JPH092886A - Treatment of organic waste and equipment therefor - Google Patents

Treatment of organic waste and equipment therefor

Info

Publication number
JPH092886A
JPH092886A JP7154902A JP15490295A JPH092886A JP H092886 A JPH092886 A JP H092886A JP 7154902 A JP7154902 A JP 7154902A JP 15490295 A JP15490295 A JP 15490295A JP H092886 A JPH092886 A JP H092886A
Authority
JP
Japan
Prior art keywords
organic waste
temperature
fermentation
storage tank
drying
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP7154902A
Other languages
Japanese (ja)
Inventor
Akira Ito
璋 伊東
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP7154902A priority Critical patent/JPH092886A/en
Publication of JPH092886A publication Critical patent/JPH092886A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Fertilizers (AREA)

Abstract

PURPOSE: To provide an organic waste treatment capable of efficiently performing fermentation and decomposition of the organic waste by effectively using a fermentation and decomposition type fermenting microorganism making volume of the organic waste about zero. CONSTITUTION: This organic substance-treating method is an organic waste treating method wherein the inside of a receiving tank 1 received with the organic waste is stirred by a stirring mechanism 20, simultaneously a hot air heated with a heater is circulated in the receiving tank 1 and the organic waste is fermented while heating and stirring the organic waste in the tank. The organic waste is thrown into the receiving tank 1 and a fermenting operation is performed so that the organic waste becomes a prescribed fermenting temperature only in a prescribed fermenting operation time, then the operation is switched to a drying operation, and the drying operation is performed so that the organic waste becomes the prescribed drying temperature only in a prescribed drying operation time.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、生ごみ等の有機廃棄物
を発酵・乾燥処理する有機廃棄物処理方法とその装置に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an organic waste treatment method and apparatus for fermenting and drying organic waste such as garbage.

【0002】[0002]

【従来の技術】給食センター、仕出し業、レストラン等
から出される大量の残飯、残菜等の生ゴミを処理する場
合、それらを集めて発酵微生物と共に発酵槽に入れ、槽
内を加熱し撹拌しながら、微生物の発酵作用により生ゴ
ミを発酵・乾燥させて処理する有機廃棄物処理方法が普
及しつつある。
2. Description of the Related Art When processing a large amount of food waste such as leftover food and leftover food from a food service center, catering industry, restaurant, etc., they are collected and put into a fermenter together with fermenting microorganisms, and the inside of the tank is heated and stirred. However, an organic waste treatment method in which raw garbage is fermented and dried by the fermentation action of microorganisms to be treated is becoming widespread.

【0003】[0003]

【発明が解決しようとする課題】また、この種の有機廃
棄物処理方法において、近年、有機廃棄物を発酵処理に
より水と炭酸ガス等に変えてその体積を略ゼロとするよ
うな発酵・分解型の発酵微生物が開発され、毎日投入さ
れる生ゴミを略1日で発酵・分解させながら、毎日投入
される生ゴミを消滅処理することが試みられている。
In addition, in this type of organic waste treatment method, in recent years, fermentation and decomposition such that the organic waste is converted to water and carbon dioxide gas by fermentation treatment so that the volume thereof becomes almost zero. A type of fermenting microorganism has been developed, and it has been attempted to ferment and decompose raw garbage that is thrown in every day in about one day, while eliminating the raw garbage that is thrown in every day.

【0004】しかし、生ゴミは一般にその含水率が、8
0〜90%と発酵微生物の発酵に適した含水率(50〜
60%)よりかなり高く、生ゴミと共にオガコ等の水分
調整材を多量に投入し、発酵に適した含水率となるよう
にして処理する必要がある。
However, the garbage generally has a water content of 8
0-90% and water content suitable for fermentation of fermenting microorganisms (50-
It is considerably higher than 60%), and it is necessary to add a large amount of a water adjusting material such as sawdust and the like together with raw garbage, and treat it so that the water content is suitable for fermentation.

【0005】また、オガコ等の水分調整材は、この種の
発酵微生物によっては殆ど発酵・分解されず、体積が殆
ど減少しないため、略1日の発酵処理により、生ゴミが
発酵・分解されて殆ど消滅した場合でも、かなりの量の
水分を含んだ水分調整材がそこに残留するという問題が
あった。
Water-regulating materials such as sawdust are hardly fermented / decomposed by this type of fermenting microorganisms, and their volumes are hardly reduced. Even if it almost disappeared, there was a problem that a moisture conditioner containing a considerable amount of moisture remained there.

【0006】このため、次の日に生ゴミを投入して処理
する場合、さらに多くの水分調整材を投入して水分調整
をしないと、生ゴミの発酵・分解を効率良く行うことが
できず、有機廃棄物の体積を略ゼロにする発酵・分解型
の発酵微生物を効果的に使用することができない問題が
あった。
For this reason, when the raw garbage is put into the next day for processing, the raw garbage cannot be efficiently fermented and decomposed unless more water is added to adjust the water content. However, there is a problem that the fermentation / decomposition type fermenting microorganisms that make the volume of organic waste almost zero cannot be effectively used.

【0007】本発明は、上記の課題を解決するためにな
されたもので、有機廃棄物の体積を略ゼロにする発酵・
分解型の発酵微生物を効果的に使用することができる有
機廃棄物処理方法とその装置を提供することを目的とす
る。
The present invention has been made in order to solve the above-mentioned problems, and is a fermentation / reduction method for reducing the volume of organic waste to almost zero.
An object of the present invention is to provide an organic waste treatment method and an apparatus for the same, which can effectively use decomposing type fermenting microorganisms.

【0008】[0008]

【課題を解決するための手段】このために、本発明の有
機廃棄物処理方法は、有機廃棄物を入れた収容槽内を撹
拌機構により撹拌すると共に、加熱器で加熱した熱風を
収容槽内に循環させ、槽内の有機廃棄物を加熱・撹拌し
ながら、有機廃棄物を発酵処理する有機廃棄物処理方法
において、有機廃棄物を収容槽に投入した後、予め設定
した発酵運転時間だけ、有機廃棄物が設定発酵温度とな
るように発酵運転を行い、次に、乾燥運転に切換え、予
め設定した乾燥運転時間だけ、有機廃棄物が設定乾燥温
度となるように乾燥運転を行うことを特徴とする。
To this end, according to the method for treating organic waste of the present invention, the inside of the storage tank containing the organic waste is stirred by the stirring mechanism and the hot air heated by the heater is stored in the storage tank. In the organic waste treatment method of fermenting the organic waste while heating and stirring the organic waste in the tank, after introducing the organic waste into the storage tank, only a preset fermentation operation time, The fermentation operation is performed so that the organic waste reaches the set fermentation temperature, then the drying operation is switched to, and the drying operation is performed so that the organic waste reaches the set drying temperature for a preset drying operation time. And

【0009】また、その装置は、有機廃棄物を入れる収
容槽内に撹拌羽根を回転駆動する撹拌機構が配設され、
収容槽の底部の下側に熱風通路が配設され、収容槽内の
上部に槽内を加熱する加熱器が配設され、収容槽上部と
熱風通路がダクトにより連通接続され、熱風通路の熱風
を吸引して熱風を循環させるように収容槽内上部に送風
するブロワが配設されてなる有機廃棄物処理装置におい
て、収容槽の底部近傍に配置され有機廃棄物の温度を検
出する廃棄物温度センサと、運転時の設定発酵温度と設
定乾燥温度を設定する温度設定器と、発酵運転時間と乾
燥運転時間を設定するタイマーと、収容槽内の有機廃棄
物が設定発酵温度となるように加熱器を制御する発酵運
転と、有機廃棄物が設定乾燥温度となるように加熱器を
制御する乾燥運転とを、予め設定された発酵運転時間と
乾燥運転時間に基づき切換えて運転制御する運転制御装
置と、を備えたことを特徴とする。
Further, the apparatus is provided with a stirring mechanism for rotating and driving a stirring blade in a storage tank for containing organic waste,
A hot air passage is disposed below the bottom of the storage tank, a heater for heating the interior of the storage tank is disposed above the storage tank, and the upper portion of the storage tank and the hot air passage are connected by a duct to connect the hot air in the hot air passage. In the organic waste treatment device that is equipped with a blower that blows air into the upper part of the storage tank so as to circulate the hot air, the waste temperature is located near the bottom of the storage tank and detects the temperature of the organic waste. A sensor, a temperature setter that sets the set fermentation temperature and set drying temperature during operation, a timer that sets the fermentation operating time and drying operating time, and heats the organic waste in the storage tank to the set fermentation temperature. Control device for controlling the fermentation operation for controlling the vessel and the drying operation for controlling the heater so that the organic waste reaches the set drying temperature by switching between the fermentation operation time and the drying operation time set in advance With The features.

【0010】[0010]

【作用・効果】このような有機廃棄物処理方法と装置で
は、先ず、収容槽内に生ゴミ等の有機廃棄物と共に、適
量のオガコ等の水分調整材と発酵微生物(有機廃棄物の
体積を略ゼロにする発酵・分解型の微生物)を投入す
る。そして、加熱器、ブロワ、撹拌機構を動作させ、熱
風通路と収容槽内に熱風を循環させて、収容槽内を予め
設定した発酵温度に加温し、槽内の有機廃棄物等を撹拌
しながら、発酵微生物による有機廃棄物の発酵を行う。
[Operation / Effect] In such an organic waste treatment method and apparatus, first, an appropriate amount of organic waste such as garbage and a water conditioner such as sawdust and fermenting microorganisms (organic waste volume Fermentation / decomposition type microorganisms) that is almost zero are added. Then, the heater, the blower, and the stirring mechanism are operated to circulate the hot air in the hot air passage and the storage tank to heat the inside of the storage tank to the preset fermentation temperature and stir the organic waste in the tank. Meanwhile, the organic waste is fermented by the fermenting microorganisms.

【0011】この発酵運転は、予め設定した時間だけ行
われ、収容槽内の有機廃棄物の温度が発酵に適した温度
に維持される。この間、発酵微生物による発酵が促進さ
れ、その発酵・分解によって、有機廃棄物が水と炭酸ガ
ス等に分解され、廃棄物の体積は減少し、所定の発酵時
間後には有機廃棄物の体積は殆どゼロとなり、水分調整
材が残る。
This fermentation operation is performed for a preset time, and the temperature of the organic waste in the storage tank is maintained at a temperature suitable for fermentation. During this period, the fermentation by the fermenting microorganisms is promoted, and the fermentation / decomposition decomposes the organic waste into water, carbon dioxide gas, etc., and the volume of the waste is reduced. It becomes zero, and the moisture conditioner remains.

【0012】この後、乾燥運転に移行し、収容槽内の温
度は発酵温度より高い乾燥温度に昇温され、撹拌機構が
連続運転されて乾燥運転が行われる。この乾燥運転は、
所定の設定乾燥時間だけ実施され、これによって、有機
廃棄物の残留物や水分調整材中の水分が効率良く蒸発
し、収容槽内が乾燥状態となって運転が終了する。
Thereafter, the drying operation is started, the temperature in the storage tank is raised to a drying temperature higher than the fermentation temperature, and the stirring mechanism is continuously operated to perform the drying operation. This drying operation is
It is carried out for a predetermined set drying time, whereby the residue of the organic waste and the water in the water content adjusting material are efficiently evaporated, and the inside of the storage tank is in a dry state, and the operation ends.

【0013】このように、発酵運転の後、温度を高くし
て撹拌を連続して行う乾燥運転が実施されるため、生ゴ
ミと共に投入した水分調整材中に含まれる水分が蒸発
し、収容槽内を良好な乾燥状態として処理を終了するこ
とができる。このため、次の生ゴミ等の有機廃棄物を投
入する際には、水分調整材を殆ど入れずに有機廃棄物と
発酵微生物を投入するだけで、良好な発酵・分解を行っ
て有機廃棄物を繰り返し処理することができる。さら
に、一般に、生ゴミを発酵温度に保持した場合、幼虫
(うじ虫)が発生しやすいが、温度を高くして乾燥運転
を行うことにより、幼虫の発生を抑えることができる。
As described above, after the fermentation operation, since the drying operation in which the temperature is raised and the stirring is continuously performed is carried out, the water contained in the water content adjusting material charged together with the garbage is evaporated, and the storage tank is evaporated. It is possible to finish the processing by setting the inside to a good dry state. For this reason, when the next organic waste such as raw garbage is input, the organic waste and the fermenting microorganisms are simply added without adding a water-adjusting material, and good fermentation / decomposition is carried out to perform organic waste. Can be repeatedly processed. Further, in general, when raw garbage is kept at the fermentation temperature, larvae (maggots) are likely to be generated, but by increasing the temperature and performing a drying operation, the generation of larvae can be suppressed.

【0014】[0014]

【実施例】以下、本発明の実施例を図面に基づいて説明
する。
Embodiments of the present invention will be described below with reference to the drawings.

【0015】図1は有機廃棄物処理装置の正面図を、図
2はその右側面図を示している。
FIG. 1 is a front view of the organic waste treatment apparatus, and FIG. 2 is a right side view thereof.

【0016】1は有機廃棄物Aを入れる収容槽であり、
曲面状の底壁4を有し、上部に投入ハッチ2が、底壁4
に取出し用ハッチ3が開閉可能に設けられている。ま
た、収容槽1の背面側壁5および底壁4に沿って、温風
が通過可能な加熱ダクト部6が設けられている。
1 is a storage tank for containing the organic waste A,
It has a curved bottom wall 4, and the input hatch 2 is at the top,
A take-out hatch 3 is provided to be openable and closable. Further, along the rear side wall 5 and the bottom wall 4 of the storage tank 1, a heating duct portion 6 through which warm air can pass is provided.

【0017】加熱ダクト部6は、背面側壁5上部に設け
られた連通口9により収容槽1内上部と連通されてお
り、底部には蛇行用仕切板8が配設されて、底壁4に蛇
行して沿う温風蛇行通路7が形成されており、その一端
には、循環ダクト15を接続するための接続口10が設
けられている。このように表面積の大きい加熱ダクト部
6が、収容槽1の背面側壁5および底壁4に接して配設
されるため、収容槽1に対する熱伝導性が良好であり、
収容槽1は加熱ダクト部6からの伝導熱を効率よく受け
得る構造である。
The heating duct portion 6 is communicated with the upper portion inside the storage tank 1 through a communication port 9 provided on the upper portion of the rear side wall 5, and a meandering partition plate 8 is disposed on the bottom portion, and the heating wall portion 6 is provided on the bottom wall 4. A meandering hot air passage 7 is formed, and a connection port 10 for connecting a circulation duct 15 is provided at one end thereof. Since the heating duct portion 6 having such a large surface area is arranged in contact with the back side wall 5 and the bottom wall 4 of the storage tank 1, the thermal conductivity to the storage tank 1 is good,
The storage tank 1 has a structure capable of efficiently receiving the conductive heat from the heating duct portion 6.

【0018】収容槽1および加熱ダクト部6の周囲は断
熱材を入れた断熱壁によって包囲され、収容槽1内の上
部には、その右側から加熱器12が挿入されるように配
設されている。
The surroundings of the storage tank 1 and the heating duct portion 6 are surrounded by a heat insulating wall containing a heat insulating material, and a heater 12 is arranged in the upper part of the storage tank 1 so that the heater 12 is inserted from the right side thereof. There is.

【0019】加熱器12の加熱源としては燃焼バーナが
使用されるが、常にパイロットバーナーが点火している
ハイ・ロー式のものが、加熱による有機廃棄物Aの温度
差を防止するため、および脱臭効果を上げる点で好まし
い。さらに、図3、図4に示すように、遠赤外線放射多
孔板13が加熱部を包囲するように設けられている。こ
の遠赤外線放射多孔板13は金属多孔板の表面に、加熱
時に遠赤外線を放射するセラミック等をコーティングし
て形成されている。
A combustion burner is used as the heating source of the heater 12, but a high / low type in which a pilot burner is constantly ignited is used to prevent the temperature difference of the organic waste A due to heating, and It is preferable in terms of enhancing the deodorizing effect. Further, as shown in FIGS. 3 and 4, a far infrared ray radiating porous plate 13 is provided so as to surround the heating section. The far-infrared radiation porous plate 13 is formed by coating the surface of a metal porous plate with ceramic or the like that emits far-infrared rays when heated.

【0020】加熱ダクト部6の接続口10には、循環ダ
クト15の一端が連通接続され、循環ダクト15の他端
はブロワ16の吸気側に接続されている。ブロワ16の
吐出側は、収容槽1内の上部に開口した吹出し口17に
接続されている。
One end of the circulation duct 15 is connected to the connection port 10 of the heating duct portion 6, and the other end of the circulation duct 15 is connected to the intake side of the blower 16. The discharge side of the blower 16 is connected to a blowout port 17 that opens at the top of the storage tank 1.

【0021】循環ダクト15には、ブロワ16の吸気側
に外気を供給するとともに、その給気量を調整可能な調
整蓋18aを備えた給気口18が配設される。この給気
口18はブロワ16と接続口10との間であれば何れの
位置に配置してもよい。
The circulation duct 15 is provided with an air supply port 18 having an adjusting lid 18a for supplying the outside air to the intake side of the blower 16 and adjusting the amount of the supplied air. The air supply port 18 may be arranged at any position between the blower 16 and the connection port 10.

【0022】したがって、ブロワ16の運転により、加
熱ダクト部6を介して収容槽1の上部、つまり加熱器1
2によって加熱された熱気が吸引され、加熱ダクト部6
を通った温風が循環ダクト15を通り、さらに給気口1
8より適量の外気が供給されて、外気と混合された温風
は、再び吹出し口17より収容槽1内に送風される。な
お、収容槽1上部の左側には、自然排気を行う排気ダク
ト25が設けられており、内部で発生した蒸気や余分な
空気が適度に排気される。
Therefore, by operating the blower 16, the upper portion of the storage tank 1, that is, the heater 1 is heated through the heating duct portion 6.
The hot air heated by 2 is sucked in, and the heating duct portion 6
The hot air that has passed through the circulation duct 15 and the air supply port 1
An appropriate amount of outside air is supplied from 8, and the warm air mixed with the outside air is blown into the accommodation tank 1 through the outlet 17 again. An exhaust duct 25 for performing natural exhaust is provided on the left side of the upper part of the storage tank 1, so that steam generated inside and excess air are appropriately exhausted.

【0023】さらに、収容槽1の内部には、有機廃棄物
Aの撹拌機構20が配設されている。この撹拌機構20
は、水平に軸支された回転軸21の周囲に、多数の撹拌
羽根22を取付けて構成され、回転軸21の端部に固定
したスプロケット23がチェーンを介してモータ24に
連係され、このモータ24により回転・駆動される。
Further, inside the storage tank 1, a stirring mechanism 20 for the organic waste A is arranged. This stirring mechanism 20
Is constructed by mounting a large number of stirring blades 22 around a rotary shaft 21 supported horizontally, and a sprocket 23 fixed to an end of the rotary shaft 21 is linked to a motor 24 via a chain. It is rotated and driven by 24.

【0024】また、収容槽1内の上部には、その上部空
間における排気口側と加熱部側を縦に仕切るように仕切
板27が取付けられている。この仕切板27は、排気ダ
クト25の開口部と加熱器12および吹出し口17との
間に設けられており、その下端の高さ位置は、投入され
る適量の有機廃棄物Aの上面よりも、やや上方になるよ
うに設定されている。
A partition plate 27 is attached to the upper part of the storage tank 1 so as to vertically separate the exhaust port side and the heating part side in the upper space. The partition plate 27 is provided between the opening of the exhaust duct 25 and the heater 12 and the outlet 17, and the height position of the lower end thereof is higher than the upper surface of the appropriate amount of the organic waste A to be charged. , Is set to be slightly higher.

【0025】槽内の有機廃棄物の温度を検出するため
に、収容槽1の底部に廃棄物温度センサ31が設置され
る。この温度センサ31は、後述の運転制御装置30に
接続される。また、この廃棄物温度センサ31は、廃棄
物の温度を検出すればよいため、槽内の底部近傍などに
設けることもできる。
A waste temperature sensor 31 is installed at the bottom of the storage tank 1 in order to detect the temperature of the organic waste in the tank. The temperature sensor 31 is connected to the operation control device 30 described later. Further, since the waste temperature sensor 31 only needs to detect the temperature of the waste, it can be provided near the bottom of the tank.

【0026】運転制御装置30は、例えば汎用のシーケ
ンサなどから構成され、撹拌機構20とブロワ16のモ
ータ及び加熱器12の燃焼バーナをオンオフ制御する回
路、運転時間を設定するタイマー34がそこに接続され
る。さらに、運転時の上限処理温度を設定する温度設定
器32が運転制御装置30に接続される。
The operation control device 30 is composed of, for example, a general-purpose sequencer, and a circuit for controlling on / off of the stirring mechanism 20, the motor of the blower 16 and the combustion burner of the heater 12, and the timer 34 for setting the operation time are connected thereto. To be done. Further, a temperature setter 32 that sets the upper limit processing temperature during operation is connected to the operation control device 30.

【0027】温度設定器32には、発酵運転時の温度と
して例えば45℃が設定され、乾燥運転時の温度として
例えば70℃が設定される。タイマー34には発酵運転
時間として例えば20時間、乾燥運転時間として例えば
4時間が設定される。
In the temperature setter 32, the temperature during fermentation operation is set to, for example, 45 ° C., and the temperature during drying operation is set to, for example, 70 ° C. The fermentation operation time is set to 20 hours, and the drying operation time is set to 4 hours, for example, in the timer 34.

【0028】運転制御装置30は、廃棄物温度センサ3
1の検出する有機廃棄物の温度と温度設定器32の設定
温度に基づいて加熱器12とブロワ16の運転を制御す
るように動作し、予め設定されたプログラムに基づき、
運転開始から先ず発酵運転を行い、続いて乾燥運転を行
うように構成される。
The operation control device 30 includes a waste temperature sensor 3
1 to operate to control the operation of the heater 12 and the blower 16 based on the temperature of the organic waste detected and the set temperature of the temperature setting device 32, and based on a preset program,
From the start of operation, the fermentation operation is performed first, and then the drying operation is performed.

【0029】次に、上記構成の有機廃棄物処理装置の動
作を説明する。
Next, the operation of the organic waste treatment apparatus having the above structure will be described.

【0030】レストラン、仕出し業等から出される有機
廃棄物(生ゴミ)は、毎日略一定時刻に、処理装置の収
容槽1内に投入する。このとき、適量のオガコ等の水分
調整材と発酵微生物を同時に投入する。発酵微生物とし
ては、生ゴミを発酵・分解して水と炭酸ガス等に変え、
生ゴミの体積を殆どゼロにする発酵・分解型の発酵微生
物を使用する。
Organic waste (raw garbage) produced from restaurants, catering businesses, etc. is put into the storage tank 1 of the processing apparatus at a substantially constant time every day. At this time, an appropriate amount of a water conditioner such as sawdust and a fermenting microorganism are simultaneously added. As fermenting microorganisms, raw garbage is fermented and decomposed into water and carbon dioxide,
Fermentation / decomposition type fermenting microorganisms that reduce the volume of garbage to almost zero are used.

【0031】運転開始に伴ない、モータ24を起動して
撹拌機構20の撹拌羽根22を回転させ、有機廃棄物A
を撹拌する。同時に加熱器12を始動して加熱を開始
し、ブロワ16を運転すると、加熱ダクト部6および循
環ダクト15が負圧となる。収容槽1内上部の熱気が加
熱ダクト部6に吸引され、その熱気は温風蛇行通路7を
経由して接続口10から循環ダクト15に入る。さら
に、循環ダクト15の管路において、給気口18より適
量の外気を吸引し、外気と混合された温風が吹出し口1
7より再び収容槽1に戻される。
With the start of the operation, the motor 24 is started to rotate the stirring blades 22 of the stirring mechanism 20, and the organic waste A
Is stirred. At the same time, when the heater 12 is started to start heating and the blower 16 is operated, the heating duct section 6 and the circulation duct 15 become negative pressure. The hot air in the upper part of the storage tank 1 is sucked into the heating duct section 6, and the hot air enters the circulation duct 15 from the connection port 10 via the warm air meandering passage 7. Further, in the conduit of the circulation duct 15, an appropriate amount of outside air is sucked through the air supply port 18, and the warm air mixed with the outside air is blown out from the outlet 1.
It is returned to the storage tank 1 again from 7.

【0032】加熱器12の運転によって加熱された遠赤
外線放射多孔板13からは遠赤外線が放射され、その遠
赤外線と輻射熱によって収容槽1内の有機廃棄物Aは、
撹拌されながら加熱される。さらに、熱気を通す加熱ダ
クト部6が、収容槽1の背面側壁5および底壁4に直接
接して取り付けられているため、加熱器12の熱が収容
槽1の中部、底部に伝導され、収容槽1はその伝導熱に
よっても加熱される。また、循環ダクト15を通過した
温風が吹出し口17から槽内の有機廃棄物Aに向けて吹
付けられるため、その温風によっても、槽内の有機廃棄
物Aは加温される。
Far infrared rays are radiated from the far infrared radiating porous plate 13 heated by the operation of the heater 12, and the organic waste A in the storage tank 1 is radiated by the far infrared rays and the radiant heat.
Heated with stirring. Further, since the heating duct portion 6 for passing hot air is attached in direct contact with the rear side wall 5 and the bottom wall 4 of the accommodation tank 1, the heat of the heater 12 is conducted to the middle portion and the bottom portion of the accommodation tank 1 and accommodated. The tank 1 is also heated by its conduction heat. Further, since the warm air that has passed through the circulation duct 15 is blown from the outlet 17 toward the organic waste A in the tank, the warm air also heats the organic waste A in the tank.

【0033】このように、加熱器12、ブロワ16、撹
拌機構20が運転されることにより、収容槽1内の生ゴ
ミが、適度に撹拌されながら加温され、収容槽1内が温
度設定器32の設定温度である約45℃(発酵に最適な
温度)となるように制御され、収容槽1内の生ゴミは発
酵微生物により発酵・分解されていく。そして、この間
に発生した水蒸気や炭酸ガスは、排気ダクト25から排
気され、生ゴミの発酵・分解により生ゴミの体積は徐々
に減少し、生ゴミや水分調整材中の水分も減少してい
く。
As described above, by operating the heater 12, the blower 16, and the stirring mechanism 20, the raw garbage in the storage tank 1 is heated while being appropriately stirred, and the temperature setting device in the storage tank 1 is set. The temperature is controlled to be about 45 ° C. (the optimum temperature for fermentation), which is the set temperature of 32, and the garbage in the storage tank 1 is fermented and decomposed by the fermenting microorganisms. Then, the water vapor and carbon dioxide gas generated during this period are exhausted from the exhaust duct 25, the volume of raw garbage is gradually reduced due to the fermentation and decomposition of the raw garbage, and the water content in the raw garbage and the water content adjusting material is also reduced. .

【0034】温度設定器32に設定された発酵運転時間
は例えば20時間であり、図5に示すように、生ゴミが
投入され発酵運転が開始された後、20時間は収容槽1
内の生ゴミの温度が約45℃に維持される。この間、発
酵微生物による発酵が促進され、その発酵によって、生
ゴミが水と炭酸ガスに変えられ、生ゴミの体積は減少
し、20時間後には生ゴミの体積は殆どゼロとなる。
The fermentation operation time set in the temperature setting device 32 is, for example, 20 hours, and as shown in FIG. 5, 20 hours after the garbage is fed and the fermentation operation is started, the storage tank 1 is operated.
The temperature of the garbage inside is maintained at about 45 ° C. During this period, the fermentation by the fermenting microorganisms is promoted, the fermentation converts the raw garbage into water and carbon dioxide, the volume of the raw garbage decreases, and the volume of the raw garbage becomes almost zero after 20 hours.

【0035】そして、発酵運転時間(20時間)が経過
すると、自動的に乾燥運転に変り、設定温度が45℃か
ら乾燥温度の75℃に変る。このため、加熱器12の制
御により、収容槽1内の温度が約75℃に上昇加熱さ
れ、撹拌機構20が連続運転となり、これによって、収
容槽1内の有機廃棄物からの水分の蒸発が促進され、乾
燥運転が設定乾燥時間(4時間)だけ実施される。
When the fermentation operation time (20 hours) has elapsed, the operation automatically changes to the drying operation, and the set temperature changes from 45 ° C. to the drying temperature of 75 ° C. Therefore, by controlling the heater 12, the temperature in the storage tank 1 is raised to about 75 ° C., and the stirring mechanism 20 is continuously operated. As a result, evaporation of water from the organic waste in the storage tank 1 is caused. Accelerated, the drying operation is carried out for the set drying time (4 hours).

【0036】このように、発酵運転の後、温度を高くし
て撹拌を連続して行う乾燥運転が実施されるため、生ゴ
ミと共に投入した水分調整材中に含まれる水分が蒸発
し、1日(24時間)の処理が終了した時点では、収容
槽1に残留した残留物(主に水分調整材)の含水率は約
30〜40%と低くなる。
As described above, after the fermentation operation, since the drying operation in which the temperature is raised and the stirring is continuously performed is carried out, the water contained in the water content adjusting material charged together with the raw garbage is evaporated, and the drying operation is continued for one day. When the treatment of (24 hours) is completed, the water content of the residue (mainly the water content adjusting material) remaining in the storage tank 1 becomes as low as about 30 to 40%.

【0037】このため、翌日に新な生ゴミを収容槽1に
投入して同様の発酵・分解処理を行なう際、収容槽1内
には含水率の低い水分調整材が残留するのみであるた
め、新な水分調整材を加えることなく、生ゴミと発酵微
生物を投入するだけで、再び発酵運転を開始することが
できる。
Therefore, when new garbage is put into the storage tank 1 on the next day and the same fermentation / decomposition process is carried out, only the water conditioner having a low water content remains in the storage tank 1. The fermentation operation can be restarted by adding raw garbage and fermenting microorganisms without adding a new moisture adjusting material.

【0038】そして、その日の処理も、上記と同様に、
設定発酵時間(20時間)とそれに続く設定乾燥時間
(4時間)の間、発酵運転と乾燥運転が実施され、上記
と同様に、生ゴミを発酵・分解して水と炭酸ガス等に分
解・処理することができる。さらに、一般に、生ゴミを
発酵温度に保持した場合、幼虫(うじ虫)が発生しやす
いが、温度を高くして乾燥運転を行うことにより、幼虫
の発生を抑えることができる。
The processing for that day is also the same as above.
During the set fermentation time (20 hours) and the subsequent set drying time (4 hours), the fermentation operation and the drying operation are performed, and as in the above, the garbage is fermented and decomposed into water and carbon dioxide gas. Can be processed. Further, in general, when raw garbage is kept at the fermentation temperature, larvae (maggots) are likely to be generated, but by increasing the temperature and performing a drying operation, the generation of larvae can be suppressed.

【0039】なお、上記実施例では、設定発酵温度を4
5℃としたが、発酵微生物に応じて発酵温度を例えば4
0℃〜50℃の範囲で設定することができ、また、乾燥
温度は例えば70〜80℃に設定することができる。
In the above embodiment, the set fermentation temperature was set to 4
Although the temperature is set to 5 ° C., the fermentation temperature is set to, for example, 4 depending on the fermenting microorganism.
The temperature can be set in the range of 0 ° C to 50 ° C, and the drying temperature can be set to 70 to 80 ° C, for example.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の一実施例を示す有機廃棄物処理装置の
正面図である。
FIG. 1 is a front view of an organic waste treatment apparatus showing one embodiment of the present invention.

【図2】同右側面図である。FIG. 2 is a right side view of the same.

【図3】図2の III− III断面図である。FIG. 3 is a sectional view taken along the line III-III of FIG. 2;

【図4】図1の IV − IV 断面図である。FIG. 4 is a sectional view taken along line IV-IV of FIG. 1;

【図5】運転中の槽内(有機廃棄物)の温度の変化を示
すグラフである。
FIG. 5 is a graph showing changes in the temperature in the tank (organic waste) during operation.

【符号の説明】 1−収容槽、 4−熱風通路、 5−ダクト、 6−加熱器、 8−ブロワ、 20−撹拌機構、 30−運転制御装置、 31−廃棄物温度センサ、 32−温度設定器、 34−タイマー。[Explanation of reference symbols] 1-accommodation tank, 4-hot air passage, 5-duct, 6-heater, 8-blower, 20-stirring mechanism, 30-operation control device, 31-waste temperature sensor, 32-temperature setting Bowl, 34-timer.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 有機廃棄物を入れた収容槽内を撹拌機構
により撹拌すると共に、加熱器で加熱した熱風を該収容
槽内に循環させ、槽内の有機廃棄物を加熱・撹拌しなが
ら、有機廃棄物を発酵処理する有機廃棄物処理方法にお
いて、 有機廃棄物を収容槽に投入した後、予め設定した発酵運
転時間だけ、有機廃棄物が設定発酵温度となるように発
酵運転を行い、次に、乾燥運転に切換え、予め設定した
乾燥運転時間だけ、有機廃棄物が設定乾燥温度となるよ
うに乾燥運転を行うことを特徴とする有機廃棄物処理方
法。
1. A stirrer is used to stir the inside of a storage tank containing organic waste, and hot air heated by a heater is circulated in the storage tank to heat and stir the organic waste in the tank. In an organic waste treatment method of fermenting organic waste, after the organic waste is put into a storage tank, the fermentation operation is performed so that the organic waste reaches a set fermentation temperature for a preset fermentation operation time. In addition, the method for treating organic waste is characterized in that the drying operation is switched to the drying operation and the drying operation is performed so that the organic waste reaches a set drying temperature for a preset drying operation time.
【請求項2】 請求項1記載の有機廃棄物処理方法にお
いて、発酵運転時には前記撹拌機構を間欠運転し、乾燥
運転時には該撹拌機構を連続運転する有機廃棄物処理方
法。
2. The organic waste treatment method according to claim 1, wherein the stirring mechanism is intermittently operated during fermentation operation, and the stirring mechanism is continuously operated during drying operation.
【請求項3】 有機廃棄物を入れる収容槽内に撹拌羽根
を回転駆動する撹拌機構が配設され、該収容槽の底部の
下側に熱風通路が配設され、該収容槽内の上部に槽内を
加熱する加熱器が配設され、該収容槽上部と該熱風通路
がダクトにより連通接続され、該熱風通路の熱風を吸引
して熱風を循環させるように該収容槽内上部に送風する
ブロワが配設されてなる有機廃棄物処理装置において、 該収容槽の底部近傍に配置され有機廃棄物の温度を検出
する廃棄物温度センサと、 運転時の設定発酵温度と設定乾燥温度を設定する温度設
定器と、 発酵運転時間と乾燥運転時間を設定するタイマーと、 収容槽内の有機廃棄物が設定発酵温度となるように加熱
器を制御する発酵運転と、該有機廃棄物が設定乾燥温度
となるように加熱器を制御する乾燥運転とを、予め設定
された発酵運転時間と乾燥運転時間に基づき切換えて運
転制御する運転制御装置と、 を備えたことを特徴とする有機廃棄物処理装置。
3. An agitation mechanism for rotating and driving an agitation blade is provided in a container for containing organic waste, a hot air passage is provided below a bottom of the container, and an upper part of the container is provided with an hot air passage. A heater for heating the inside of the tank is arranged, the upper part of the containing tank and the hot air passage are connected by a duct, and the hot air in the hot air passage is sucked and blown to the upper inside of the containing tank so as to circulate the hot air. In an organic waste treatment device provided with a blower, a waste temperature sensor arranged near the bottom of the storage tank to detect the temperature of the organic waste, and a set fermentation temperature and a set drying temperature during operation are set. A temperature setter, a timer that sets the fermentation operation time and the drying operation time, a fermentation operation that controls the heater so that the organic waste in the storage tank reaches the set fermentation temperature, and the organic waste sets the drying temperature. Control the heater so that Preparative organic waste treatment apparatus comprising: the operation control device for controlling the operation switching based on a preset fermented operation time drying operation time, further comprising a.
JP7154902A 1995-06-21 1995-06-21 Treatment of organic waste and equipment therefor Pending JPH092886A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7154902A JPH092886A (en) 1995-06-21 1995-06-21 Treatment of organic waste and equipment therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7154902A JPH092886A (en) 1995-06-21 1995-06-21 Treatment of organic waste and equipment therefor

Publications (1)

Publication Number Publication Date
JPH092886A true JPH092886A (en) 1997-01-07

Family

ID=15594465

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7154902A Pending JPH092886A (en) 1995-06-21 1995-06-21 Treatment of organic waste and equipment therefor

Country Status (1)

Country Link
JP (1) JPH092886A (en)

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