JPH0889929A - Organic waste treating device - Google Patents

Organic waste treating device

Info

Publication number
JPH0889929A
JPH0889929A JP6227823A JP22782394A JPH0889929A JP H0889929 A JPH0889929 A JP H0889929A JP 6227823 A JP6227823 A JP 6227823A JP 22782394 A JP22782394 A JP 22782394A JP H0889929 A JPH0889929 A JP H0889929A
Authority
JP
Japan
Prior art keywords
temperature
organic waste
setting device
storage tank
waste
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
JP6227823A
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 JP6227823A priority Critical patent/JPH0889929A/en
Publication of JPH0889929A publication Critical patent/JPH0889929A/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

  • Drying Of Solid Materials (AREA)
  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)
  • Fertilizers (AREA)

Abstract

PURPOSE: To easily do switching between a normal operation and an organic waste treating operation in which a group of special effective microorganisms is added to easily make treatment suitable for microorganisms by controlling the operations of a heater and a blower each based on the detected temperature and the set temperature of organic waste. CONSTITUTION: Waste temperature sensors 31a, 31b are arranged near the bottom part of a housing tank 1 to detect the temperatures of organic waste. The upper limit treating temperature in a normal operation is set by the 1st temperature setting device 32, and also the upper limit treating temperature when organic waste to which a group of effective microorganisms has been added is treated is set by the 2nd temperature setting device 33. Switching between the normal operation using the 1st temperature setting device 32 and the operation using the group of effective microorganisms using the 2nd temperature setting device 33 is done by a changeover switch means 35. Operations of a heater 12 and a blower are each controlled by a controller 30, based on the temperatures of the organic waste detected by the waste temperature sensors 31 and the set temperatures of both the 1st and the 2nd temperature setting devices 32, 33.

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
を乾燥処理或は発酵処理する有機廃棄物処理装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an organic waste treatment apparatus for drying or fermenting 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、残菜等の生ごみを処理する場
合、それらを集めて発酵槽に入れ、槽内を加熱し撹拌し
ながら、微生物の発酵作用により生ごみを発酵させ、或
は同時に乾燥させて、それらを堆肥化する有機廃棄物処
理装置が、近年普及しつつある。
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, restaurants, etc., collect them and put them in a fermenter, and heat and agitate the inside of the tank while stirring the microorganisms. In recent years, an organic waste treatment device for fermenting raw garbage by the fermentation action of or, and drying it at the same time to compost them has become widespread.

【0003】[0003]

【発明が解決しようとする課題】この種の従来の一般的
な有機廃棄物処理装置は、有機廃棄物を乾燥処理する
際、発酵槽が、タイマーを用いて限時運転する構造であ
るため、例えば90%程度の含水率の生ごみを2%程度
の含水率に乾燥処理する場合、生ごみの量やその含水率
に応じて乾燥処理時間を予想し、その時間をタイマーに
セットして限時運転を行っていた。
In a conventional general organic waste treatment apparatus of this type, when the organic waste is dried, the fermentation tank has a structure in which a timer is used for a limited period of time. When drying the garbage with a moisture content of about 90% to a moisture content of about 2%, anticipate the drying treatment time according to the amount of the garbage and its moisture content, and set that time on a timer to operate in a timed manner. Was going on.

【0004】このため、タイマーにセットした運転時間
が、生ごみの量や加熱量に応じた適正時間よりずれてい
た場合、有機廃棄物が乾燥不足や過乾燥になり、所望の
乾燥状態や発酵状態の有機廃棄物を得ることが難しかっ
た。
Therefore, when the operating time set in the timer is deviated from the appropriate time corresponding to the amount of food waste and the amount of heating, the organic waste becomes insufficiently dried or overdried, and the desired dry state or fermentation is performed. It was difficult to obtain organic waste in the state.

【0005】そこで、廃棄物の温度を検出する温度セン
サを設置し、温度センサの検出温度が予め設定器に設定
した温度に上昇したとき、加熱器とブロワの運転停止を
制御する制御装置を備えた処理装置が提案された。
Therefore, a temperature sensor for detecting the temperature of the waste is installed, and a control device for controlling the operation stop of the heater and the blower is provided when the temperature detected by the temperature sensor rises to the temperature set in the preset unit. A processing device was proposed.

【0006】しかし、最近、通常の発酵微生物に代え
て、比較的低い温度で活動する有効微生物群(有機物を
有効に発酵分解する好気性微生物と嫌気性微生物を混合
した微生物の集合体)を添加して発酵・乾燥させる場合
があり、このような特殊な微生物群を廃棄物中に添加し
て処理させるためには、その微生物に応じた温度に発酵
槽内を維持し、所定時間の運転をする必要があるが、こ
のような有効微生物群に応じた運転が簡単に切換えてで
きにくい問題があった。
However, recently, instead of the usual fermenting microorganisms, a group of effective microorganisms that act at relatively low temperatures (aggregates of microorganisms that mix aerobic and anaerobic microorganisms that effectively ferment and decompose organic matter) are added. It may be fermented and dried, and in order to add and treat such special microorganisms in the waste, the fermentation tank should be maintained at a temperature according to the microorganisms and operated for a predetermined time. However, there is a problem that it is difficult to easily switch the operation depending on the effective microorganism group.

【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、通常運転と特殊な有効微生物群を添加し
た有機廃棄物の処理運転とを簡単に切換えて、微生物に
合った処理を容易に行うことができる有機廃棄物処理装
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 can easily switch between normal operation and treatment operation of organic waste to which special effective microorganisms are added to perform treatment suitable for microorganisms. It is an object of the present invention to provide an organic waste treatment device that can be easily performed.

【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、通常運転時の上限処理温度を設定する
第一温度設定器と、有効微生物群を添加した有機廃棄物
を処理する際の上限処理温度を設定する第二温度設定器
と、第一温度設定器を使用する通常運転時と第二温度設
定器を使用する有効微生物群使用の運転時とを切換える
切換スイッチ手段と、廃棄物温度センサの検出する有機
廃棄物の温度と第一温度設定器及び第二温度設定器の設
定温度に基づいて加熱器とブロワの運転を制御する運転
制御装置と、を備えて構成される。
To this end, in the organic waste treatment apparatus of the present invention, a stirring mechanism for rotating and driving a stirring blade is provided in a storage tank for storing organic waste, and a stirring mechanism is installed at the bottom of the storage tank. A hot air passage is arranged on the lower side, a heater for heating the inside of the storage tank is arranged in the upper part of the storage tank, the upper part of the storage tank and the hot air passage are connected by a duct, and the hot air in the hot air passage is sucked in In an organic waste treatment device in which a blower for blowing air is installed in the upper part of the storage tank so as to circulate, a waste temperature sensor that is located near the bottom of the storage tank to detect the temperature of the organic waste, and normal operation The first temperature setter that sets the upper limit treatment temperature at the time, the second temperature setter that sets the upper limit treatment temperature when treating the organic waste to which the effective microorganism group is added, and the first temperature setter are used. During normal operation and using the second temperature setting device Yes A change-over switch means for switching between using the microorganism group and operating the heater and blower based on the temperature of the organic waste detected by the waste temperature sensor and the set temperatures of the first temperature setter and the second temperature setter. And an operation control device for controlling the.

【0009】[0009]

【作用】通常の発酵微生物を添加した有機廃棄物を処理
する場合、切換スイッチ手段を第一温度設定器を使用す
る通常運転用に切換え、収容槽にその有機廃棄物を投入
し、撹拌機構の撹拌羽根を回転させ、同時に加熱器を動
作させると共にブロワを運転する。
In the case of treating an organic waste to which a normal fermenting microorganism is added, the changeover switch means is switched to the normal operation using the first temperature setting device, the organic waste is put into the storage tank, and the stirring mechanism is operated. The stirring blade is rotated, and at the same time, the heater is operated and the blower is operated.

【0010】収容槽内の有機廃棄物は、加熱器からの輻
射熱によって加熱されると共に、槽内上部の空気も加熱
される。そして、加熱された空気は、ブロワによってダ
クトを通り、底部の熱風通路に送られ、収容槽の底部も
加熱され、その後の熱風はブロワによって収容槽の上部
に吹出される。ブロワの作用により熱風が循環され、上
からの輻射熱と底部からの熱により、槽内の有機廃棄物
は効率良く加熱され、乾燥されていく。
The organic waste in the storage tank is heated by the radiant heat from the heater and the air in the upper part of the tank is also heated. Then, the heated air passes through the duct by the blower and is sent to the hot air passage at the bottom, the bottom of the storage tank is also heated, and the hot air thereafter is blown out to the upper part of the storage tank by the blower. Hot air is circulated by the action of the blower, and the radiant heat from above and the heat from the bottom efficiently heat and dry the organic waste in the tank.

【0011】第一温度設定器は、上限温度つまり処理終
了時の廃棄物温度を例えば100℃に設定して加熱運転
を開始するが、上記のような効率の良い加熱構造を有し
ているため、含水率が85%〜90%と水分を非常に多
く含んだ有機廃棄物であっても、槽内の温度は良好に上
昇し、有機廃棄物の水分は効率良く蒸発して排気され、
含水率は低下していく。上記構成の処理装置の場合、実
験結果によれば、含水率の大きい有機廃棄物(含水率9
0%程度の生ごみ)を乾燥処理した場合、加熱器の熱量
や有機廃棄物の量に拘らず、廃棄物の温度と乾燥状態の
有機廃棄物の含水率は、例えば、80℃で約22%、9
2℃で約15%、100℃で約8%、とほぼ一定の関係
を示すことが判明している。
The first temperature setter starts the heating operation by setting the upper limit temperature, that is, the waste temperature at the end of the treatment to, for example, 100 ° C., but has the above-mentioned efficient heating structure. , Even if the organic waste has a very high water content of 85% to 90%, the temperature in the tank rises well, and the water of the organic waste is efficiently evaporated and exhausted.
The water content decreases. In the case of the treatment device having the above-mentioned configuration, according to the experimental results, organic waste having a large water content (water content 9%
When about 0% of raw garbage is dried, the temperature of the waste and the water content of the organic waste in a dry state are, for example, about 22 at 80 ° C regardless of the heat quantity of the heater and the amount of the organic waste. %, 9
It has been found that there is an almost constant relationship between about 15% at 2 ° C and about 8% at 100 ° C.

【0012】したがって、この処理装置を使用して例え
ば含水率8%の乾燥処理品を得ようとする場合、収容槽
底部の温度(槽内の有機廃棄物の温度に対応する)を検
出し、その温度が100℃に達したとき、加熱器の運転
を停止すれば、加熱器の熱量や有機廃棄物の量に拘ら
ず、所望の含水率の乾燥処理品を容易に得ることができ
る。
Therefore, when using this processing apparatus to obtain a dried product having a water content of 8%, for example, the temperature at the bottom of the storage tank (corresponding to the temperature of the organic waste in the tank) is detected, If the operation of the heater is stopped when the temperature reaches 100 ° C., a dried product having a desired water content can be easily obtained regardless of the heat amount of the heater and the amount of organic waste.

【0013】一方、有効微生物群を添加した有機廃棄物
を処理する場合、切換スイッチ手段を、第二温度設定器
を使用する運転用に切換え、収容槽にその有機廃棄物を
投入し、撹拌機構の撹拌羽根を回転させ、同時に加熱器
を動作させると共にブロワを運転する。第一温度設定器
は、設定温度を例えば60℃に設定して運転を開始する
が、有機廃棄物の上限温度が60℃に抑制されるため、
比較的低い温度で活動する有効微生物群を活性化した状
態で、発酵・乾燥処理することができる。
On the other hand, when treating the organic waste to which the effective microorganism group is added, the changeover switch means is switched to the operation using the second temperature setting device, the organic waste is put into the storage tank, and the stirring mechanism is used. Rotate the stirring blade of No. 1 and simultaneously operate the heater and operate the blower. The first temperature setter starts the operation by setting the set temperature to, for example, 60 ° C, but since the upper limit temperature of the organic waste is suppressed to 60 ° C,
Fermentation / drying treatment can be carried out in a state in which the effective microorganism group that operates at a relatively low temperature is activated.

【0014】また、有効微生物群を添加した有機廃棄物
は水分が非常に多いが、この処理装置では、撹拌と熱
風、輻射熱等により効率良く加熱し、蒸気は排出するた
め、廃棄物を良好に乾燥させることができる。
Further, the organic waste added with the effective microorganism group has a very large amount of water, but in this treatment apparatus, the waste is satisfactorily heated because it is efficiently heated by stirring, hot air, radiant heat, etc., and steam is discharged. It can be dried.

【0015】[0015]

【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.

【0016】図1は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 shows a front view of the processing apparatus, and FIG. 2 shows a right side view thereof.

【0017】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.

【0018】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接続の接続口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 along a meandering direction, 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 disposed in contact with the rear side wall 5 and the bottom wall 4 of the storage tank 1, the thermal conductivity to the storage tank 1 is good and the storage tank 1
Is a structure capable of efficiently receiving the conduction heat from the heating duct portion 6.

【0019】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 at the upper part of the storage tank 1 from the right side thereof. There is.

【0020】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 a heating source of the heater 12, but a high / low type in which a pilot burner is constantly ignited is used to prevent a 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.

【0021】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.

【0022】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 provided with an adjusting lid 18a for supplying the outside air to the intake side of the blower 16 and adjusting the amount of air supply. The air supply port 18 may be arranged at any position between the blower 16 and the connection port 10.

【0023】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 part of the storage tank 1, that is, the heater 1 is operated 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.

【0024】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により回転されるように形成
されている。
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 formed so as to be rotated by 24.

【0025】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.

【0026】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31a,31b
が設置される。この2つの温度センサ31a,31b
は,後述の第一温度設定器32、第二温度設定器33に
対応して設けられ、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。
In order to detect the temperature of the organic waste in the tank, waste temperature sensors 31a and 31b are provided at the bottom of the storage tank 1.
Is installed. These two temperature sensors 31a and 31b
Are provided corresponding to a first temperature setting device 32 and a second temperature setting device 33, which will be described later, and are connected to the operation control device 30. 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.

【0027】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、通常運転時の上限処理温度を設定する第一
温度設定器32と、有効微生物群を添加した有機廃棄物
を処理する際の上限処理温度を設定する第二温度設定器
33と、第一温度設定器32を使用する通常運転時と第
二温度設定器33を使用する有効微生物群使用の運転時
とを切換える切換スイッチ手段35とが、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 a timer 34 for setting the operation time are connected thereto. To be done. Furthermore, a first temperature setting device 32 that sets an upper limit processing temperature during normal operation, a second temperature setting device 33 that sets an upper limit processing temperature when processing an organic waste to which an effective microorganism group is added, and a first temperature setting device 33. The changeover switch means 35 for switching between the normal operation using the temperature setting device 32 and the operation using the effective microorganism group using the second temperature setting device 33 is connected to the operation control device 30.

【0028】また、運転制御装置30は、廃棄物温度セ
ンサ31a,31bの検出する有機廃棄物の温度と第一
温度設定器32及び第二温度設定器33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。第一
温度設定器32には例えば100℃が設定され、第二温
度設定器33には例えば60℃が設定される。
Further, the operation control device 30 selects the heater 12 based on the temperature of the organic waste detected by the waste temperature sensors 31a and 31b and the set temperatures of the first temperature setter 32 and the second temperature setter 33. The operation of the blower 16 is controlled. For example, 100 ° C. is set in the first temperature setting device 32, and 60 ° C. is set in the second temperature setting device 33.

【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】通常の発酵微生物を添加した有機廃棄物を
処理する場合、切換スイッチ手段35を、第一温度設定
器32を使用する通常運転用に切換える。そして、処理
する生ごみ等の有機廃棄物Aを、上部の投入用ハッチ2
を開いて収容槽1内に投入する。
In the case of treating an organic waste to which a normal fermenting microorganism is added, the changeover switch means 35 is changed over to the normal operation using the first temperature setting device 32. Then, the organic waste A such as raw garbage to be processed is fed into the upper hatch 2
Is opened and put into the storage tank 1.

【0031】次に、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。従って、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17より再び
収容槽1に戻される。
Next, the motor 24 is started to start the stirring mechanism 20.
The stirring blade 22 of is rotated to stir the organic waste A.
At the same time, the heater 12 is started to start heating, and the blower 16
Is operated, the heating duct portion 6 and the circulation duct 15 become negative pressure. Therefore, the hot air in the upper part of the storage tank 1 is sucked into the heating duct portion 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 returned to the storage tank 1 through the outlet 17 again.

【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、
撹拌されながら効率良く加熱される。
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.
Efficiently heated with stirring.

【0033】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効果的
にされる。さらに、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は効
率良く多重加熱・乾燥される。
Further, since the heating duct portion 6 for passing hot air is attached directly to the rear side wall 5 and the bottom wall 4 of the storage tank 1, the heat of the heater 12 is conducted to the middle portion and the bottom portion of the storage tank 1. The storage tank 1 is also made effective by the conduction heat. Furthermore, 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 organic waste A in the tank can also be efficiently multi-heated and dried by the hot air. To be done.

【0034】そして、加熱された有機廃棄物Aより発生
した水蒸気を含む収容槽1内部の空気は、ブロワ16か
らの吐出により正圧となり、その一部が仕切板27と有
機廃棄物Aとの間を通って排気ダクト25から適度に排
出される。
Then, the air in the storage tank 1 containing the steam generated from the heated organic waste A becomes a positive pressure due to the discharge from the blower 16, and a part of the air is separated between the partition plate 27 and the organic waste A. It is appropriately discharged from the exhaust duct 25 through the space.

【0035】このとき、収容槽1内における仕切板27
の右方側の圧力は、仕切板27の左方側の圧力より高
く、その圧力差によって、排気は仕切板27の下方を迂
回して良好に排出される。従って、熱気が直ちに排気さ
れることがなく、その排出経路が長くなり、排気が高温
雰囲気中を通過するため、脱臭効果も良好となる。
At this time, the partition plate 27 in the storage tank 1
The pressure on the right side of is higher than the pressure on the left side of the partition plate 27, and due to the pressure difference, the exhaust gas bypasses the lower part of the partition plate 27 and is discharged well. Therefore, the hot air is not immediately exhausted, the exhaust path becomes long, and the exhaust gas passes through the high temperature atmosphere, so that the deodorizing effect is also improved.

【0036】また、仕切板27によって、加熱器12お
よび遠赤外線放射多孔板13からの輻射熱が排気ダクト
25側へ放散されることが防止されるため、収容槽1内
を効率良く加熱することができる。
Further, since the partition plate 27 prevents the radiant heat from the heater 12 and the far-infrared radiation porous plate 13 from being dissipated to the exhaust duct 25 side, the inside of the storage tank 1 can be efficiently heated. it can.

【0037】運転開始時は、熱風温度を最高温度付近に
保持し、且つ上記のような効率の良い加熱構造を有して
いるため、含水率が85%〜90%と水分を非常に多く
含んだ有機廃棄物であっても、槽内の温度は急速に上昇
し、有機廃棄物の水分は効率良く蒸発して排気され、含
水率は低下していく。
At the start of the operation, the hot air temperature is maintained near the maximum temperature and the heating structure having high efficiency as described above is used. Therefore, the water content is 85% to 90% and the water content is very high. However, even for organic waste, the temperature in the tank rises rapidly, the water content of the organic waste is efficiently evaporated and exhausted, and the water content decreases.

【0038】上記構成の処理装置の場合、実験結果によ
れば、含水率の大きい有機廃棄物(含水率90%程度の
生ごみ)を乾燥処理した場合、加熱器の熱量や有機廃棄
物の量に拘らず、廃棄物の温度と乾燥状態の有機廃棄物
の含水率は、例えば、80℃で22%、92℃で15
%、100℃で約8%、とほぼ一定の関係を示すことが
判明している。
In the case of the treatment apparatus having the above-mentioned structure, according to the experimental results, when the organic waste having a large water content (garbage with a water content of about 90%) is dried, the heat quantity of the heater and the amount of the organic waste. Regardless of the temperature of the waste and the water content of the organic waste in the dry state, for example, 22% at 80 ° C and 15% at 92 ° C.
%, And about 8% at 100 ° C., it has been found to show a substantially constant relationship.

【0039】このため、乾燥処理によって、有機廃棄物
の含水率が約25%程度まで低下すると、図5のグラフ
Bに示すように、有機廃棄物の温度上昇が再び発生して
乾燥が急速に進み、廃棄物の温度が設定温度(ここでは
100℃)に達する。運転制御装置が廃棄物温度センサ
31aを介してこの温度を検出したとき、加熱器12が
停止され、その後、ブロワ16、撹拌機構20が一定時
間運転を継続した後、運転を終了する。
Therefore, when the water content of the organic waste is reduced to about 25% by the drying treatment, as shown in the graph B of FIG. Then, the temperature of the waste reaches the set temperature (here, 100 ° C.). When the operation control device detects this temperature via the waste temperature sensor 31a, the heater 12 is stopped, and then the blower 16 and the stirring mechanism 20 continue to operate for a certain period of time, and then the operation ends.

【0040】したがって、有機廃棄物処理装置を使用し
て例えば含水率8%の乾燥処理品を得ようとする場合、
収容槽底部の温度(槽内の有機廃棄物の温度に対応す
る)を検出し、その温度が100℃に達したとき、加熱
器12の運転を停止すれば、加熱器12の熱量や有機廃
棄物の量に拘らず、所望の含水率の乾燥処理品を容易に
得ることができる。
Therefore, when an organic waste treatment device is used to obtain a dried product having a water content of 8%, for example,
The temperature of the bottom of the storage tank (corresponding to the temperature of the organic waste in the tank) is detected, and when the temperature reaches 100 ° C., if the operation of the heater 12 is stopped, the heat amount of the heater 12 and the organic waste It is possible to easily obtain a dried product having a desired water content regardless of the amount of the product.

【0041】一方、特殊な有効微生物群(有機物を有効
に発酵分解する好気性微生物と嫌気性微生物を混合した
微生物の集合体)を添加した有機廃棄物を処理する場
合、切換スイッチ手段35を、第二温度設定器33を使
用する運転用に切換え、収容槽1に有機廃棄物を投入
し、撹拌機構20の撹拌羽根22を回転させ、同時に加
熱器12を動作させると共にブロワ16を運転する。
On the other hand, when treating an organic waste to which a special effective microorganism group (aggregate of microorganisms in which aerobic microorganisms and anaerobic microorganisms that effectively ferment and decompose organic matter are mixed) is treated, the changeover switch means 35 is The operation is switched to the operation using the second temperature setting device 33, the organic waste is charged into the storage tank 1, the stirring blades 22 of the stirring mechanism 20 are rotated, and at the same time, the heater 12 is operated and the blower 16 is operated.

【0042】第二温度設定器33は、温度を例えば60
℃に設定して加熱運転を開始する。有機廃棄物の上限温
度を60℃に設定する温度設定器33と廃棄物温度セン
サ31bにより有機廃棄物の温度を管理しながら運転す
るため、低温で活動する有効微生物群を活性化した状態
で発酵・乾燥処理が行われる。運転はタイマー34にセ
ットした時間継続され、図5のグラフCに示すように、
60℃付近で発酵・乾燥処理が継続される。そして、タ
イマー34の時間に達したとき、加熱器12の運転を停
止し、その後、ブロワ16と撹拌機構20が一定時間運
転を継続した後、運転を終了する。
The second temperature setting device 33 sets the temperature to 60, for example.
Set to ℃ and start the heating operation. Since the organic waste is operated while controlling the temperature of the organic waste by the temperature setter 33 for setting the upper limit temperature of the organic waste to 60 ° C. and the waste temperature sensor 31b, fermentation is carried out in a state in which active microorganisms that are active at low temperatures are activated. -A drying process is performed. The operation is continued for the time set in the timer 34, and as shown in the graph C of FIG.
The fermentation and drying process is continued at around 60 ° C. Then, when the time of the timer 34 is reached, the operation of the heater 12 is stopped, after which the blower 16 and the stirring mechanism 20 continue to be operated for a certain period of time, and then the operation is terminated.

【0043】このように、有機廃棄物の温度が有効微生
物群に適した温度で発酵・乾燥処理が行われるため、有
効微生物群を活性化した状態で処理することができる。
また、より高い温度で運転する通常運転とこの有効微生
物を添加し低い温度の運転とは、切換スイッチ手段35
を操作するだけで、簡単に切換えて運転することがで
き、誤操作が少なくなる。
As described above, since the fermentation / drying treatment is carried out at the temperature of the organic waste which is suitable for the effective microorganism group, the effective microorganism group can be treated in an activated state.
In addition, the normal operation of operating at a higher temperature and the operation of a lower temperature with the addition of this effective microorganism are performed by the changeover switch means 35.
Just by operating, you can easily switch and operate, reducing erroneous operations.

【0044】[0044]

【発明の効果】以上説明したように、本発明の有機廃棄
物処理装置によれば、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、通常運転
時の上限処理温度を設定する第一温度設定器と、有効微
生物群を添加した有機廃棄物を処理する際の上限処理温
度を設定する第二温度設定器と、第一温度設定器を使用
する通常運転時と第二温度設定器を使用する有効微生物
群使用の運転時とを切換える切換スイッチ手段と、廃棄
物温度センサの検出する有機廃棄物の温度と第一温度設
定器及び第二温度設定器の設定温度に基づいて加熱器と
ブロワの運転を制御する運転制御装置と、を備えて構成
したから、通常の有機廃棄物の場合には比較的高い温度
で廃棄物を効率良く乾燥処理することができ、また、有
効微生物群を添加した有機廃棄物については、有効微生
物群に適した温度で発酵・乾燥処理を行うことができる
ため、有効微生物群を活性化した状態で処理することが
できる。
As described above, according to the organic waste treatment apparatus of the present invention, the waste temperature sensor arranged near the bottom of the storage tank for detecting the temperature of the organic waste and the upper limit during normal operation. At the time of normal operation using the first temperature setter that sets the treatment temperature, the second temperature setter that sets the upper limit treatment temperature when treating organic waste with added effective microorganisms, and the first temperature setter And a changeover switch means for switching between the use of the effective microorganism group using the second temperature setting device and the temperature of the organic waste detected by the waste temperature sensor and the setting of the first temperature setting device and the second temperature setting device. Since it is equipped with an operation control device that controls the operation of the heater and blower based on the temperature, in the case of ordinary organic waste, the waste can be efficiently dried at a relatively high temperature. , Also added effective microorganisms The organic waste, it is possible to perform the fermentation and drying process at a temperature suitable to enable microorganisms can be treated in a state of activation of effective microorganisms.

【0045】また、より高い温度で運転する通常運転
と、有効微生物群を添加しより低い温度で行なう運転と
は、切換スイッチ手段を切換え操作するだけで、簡単に
切換えて運転することができ、誤操作により有効微生物
群をダメにしてしまう恐れが少なくなる。
Further, the normal operation, which is operated at a higher temperature, and the operation, which is performed at a lower temperature by adding the effective microorganism group, can be easily switched and operated simply by switching the changeover switch means. There is less risk of misuse of the effective microorganisms by erroneous operation.

【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 device showing an 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。3 is a sectional view taken along line III-III in FIG.

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

【図5】運転中の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 of organic waste during operation.

【符号の説明】[Explanation of symbols]

1−収容槽、 4−熱風通路、 5−ダクト、 6−加熱器、 8−ブロワ、 10−撹拌機構、 30−運転制御装置、 31a,31b−廃棄物温度センサ、 32−第一温度設定器、 33−第二温度設定器、 35−切換スイッチ手段。 1-accommodation tank, 4-hot air passage, 5-duct, 6-heater, 8-blower, 10-stirring mechanism, 30-operation control device, 31a, 31b-waste temperature sensor, 32-first temperature setting device 33-Second temperature setting device, 35-Changeover switch means.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C05F 9/02 D 7537−4H F26B 11/14 25/00 A ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location C05F 9/02 D 7537-4H F26B 11/14 25/00 A

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 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、 通常運転時の上限処理温度を設定する第一温度設定器
と、 有効微生物群を添加した有機廃棄物を処理する際の上限
処理温度を設定する第二温度設定器と、 該第一温度設定器を使用する通常運転と、該第二温度設
定器を使用する有効微生物群使用の運転とを切換える切
換スイッチ手段と、 前記廃棄物温度センサの検出する有機廃棄物の温度と第
一温度設定器及び第二温度設定器の設定温度に基づいて
前記加熱器とブロワの運転を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。
1. A stirring mechanism for rotating and driving a stirring blade is provided in a storage tank for containing organic waste, a hot air passage is provided below a bottom portion of the storage tank, and a hot air passage is provided at an upper portion of the storage tank. 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 first temperature for setting an upper limit treatment temperature during normal operation. A setting device, a second temperature setting device for setting an upper limit processing temperature when treating an organic waste to which an effective microorganism group has been added, a normal operation using the first temperature setting device, and a second temperature setting device Switching to switch between operation using effective microorganism groups using Switch means, an operation control device for controlling the operation of the heater and the blower based on the temperature of the organic waste detected by the waste temperature sensor and the set temperatures of the first temperature setting device and the second temperature setting device, An organic waste treatment device comprising:
JP6227823A 1994-09-22 1994-09-22 Organic waste treating device Pending JPH0889929A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6227823A JPH0889929A (en) 1994-09-22 1994-09-22 Organic waste treating device

Applications Claiming Priority (1)

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JP6227823A JPH0889929A (en) 1994-09-22 1994-09-22 Organic waste treating device

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JPH0889929A true JPH0889929A (en) 1996-04-09

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JP6227823A Pending JPH0889929A (en) 1994-09-22 1994-09-22 Organic waste treating device

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000037188A1 (en) * 1998-12-18 2000-06-29 Mihara Co., Ltd. Food waste treating device
KR100260505B1 (en) * 1998-03-25 2000-07-01 정재덕 A fermentation/dry apparatus of waste foods
KR100270023B1 (en) * 1998-03-30 2000-11-01 구자홍 A apparatus for food garbage using and method therreof
EP2274112A1 (en) * 2008-05-16 2011-01-19 Lee, Myeong Ryul Food garbage disposer
KR20190111289A (en) * 2018-03-22 2019-10-02 서울시립대학교 산학협력단 Bio-drying device for returning of waste gas and bio-drying method using the same

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100260505B1 (en) * 1998-03-25 2000-07-01 정재덕 A fermentation/dry apparatus of waste foods
KR100270023B1 (en) * 1998-03-30 2000-11-01 구자홍 A apparatus for food garbage using and method therreof
WO2000037188A1 (en) * 1998-12-18 2000-06-29 Mihara Co., Ltd. Food waste treating device
EP2274112A1 (en) * 2008-05-16 2011-01-19 Lee, Myeong Ryul Food garbage disposer
EP2274112A4 (en) * 2008-05-16 2014-11-12 Lee Myeong Ryul Food garbage disposer
KR20190111289A (en) * 2018-03-22 2019-10-02 서울시립대학교 산학협력단 Bio-drying device for returning of waste gas and bio-drying method using the same

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