JP2000197873A - Treatment of organic waste - Google Patents

Abstract

PROBLEM TO BE SOLVED: To treat org. waste within a short time. SOLUTION: In a method housing a material 2 to be treated comprising org. waste in a treatment chamber 5 for housing and treating waste to treat the same under stirring, an accelerator 3 comprising a holding material on which many kinds of minerals accelerating the decomposing action of the material 2 to be treated are preliminarily held is brought into contact with the material to be treated or mixed therewith under stirring to perform treatment. The accelerator 3 is desirably composed of biological minerals extracted from many kinds of organisms and biological minerals are further added to ceramic to form the holding material.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating an organic waste, in which a treated product composed of organic waste and an accelerator composed of minerals for accelerating the decomposition action thereof are supplied into a treatment chamber to treat the treated product. .

[0002]

2. Description of the Related Art Conventionally, garbage discharged in the fields of households and food processing industries is reduced in volume or made into a fertilizer, or composted from livestock dung, into a fertilizer such as pellets, and other organic wastes other than incineration. In the treatment of materials, water conditioning materials such as treated materials and sawdust, accelerators such as minerals that promote fermentation and decomposition of treated materials, and soil bacteria or special A method and an apparatus are known in which fungi (microorganisms) are charged and stirred at room temperature or under constant heating conditions while supplying air or moisture as needed.

[0003] Specific examples of the above-mentioned prior art include the following in the decomposition or annihilation (reduction) processing technology. (1) Patent No. 2,504,364 A technology for decomposing coal-based and livestock wastes by dissolving mineral components from rock-forming substances such as andesite and soil bacteria from humus. (2) JP-A-6-170349 A method of dissolving garbage by adding a soil activating mineral eluent such as barley stone, a soil bacterium and wood chips to slurryed garbage. (3) JP-A-8-80481 A method in which mineral water such as natural ore or calcium eluted from the ore, a water regulating material, edible waste oil and the like are added to garbage and microbial decomposition is carried out with stirring. (4) Japanese Patent Application Laid-Open No. 9-1116 This is a method of mixing and agitating a filler in which microorganisms inhabit garbage and decomposing the same with microorganisms. The used filler can be used as a fertilizer or a soil improving material. Method. The filler is a material obtained by reducing the volume of an organic material such as a resin or a vegetable fiber material and solidifying the material, and adding a particulate material of igneous rock or a fired sintered body to the material to elute mineral components. Is included.

[0004] In addition to the above, there are the following specific examples of a method for producing an organic fertilizer by fermenting an organic waste or the like or producing an auxiliary material for fertilizing. (5) JP-A-55-140789 A method of mixing a plant seaweed enzyme and calcium such as fish bone, a mineral mainly composed of magnesium chloride extracted from seawater, and a trace amount of potash. (6) JP-A-4-193788 A method in which fungi and the like are added to minerals such as livestock dung, sawdust, rice bran, charcoal powder, and wood ash to ferment rice straw and dead grass. (7) JP-A-7-48193 A method in which garbage and water are added to waste paper to form a paste, and fermentation is performed by adding microorganisms containing EM bacteria to mineral ore (quartz diorenite, green stone, akaishi) powder. .

[0005]

All of the above-mentioned methods for treating organic waste use minerals as accelerators for decomposition and fermentation, and the use of minerals is understood to be an indispensable technical factor. However, among the above methods (1) to (4),
(7) uses a specific natural ore as a mineral eluting material. Natural ore is difficult to obtain and costs due to the location and distribution of the material, and natural ore is a type of mineral. And the content is limited and non-uniform, so that there are drawbacks in that the expected effects cannot be obtained or the stability of the action is lacking. In addition, in order to elute mineral water from these ores, there is a drawback that an operation or an apparatus for elution is required during treatment.

Further, in the above methods (5) and (6), magnesium chloride or wood ash extracted from seawater is used as a mineral, but the type and amount of the mineral are limited, and the decomposition promoting action depends on the treatment target. In addition, there is a disadvantage that the action of promoting the decomposition of the mineral component is poor and that the mineral component cannot be used repeatedly.

[0007]

SUMMARY OF THE INVENTION In order to solve the above-mentioned conventional problems, an organic waste treatment method according to the present invention comprises a first method.
In the method of storing the processed material 2 made of organic waste in the processing chamber 5 for storing and processing the waste, and treating the processed material 2 while stirring the same, various types of materials that promote the decomposition action of the processed material 2 are provided. The process is characterized in that the accelerator 3 made of a holding material preliminarily loaded with a mineral is brought into contact with or mixed with the processed material in the processing chamber 5 for processing.

[0008] Second, the accelerator 3 is characterized in that it is a biological mineral extracted from various kinds of organisms.

Thirdly, the accelerator 3 is characterized in that it is a holding material in which biological minerals are contained in ceramics.

Fourth, the accelerator 3 is characterized in that it is a holding material made of a mineral to which biological minerals are attached or adsorbed.

Fifth, the deodorant is supplied directly to the processing chamber 5 or contained in or held in a holding material.

Sixth, the process 2 or the inside of the processing chamber 5 is heated to promote the decomposition action.

Seventh, the invention is characterized in that the water content of the processed material 2 is adjusted in order to promote the decomposition action of the processed material 2.

Eighth, an adjusting material 6 for adjusting the water content is introduced into the processing chamber 5 and is made of a material having water absorbency and water retention and evaporating water contained by heating.

Ninth, the adjusting material 6 is made of a material containing plant fibers.

Tenth, the processing chamber 5 is provided with a discharge port 55 for discharging gas generated in the processing chamber 5.

Eleventh, in the processing chamber 5, a plurality of sinks 9b
It is characterized in that the processed products 2 discharged from the group are collected and processed.

Twelfth, the invention is characterized in that the undeleted residue remaining after the treatment of the treated material 2 is used as an accelerator 3 in the treatment of another treated material.

Thirteenth, the addition of unremoved residue remaining after the treatment of the treated material 2 or the use of water brought into contact with the unremoved residue as an accelerator 3 for the treatment of another treated material is described. Features.

[0020]

An embodiment of the present invention will be described with reference to the drawings. Reference numeral 1 denotes a processing apparatus according to the present invention, which decomposes (decomposes) an organic waste (processed product) 2 to be discarded by a processing method of the present invention while stirring and mixing with an accelerator 3 composed of minerals for promoting a decomposition action. (Vaporization) and annihilation processing. As shown in FIGS. 1 and 2, a processing apparatus 1 shown in this embodiment is formed so as to accommodate a processed product 2, an accelerator (minerals) 3, an adjusting material 6 as a medium of the accelerator 3, and the like. A box-shaped processing chamber 5, a stirrer 7 that stirs and mixes the processed product 2, the accelerator 3, the adjusting material 6, and the like in the processing chamber 5 to uniformly distribute the processing chamber 2,
It comprises a temperature controller 5a comprising a heater or the like for maintaining the internal processing temperature at a predetermined temperature by means such as heating adjustment, and an auxiliary device 8 described later. In this embodiment, sawdust is used as the adjusting material 6, but a wood chip or a fibrous material similar to conventional ones may be used to assist the decomposition.

On the right side of the processing chamber 5, a drive motor 71 for connecting the stirrer 7 to the rotating shaft 70 to stir at a predetermined rotation and an auxiliary machine 1 for accommodating an auxiliary device 8 and the like to be described later.
a, and a control panel 1b for controlling the operation of each device. The processing chamber 5 in the illustrated example has a box-shaped body 51 having an opening formed with a waste input port (supply port) 50 above.
Inside, two stirrers 7, 7 provided with a helical body 72 of a known configuration having a diameter of about 50 to 60 cm on a rotating shaft 70 via a plurality of support rods, are supported in parallel in the front-rear direction and forward and reverse. By being rotatably provided, the processed material 2 can be rotationally moved while being uniformly and satisfactorily stirred and mixed into the base material including the accelerator 3 and the adjusting material 6 and the base material. In addition, the inlets 50 are provided with lids 52, 52 disposed above the respective stirring bodies 7, 7 so as to be openable and closable in the direction of the arrow (FIG. 1) with the inside as a fulcrum.

Further, the processing chamber 5 is made operable while maintaining an appropriate processing temperature by a temperature control device 5a, so that the decomposition processing of the processed material 2 can be favorably promoted. That is, on the back surface of the inner wall 53 of the processing chamber 5 which is formed in a curved shape along the rotation trajectory of the stirrer 7, a heater 5 b composed of a planar heating element of the temperature control device 5 a is provided, and the processing chamber 5 is provided. A temperature sensor 5c is provided in a space inside the heater, and the heater 5b is controlled by the control panel 1 based on temperature detection by the temperature sensor 5c.
By controlling the temperature of the inner wall 53 to be heated by operating it according to the command of b, the processing temperature in the processing chamber 5 is maintained at a predetermined level, and the organic waste 2 is decomposed satisfactorily. The side wall of the machine surrounding the processing chamber 5 is heat-insulated with a suitable heat-insulating material, and the temperature control device 5a is used.
The method is not limited to the above, and a method of sending hot air from the air outlet 56 may be used.

The gas generated when the processing object 2 is decomposed in the processing chamber 5 has a lid 52 formed in an inverted mountain shape in a side view.
Although it is possible to smoothly discharge the gas through the exhaust port 55 provided on one side of the top portion, the processing method according to the present invention does not usually generate a significant odor as described later.
The structure is simple and inexpensive without any special deodorizing device. Further, a discharge trough 57 in the shape of a saucer is provided in the upper central portion of the processing chamber 5 so that the steam generated in the processing chamber 5 is discharged as water droplets to the outside of the apparatus to facilitate humidity control of the base material. I have to.

Reference numeral 58 denotes a delivery pipe provided in the upper central portion of the processing chamber 5. The delivery pipe 58 communicates with a delivery device 80 including a tank and a pump provided on the auxiliary machine body 1 a side. The apparatus 80 is configured to be able to automatically or manually supply water for humidity adjustment or water containing the accelerator 3 to the base material in the processing chamber 5 as appropriate. Thereby, replenishment of water and the accelerator 3 can be performed simply, appropriately and efficiently without opening the lid 52 during operation.
In addition, the feeding device 80 in this embodiment generates biological mineral water by contacting and passing water through a holding material containing biological minerals, which will be described later, and outputs the mineral water from solid biological minerals through the delivery pipe 58. By supplementary supply together with the accelerator 3, the supplementary supply can be easily performed and active processing can be performed.

The feeding device 80 is not limited to a liquid type, and can appropriately feed a powdery or granular accelerator 3 or an accelerator 3 formed on a holding material described later. Is also good. Reference numeral 58a denotes a delivery pipe which is provided horizontally above the delivery pipe 58 and communicates with the upper feeding device 80. The delivery pipe 58a is provided with the accelerating agent 3 or the adjusting material 6 accommodated in the feeding device 80. Alternatively, or in a state where both are mixed, the processing chamber 5 can be appropriately replenished.

Reference numeral 51a denotes a maintenance outlet provided so that the contents can be taken out from the bottom of the processing chamber 5. The processing apparatus 1 is capable of freely adjusting the number of rotations and the operation pattern of the stirrer 7 and the adjustment width of the set temperature of the temperature control apparatus 5a, and can also be performed by a conventional processing method using microorganisms. And organic waste can be treated.

Next, a method for extracting biological minerals and a holding material for biological minerals used in the method of the present invention will be described. 1. Extraction and Treatment of Biological Minerals As described above, biological minerals are obtained by burning plants and animals to incinerate them. For example, Japanese Patent Application Laid-Open No. 10-52240, etc. It has been disclosed.

The biological minerals disclosed in the above publication (JP-A-10-52240) include plants and plants containing various effective minerals such as medicinal herbs, seaweeds and other algae, seaweeds and small fish and other seafood. Dry or raw heating at high temperature (combustion)
It is a biological mineral obtained from a residue obtained by removing harmful substances to the living body such as organic substances and organic toxic substances.

For example, the residual carbide (unburned carbon) contained in the above-mentioned residue (ash) heated (burned) at a high temperature.
Is further burned off by secondary heating to completely incinerate, and then pulverized to 200 to 300 mesh. By this operation, high-boiling and high-sublimation minerals which are not removed by the heating / combustion among various kinds of minerals mainly remain. Therefore, the lower the combustion temperature and the secondary heating and the shorter the time, the more minerals having a low boiling point and a low sublimation point. The above organisms include plant potatoes, starches, cereals, beans, vegetables, trees and their leaves and roots, fruits, mushrooms, various wild grasses, fish and shellfish, birds and beasts, and their internal organs, bones, Almost all animals and plants (organisms) can be targeted by the crust and the like.

In an embodiment of the present inventors, in plants (plants), wormwood, pine needles, cypress, bamboo, tahibo, knotweed, aloe, agarsk, ginseng, alfalfa, cut radish, moloheiya, tea leaves, ginkgo leaves, dandelion Roots, garlic, etc. are used.
Wakame and the like were used as raw material organisms for fish and shellfish, marine clams, sea cucumber, crab husks, and mushrooms. In addition, as for these raw materials, those obtained by quantitatively mixing a plurality of types in advance may be subjected to the incineration treatment, or those obtained by incineration for each raw material may be quantitatively mixed.

The composition and trace elements of the biological minerals thus extracted are as shown in Table 1, and the whole is, for example, a relatively large amount of Ca, K, Mg, P, Si or a trace amount thereof. Or, it contains various kinds of minerals such as trace amounts. Incidentally, as is apparent from Table 1, there are minerals whose weight is reduced or minerals which are increased when the raw material ash is purified by heating. These biological minerals were used in all of the following experiments, but the minerals contained in these minerals are slightly different depending on the type and amount of the raw materials, but are approximately approximated by quantitatively using various types of raw materials. This biomineral can be extracted about 5 to 10% of the dried raw material, and the higher the temperature, the greater the weight loss.

[0032]

[Table 1]

The above-mentioned minerals include those soluble in water and those poorly soluble or insoluble. When the biological mineral hold material described below is manufactured, the water-soluble mineral is not particularly required. In the case where the water-soluble mineral is easily lost in the process of manufacturing the mineral hold material (for example, when the material is ceramicized), the water-soluble mineral and the insoluble (slightly) -soluble mineral are separated by hydrofiltration in order to effectively utilize the mineral component. In some cases, only (poor) soluble minerals are used. Conversely, when the water-soluble mineral can be retained, as in the case where the hold material is a plastic material, only the water-soluble mineral solution or the water-soluble mineral powder extracted from the solution is mixed and carried (held). In some cases.

Among these, the water-soluble mineral is obtained by filtering water obtained by adding water to incinerated biological mineral, and the filtered water is aggregated to obtain about 4% concentration of mineral water. The water in the aqueous biological mineral solution is removed by evaporation to obtain a powdery water-soluble mineral, which can be dissolved in water again. The amounts of the mineral components of the water-soluble mineral obtained from the biological mineral after incineration are as shown in Table 2.

[0035]

[Table 2] (Weight in 100g (mg)) (Japan Food Research Laboratories)

2. Kinds of mineral hold materials and manufacturing method As described above, biological minerals themselves are ashed or further pulverized, so they are in the form of powder (powder), or water-soluble biological minerals are obtained by removing water from aqueous solution or aqueous solution. It is in the form of a powder. Therefore, if it is used as it is for the organic waste treatment described below, it will be consumed by one-time use. Therefore, it is increased by another holding material (carrier or extender) and used in various use environments. It is desirable that the holding form is such that it can be used repeatedly or for a long time or long term while maintaining its function.

For this reason, in the following embodiments, an inorganic material such as a ceramic material such as clay, a functional mineral such as natural zeolite, or an artificial mineral such as cement or artificial stone is used as an extender or carrier. It is possible to manufacture a biological mineral hold material in which biological minerals are mixed or impregnated with organic materials such as paper and non-woven fabric in addition to plastic molded products, wood molded products such as wood or particle board, and the like. It is possible.

(1) Ceramic Hold Material When biological minerals are carried on ceramics, ceramics of the above-mentioned biological minerals mainly composed of insoluble minerals are used. In this example, 18 g of the biological minerals shown in Table 1 are used. 200 g of crushed granite and 200 g of clay such as mud clay, which is a ceramic raw material, were mixed with water, kneaded, dried, and fired by a high heat treatment at about 1,100 ° C. for about 6 hours. Table 1 shows the elemental analysis values of the ceramics containing the biological minerals obtained in this manner. The amount of minerals is increased or decreased due to the influence of heat, the summation with the clay component, and the like when the ceramics are used.

When ceramics are mixed with biological minerals as described above, they can be molded and fired into bricks, tiles, blocks, or other shapes depending on the intended use, and the functions and uses expected of these can be obtained. It is also possible to pulverize according to the conditions and to obtain crushed granules or finely pulverized into sandy or powdery powder. Furthermore, it can be granulated in advance, dried, and fired to form a granular ceramic hold material. The ceramic raw material is not limited to the above, but may be a commonly used ceramic clay.
In addition, the above-mentioned powdery ceramic can be used in a state of being adhered to the surface of a substrate made of a metal, a mineral, another ceramic or the like by thermal spraying or the like.

(2) Zeolite Hold Material When a zeolite known for its adsorbent, deodorizing, ion exchange and other properties is used as a hold material, the insoluble mineral or the mineral ceramic powdered by (1) above is used. The powdery or fine-grained zeolite may be granulated and dried by adding water or, if necessary, an organic binder, and then dried at about 1000 ° C. at a high temperature. In an organic waste treatment experiment described below, water and 50-70% by weight of biological minerals were added to powdered natural zeolite from Shimane Prefecture, and a small amount of activated carbon powder, and kneaded to a diameter of about 8 mm. After granulation and drying, 1,000 ℃
Heated for about 1 to 3 minutes was used.

Other zeolite grains obtained by pulverizing natural zeolite ore into granules, or zeolite grains obtained by granulating and drying powdery zeolite using a binder or the like (activated carbon or other contaminants may be added as necessary). The powdery mineral ceramic shown in (1) is adhered to the surface,
For example, a zeolite hold material can be obtained by heating and integrating at a temperature of about 1000 ° C. for several minutes.

These zeolite hold materials have not only the action of biological minerals described below, but also the adsorptive property, deodorizing property and ion exchange ability of zeolite itself. In addition, when zeolite powder is used, powdery or granular zeolite ore waste generated in large quantities at natural zeolite ore mining sites can be effectively utilized.

(3) Hold material using cement When cement is used as a hold material, most of the material is used in the form of mortar or concrete, and the insoluble biological mineral itself is mainly used for the weight of the material such as cement, sand, and gravel. When used, about 5% is mixed. When the powdery or granular mineral ceramic shown in the above (1) is used, 1% is used.
It may be about 0%. However, when mineral minerals are used, they function in the same way as aggregates.
Care must be taken so that the mixing ratio with cement does not become excessive.

When the biological mineral is mixed with the mortar or concrete, the mortar or concrete has a unique effect after being solidified, but has an effect of increasing the viscosity or binding force of the mortar or concrete during the kneading process. Has the effect of supplementing the function of cement. Needless to say, hold materials using these cements can be used not only for cast-in-place mortar and concrete but also for precast members as construction materials and civil engineering materials.

(4) Plastic Holder When a biomineral is mixed into a plastic to form a molded body, the weight ratio of the biomineral (mainly insoluble) itself is around 5%, and the mineral ceramic powder described in (1) is used. When using, 5% or more is desirable. Plastic hold materials mixed with these biological minerals can be easily extinguished during the gasification and extinguishing of organic waste described below, except for those materials that are difficult to gasify and extinguish with biological minerals such as vinyl chloride. In addition, if a biodegradable resin is used as the plastic, or if a plant fiber material is mixed with the biodegradable resin, the annihilation treatment is further facilitated.

These plastics may be molded as a plate, a block, or various containers, or may be molded into a film and molded into a sheet-like or bag-like product. However, in the case of a bag that requires transparency, it is desirable to mix the above-mentioned water-soluble biological mineral solution or the powdered mineral powder extracted from the mineral solution.

(5) Fibrous Hold Material When a fibrous hold material is used as the hold material, when the hold material itself is impregnated with biological minerals, when it is applied to the surface, or when plant fiber materials are mixed with biological minerals. There is a case where a molded product is formed.

When wood (including plywood and laminated wood) having a columnar or plate shape is used as the holding material, a water-soluble mineral can be mainly impregnated into the holding material by dipping, spraying, coating, or the like. In the case of a molded material formed by pressing or further heating a pellet-like or fibrous wood material via a binder, a pellet or fibrous material which has been impregnated with a mineral aqueous solution before molding is used. It can also be molded or mixed with a powdered biological mineral (or biological mineral hold material) in advance.
Similarly, biological minerals can be supported by impregnating a water-soluble mineral into a sheet-like material such as a nonwoven fabric, paper, or a cloth, or embedding an insoluble mineral.

Next, a processing method for processing the processing object 2 using the processing apparatus 1 and the holding material configured as described above will be described. First, a description will be given of an experimental method in which the processing of the processed material 2 was performed with the contents shown in Table 3 and the results thereof.

[0050]

[Table 3]

In this experiment, the processing temperature in the processing chamber 5 was set to about 35 ° C., which is about human body temperature, the rotation speed of the stirring member 7 was set to about 1.5 rpm, and the processing time was set to 1 for the apparatus conditions.
At the same time, a processing base material having a water content of about 40 to 70% was formed by mixing and mixing the following accelerator 3, adjusting material 6, and water in the processing chamber 5 in proportions shown in the table. Then, 600 g of a total of 500 g of sardines and 100 g of lettuce with peeled leaves were put thereinto as animal and vegetable treatments 2 in a first experimental group, which will be described later. Confirmation was made for each of the second experimental group and the third experimental group. In this experiment, in order to appropriately measure the amount of the processed material 2 and to measure the processing, the processing was performed by using the processing apparatus 1 having a relatively small volume of about 30 liters in the processing chamber 5.

The conditioning material 6 is not limited to sawdust, but is made of a material containing vegetable fiber, which has a small volume reduction during treatment, as well as having a water-retaining and water-retaining property, and evaporating the water contained by heating and stirring. If it is of a nature, it can achieve its purpose, but when the treated base material is reused as fertilizer or feed for livestock, it is desirable that it be harmless to living organisms and have no environmental pollution.

In this experiment, in the first experiment group, the above-mentioned pulverized ceramic hold material was used.
Unless otherwise specified, the same ceramics as in the above-mentioned use examples are used for the ceramic accelerator used in the following experimental examples.

In the second experimental group, the above-mentioned zeolite hold material was used as the accelerator 3. The first experimental group and the second experimental group each contained 500 ml of water that had been filtered and contacted with the above-mentioned ceramic accelerator to elute biological minerals.
ml. Further, the third experimental group shows an experimental example in which the processing state of the processed material 2 in the case of using the adjusting material 6 and tap water without adding the biological mineral as the accelerator 3 is shown.

The adjusting material 6 adjusts the water content in the processing chamber 5 and is made of a material which is excellent in water absorption and water retention and easily evaporates water by heating. It is difficult to decompose and does not greatly reduce the volume, but it is necessary to temporarily retain biological minerals to make it a medium that can be easily contacted uniformly with the processed material 2 and to obtain a large quantity of inexpensive and harmless conditions. It is preferable to use a carbohydrate satisfying these conditions and made of a material containing plant fibers having strong fibrous properties. Accordingly, sawdust, rice husk, buckwheat hull, hay, etc. can be used as such an adjusting material 6, and these may be used alone or in appropriate combination. It is easy to select and confirm by sieving with the above mesh,
Sawdust that can be easily obtained and has versatility is used for the adjusting material 6.

Using the processing apparatus 1 configured as described above,
The results of an experiment performed with each condition set as shown in Table 3 are as follows. That is, the measurement result of the processed material 2 one hour after the processing operation indicates that the residual amount of the processed material 2 is approximately 30 g and the residual ratio is approximately 5.0% in the first experimental group using the ceramic accelerator. The residual amount of the treated product 2 in the second experimental group using the zeolite accelerator was approximately 50 g, and the residual ratio was approximately 8.3%.

As a result, in the present invention, the processed material 2 is rapidly decomposed in comparison with the conventional processing apparatus which mainly processes microorganisms, which requires a processing time of at least several days to several weeks. It could be processed, and it was observed that the extinction process could be performed within a very short time to such an extent that the form of the processed product 2 could hardly be confirmed with the naked eye and touch. In the third experimental group to which no biological mineral was added, the residual ratio of the treated material 2 was about 75%, and although the volume was reduced by the evaporation of water, the prototype of the treated material 2 was almost completely stopped.

It should be noted that the sardine and lettuce both in the first experimental group and the second experimental group showed good extinction of the sardine and lettuce after 1 hour, and that the base material had a good wetness. The large bone part of sardine and a very small part of the lettuce wick remained while keeping a slight shape. However, after the measurement, the processing apparatus 1 was continuously operated for about 30 minutes. It could be completely decomposed, and no residual was confirmed by visual inspection.

In the above-mentioned treatment, general organic waste is mainly composed of carbon (C), hydrogen (H), oxygen (O) and nitrogen (N). Since it is decomposed into a gas and discharged from the exhaust port 55, it is possible to reduce the pressure in the processing chamber and the gas discharged to the outside of the machine without a bad smell, and to reduce the smell of fermentation. The result was obtained.

Further, the processed product 2 after the complete decomposition is
Minerals such as calcium (Ca) and magnesium (Mg) only remain in the base material as non-gasified elements,
In the base material, an increase or decrease in the apparent amount due to the treatment of the processed material 2 is not so confirmed, and the base material in this state includes, together with the biological minerals carried in the holding material, organic waste. Since the non-transpired minerals in the material are accumulated and accumulated, it is not necessary to newly replenish the accelerator 3 and the adjusting material 6. For this reason, it was also confirmed that the next processing operation by loading the processing object 2 can be repeatedly and continuously performed over a long period of time.

However, when untreated heavy metals and other environmental pollutants are contained in the organic waste, they may be accumulated and become high in concentration. In such a case, the base material is not allowed to be contained. It is desirable to appropriately replace it within the range.

At this time, the processing apparatus 1 having the above-described structure is configured such that the accelerator 3 and the adjusting material 6 are charged into the processing chamber 5.
Sawdust is in a slightly dry state and lacks in water content. In such a case, the moisture content of the base material is 60 to 70%.
Water is supplied artificially or by a feeder 80 so that the temperature is adjusted to a predetermined processing temperature by a temperature control device 5a while controlling the water content, and the accelerating agent 3 and the adjusting material 6 are continuously mixed by a stirrer 7. Then, the processing of the processed product 2 is performed while the processed product and the base material are brought into air contact to cause aerobic decomposition (fermentation). The base material in the processing chamber 5 is continuously stirred while being maintained at a predetermined processing temperature, and can provide and maintain an environment under conditions suitable for effective bacteria associated with the presence of biological minerals in the base material, The complete decomposition action is promoted by the effective bacteria that have multiplied and activated the input treated material 2, and the decomposition action can be performed while suppressing generation of offensive odor gas and generation of wastewater due to untreated substances.

Therefore, in a treatment apparatus for treating various microorganisms for waste treatment by a conventional treatment method with an accelerator that has been selected and implanted, the volume of the base material is greatly reduced as the treatment proceeds, so that a large amount of adjustment is required. In addition to the need for materials and accelerators, incomplete processing is affected by subtle changes in conditions during long-term operation, which often leads to the generation of offensive odors. Is considered to destroy the treated product while the fungi attached to the treated product proliferate, and can decompose the treated product 2 without intentionally preparing a specific microorganism for waste treatment. ,
In addition, since there is no significant change in the volume reduction of the base material, replenishment of a large amount of adjusting materials and accelerators can be saved, and the processing time is significantly shortened to one-tenth of that of the conventional one, and there are also minute conditions during operation. There is an advantage that the processing performance is not largely influenced by the change of the odor, and the generation of offensive odor can be easily suppressed.

Particularly, a processed material having a strong odor such as garbage or animal dung described below does not generate a bad odor immediately when the processed material is stirred once or twice by mixing and mixed with the accelerator. This is particularly noticeable when a base material containing is used for the second time or later.

In addition, the configuration of the processing apparatus 1 can eliminate the need for installation of a deodorizing device or the like, can be manufactured simply and inexpensively without a complicated structure, and requires complicated maintenance work. It can be reduced in size, and can be made suitable as an easy-to-handle processing device for home use or business use.

In the above-mentioned processing operation, the above-mentioned ceramic accelerator (holding material) is hardened by firing at a high heat, and has a sharp edge on its surface. When the base material is agitated,
It is presumed that the edge of the ceramic accelerator comes into contact with sardines and lettuce to gradually decompose and accelerate the decomposition action, and since the ceramic accelerator is hard to be worn down, the cutting action can be maintained for a long time. There is. Furthermore, while kneading biological minerals with a ceramic material and forming it into a block shape, firing it by high heat treatment,
The granulated ceramic accelerator which holds biological minerals by crushing the block pieces has advantages such that the edges can be formed sharply and the production thereof can be performed easily and inexpensively.

As the accelerator 3, a zeolite accelerator (holding material) formed by supporting biological minerals on a mineral such as a zeolite material has a deodorizing effect because the zeolite material itself has a deodorizing effect. Even in the case of treating objects, there is a feature that the odor of exhaust gas can be further reduced. In addition, each of the above-mentioned holding materials can hold biological minerals for a long period of time, and can easily combine a deodorant such as carbon or titanium oxide by appropriate means such as adsorption, coating, kneading and the like.
In particular, the holding material containing titanium oxide has a feature that the waste gas can be deodorized and the supply into the processing chamber 5 can be easily performed by a reducing action performed with stirring. .

The material of the deodorant may be supplied to the processing chamber 5 directly or artificially or via a feeding device 80. Further, when the titanium oxide and the biological mineral are formed in an appropriate shape in a state where the titanium oxide alone or together with the biological mineral is contained in the holding material, the titanium oxide and the biological mineral contained in the holding material are contained in the exhaust gas. Even when a bad smell is involved, it is possible to reliably remove and exhaust the gas.

Next, a description will be given of an experimental example in which a large-sized processing apparatus 1 is used separately from the above-described experiments to confirm processing on various processed objects. The description of the same items and functions as those in the experiment will be omitted. In this experiment, the capacity of the processing chamber 5 is about 600 liters, the processing temperature in the processing chamber 5 is about 40 ° C. to 60 ° C., and the rotation speed of the stirring body 7 is about 1.5 rpm.
The processing capacity can be increased by increasing the processing temperature at about 70 ° C. or by increasing the number of rotations of the stirrer 7. However, the number of rotations is set to the above number from the practical viewpoint such as reducing running costs. . Accelerator 3 is composed of 2.4 kg of ceramic accelerator and 1.6 K of powdered biological mineral.
g.

The conditioning material 6 is introduced into the processing chamber 5 at a ratio of about 50 kg of sawdust to about 6 kg of rice bran, so that the base material formed after the treatment is more effectively used as a high-quality fertilizer or soil conditioner. To be able to. Further, the base material obtained by combining the accelerator 3 and the adjusting material 6 adjusts the moisture content thereof to about 60 to 70%, and after one hour from the operation of charging the processing object 2 into the processing chamber 5, the processing state of the processing material is incomplete. Was confirmed.

In this case, the processed material 2 charged is 9 K
g, side dish 16Kg, fish ash 8Kg, salad (including macaroni) 12Kg, vegetable waste 9Kg, fried 3Kg, fresh cream 11Kg, etc., totaling about 70Kg.
The ratio between the capacity and the processed material 2 was set to a desirable mixing ratio of about 3: 1, and the base material was charged into the operating processing chamber 5 while being heated and stirred. After the processing experiment of the processed material 2, plastics described later were continuously put into the same base material, and an experiment for confirming the processing state was performed.

Next, the results of an experiment performed in the above-described embodiment will be described. That is, one hour after the processing operation, the lid 52 was opened and the processing status in the processing chamber 5 was confirmed.
Are mixed with the base material without stopping the original form, and become a clay-like material, and are agitated.Vegetables and fruits have their cores remaining with fibrous material, and fish fins and thick bones Only a part remained, and it was confirmed that a favorable process was performed in a short time with a very high efficiency as compared with a conventional treatment apparatus and with a suppressed odor or the like. In addition, the above-mentioned residue can be almost completely eliminated by continuous operation for 2 hours. At this time, the base material is a moist bran floor having an appropriate humidity and is in a standby state in which the next processed material 2 can be charged. Was.
Since fresh log-shaped radish takes a long time to be decomposed, it is desirable to put such radish into a processed form that can be easily decomposed by a pre-treatment process such as shredding or crushing or crushing. .

Next, a description will be given of an experimental example in which the processed material 2 is put in place of plastics. In this case, the processed material 2 is
About 10 trays for packing Styrofoam food and a small box of the same material, which has been pulverized to a size of about 5 cm square, are simultaneously placed in the processing chamber 5 every several hours during the processing operation. The processing status of was confirmed. According to this, when the inside of the processing chamber 5 was seen when approximately 15 hours had passed, the tray was almost disappeared, and the slightly remaining fragments of the box were shrunk in a brittle state.

Chinese cabbage waste discharged at the other cabbage shipping area,
The same experiment as above was performed on tofu sprouts and bean sprouts in a tofu manufacturing plant.

(1) Chinese cabbage waste (September 29, 1999-1
(Aug. 9) 30 to 100 kg of objects are put in at regular intervals every day, for a total of 6
As a result of the 39 kg treatment, the volume was reduced to almost zero one day later, and the remaining amount of 39 kg by weight was 95.6%.
Was achieved (however, the device capacity was 100 liters,
(Base material weight 125 kg, mineral hold material 8% based on sawdust, set base material temperature 50 ° C).

(2) Tofu rag (from April 1, 1999 to 4
(Month 28) 40 to 220 liters of an object were introduced almost every day for 22 days, and a total of 1,660 liters were processed and left for 29 days to 35 days.
With an integrated reduction of 1,480 liters, the initial base material amount is 220
Subtracting liters means that almost the entire volume has disappeared. The processing conditions are common to (1).

(3) Sprouts [0096] As a result of processing about 50 kg of sprouts every day for 18 days, the total amount of sprouts was 895 Kg, the remaining amount was 19.5 Kg, and 97.8
% Weight reduction was achieved, as well as a 98.1% volume reduction. The processing conditions are common to the above (1) and (2).

The crushed pieces of the box were approximately 1-2 after 24 hours of operation.
After 48 hours, the particles had disappeared to such an extent that visual confirmation became impossible. In this case as well, there was no odor, the base material could be continuously operated in a bran floor, and it was difficult to eliminate plastics with a conventional processing apparatus, so that excellent experimental results could be obtained. In the treatment of plastics, the decomposition treatment can be performed more efficiently by increasing the heating temperature to about 70 ° C. or increasing the stirring speed.

In addition to the above experiment, excrement of livestock (cows, pigs, etc.) was introduced into the processing chamber 5, and the decomposition treatment could be performed satisfactorily and promptly. In this case, In addition, the efficiency can be improved by separating urine in the pretreatment and treating only feces, and since feces contain a large amount of fiber, there is no need for the adjusting material 6 after dehydration. The base material itself can be formed and efficiently decomposed. Effluent after the treatment was not only an effective fertilizer for crops and the like, but also good results such as effective reuse as feed for livestock could be obtained.

In the treatment of manure as described above,
The use of the accelerating agent 3 formed on the above-mentioned holding material has an advantage that the treatment of manure can be efficiently performed with a small amount of biological minerals. Therefore, there is a feature that a new farming form that can provide low-cost livestock and a suitable environment can be created.

When raw garbage or animal dung is made into a fertilizer, the base material remaining after the decomposition treatment itself contains a large amount of minerals, and thus can be effectively used as a fertilizer or a soil improvement material. When a treatment under a neutral atmosphere is required, the decomposition treatment can be performed in a state where the processing chamber is closed and air is blocked.

On the other hand, in the case of composting the object to be treated itself, a decomposition treatment is performed as a primary treatment in an aerobic environment with air supply / exhaust and the like. It can be realized by performing processing while performing appropriate switching (stirring) in an anaerobic atmosphere in which supply and discharge of methane are not performed. The secondary processing does not necessarily need to be performed by the same device or facility.

Here, a further experimental example will be described. Incidentally, various kinds of processed materials are usually treated at appropriate processing temperatures (approximately 39 ° C. for living things and about 60 to 70 ° C. for non-living things) at the time of processing according to the kind, Table 4 shows an example of the decomposition time of the processed product obtained by performing the processing under the same stirring conditions, which also significantly reduces the processing performance of the conventional processing apparatus mainly composed of microorganisms. Good results such as high-performance processing can be performed in a short time.

[0084]

[Table 4]

Next, another embodiment and an example of use of the method and apparatus for treating organic waste according to the present invention will be described with reference to FIGS. First, Fig. 3 shows apartments, apartments,
In a building 9a such as an apartment house, a plurality of kitchen sinks 9b installed for each room are connected via a conduit 90,
By connecting this to a processing apparatus 1 installed in an appropriate place outside the building 9a in a state where it is gathered in one conduit 91, the waste (processed material) 2 discharged from each sink 9b is different from that of the above-described embodiment. A large-scale processing apparatus 1 having a similar configuration can perform batch processing.
Thus, low-cost processing can be efficiently performed without separately installing the small processing apparatus 1 in each room or house.

In this case, the pretreatment device 92 is attached to the sink 9b.
By installing a disposer 9c for crushing the processed food waste 2 such as vegetables and fish,
Can be smoothly fed to the processing chamber 5 without clogging the conduits 90 and 91 via flowing water. In addition, by providing a dehydrating device 93 and a transport device 94 as a pre-processing device 92 between the conduit 91 and the processing device 1, while appropriately separating the processed material 2 and flowing water,
The processed product 2 after dehydration can be fed and transported toward the processing apparatus 1.

As shown in the figure, it is desirable that a plurality of processing apparatuses 1 be installed. In this case, one processing apparatus 1 is provided by a distributing / conveying apparatus 94a provided at the tip of the conveying apparatus 94 so as to be able to swing and convey. After a predetermined amount of the processed material 2 is supplied to the first processing device 1, if the processed material 2 is automatically supplied to the next processing device 1 automatically, each processing device 1 has a sufficient processing time, The product 2 can be continuously and efficiently processed even by a batch-type processing means.

Next, the embodiment shown in FIG. 4 will be described. The processing apparatus 1 has substantially the same configuration as that described above, and the processing chamber 5 includes a stirrer 7 that stirs the processed material 2 and the base material from one side to the other side while stirring them. And a supply unit 5 formed on the upstream side of the conveyance.
The pre-processing device 92 is installed on the k-side, and the lower discharge unit 5
In h, a post-processing device 95 including a drying device 95a, a bag filling device 95b, and the like is installed. Further, the processing chamber 5 is provided with tanks 10, 11, and 12 for separately storing the adjusting material 6, the accelerator 3, and water or water containing biological minerals, and these are provided with capacity sensors, temperature sensors, and humidity sensors installed therein. The automatic supply is performed based on the detection of the sensors and the like, and control is performed so that appropriate processing can always be performed.

The pretreatment device 92 in the illustrated example comprises a hopper 92a for charging the processed material 2, a dehydration device 93, a transport device 94, and the like. A water treatment device 96 is provided below the dehydration device 93, and the drain is disposable. The water is returned to 9c and the purified water is taken out of the machine and discharged. The tank 1 for storing the adjusting material 6 in the middle of the transport device 94.
Similarly, a tank 11 for accommodating 0 and the accelerating agent 3 is provided so as to promote the processing of the processed material 2 in advance on the upper side of the processing chamber 5.

As a result, the processing material 2 put into the hopper 92a is stirred and conveyed by adding the adjusting material 6 and the accelerating agent 3 while being conveyed while being pulverized and dehydrated by the pretreatment device 92. The processed material 2 that has passed can be sent to the processing chamber 5 to promote complete decomposition processing, and the processed material 2 that has been powdered from the end thereof is further dried in the post-processing device 95, packed and continuously. It can be taken out efficiently. In addition, when it is desired to mix an additive such as fertilizer or okara into the processed base material, the mixing process is performed by a mixing device 97 provided on a separate path at the end of the processing chamber 5, and the mixed material is taken out and discharged. You can also

Next, the embodiment shown in FIG. 5 will be described. In the processing apparatus 1, the processing chamber 5 is formed in a rotating drum shape and also serves as a stirring body. When the processing chamber 5 is rotated by the rotation driving device 98 while being heated by the heater 5b, the processing object 2 and the base material are stirred and mixed. In addition, supply and discharge mechanisms 58 and 58a for supplying an appropriate amount of the accelerator 3 are provided inside, and a hopper 92a for inputting the processed material is provided on the upper side. A hopper 92b for supplying the adjusting material 6 is provided. According to this, by making the diameter of the processing chamber 5 large,
In addition to being able to efficiently process large quantities of processed materials 2,
By opening and shutting off from the outside air, it is possible to perform treatment under both aerobic and anaerobic environments, and there are advantages such as being effective as a compost production plant.

Next, the embodiment shown in FIG. 6 will be described. In this processing apparatus 1, the processing room 5 is constituted by the building 9a itself, and the room is air-conditioned to a constant processing temperature. The agitator 7 in the illustrated example moves from one side of the room to the other side. It is provided so as to be rotatable forward and backward and to be able to reciprocate.

In this case, the processed material 2 such as animal dung is supplied into the processing chamber 5 by an appropriate working machine such as a power shovel, and then the adjusting material 6 is supplied by appropriate supply structures 58 and 58a.
And the accelerator 3 are supplied so that the agitation body 7 can be rotated and moved while the back-mixing of the processed material 2 and the base material can be easily performed.

In this case, when the side wall 51 such as the floor surface and the wall surface is formed of ceramic containing biological mineral or concrete containing biological mineral, or when the paint containing biological mineral is applied to the wall surface of concrete or the like, the treatment of the processed material 2 is performed. Can be performed more actively by utilizing the wall surface.

Further, the processing chamber 5 in this case may be a simple facility such as a plastic greenhouse or the like, or may be an open-top type simply formed in a groove shape. In such a case, it is necessary to heat the processing object by circulating a heater, steam, hot water, or the like from the bottom or the side wall of the groove, but it is preferable to provide a roof or a peripheral wall. In these cases, the facilitator 3 is added or sprayed to animal dung and the like arranged in a predetermined thickness on the floor surface, and is extinguished by stirring while heating with solar heat or forced heating, or composting treatment. It is possible to

Further, in this experiment, an example was described in which the promoting agent 3 used a biological mineral which has already been developed and filed by the present applicant. However, the present invention is not limited thereto, and a biological mineral obtained by other means may be used. Or mineral minerals may be used.

In addition, since the adjusting material (base material) used once contains minerals more than the first dose, the base material itself can be used as an accelerator.
Wash water or added water that has come into contact with these base materials can also be used as an accelerator.

As the holding material used in the present invention, in addition to the above-mentioned ceramics and zeolite grains, those obtained by mixing other natural minerals or synthetic resin materials with biological minerals, and granulating or pulverizing the same can also be used.

In the present invention described above, it is assumed that other harmful bacteria are almost killed or decomposed by the microorganisms involved in the decomposition or by the temperature due to heating or heat generation. If harmful bacteria or viruses are contained in the remnants, sterilization can be easily performed by heating the processing chamber itself to about 100 ° C. with a heater or hot air supply or other means provided with the processing chamber itself. . Alternatively, sterilization can be performed by providing an ultraviolet lamp inside and irradiating the base material with ultraviolet light.

[0100] Even if the effective bacteria in the remaining base material are killed by the above sterilization, the mineral remains as it is, and the fungi having the next decomposing action are replenished by introducing a processed material such as garbage. After that, it can be rapidly propagated by the processing environment in the processing chamber.

<Consideration of the Action of Biological Minerals that Promote the Decomposition or Destruction of Organic Substances> In the above-described various experiments, various types of biological minerals extracted from living organisms can be produced from animals and plants in an environment where a certain temperature and moisture are adjusted. Not only waste such as food (so-called garbage) but also pulp products such as paper, synthetic resin fibers such as disposable diapers, and synthetic resin materials such as polystyrene resin used in foamed styrene and cassette tape cases. It was found that up to the part (note: it was experimentally recognized that vinyl chloride resin was hardly decomposed) was decomposed in a very short time. By the way, it usually takes 25 to 40 days to decompose (disappear) conventional garbage, etc., even in the case of a plant treatment that composts relatively easily decomposed fish and shellfish meat and starch at an early stage. In order to remove odor from livestock dung, including primary fermentation (aerobic) and secondary fermentation (anaerobic), several days or more are required.

However, the scientific, biological, and physical mechanisms of how the biological mineral acts on the above-mentioned rapid decomposition action in the present invention have not been elucidated at this stage except by inference.

The inventor dares to deduce this point. One or more of a large number, a very small amount, or a very small amount of minerals contained in a living organism is converted into the first substance through the electron transfer promoting action. The possibility of promoting the energy metabolism of organisms such as decomposing bacteria, the second possibility of promoting the decomposition reaction by promoting the adsorption or repulsion of electrons,
Third, it is possible to presume the possibility of the catalytic action of the reaction (there is no decrease in minerals even after decomposition of the treated product).

Further, since the above-mentioned minerals are once accumulated through a filter of a living body and harmful organic compounds are removed by high-temperature treatment (combustion, etc.), they do not contain harmful substances which are not compatible with living bodies. Is characterized by the fact that minerals act in a small amount in a complex manner with omnidirectionality.

[0105]

The present invention has the following effects by using the method and apparatus for treating organic waste as described above. By adding an accelerator consisting of minerals that promote the decomposition action of the processed product to the processed product made of organic waste and stirring the mixture in the processing chamber, the processed product is efficiently controlled while suppressing the generation of bad smell and wastewater. It can be processed in a very short time.

In addition to using a biological mineral obtained by extracting an accelerator from a living organism, a holding material in which the biological mineral is contained in a ceramic, a holding material made of a mineral to which a biological mineral is adhered or adsorbed, or a biomaterial is used. When the mineral is added to the water, the biological mineral can be easily supplied into the processing chamber.

At this time, it is preferable to heat the inside of the processing chamber and adjust the water content of the processing object in order to promote the decomposition action of the processing object. When the material containing the plant fiber that evaporates is used, the treatment of the processed material can be performed more reliably.

The present invention also relates to a conventional treatment apparatus for treating a treated product with an accelerator mainly composed of a specific microorganism.
A simple and inexpensive construction of the processing equipment can be achieved without the need to supply a large amount of adjusting materials or specific microbial bacteria, and without the generation of offensive odors due to delicate conditions during operation. In addition, it can be used for large-scale organic waste treatment such as small household treatment equipment, large kitchen equipment, or an integrated disposal facility for animal dung and human waste, without requiring complicated maintenance work. There is.

Further, since the method of the present invention contains various kinds of balanced minerals extracted from living organisms, it can exert a stable action on a wide range of objects to be treated.
There is an advantage that materials can be easily obtained.

Further, since the holding material such as ceramic which is a carrier of the mineral can be artificially manufactured in any region, it can be stably supplied without being affected by resource problems and distribution conditions. Can be adjusted according to the purpose, quality stability can be ensured, the life time of the accelerator is long, the effect is persistent and the possibility of repeated use is provided, and the used accelerator is collected when necessary Can be easily performed.

[Brief description of the drawings]

FIG. 1 is a cross-sectional view of a processing apparatus that performs a processing method according to the present invention.

FIG. 2 is a side sectional view of FIG. 1;

FIG. 3A is a perspective view illustrating an example of use of a processing apparatus according to another embodiment of the present invention. (B) is a schematic diagram showing the processing method of (A).

FIG. 4 is a schematic diagram illustrating a processing apparatus according to another embodiment of the present invention, which includes a pre-processing apparatus and a post-processing apparatus.

FIG. 5A is a perspective view of a processing apparatus according to another embodiment of the present invention. 2B is a cross-sectional view illustrating a configuration of a main part of FIG.

FIG. 6A is a perspective view of a processing apparatus according to another embodiment of the present invention. 2B is a cross-sectional view illustrating a configuration of a main part of FIG.

[Explanation of symbols]

 DESCRIPTION OF SYMBOLS 1 Processing apparatus 2 Processed material 3 Accelerator 5 Processing chamber 6 Adjusting material 7 Stirrer 7b Heater 8 Auxiliary equipment 9b Sink 51 Side wall 55 Exhaust port 58 Delivery pipe 80 Feeding device 92 Pretreatment device

Claims (13)

[Claims] 1. A method in which a treated material (2) comprising organic waste is accommodated in a treatment chamber (5) for accommodating and treating waste, and the treated material (2) is treated with stirring. Organic waste treated by contacting or agitating and mixing an accelerator (3) consisting of a holding material pre-loaded with various minerals that promote the decomposition action of (2) in the processing chamber (5) Processing method. 2. The method for treating organic waste according to claim 1, wherein the accelerator (3) is a biological mineral extracted from various kinds of organisms. 3. The method for treating organic waste according to claim 1, wherein the accelerator (3) is a holding material containing a biological mineral in ceramic. 4. The method for treating organic waste according to claim 1, wherein the accelerator (3) is a holding material made of a mineral to which biological minerals are attached or adsorbed. 5. A deodorant is supplied directly to the processing chamber (5) or contained in or held in a holding material.
Or the organic waste treatment method of 3 or 4. 6. A treated product (2) for promoting a decomposition action
The method according to claim 1, wherein the inside of the treatment chamber is heated. 7. The method for treating organic waste according to claim 1, wherein the water content of the processed material (2) is adjusted so as to promote the decomposition action of the processed material (2). 8. The organic material according to claim 7, wherein an adjusting material (6) for adjusting moisture is introduced into the processing chamber (5), and is made of a material having water absorbency and water retention and evaporating moisture contained by heating. Waste treatment method. 9. The method according to claim 8, wherein the conditioning material (6) is made of a material containing plant fibers. 10. The organic waste treatment method according to claim 9, wherein the processing chamber (5) includes an outlet (55) for discharging gas generated in the processing chamber (5). 11. A plurality of sinks (9) is provided in the processing chamber (5).
The processed material (2) discharged from b) is collected and processed.
Or the organic waste treatment method of 9 or 10. 12. The process according to claim 1, wherein unremoved residue remaining after the treatment of the treated product (2) is used as an accelerator (3) in the treatment of another treated product. 7
Or the organic waste treatment method according to 8 or 9 or 10 or 11. 13. Addition of an unerased residue remaining after the treatment of the treated material (2) or use of water contacted with the unerased residue as an accelerator (3) for the treatment of another treated material. The method for treating organic waste according to claim 1, 2 or 3 or 4 or 5 or 6 or 7 or 8 or 9 or 10 or 11.