further deodorizes it. The gas may be returned as it is, but it is more preferable to cool the gas and blow a dehumidified gas (hot air). Although the gas is cooled only by taking it out of the housing, a cooling fin, a cooling bellows or the like may be installed as desired in order to further promote this.

  A hot air blower 52 is provided below the connection pipe (or cooling pipe) 51. The gas taken out from the outlet 8 is directly returned to the fermenter B through or without the actinomycetes deodorizing device 53 and used for deodorization or the like. During the passage of the connection pipe 51, the gas is usually cooled and the condensed water is stored at the bottom of the hot air blower 52. The gas thus dehumidified (usually still hot air) is sent to the actinomycetes deodorizing device 53 by the fan Fa.

  The actinomycete deodorization device 53 is divided into upper and lower parts by a partition plate 54 having a breathable structure such as a net, and the organic waste after fermentation treatment taken out from the discharge part outlet 5 is placed in the upper part. The section is detachably connected to the hot air blowing device 52. By blowing warm air to the waste, deodorization of the waste is further promoted by the action of actinomycetes and a good compost product can be obtained. This may be pulled out of the housing by a caster to make a product. Moreover, the gas which passed this actinomycete deodorizing apparatus 53 contains actinomycetes, and deodorization and decomposition | disassembly of organic waste are further accelerated | stimulated by returning this in the fermenter B. Therefore, this dehumidification deodorization apparatus C can also be called a circulation type dehumidification deodorization apparatus.

  Another embodiment of the dehumidifying and deodorizing apparatus C is shown in FIG. A large number of partition plates 64 are provided on a net (not shown) of the actinomycete deodorizing device 63, a heating wire 65 is provided between them, and fermented organic waste is placed thereon, and a thermostat 66 is provided. It is operated and heat-treated. The operation is the same as that described in the apparatus of FIG. 5, but according to this apparatus, the fermentation drying is further promoted. It can also be used to finish products.

  The operation of this apparatus is as follows. That is, garbage and actinomycetes are introduced from the inlet H, and the garbage is crushed and mixed through the rotary pulverizing inoculation device S, and thoroughly mixed with actinomycetes to inoculate and inoculate. It is introduced into the cylindrical body 1 through the supply port 4.

  In the cylindrical body 1, the contact between the actinomycetes and the air is increased by being stirred by the stirring claws 7, and the air permeability is further enhanced through the net, and the fermentation by the aerobic actinomycetes is promoted to generate heat and the organic matter is decomposed. At the same time, moisture (steam) and odor are generated. These gases are sent from the housing 3 to the cooling pipe 51 through the gas outlet 8. On the other hand, the organic waste moves in the cylindrical body 1 in the direction of the discharge outlet 5 and the organic matter is decomposed during that time, so that the treated organic waste is sequentially deodorized actinomycetes from the discharge outlet. Take out to device 53.

The dehumidified hot air blown from the hot air blower 52 passes between the treated organic wastes placed on the partition plate 54 and returns to the cylindrical body 1 while containing actinomycetes. Is done. Then, the organic waste is further decomposed and deodorized by the action of actinomycetes (the detailed mechanism must be studied in the future). The organic waste after this treatment is used as a compost product, but since it contains actinomycetes, it can be called actinomycete culture, and part of it is returned to the hopper H as a reusable inoculum and recycled. In addition to being able to use it, it can also be used to adjust the moisture content of food waste. For example, food waste (water content of about 90%) is adjusted to 15-20% water, and the number of actinomycetes is also 2-8 × 10 ⁸ / g.

  When 20 kg of the reused inoculum and 40 kg of garbage obtained in this way were processed in a fermenter in a housing of 2.8 m in length and 1.4 m in height, it was processed with a short stay of only 5 to 6 days. Was finished and good compost was obtained. Meanwhile, the generation of malodor was suppressed and the water was removed as condensed water. The size of the cylindrical body is, as a non-limiting example, a diameter of 0.5 to 2 m, preferably 0.8 to 1 m, and a length of 1.5 to 8 m, preferably 1.8 to 4 m. It is not limited.

  The gas taken out from the gas outlet 8 of the housing passes through the pipe 51 and is cooled during that time to be separated into condensed water and hot air, and the hot air passes through the treated organic waste on the partition plate 54. Then, after further performing at least one action such as deodorization, dehydration, aging, etc., it is returned to the tubular body 1 and decomposed organic waste by the action of actinomycetes contained in the warm air, Deodorization is further promoted. The condensed water can be discharged as it is.

  What is treated in the present invention is an organic material, and various organic materials including organic waste such as garbage are widely included. Non-limiting examples thereof include the following.

  Food waste, leftover food and other unwanted foods discharged from restaurants and hotels, waste discharged from food manufacturing factories, various food manufacturing jars, fermented jars such as beer jars, internal organs of livestock and seafood and other inedible parts, Agricultural production by-products such as straw, pruning waste from weeds and trees, dairy farms, emissions from fish and vegetable markets, etc. Small, selected or non-standard crops, fruit trees, flowers, seafood.

In the present invention, actinomycetes and, if necessary, molds are used in combination.
As the actinomycetes, any of high-temperature, medium-temperature, and low-temperature actinomycetes can be used singly or in combination. For example, the following actinomycetes are exemplified: 13344, Streptomyces thermophilus ATCC 19822, etc.), Nocardia (Nocardia erythropolia IFO 12682, etc.), Micromonospora genus (such as Micromonospora purpures ATCC 15835), Actinomyces (Actinomyces griseoruber ATCC 12466, etc.), Akuchinobifida genus (Actinobifida dichotomica FO 2466, etc.), thermo-actinomycin Mrs. genus (Thermoactinomyces glaucus IFO 12530, etc.), such as thermo-mono Supora belonging to the genus (such as Thermomonospora viridis IFO 12207), and the like.

Any actinomycetes can be used as long as it can decompose organic matter such as garbage. In addition to the above examples, actinomycetes exemplified below can be used singly or in combination of two or more:
Streptomyces griseolas IFO3402, Streptomyces griseus IFO3119, Streptomyces griseus IFO3102, Terumoactinomyces bulgaris IFO12516, Micromonospora brune IFO14069, Thermomonospora husca IFO14071 etc. can be used as suitable bacteria It is.

  The fungi may be bacteria of any genus as long as they can decompose organic matter such as garbage. Examples include Penicillium genus (Penicillium chrysogenum IFO4626), Aspergillus genus (Aspergillus niger IFO4407, Aspergillus awamori IFO4033, Aspergillus candidas IFO 4311 etc.).

  As the inoculum used in the present invention, only one of actinomycetes and / or fungi may be used, but two, three or four species selected from high temperature actinomycetes, medium temperature actinomycetes, and low temperature actinomycetes are used. The above may be used, and Aspergillus niger or the like may be mixed therewith. The inoculum or mixed inoculum is suspended in water, sprayed on cow dung medium, and sufficiently proliferated by culturing for about 5 to 15 days at about 25 to 35 ° C. while stirring about 1 to 3 times a day. The proliferated one can be used as an inoculum for the main culture while maintaining the medium. Of course, in addition to the above, a medium commonly used for culturing actinomycetes can also be applied and used as the medium.

  As an inoculum, the culture and / or isolated cells themselves cultivated as described above can be used, those taken out from the discharge outlet of the stirred fermenter, those staying in the tank, or Those treated with an actinomycete deodorization device or an electrolyzed fermentation drying device, or product compost can also be used, and can also be used in combination with the culture (and / or isolated fungus).

These inoculums can be mixed with other microorganisms as long as the total number is 0.5 × 10 ⁶ / g or more (preferably 2 × 10 ⁸ / g or more).

  According to the present invention, even organic waste such as garbage with a high water content can be decomposed and composted in a very short period of time (for example, 5 to 6 days). Since generation of steam (moisture) is also suppressed, combined with downsizing and downsizing of the apparatus, waste treatment can be performed without causing secondary pollution even in urban areas.

  In addition, the present invention basically uses heat generated by actinomycetes (thermophilic, mesophilic, and thermophilic), thus saving energy and using solar energy. Since warm air and inoculum can be reused, waste treatment can be carried out at an extremely low cost, which is excellent in that it does not require much labor and delicate operations.

Examples of each of the devices A to C and the overall effect are as follows.
(Effect of A)
1. Inoculate actinomycetes with deodorizing power and fly killing power at the same time as garbage crushing to promote fermentation.
(Effect of B)
2. The interior net fermenter increases the activity of aerobic actinomycetes and completes fermentation in 60-70 ° C for 3 days.
3. The external equipment of the net-stained fermenter uses transparent plastic and utilizes sunlight.
(Effect of C)
4). Circulating dehumidification and deodorization equipment is reused for deodorization by actinomycetes and ripening of compost, and partly for inoculation and moisture adjustment.
(Overall effect)
5). Energy saving, foul odor prevention, rapid compost production, and compact device invention by utilizing fermentation heat, solar heat, double heat insulation, air convection, deodorization, fly insect sterilization.

  Examples of the present invention will be described below, but the present invention is not limited to these examples.

  Using Streptomyces griseolus IFO 3402 as actinomycetes, garbage was treated with the organic waste treatment apparatus according to the present invention.

20 kg of actinomycete culture was inoculated into 40 kg of food waste at a restaurant, and crushed and inoculated every day with the A apparatus at a rate of 20 kg, and put into the fermentation apparatus B (tubular body: diameter 1 m, length 3 m). In order to promote fermentation, the stirring material is stirred for 10 minutes at a rate of 2 revolutions / minute with the power of the B apparatus, and after standing for 12 hours, a timer is added to make the air supply and moisture uniform. And rotated at a rate of 2 revolutions / minute for 10 minutes. This operation was continued for 5 days.
As a result, the product temperature of the first day input reached 60 ° C. after 20 hours, reached the maximum temperature of 70 ° C. after 2 days, decreased to 50 ° C. after 3 days, and decreased to 30 ° C. after 5 days. Six days later, about 40 kg was discharged from the outlet of the B apparatus to the C electroplate fermentation drying apparatus.
In the C apparatus (FIG. 6), when the bed temperature was adjusted to 40 ° C. to 60 ° C. and treated for 2 days, about 30 kg of compost having 20% moisture and 2-8 × 10 ⁸ / g actinomycetes was obtained. About 20 kg of this high-concentration actinomycete compost was used as an inoculum and used again for 40 kg of new garbage. The remaining 10 kg was used as compost after further treatment for 5 days in the C apparatus. In addition, the electrothermal temperature of this C apparatus works effectively with the childcare temperature of B apparatus.

  This treatment method was carried out continuously for 50 days. Meanwhile, the generation of malodor was reduced by the ability to assimilate actinomycetes, and the chitin of fly insect eggs and rice husks were decomposed by the action of actinomycetes, so that no adult flies were generated. On the other hand, the first, 15th and 30th changes in the lower fatty acid of this continuously treated product were measured with a gas chromatograph, and the results are shown in FIGS. As a result, the odor almost disappeared after the 5-day treatment for the B device and the 5-day treatment for the C device at any time. In the figure, ACETIC represents acetic acid, PROPIO represents propionic acid, ISOBUT represents isobutyric acid, BUTYRI represents normal butyric acid, ISOVAI represents isovaleric acid, VALERL represents normal valeric acid, and ISOCAP represents isocaproic acid.

When the same treatment as in Example 1 was carried out using the mixture of cattle feces culture of the following actinomycetes (total number of bacteria 5 × 10 ⁸ / g) as the inoculum instead of Streptomyces griseolus IFO 3402 Compost was obtained.

  Streptomyces griseus IFO3102, Terumoactinomyces monospors IFO14050, Micromonospora brune IFO14069, and Thermonospora fusca IFO14071.

It is a partially cutaway side view of an organic waste disposal apparatus. It is an exploded view of an organic waste disposal apparatus. The garbage crushing inoculum inoculation apparatus A is shown. The both end surfaces of a double-equipped net-stirred fermenter are shown. The circulation type dehumidification deodorizing apparatus C is shown. Fig. 2 shows an electrobed fermentation drying apparatus. It is a gas chromatogram (first time) of lower fatty acids during the production of food waste (including 10% waste fish) compost by selected actinomycetes. It is a gas chromatograph (15 consecutive treatments) of lower fatty acids during the production of food waste (including 19% waste fish) compost by selected actinomycetes. It is a gas chromatograph (30 times continuous treatment) of lower fatty acids during the production of food waste (including 30% waste fish) compost by selected actinomycetes.

Claims (15)

  Stirring made of a material having a ventilation part and having a cross section of a triangle, polygon, or circle in a horizontal shape, and stirring organic waste and actinomycetes contained therein An apparatus for treating organic waste, comprising an apparatus for fermenting organic waste while ventilating and treating with at least one action of heat generation, dehumidification, and deodorization.   The apparatus according to claim 1, wherein at least a lower half of the cylindrical body is made of a material having a ventilation portion.   A cylindrical body made of a material having a ventilation section and having a workpiece supply section and a workpiece discharge section is arranged in a horizontal shape, and organic waste and actinomycetes that are the workpieces supplied from the workpiece supply section are disposed. A stirrer for stirring is provided in the housing, and this is accommodated in the housing, the organic waste is fermented and decomposed by actinomycetes, and a gas outlet for taking out the gas generated at that time is installed in the housing. An organic waste processing apparatus, characterized in that a stirring fermenter is formed by connecting this to a pipe provided outside the housing.   The apparatus according to any one of claims 1 to 3, wherein an organic waste-disrupting inoculum inoculation device provided with a hopper and crushing and mixing means is arranged on the upstream side of the stirred fermenter.   The dehumidification and deodorization device according to claim 3, wherein the connection pipe is provided with a cooling portion and a condensed water outlet and a blower device are provided at a lower portion thereof, and the warm air separated from the condensed water is returned into the housing. The device according to the same item, characterized in that   6. The apparatus according to claim 5, wherein the treated organic waste is interposed in the middle of returning the warm air to the cylindrical body in the housing.   A condensate outlet and a blower are installed at the bottom of the cooling pipe that extracts and cools the gas generated when treating organic waste with actinomycetes, and organic waste that has been treated with hot air from which condensed water has been separated is placed. An organic waste treatment apparatus comprising: an actinomycete deodorization apparatus which is further deodorized by blowing air from a lower portion of a perforated tray placed thereon.   The apparatus according to any one of claims 3 to 7, wherein a stirring fermenter, an organic waste-destroying inoculum inoculation apparatus, and a deodorization apparatus are connected and arranged integrally or detachably.   The apparatus according to claim 8, further comprising a caster.   The organic waste processing method characterized by processing organic waste using the apparatus of any one of Claims 1-9.   The method according to claim 10, wherein dehumidification or deodorization is also performed.   The method according to claim 10 or 11, wherein the treatment is performed continuously or repeatedly. The method or apparatus according to any one of claims 1 to 12, wherein the organic waste is at least one of the following organic waste or organic matter.
Food waste, leftover food and other waste foods discharged from restaurants and hotels, waste discharged from food manufacturing factories, various food manufacturing jars, fermented jars such as beer jars, internal organs of livestock and seafood, and other inedible parts, Agricultural production by-products such as straw, weed and tree pruning waste, dairy farms, emissions from fish and vegetable markets and other small, sorted or non-standard crops, fruit trees, flowers, seafood, livestock excrement , Pet excrement, barn waste.   The method according to any one of claims 1 to 2, wherein one or two or more microorganisms belonging to Streptomyces, Nocardia, Actinomyces, Actinobifida, Thermomonospora, Thermoactinomyces, Micromonospora are used as actinomycetes. Or device.   The method or apparatus according to any one of claims 1 to 14, characterized in that the treatment of organic waste is compost production.

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