JPH0448982A - Garbage treatment apparatus - Google Patents
Garbage treatment apparatusInfo
- Publication number
- JPH0448982A JPH0448982A JP2159004A JP15900490A JPH0448982A JP H0448982 A JPH0448982 A JP H0448982A JP 2159004 A JP2159004 A JP 2159004A JP 15900490 A JP15900490 A JP 15900490A JP H0448982 A JPH0448982 A JP H0448982A
- Authority
- JP
- Japan
- Prior art keywords
- kitchen waste
- garbage
- temp
- temperature
- air
- 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
Links
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明(よ 家庭あるいは業務上で発生する厨芥の処理
に利用されるものであム
従来の技術
厨芥に含まれる水分量は70〜80%であり、この水分
が厨芥の腐敗や悪臭の大きな原因となっていた また
厨芥をごみ置き場まで持ち運ぶ際へごみ袋から水滴が漏
れ基板 建物の廊下やエレベータ等を汚してい九 そこ
玄 従来 このような処理が厄介な厨芥を処理する装置
として↓よ ディスポーザーと呼ばれる機械式処理装置
と、焼却炉と呼ばれる燃焼式処理装置との2方式があっ
t4機械式処理装置すなわちディスポーザ1よ ごみを
フライホイールの回転によりはね飛ばし シュレダーで
粉砕し ハンマーで叩きつぶして、下水に流して処理す
る方式であも
これに対して、燃焼式処理装置すなわち焼却炉は ごみ
を間欠的に燃焼させるバッチ燃焼炉と、ごみをベルトに
より炉内に次々と移動させ連続的に燃焼させる連続燃焼
炉があム どちらの燃焼炉L ガス燃料あるいは液体燃
料をバーナで燃焼しその燃焼熱でごみを焼却して処理す
る方法であ本発明が解決しようとする課題
このような従来の厨芥処理装置にζ友 以下に示すよう
な課題があっな
ディスポーザーは機械的に生ごみを細かく処理している
力(卵殻 貝殻 繊維質等が分解されず、下水に流した
場合に 排水の中に多量の固形分を含へ そのために下
水道を詰まらせたり、異臭を発生させたりするという大
きな問題が生じていちまた 焼却炉はいろいろな種類の
ごみを一度に取扱いで献 処理残量を著しく減少させ、
病原菌などを完全に死滅させるという特徴がある力交
そのために構造が複雑て 装置が大型になり、燃焼制御
がむずかしくなり、このために発煙や発臭などを起こし
やすく、環境汚染を生じるなどの大きな欠点があった
一人 厨芥の含水量は70〜80%であり、加熱乾燥に
より厨芥に含まれる水分を除去すれば 厨芥の重量を2
0〜30%に減少することができも しかL 厨芥を加
熱乾燥した場合、厨芥内部を均一に加熱することは難し
く、厨芥の乾燥は不均一に進行すも したがって厨芥の
乾燥が終了した時点では 厨芥内部にかなりの温度分布
が存在するようになム 家庭などから排出される厨芥に
は 食品などの包装に使われているプラスチック類が混
入する場合が多(−このため厨芥内部に温度分布が存在
すると、これらの包装用プラスチックが高温になり、厨
芥の乾燥過程で有害ガスを発生したり、悪臭を出す原因
になム
本発明は簡単な構成で、厨芥を無臭でかつ有害ガスの発
生を抑えて乾燥処理する厨芥処理装置を提供するもので
あム
課題を解決するための手段
厨芥の収納室と、厨芥の加熱手段と、厨芥から発生した
ガス体の搬送用空気を収納室に供給する送風手段と、収
納室の下流に設けた排気口とから構成さhi芥の温度が
100℃以上250℃以下になるように 厨芥を加熱す
るものであムまた 収納室内における搬送用空気の供給
経路を、厨芥の上方空間とし 搬送用空気が厨芥に直接
接触しないようにするものである。DETAILED DESCRIPTION OF THE INVENTION Industrial Field of Application The present invention is used for processing kitchen waste generated at home or in business. , this moisture was a major cause of spoilage and bad odors in kitchen waste.
When kitchen waste is carried to the garbage storage site, water droplets leak from the garbage bag and pollute the board, hallways, elevators, etc. of buildings. There are two methods: a combustion type treatment device called an incinerator, and a combustion type treatment device called an incinerator.T4Mechanical treatment device, that is, a disposer 1The garbage is thrown away by the rotation of a flywheel, crushed by a shredder, crushed by a hammer, and disposed of by discharging it into the sewer. On the other hand, there are two types of combustion processing equipment, or incinerators: batch combustion furnaces that burn waste intermittently, and continuous combustion furnaces that move waste one after another into the furnace using a belt and burn it continuously. Am Which combustion furnace L Problems that the present invention aims to solve with a method of burning gas fuel or liquid fuel in a burner and incinerating waste with the combustion heat. Disposers have the following problems: they mechanically process food waste finely (eggshells, seashells, fibers, etc.) are not decomposed, and when disposed of into the sewer, the wastewater contains a large amount of solids. This has caused major problems such as clogging sewers and emitting strange odors.Furthermore, incinerators handle many different types of waste at once, significantly reducing the amount left for disposal.
A type of physical therapy that is characterized by the ability to completely kill pathogens, etc.
As a result, the structure is complicated, the equipment becomes large, combustion control is difficult, and this causes major drawbacks such as easy smoke and odor generation, and environmental pollution. %, and if the moisture contained in kitchen waste is removed by heating and drying, the weight of kitchen waste will be 2.
When kitchen waste is heated and dried, it is difficult to uniformly heat the inside of the kitchen waste, and the drying of the kitchen waste proceeds unevenly. Therefore, when the kitchen waste is finished drying, There is now a considerable temperature distribution inside kitchen waste. Kitchen waste discharged from households is often contaminated with plastics used for packaging foods. If present, these packaging plastics will become hot and cause harmful gases or bad odors to be generated during the drying process of kitchen waste. To provide a kitchen waste processing device that performs a drying process by suppressing food waste. Means for solving the problem A kitchen waste storage chamber, a heating means for kitchen waste, and a supply of air for conveying the gas generated from the kitchen waste to the storage chamber. It is composed of an air blowing means and an exhaust port provided downstream of the storage chamber, and is used to heat the kitchen waste so that the temperature of the garbage is 100°C or higher and 250°C or lower. is the space above the kitchen waste to prevent the conveying air from coming into direct contact with the kitchen waste.
作用
この技術的手段による作用は次のようになム収納室に厨
芥を収納すも この状態で、収納室に設けた加熱手段を
運転するとともに 収納室に搬送用空気を供給すム 厨
芥の温度が上昇し 厨芥に含まれる水分が蒸発L 厨
芥は乾燥し始める。The effect of this technical means is as follows: The kitchen waste is stored in the storage room. In this state, the heating means installed in the storage room is operated, and the air for conveyance is supplied to the storage room. The temperature of the food waste is rises and the water contained in the kitchen waste evaporates L The kitchen waste begins to dry.
ここで収納室には厨芥の温度を検出する温度検出手段が
設けられ 乾燥時に厨芥の温度をモニターしなか収 厨
芥の乾燥を行う。厨芥の温度は温度検出手段からの信号
により、100℃以上250℃以下の範囲で設定できる
ようへ 加熱手段の加熱量をコントロールしていも 厨
芥の温度が100℃以上250℃以下の領域では厨芥の
水分は蒸発する力(厨芥に混入した食品包装用プラスチ
ックは熱分解しな(℃ このために 厨芥の乾燥過程で
有害ガスを発生したり、悪臭を出すことはな(も厨芥が
収納室に収納された直後は厨芥の回りには酸素が存在す
ム 加熱され乾燥が進むと厨芥から水蒸気が発生L 厨
芥の回りは水蒸気で満たされるようになり、無酸素状態
となも したがって、収納室内における搬送用空気の供
給経路を、厨芥の上方空間とし 搬送用空気が厨芥に直
接接触しないように 搬送用空気を厨芥の収納室に供給
すると、乾燥過程において厨芥の雰囲気は絶えず無酸素
状態になム このた敦 厨芥の加熱時に厨芥の自然発火
を抑制するととも艮 熱分解ガスが酸化されず悪臭の発
生を抑えることができも加熱手段にマグネトロンを用い
た場合は以下のような作用があ4JR芥の中にフォーク
やスプーンなどのような金属物が混入した状態で、マイ
クロ波を用いて厨芥の乾燥処理を行った場合 金属物は
マイクロ波を受信してスパークを発生しゃすくなも し
たがって厨芥の雰囲気に酸素が存在すると、このスパー
クにより厨芥が発火L−厨芥の温度が急激に上昇し 有
害ガスや悪臭が発生すムそこで厨芥の温度をモニターし
なが6N芥にマイクロ波を照射して乾燥を行うとともに
搬送用空気が厨芥に直接接触しないようぬ 搬送用空
気を厨芥の収納室に供給する。このために 厨芥の温度
は100℃以上250℃以下の範囲で維持され たとえ
厨芥に混入した金属物がマイクロ波を受信してスパーク
を発生してL 厨芥の発火を防止しできも
実施例
以下、本発明の一実施例を添付図面に基づいて説明すも
第1図において、収納室1の内部に厨芥2が収納されも
収納室1の外壁にはヒータ3が設置されており、ヒー
タ3に通電することにより、厨芥2を加熱乾燥できも
送風機4は空気室5を介して空気口6から搬送用空気を
収納室1に供給すム厨芥2の温度を検出するために温度
検出部7が設けられていも 温度検出部7は本実施例の
ように厨芥2に直接接触して取り付けてもよいL 厨
芥2に近接して設けてもよしも ここで、温度検出部7
は サーモカップ/14 光センサなどで、温良光な
どを検知して、厨芥2の温度を検出できるものであム
本実施例ではサーモカップルを用いていも 温度検出部
7の信号は温度コントローラ8に送られ 厨芥2の温度
が設定値になるようにヒータ3の通電量をコントロール
すも
収納室1の下流に設けられた触媒9はその周囲を触媒加
熱用ヒータ(図示せず)で覆われ 触媒がたえず活性温
度を維持するように保温されていも始動時に触媒加熱用
ヒータに通電し あらかじめ触媒9を活性温度まで昇温
させも 触媒9が活性温度に到達すると、ヒータ3の通
電を開始し収納室1に搬送用空気を供給すも ヒータ3
により厨芥2の温度が上昇LA 厨芥2の水分が蒸発
し厨芥2は乾燥し始めも 蒸発した水分は排気1410
から排出されも 乾燥時は厨芥2の温度を温度検出部7
からの信号によりモニターしなが収 厨芥2の乾燥を行
う。厨芥2の温度は100℃以上250℃以下の範囲で
設定できるように 温度コントローラ8によりヒータ3
の加熱量をコントロールすも一般凶 食品包装用プラス
チックにはポリエチレン、ポリプロピレン、ポリスチレ
ン、塩化ビニ/14 塩化ビニリデン等が良く使われ
も これら食品包装用プラスチックの昇温過程における
重量減少率を第2図〜第7図に示す(喜多信之著 プラ
スチックの燃焼性 工業調査会)。第2図はポリエチレ
ン、第3図はポリプロピレン、第4図はポリスチレン、
第5図はポリ塩化ビニ/k 第6図はポリ塩化ビニリ
デン、第7図はポリエチレンテレフタレートについて示
してあム これらの図より250℃〜400℃の温度範
囲で、各種プラスチックが急激に熱分解することがわか
ム この時、各種プラスチックから塩素ガス 塩化水素
ガス −酸化炭棗 アルデヒド等の有毒ガスが発生し
悪臭もきつくなも 特に塩素ガスや塩化水素ガスは浄化
用触媒で除去することは難しく、これらのガスの発生は
極力抑えなければならな(l
−X 水の沸点は100℃であり、厨芥の温度を10
0℃以上にすると、厨芥中の水分は急激に蒸発すも
したがって、たとえ厨芥2に食品包装用プラスチックが
混入してL ヒータ3の加熱量をコントロールシ厨芥2
の温度を100℃以上250 t:以下に設定すれは
プラスチックの熱分解を最小限に抑えて、厨芥2を加熱
乾燥でき、厨芥の乾燥過程で有害ガスが発生せず、悪臭
を出さず6ζ 厨芥を乾燥処理できも
さらに収納室1内における搬送用空気の供給経路を、厨
芥2の上方空間とし 搬送用空気を厨芥2に直接接触さ
せないと次のような作用が加わム厨芥2が収納室lに収
納された直後は厨芥2の回りはまだ空気雰囲気であり、
酸素が存在すム 厨芥2が加熱され乾燥が進むと厨芥2
から水蒸気が発生し 厨芥2の回りは水蒸気で満たされ
るようになり、無酸素状態となも したがって、第1図
のようへ 空気口6を収納室1の上部でかつ厨芥2の上
方に設けると、搬送用空気を収納室lに供給してk 搬
送用空気は厨芥2に直接接触しないようになり、乾燥過
程において厨芥2の雰囲気は絶えず無酸素状態になa
このた八 厨芥2の加熱時に厨芥2の自然発火を抑制す
るとともGζ 加熱乾燥時に発生する熱分解ガスが酸化
されず悪臭の発生を抑えることができも
また 第8図に示すように収納室l内に別個の厨芥収納
容器11を設6す、その中に厨芥2を収納することによ
り、空気口6を収納室1の上°部でかつ厨芥2の上方に
設けることなしく 搬送用空気が直接厨芥2に接触しな
くなム したがって、乾燥過程において厨芥2の雰囲気
は絶えず無酸素状態にすることができも
次に加熱手段にマイクロ波を用いた場合の実施例につい
て、第9図に基づいて説明すも第9図において、収納室
lの内部に厨芥2が収納されム マグネトロン12は導
波管13を介して収納室1に接続されていも 2450
MHzのマイクロ波がマグネトロン12より発信され
導波管13を通り、収納室1に照射されム 導波管13
と収納室1の接続部にはマイクロ波透過体14を設(す
、マグネトロン12の発信部を保護してあム 送風機4
はマグネトロン12の冷却用空気を供給するとともへ
分岐管15で一部の空気を分岐し 空気室5を通って、
空気口6から搬送用空気を収納室1に供給すム厨芥2の
温度を検出するために温度検出部7が設けられていも
収納室1の下流に設けられた触媒9はその周囲を触媒加
熱用ヒータ(図示せず)で覆われ 触媒がたえず活性温
度を維持するように保温されている。Here, the storage room is provided with a temperature detection means for detecting the temperature of the kitchen waste, and the collected kitchen waste is dried without monitoring the temperature of the kitchen waste during drying. The temperature of kitchen waste can be set within the range of 100°C to 250°C based on the signal from the temperature detection means. Moisture has the ability to evaporate (plastics for food packaging mixed in kitchen waste will not thermally decompose (°C). For this reason, the process of drying kitchen waste will not generate harmful gases or emit bad odors (if kitchen waste is stored in the storage room) Immediately after being washed, there is oxygen around the kitchen waste. As the food is heated and dried, steam is generated from the food waste. The area around the food waste becomes filled with water vapor, creating an oxygen-free condition. Therefore, transport in the storage room The air supply route is set in the space above the kitchen waste so that the transport air does not come into direct contact with the kitchen waste.If the transport air is supplied to the kitchen waste storage room, the atmosphere of the kitchen waste will constantly be in an oxygen-free state during the drying process. Atsushi Although it is said that it suppresses the spontaneous combustion of kitchen waste when heating kitchen waste, the pyrolysis gas is not oxidized and the generation of bad odors can be suppressed, but when a magnetron is used as a heating means, the following effects occur when heating kitchen waste. If you use microwaves to dry kitchen waste with metal objects such as forks and spoons mixed in, the metal objects will receive the microwaves and generate sparks. If oxygen is present, this spark will cause the kitchen waste to ignite.The temperature of the kitchen waste will rise rapidly, producing harmful gases and bad odors.Therefore, while monitoring the temperature of the kitchen waste, 6N food is irradiated with microwaves to dry it. At the same time, the conveying air is supplied to the kitchen waste storage chamber so that the conveying air does not come into direct contact with the kitchen waste.For this reason, the temperature of the kitchen waste is maintained within the range of 100°C or more and 250°C or less, even if metal objects mixed in the kitchen waste are Embodiment Hereinafter, an embodiment of the present invention will be explained based on the accompanying drawings. Even if the kitchen waste 2 is stored, a heater 3 is installed on the outer wall of the storage room 1, and by energizing the heater 3, the kitchen waste 2 can be heated and dried.
The blower 4 may be provided with a temperature detection section 7 to detect the temperature of the kitchen waste 2 which supplies transport air to the storage chamber 1 from the air port 6 via the air chamber 5. It may be installed in direct contact with the kitchen waste 2 as shown in L. It may also be installed close to the kitchen waste 2.
Thermo cup/14 A device that can detect the temperature of kitchen waste 2 by detecting warm light using a light sensor or the like.
Although a thermocouple is used in this embodiment, the signal from the temperature detection section 7 is sent to the temperature controller 8, which controls the amount of electricity supplied to the heater 3 so that the temperature of the kitchen waste 2 reaches the set value. The exposed catalyst 9 is surrounded by a catalyst heater (not shown), and even though the catalyst is constantly kept warm to maintain its activation temperature, the catalyst heater is energized at startup to bring the catalyst 9 up to its activation temperature in advance. When the catalyst 9 reaches the activation temperature, the heater 3 starts to be energized and conveying air is supplied to the storage chamber 1.
The temperature of the kitchen waste 2 rises LA.The water in the kitchen waste 2 evaporates and the kitchen waste 2 begins to dry.The evaporated water is exhausted to the exhaust 1410
During drying, the temperature of the kitchen waste 2 is detected by the temperature detection unit 7.
The drying of the collected kitchen waste 2 is carried out while being monitored by the signal from. The temperature of the kitchen waste 2 can be set within the range of 100°C to 250°C.The temperature controller 8 controls the temperature of the heater 3.
Polyethylene, polypropylene, polystyrene, vinyl chloride/14 vinylidene chloride, etc. are often used for food packaging plastics.Figure 2 shows the weight loss rate of these food packaging plastics during the heating process. ~ Shown in Figure 7 (Nobuyuki Kita, Flammability of Plastics Industrial Research Group). Figure 2 is polyethylene, Figure 3 is polypropylene, Figure 4 is polystyrene,
Figure 5 shows polyvinylidene/k, Figure 6 shows polyvinylidene chloride, and Figure 7 shows polyethylene terephthalate.From these figures, various plastics rapidly thermally decompose in the temperature range of 250℃ to 400℃. At this time, various plastics generate toxic gases such as chlorine gas, hydrogen chloride gas, carbon oxide, and aldehyde.
Chlorine gas and hydrogen chloride gas are particularly difficult to remove with purification catalysts, and the generation of these gases must be suppressed as much as possible (l-X The boiling point of water is 100℃, temperature to 10
If the temperature is above 0°C, the moisture in the kitchen waste will evaporate rapidly, so even if plastic for food packaging gets mixed into the kitchen waste 2, the heating amount of the heater 3 can be controlled.
If you set the temperature to 100℃ or more and 250t: or less,
The kitchen waste 2 can be heated and dried while minimizing the thermal decomposition of the plastic, and the process of drying the kitchen waste does not generate any harmful gas or odor. If the supply route is set to the space above the kitchen waste 2 and the conveyance air is not brought into direct contact with the kitchen waste 2, the following effects will be added. Immediately after the kitchen waste 2 is stored in the storage chamber 1, there will still be an air atmosphere around the kitchen waste 2. and
When the kitchen waste 2 is heated and dried, the kitchen waste 2
Steam is generated, and the area around the kitchen waste 2 becomes filled with water vapor, creating an anoxic state. Therefore, as shown in Figure 1, if the air vent 6 is provided in the upper part of the storage chamber 1 and above the kitchen waste 2. , the conveying air is supplied to the storage chamber l, so that the conveying air does not come into direct contact with the kitchen waste 2, and the atmosphere of the kitchen waste 2 is constantly kept in an oxygen-free state during the drying process.
In addition to suppressing the spontaneous combustion of the kitchen waste 2 when it is heated, the thermal decomposition gas generated during heating and drying is not oxidized and the generation of bad odors can be suppressed. A separate kitchen waste storage container 11 is provided in the interior of the storage chamber 1, and by storing the kitchen waste 2 therein, the air for conveyance can be removed without having to provide the air vent 6 at the top of the storage chamber 1 and above the kitchen waste 2. Therefore, the atmosphere of the kitchen waste 2 can be constantly kept in an oxygen-free state during the drying process. To explain, in FIG. 9, the kitchen waste 2 is stored inside the storage chamber l, and the magnetron 12 is connected to the storage chamber 1 via the waveguide 13.
MHz microwaves are transmitted from magnetron 12.
It passes through the waveguide 13 and is irradiated into the storage chamber 1. Waveguide 13
A microwave transmitting member 14 is installed at the connection between the storage chamber 1 and the magnetron 12 to protect the transmitting part of the magnetron 12.
supplies cooling air for the magnetron 12 and
Part of the air is branched off by the branch pipe 15 and passes through the air chamber 5.
Even though a temperature detection unit 7 is provided to detect the temperature of the kitchen waste 2 that supplies transport air to the storage chamber 1 from the air port 6, the catalyst 9 provided downstream of the storage chamber 1 catalytically heats the surrounding area. The catalyst is covered with a heater (not shown) to keep the catalyst constantly at its active temperature.
始動時に触媒加熱用ヒータに通電し あらかじめ触媒9
を活性温度まで昇温させム 触媒9が活性温度に到達す
ると、マグネトロン12の通電と搬送用空気の供給を開
始すム マイクロ波は厨芥2に含まれる水分により吸収
され 厨芥2は乾燥し始めも 蒸発した水分はマグネト
ロン12の冷却用空気で希釈されて、排気筒10から排
出されも 乾燥時は厨芥2の温度を温度検出部7からの
信号によりモニターしながi−N芥2の乾燥を行う。厨
芥2の温度は100℃以上250℃以下の範囲で設定で
きるように マグネトロン12によりマイクロ波の照射
量をコントロールするために プラスチックを熱分解す
ることなく、厨芥2を加熱乾燥でき、厨芥の乾燥過程で
有害ガスを発生したり、悪臭を出さずに厨芥を乾燥処理
できる。At startup, the heater for heating the catalyst is energized and the catalyst 9 is heated in advance.
When the catalyst 9 reaches the activation temperature, the magnetron 12 is energized and the supply of conveying air is started.The microwave is absorbed by the moisture contained in the kitchen waste 2, and the kitchen waste 2 begins to dry. The evaporated water is diluted with the cooling air of the magnetron 12 and exhausted from the exhaust stack 10.During drying, the temperature of the kitchen waste 2 is monitored by the signal from the temperature detection section 7, and the i-N waste 2 is dried. conduct. The temperature of the kitchen waste 2 can be set in the range of 100°C to 250°C. The amount of microwave irradiation is controlled by the magnetron 12. The kitchen waste 2 can be heated and dried without thermally decomposing the plastic, and the drying process of the kitchen waste can be Kitchen waste can be dried without producing harmful gases or bad odors.
ま2Q R芥2の中にフォークやスプーンなどのよう
な金属物が混入した状態で、マイクロ波を用いて厨芥2
の乾燥処理を行った場合、金属物はマイクロ波を受信し
てスパークを発生しやす(なムしかし 空気口6は収納
室1の上部でかつ厨芥2の上方に設けであるためへ 搬
送用空気を収納室1に供給してL 搬送用空気は厨芥2
に直接接触しないことになム このため乾燥過程におい
て厨芥2の雰囲気は絶えず無酸素状態になも したがっ
て、たとえマイクロ波により発生する金属物表面でのス
パークが乾燥時に発生してLi芥2の自然発火を抑制す
ることができも 加えて、厨芥2の雰囲気は無酸素状態
のために熱分解ガスが酸化され哄 悪臭の発生を抑える
ことができも発明の効・果
以上のように本発明の厨芥処理装置において(表厨芥乾
燥時の有害ガスの発生や悪臭の発生を防止することがで
きもWhen metal objects such as forks and spoons are mixed in the kitchen waste 2 using microwaves,
However, since the air vent 6 is located at the top of the storage chamber 1 and above the kitchen waste 2, the metal objects are likely to receive microwaves and generate sparks. L is supplied to the storage room 1. Conveying air is supplied to the kitchen waste 2.
Therefore, during the drying process, the atmosphere of the kitchen waste 2 is constantly in an oxygen-free state. Therefore, even if sparks generated by microwaves on the surface of the metal object are generated during drying, the Li waste 2 will naturally In addition, since the atmosphere in the kitchen waste 2 is oxygen-free, the thermal decomposition gas is oxidized and the generation of foul odors can be suppressed. In kitchen waste processing equipment (it is possible to prevent the generation of harmful gases and bad odors when drying kitchen waste)
第1図は本発明の一実施例の厨芥処理装置の断面図 第
2図はポリエチレンの昇温過程における重量減量率を示
す特性@ 第3図はポリプロピレンの昇温過程における
重量減量率を示す特性医第4図はポリスチレンの昇温過
程における重量減量率を示す特性医 第5図はポリ塩化
ビニルの昇温過程における重量減量率を示す特性皿 第
6図はポリ塩化ビニリデンの昇温過程における重量減量
率を示す特性皿 第7図はポリエチレンテレフタレート
の昇温過程における重量減量率を示す特性@ 第8図お
よび第9図は本発明の他実施例の厨芥処理装置の断面図
てあム
ト・・収納室 2・・・厨芥 3・・・ヒー久 4・・
・送風風 7・・・温度検出@ 9・・・触i 12
・・・マグネトロン、13・・・導波管。
代理人の氏名 弁理士 粟野重孝 ほか1名/−一収州
i
2−・−厨芥
3− ヒータ
4−′th凰機
7−温贋検出瞥)
9− 触媒
6−隻気口
11・−厨芥収束内容器
第
図
らJ
図
第
図
第
図
1θ
第
図
第
図
第
図
12 マゲ不トロン
1341シ1it
tS j57 山JLfFig. 1 is a cross-sectional view of a kitchen waste processing apparatus according to an embodiment of the present invention. Fig. 2 is a characteristic showing the weight loss rate of polyethylene during the temperature rising process. Figure 3 is a characteristic showing the weight loss rate of polypropylene during the temperature rising process. Figure 4 shows the weight loss rate of polystyrene during the heating process. Figure 5 shows the weight loss rate of polyvinyl chloride during the heating process. Figure 6 shows the weight of polyvinylidene chloride during the heating process. Characteristic plate showing the weight loss rate Figure 7 shows the characteristics showing the weight loss rate during the temperature rising process of polyethylene terephthalate. Storage room 2...Kitchen waste 3...Hyaku 4...
・Blow air 7... Temperature detection @ 9... Touch i 12
...Magnetron, 13...Waveguide. Name of agent: Patent attorney Shigetaka Awano and 1 other person/-Ichigoshui 2-・-Kitchen waste 3-Heater 4-'th oven 7-Hot counterfeit detection) 9-Catalyst 6-Air port 11・-Kitchen waste Convergence inner container Fig. et al. J Fig. Fig. Fig. 1θ Fig. Fig. Fig. 12
Claims (3)
生したガス体の搬送用空気を前記収納室に供給する送風
手段と、前記収納室の下流に設けた排気口とを有し、厨
芥の温度が100℃以上250℃以下になるように、前
記加熱手段の加熱量を設定したことを特徴とする厨芥処
理装置。(1) It has a storage chamber for kitchen waste, a means for heating the kitchen waste, a blowing means for supplying air for transporting gas generated from the kitchen waste to the storage chamber, and an exhaust port provided downstream of the storage chamber. A kitchen waste processing apparatus, characterized in that the heating amount of the heating means is set so that the temperature of the kitchen waste is 100° C. or higher and 250° C. or lower.
の上方空間としたことを特徴とする請求項1記載の厨芥
処理装置。(2) The kitchen waste processing apparatus according to claim 1, wherein the supply path of the conveying air in the storage chamber is a space above the kitchen waste.
は2記載の厨芥処理装置。(3) The kitchen waste processing apparatus according to claim 1 or 2, wherein microwaves are used as the heating means.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2159004A JPH0448982A (en) | 1990-06-18 | 1990-06-18 | Garbage treatment apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2159004A JPH0448982A (en) | 1990-06-18 | 1990-06-18 | Garbage treatment apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0448982A true JPH0448982A (en) | 1992-02-18 |
Family
ID=15684137
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2159004A Pending JPH0448982A (en) | 1990-06-18 | 1990-06-18 | Garbage treatment apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0448982A (en) |
-
1990
- 1990-06-18 JP JP2159004A patent/JPH0448982A/en active Pending
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