JPH0788460A - Raw refuse treatment device - Google Patents
Raw refuse treatment deviceInfo
- Publication number
- JPH0788460A JPH0788460A JP5208718A JP20871893A JPH0788460A JP H0788460 A JPH0788460 A JP H0788460A JP 5208718 A JP5208718 A JP 5208718A JP 20871893 A JP20871893 A JP 20871893A JP H0788460 A JPH0788460 A JP H0788460A
- Authority
- JP
- Japan
- Prior art keywords
- fermentation tank
- air
- furnace
- fermentation
- fermenter
- 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
- Treating Waste Gases (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、主としてレストランな
どから排出される業務用生ゴミを、70〜80度という
比較的に高い温度で、高温発酵菌を使つて発酵・分解・
乾燥を行つて、肥料や飼料として有効に利用することが
できるように処理するための生ゴミ処理装置に関するも
のである。BACKGROUND OF THE INVENTION The present invention is for the purpose of fermenting, decomposing, and decomposing industrial garbage, which is mainly discharged from restaurants and the like, at a relatively high temperature of 70 to 80 degrees Celsius by using high temperature fermenting bacteria.
The present invention relates to an apparatus for treating food waste which is dried and treated so that it can be effectively used as fertilizer or feed.
【0002】[0002]
【従来の技術】一般に、レストランなどから排出される
業務用生ゴミは、そのほとんどが、焼却または埋め立て
のかたちで処分されているが、生ゴミには蛋白質などの
有機質物が含まれていて、その有効利用を図ることが可
能である。2. Description of the Related Art Generally, most of industrial garbage discharged from restaurants and the like is disposed of by incineration or landfill, but the organic garbage such as protein is contained in the garbage, It is possible to make effective use of it.
【0003】このため、生ゴミを発酵槽の中に入れ、常
温、中温(40〜60度)あるいは高温(70〜90
度)に加熱し、夫々の温度に適した発酵菌を投入して、
生ゴミを発酵・分解・乾燥させることにより、生ゴミを
取り扱いが容易な粉末顆粒状にして回収するようにした
生ゴミ処理装置が創案された。For this reason, raw garbage is put in a fermenter and kept at room temperature, medium temperature (40-60 degrees) or high temperature (70-90).
Temperature) and put fermenting bacteria suitable for each temperature,
A raw garbage processing device was devised, in which the raw garbage was collected in the form of powder granules that were easy to handle by fermenting, decomposing, and drying the raw garbage.
【0004】このような生ゴミ処理装置においては、生
ゴミの乾燥にともなつて発生浮遊する水蒸気、粉塵、悪
臭成分が発酵槽から排出される空気の中に含まれるが、
その排出される空気をそのまま大気中に放出してしまう
と、不快感を与える水蒸気の白煙が立ち昇つたり粉塵や
悪臭が漂つたりするという二次公害が発生することとな
るため、排出される空気に加熱処理を施して無公害状態
にするための脱臭炉を設ける必要がある。In such an apparatus for treating food waste, water vapor, dust, and malodorous components that are generated and suspended as the food waste is dried are contained in the air discharged from the fermentation tank.
If the discharged air is released into the atmosphere as it is, secondary pollution such as white smoke of water vapor, which causes discomfort, rises, and dust and foul odors are generated. It is necessary to provide a deodorizing furnace to heat the generated air to a pollution-free state.
【0005】[0005]
【発明が解決しようとする課題】脱臭炉を設けた生ゴミ
処理装置として、従来は、発酵槽、発酵槽加熱用バーナ
ー、発酵槽内の空気の排出経路に設けた脱臭炉、及び、
脱臭炉加熱用バーナーから構成したものが公知である。
かかる装置は、発酵槽内の生ゴミを発酵槽加熱用バーナ
ーによつて昇温させることにより発酵・分解・乾燥処理
し、この発酵槽から排出される空気中の水蒸気、粉塵、
悪臭成分を脱臭炉内において脱臭炉加熱用バーナーで7
00〜900度に加熱し、水蒸気を視認できないほどの
微粒状にするとともに粉塵と悪臭成分を焼き切り、これ
によつて、不快感を与える水蒸気の白煙が立ち昇つたり
粉塵や悪臭が漂つたりするという生ゴミ処理にともなう
二次公害の発生を防止するようになつている。As a raw garbage processing apparatus provided with a deodorizing furnace, conventionally, a fermenter, a burner for heating the fermenting tank, a deodorizing furnace provided in an air discharge path in the fermenting tank, and
A burner for heating a deodorizing furnace is known.
Such an apparatus performs fermentation / decomposition / drying treatment by raising the temperature of raw garbage in the fermenter with a burner for heating the fermenter, steam in the air discharged from the fermenter, dust,
Remove the malodorous components in the deodorizing furnace with a burner for heating the deodorizing furnace.
It is heated to 0 to 900 degrees Celsius to make water vapor into fine particles that are invisible and burn out dust and malodorous components, which causes offensive white smoke of water vapor and dust and malodorous drift. It is designed to prevent the occurrence of secondary pollution associated with the processing of garbage.
【0006】しかしながら、上記の生ゴミ処理装置は、
生ゴミの分解・発酵・乾燥処理を行うためのバーナー及
び二次公害を防止するためのバーナーとして夫々専用の
ものを用いており、このために、バーナーの燃料費が高
くつくという欠点があつた。しかも、発酵槽加熱用のバ
ーナーは発酵槽を上側から加熱するようになつていたた
め、加熱効率が悪く、この点もバーナーの燃料費が高く
つく原因となつていた。 本発明は、このような事情に
鑑みて創案されたものであり、燃料費の節減を図りつつ
二次公害の防止を行うことができるようにした生ゴミ処
理装置を提供することを目的とするものである。However, the above-mentioned garbage processing device is
The burner for decomposing / fermenting / drying the garbage and the burner for preventing the secondary pollution have their own dedicated burners, which has the disadvantage of high fuel cost. . Moreover, since the burner for heating the fermenter was designed to heat the fermenter from the upper side, the heating efficiency was poor, and this also contributed to the high fuel cost of the burner. The present invention was devised in view of such circumstances, and an object of the present invention is to provide a garbage disposal device capable of preventing secondary pollution while reducing fuel costs. It is a thing.
【0007】[0007]
【課題を解決するための手段】上記の課題を解決するた
めの手段として、本発明は、処理炉本体内に両側部と底
部に空間を空けて設けられて内部に駆動機構により回転
する攪拌翼を備えた発酵槽と、その発酵槽内の空気を熱
交換により与熱して加熱する脱臭炉と、その脱臭炉内の
空気を処理炉本体内の発酵槽の一側の空間に導入する導
入管と、処理炉本体内の空気を発酵槽の他側の空間から
外部に排出させる排気管とから構成した。Means for Solving the Problems As a means for solving the above problems, the present invention provides a stirring blade which is provided in a main body of a processing furnace with spaces on both sides and a bottom and which is rotated by a drive mechanism inside. And a deodorizing furnace that heats and heats the air in the fermenting tank by heat exchange, and an introducing pipe that introduces the air in the deodorizing furnace into the space on one side of the fermenting tank in the processing furnace body. And an exhaust pipe for discharging the air in the main body of the processing furnace from the space on the other side of the fermentation tank to the outside.
【0008】[0008]
【発明の作用及び効果】本発明において、生ゴミの処理
を行う際には、まず、発酵槽内に生ゴミ、適量の発酵
菌、及び、必要に応じて乾燥おから等の水分調整剤を投
入して、これらを攪拌翼によつて攪拌し、脱臭炉のバー
ナーを点火する。このバーナーの点火により脱臭炉内の
空気が700〜900度の高温に加熱され、加熱された
空気は熱風となつて導入管を通ることにより処理炉本体
内の発酵槽一側の空間に流入し、他側の空間から排気管
を通って排出される。In the present invention, when treating raw garbage, first, raw garbage, an appropriate amount of fermenting bacteria, and, if necessary, a water conditioner such as dried okara are added to the fermenter. After charging, these are stirred by a stirring blade and the burner of the deodorizing furnace is ignited. By the ignition of this burner, the air in the deodorizing furnace is heated to a high temperature of 700 to 900 degrees Celsius, and the heated air flows into the space on the one side of the fermentation tank in the main body of the processing furnace by passing through the introduction pipe as hot air. , Is discharged from the space on the other side through the exhaust pipe.
【0009】この流入した熱風により発酵槽が両側面及
び下面から加熱される。このとき、熱風は上記のように
700〜900度の高温に熱せられていたものであつて
十分な熱量を有していることから、発酵槽及び発酵槽内
の生ゴミは70〜90度の高温に昇温され、発酵菌の増
殖によつて生ゴミの発酵・分解・乾燥が進む。この間生
ゴミ中の水分が気化して生じる水蒸気及び生ゴミの乾燥
にともなつて浮遊する粉塵や悪臭成分は発酵槽内の空気
とともに高温度の脱臭炉における熱交換により与熱され
たのち脱臭炉内において火炎により燃焼される。このた
め、空気中の水蒸気は視認できないほどの微粒状になる
とともに粉塵と悪臭成分は焼き切られる。このようにし
て脱臭炉内で無公害化された空気は上記のように導入管
を通つて処理炉本体内の発酵槽の一側の空間に流入し、
発酵槽を加熱したのち他側の排気管を通して大気中に放
出されるが、このときに、不快感を与える水蒸気の白煙
が立ち昇つたり周囲に粉塵や悪臭が漂うことがない。発
酵槽内における生ゴミの処理は、70〜90度の高温で
行われるため、加熱を開始してから短時間で終了する。
処理が完了したら、発酵槽内の粉末顆粒状の処理済み物
を冷却した後に回収する。 上述のように、本発明にお
いては、排気に際して不快感を与える水蒸気の白煙が立
ち昇つたり周囲に粉塵や悪臭が漂うことがなく、生ゴミ
処理にともなう二次公害の発生が防止される。The inflowing hot air heats the fermenter from both sides and bottom. At this time, since the hot air was heated to a high temperature of 700 to 900 degrees as described above and has a sufficient amount of heat, the fermenter and the raw garbage in the fermenter have a temperature of 70 to 90 degrees. The temperature is raised to a high temperature, and the fermentation / decomposition / drying of raw garbage proceeds due to the growth of fermenting bacteria. During this period, water vapor in the garbage is vaporized, and dust and malodorous components floating with the drying of the garbage are heated by the heat exchange in the high-temperature deodorizing furnace together with the air in the fermentation tank, and then the deodorizing furnace. It is burned by a flame inside. For this reason, the water vapor in the air becomes fine particles that cannot be visually recognized, and the dust and malodorous components are burned out. The air thus detoxified in the deodorizing furnace flows into the space on one side of the fermentation tank in the main body of the processing furnace through the introduction pipe as described above,
After heating the fermenter, it is released into the atmosphere through the exhaust pipe on the other side, but at this time, white smoke of water vapor, which gives an unpleasant feeling, does not rise and dust and a bad odor do not drift around. Since the processing of raw garbage in the fermenter is performed at a high temperature of 70 to 90 degrees, it ends in a short time after starting heating.
When the treatment is completed, the treated powdery granular material in the fermenter is cooled and then collected. As described above, in the present invention, white smoke of water vapor, which gives an unpleasant feeling when exhausting, does not rise or dust or a bad odor is present in the surroundings, and the occurrence of secondary pollution associated with garbage processing is prevented. .
【0010】しかも、発酵槽内の生ゴミを昇温させるた
めの加熱源として、生ゴミ昇温専用の加熱源を設けるの
ではなく、二次公害防止用の加熱源である脱臭炉の排熱
を流用し、かつ、発酵槽への加熱を発酵槽の上側からで
はなく発酵槽の両側面と下面から行うことによつて加熱
効率の向上を図るようになつているほか、発酵槽から吸
い出された脱臭処理の必要な空気は脱臭炉における熱交
換により与熱されてから脱臭炉内に吹き込まれるように
なつているので、脱臭炉の温度を下げる要因となること
が少なく、これらの相乗効果で熱効率が著しく向上する
ようになつているのであつて、これにより、バーナーの
燃料消費量が比較的少なく済む。Moreover, as a heating source for raising the temperature of the raw garbage in the fermenter, a heat source dedicated to raising the temperature of the raw garbage is not provided, but exhaust heat of a deodorizing furnace which is a heating source for preventing secondary pollution. The heating efficiency is improved by diverting the heat from the fermentation tank from the both sides and the bottom surface of the fermentation tank instead of from the upper side of the fermentation tank. The deodorized air that needs to be deodorized is heated by heat exchange in the deodorizing furnace and then blown into the deodorizing furnace. The heat efficiency of the burner is significantly improved, which results in a relatively low fuel consumption of the burner.
【0011】すなわち、本発明によれば、燃料費の節減
を図りつつ二次公害の発生を防止することができるとい
う効果がある。That is, according to the present invention, it is possible to reduce the fuel cost and prevent the occurrence of secondary pollution.
【0012】[0012]
【実施例】以下、本発明の一実施例を添付図面に基づい
て説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the accompanying drawings.
【0013】処理炉本体1は断熱性を有する板材によつ
て構成されており、その内部には、処理炉本体1外へ開
口する図示しない蓋付きの投入口及び回収口を備えた発
酵槽3が、その両側面及び下面と処理炉本体1との間に
流通空間を空けた状態で固設されている。The processing furnace main body 1 is composed of a plate material having a heat insulating property, and inside the fermentation furnace 3, a fermenting tank 3 having an input port with a lid (not shown) opened to the outside of the processing furnace main body 1 and a recovery port is provided. However, it is fixed in a state where a circulation space is formed between the both side surfaces and the lower surface and the processing furnace main body 1.
【0014】発酵槽3の内部には駆動軸4に連結された
攪拌翼5が収容されており、この攪拌翼5は、処理炉本
体1の外部に設けたモーター(本発明の構成要素である
駆動機構に相当する)6の駆動によりスプロケツト7、
8及びチエーン9を介して連動する駆動軸4と一体に回
転するようになつている。Inside the fermenter 3, a stirring blade 5 connected to a drive shaft 4 is housed, and the stirring blade 5 is a motor provided outside the processing furnace main body 1 (which is a component of the present invention). (Corresponding to a drive mechanism) 6 drives the sprocket 7,
8 and a drive shaft 4 which is interlocked via a chain 9.
【0015】処理炉本体1の上方には、断熱性材によつ
て筒形に成形された外筒12の中に熱伝導率の高い材料
からなる燃焼筒11を間隙を空けて挿入した二次公害防
止用の脱臭炉10が設けられており、この脱臭炉10に
は、燃焼筒11内に向けて火炎を噴出するバーナー15
が設けられているとともに、燃焼筒11のバーナー15
の近くには流入口13が形成され、また、外筒12のバ
ーナー15から離れた位置には、発酵槽3から吸い込ん
だ空気を送り込む送風機17の吹込口16が形成されて
いる。なお、燃焼筒11の吸込口13の付近にはパンチ
ングメタル14が張設されている。Above the main body 1 of the processing furnace, a combustion cylinder 11 made of a material having a high thermal conductivity is inserted into a cylindrical outer cylinder 12 made of a heat insulating material with a gap between them. A deodorizing furnace 10 for pollution prevention is provided. The deodorizing furnace 10 has a burner 15 for ejecting a flame toward a combustion cylinder 11.
Is provided, and the burner 15 of the combustion cylinder 11 is provided.
An inlet 13 is formed in the vicinity of, and a blower 16 of a blower 17 for feeding the air sucked from the fermentation tank 3 is formed at a position apart from the burner 15 of the outer cylinder 12. A punching metal 14 is stretched around the suction port 13 of the combustion cylinder 11.
【0016】燃焼筒11の先端には切換弁18が図に実
線で示す位置にあるとき高温度の空気を処理炉本体1と
発酵槽3の一側の側面との間に導入する導入管19が接
続されており、処理炉本体1の他側の面には放出管24
に連通する排気管20が接続されている。An introduction pipe 19 for introducing high temperature air between the main body 1 of the processing furnace and one side surface of the fermentation tank 3 when the switching valve 18 is at the position shown by the solid line in the drawing at the tip of the combustion cylinder 11. Is connected to the surface of the processing furnace main body 1 on the other side.
Is connected to an exhaust pipe 20.
【0017】また、処理炉本体1の前記一側には、外気
を吹き込む冷却用の送風機21が備えられ、発酵槽3の
前記他側には高温度の空気の一部を取り入れる取入口2
3が形成されている。Further, a cooling blower 21 for blowing outside air is provided on the one side of the processing furnace body 1, and an inlet 2 for taking in a part of high temperature air is provided on the other side of the fermentation tank 3.
3 is formed.
【0018】次に、本実施例の作用を説明する。Next, the operation of this embodiment will be described.
【0019】まず、図示しない投入口を開けて発酵槽3
内に生ゴミと適量の発酵菌を投入する。使用する発酵菌
としては、島本微生物工業株式会社製の「バイムフー
ド」等が好適であるが、その外に、好気性の高温発酵菌
を主体にした多種類の微生物の混合体を使用することも
できる。さらに、生ゴミの水分が多い場合には、乾燥お
からや米糠等を水分調整剤として投入する。First, the fermenter 3 is opened by opening a charging port (not shown).
Put raw garbage and an appropriate amount of fermenting bacteria inside. As the fermenting bacterium to be used, "Bime Food" manufactured by Shimamoto Microorganism Industry Co., Ltd. and the like are preferable, but in addition to that, it is also possible to use a mixture of various types of microorganisms mainly composed of aerobic high temperature fermenting bacterium. it can. Furthermore, when the water content of raw garbage is high, dried okara, rice bran, etc. are added as a water content adjusting agent.
【0020】次に、切換弁18を、図1に実線で示すよ
うに、燃焼筒11が導入管19に連通する状態とし、モ
ーター6を駆動することにより発酵槽3内の攪拌翼5を
正逆回転させ、脱臭炉10のバーナー15に点火する。Next, as shown by the solid line in FIG. 1, the switching valve 18 is brought into a state in which the combustion cylinder 11 communicates with the introduction pipe 19, and the motor 6 is driven so that the stirring blades 5 in the fermentation tank 3 are straightened. The burner 15 of the deodorization furnace 10 is ignited by rotating in the reverse direction.
【0021】脱臭炉10内の空気は、バーナー15によ
つて700〜900度の高温に加熱される。この加熱さ
れた空気は、熱風となり、導入管19を通つて処理炉本
体1内に流入し、発酵槽3の周りを約半周して排気管2
0を通り、放出管24から大気中に放出される。The air in the deodorizing furnace 10 is heated by the burner 15 to a high temperature of 700 to 900 degrees. The heated air becomes hot air, flows into the processing furnace main body 1 through the introduction pipe 19, and makes a half turn around the fermentation tank 3, and the exhaust pipe 2
It passes through 0 and is discharged into the atmosphere from the discharge pipe 24.
【0022】発酵槽3内の生ゴミは、攪拌翼5で攪拌さ
れることによつて粉砕されつつ、処理炉本体1内におい
て発酵槽3の外底面と外側面を外部から包み込む熱風に
よつて70〜90度の温度に昇温され、発酵菌の増殖に
よつて発酵、分解及び乾燥が始まる。The raw garbage in the fermenter 3 is crushed by being stirred by the agitating blades 5 and is crushed by the hot air that wraps the outer bottom surface and the outer surface of the fermenter 3 inside the processing furnace main body 1 from the outside. The temperature is raised to 70 to 90 ° C., and fermentation, decomposition and drying start due to the growth of fermenting bacteria.
【0023】かくして、生ごみは約2時間後に顆粒粉末
状となる。Thus, the raw garbage becomes a granular powder after about 2 hours.
【0024】処理完了後は、バーナー15の点火と攪拌
翼5による攪拌を続けたままで切換弁18で、図1に鎖
線で示すように、導入管19を閉じて脱臭炉10から処
理炉本体1への熱風の流入を阻止するようにするととも
に送風機21を起動して外気を処理炉本体1に導入させ
る状態とする。これにより、脱臭炉10からの排熱によ
る発酵槽3への加熱が停止するとともに、処理炉本体1
内に流入する低温の外気により発酵槽3及びその発酵槽
3内に残つた粉末顆粒状の処理済み物が冷却される。そ
して、この冷却を約30分間行つた後に、処理済み物を
図示しない回収口を開いて回収する。After the completion of the treatment, the switching valve 18 keeps igniting the burner 15 and stirring by the stirring blade 5 and the introduction pipe 19 is closed as shown by the chain line in FIG. The inflow of hot air into the processing furnace main body 1 is prevented and the blower 21 is activated to introduce the outside air into the processing furnace main body 1. As a result, the heating of the fermenter 3 by the exhaust heat from the deodorizing furnace 10 is stopped, and the processing furnace main body 1
The fermenter 3 and the powdery granular processed material left in the fermenter 3 are cooled by the low-temperature outside air flowing therein. Then, after this cooling is performed for about 30 minutes, the processed product is recovered by opening a recovery port (not shown).
【0025】また、発酵槽3内で発酵・分解・乾燥の処
理が進行している間、及び、これらの処理が完了してか
ら処理済み物を回収するまでの冷却が行われている間、
生ゴミ中の水分が気化して生じる水蒸気及び生ゴミの乾
燥にともなつて浮遊する粉塵と悪臭成分は、発酵槽3に
形成された取入口23から流入する処理炉本体1内の空
気とともに送風機17により吹込口16を通つて圧送さ
れて流入口13から燃焼筒11内に吹き込まれるのであ
つて、その間に燃焼筒11との熱交換により十分に加熱
される。燃焼筒11内に吹き込まれたガスはパンチング
メタル14との衝突により渦を巻いているバーナー15
の炎と混合することにより燃焼して水蒸気が700〜9
00度の高温となつて視認できないほどの微粒状になる
とともに、流入する空気中の粉塵と悪臭成分が焼き切ら
れる。While the fermentation, decomposition, and drying processes are in progress in the fermenter 3, and during the cooling from the completion of these processes to the collection of the processed products,
Water vapor generated by vaporization of water in the garbage and dust and malodorous components floating with the drying of the garbage, together with the air in the processing furnace body 1 flowing from the intake port 23 formed in the fermentation tank 3, are blowers. It is pressure-fed by 17 through the blow-in port 16 and blown into the combustion cylinder 11 from the inflow port 13, while it is sufficiently heated by heat exchange with the combustion cylinder 11. The gas blown into the combustion cylinder 11 collides with the punching metal 14 and is swirled by the burner 15
Combustion by mixing with the flame of 700 to steam
At a high temperature of 00 degrees, it becomes invisible fine particles and dust and odorous components in the inflowing air are burned out.
【0026】このように脱臭炉10内で加熱処理された
処理済み空気は、放出管24を通して大気中に放出され
るのであるが、排気に際しては、不快感を与える水蒸気
の白煙が立ち昇つたり周囲に粉塵や悪臭が漂うという二
次公害が発生することはない。 上述のように、発酵槽
3内の生ゴミを昇温させるための加熱源として、生ゴミ
昇温専用のバーナーを設けるのではなく、二次公害防止
用の脱臭炉10のバーナー15の排熱が流用されてお
り、また、脱臭炉10においては焼却される空気が燃焼
筒11との熱交換により与熱されるようになつており、
しかも、発酵槽3の加熱を発酵槽3の上側からではなく
発酵槽3の下側と側方とから行うことによつて加熱効率
の向上が図られている。したがつて、燃料消費量が少な
くて済み、生ゴミの処理に要するコスト、及び、生ゴミ
処理にともなう二次公害発生の防止に要するコストが低
く抑えられる。The treated air thus heat-treated in the deodorizing furnace 10 is discharged into the atmosphere through the discharge pipe 24. At the time of exhaust, white smoke of water vapor, which causes discomfort, rises. There is no secondary pollution such as dust or odors around the area. As described above, as a heat source for raising the temperature of the raw garbage in the fermenter 3, a burner dedicated to raising the temperature of the raw garbage is not provided, but exhaust heat of the burner 15 of the deodorizing furnace 10 for secondary pollution prevention is provided. Is also diverted, and in the deodorizing furnace 10, the air to be incinerated is heated by heat exchange with the combustion tube 11,
Moreover, the heating efficiency is improved by heating the fermenter 3 not from the upper side of the fermenter 3 but from the lower side and the side of the fermenter 3. Therefore, the fuel consumption amount is small, and the cost required for the treatment of raw garbage and the cost required for preventing the occurrence of secondary pollution due to the treatment of raw garbage can be kept low.
【0027】また、発酵槽の内面の一部または全部に遠
赤外線塗料もしくはセラミツクなど遠赤外線を放射しや
すい材料を塗布または装着することによって、その輻射
熱を有効に利用し、発酵分解しつつある生ゴミの水分の
蒸発を助長するようにしてもよい。Further, by applying or mounting a material that easily radiates far infrared rays such as far infrared paint or ceramics on a part or all of the inner surface of the fermenter, the radiant heat is effectively used and fermentation and decomposition are being performed. You may make it accelerate | stimulate evaporation of the water | moisture content of dust.
【図1】本発明の一実施例の断面図である。FIG. 1 is a sectional view of an embodiment of the present invention.
1:処理炉本体 3:発酵槽 5:攪拌翼 6:モータ
(駆動機構) 10:脱臭炉 11:燃焼筒 12:外
筒 13:流入口 15:バーナー 17:送風機 1
9:導入管 20:排気管1: Processing furnace body 3: Fermenter 5: Stirring blade 6: Motor (driving mechanism) 10: Deodorizing furnace 11: Combustion cylinder 12: Outer cylinder 13: Inlet port 15: Burner 17: Blower 1
9: Inlet pipe 20: Exhaust pipe
───────────────────────────────────────────────────── 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 B01D 53/74 B01D 53/34 116 H (72)発明者 伊藤 伸治 神奈川県横浜市磯子区汐見台3−3−33の 5−525 (72)発明者 佐野 充挙 愛知県東海市養父町南掘畑5─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location B01D 53/74 B01D 53/34 116 H (72) Inventor Shinji Ito 3 Shiomidai, Isogo-ku, Yokohama, Kanagawa Prefecture -3-53-5-525 (72) Inventor Mitsuhisa Sano 5 Minamiborihata, Yabu-cho, Tokai City, Aichi Prefecture
Claims (1)
けて設けられて内部に駆動機構により回転する攪拌翼を
備えた発酵槽と、該発酵槽内の空気を熱交換により与熱
して加熱する脱臭炉と、該脱臭炉内の空気を前記処理炉
本体内の前記発酵槽の一側の空間に導入する導入管と、
前記処理炉本体内の空気を前記発酵槽の他側の空間から
外部に排出させる排気管とから構成されていることを特
徴とする生ゴミ処理装置。1. A fermenter, which is provided in the main body of the processing furnace with a space on both sides and a bottom and has stirring blades which are rotated by a drive mechanism, and heats the air in the fermenter by heat exchange. A deodorizing furnace that heats by heating, and an introducing pipe that introduces air in the deodorizing furnace into a space on one side of the fermentation tank in the processing furnace body,
An organic waste treatment device comprising: an exhaust pipe for discharging the air in the treatment furnace main body from the space on the other side of the fermentation tank to the outside.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5208718A JPH0788460A (en) | 1993-07-30 | 1993-07-30 | Raw refuse treatment device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5208718A JPH0788460A (en) | 1993-07-30 | 1993-07-30 | Raw refuse treatment device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0788460A true JPH0788460A (en) | 1995-04-04 |
Family
ID=16560940
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5208718A Pending JPH0788460A (en) | 1993-07-30 | 1993-07-30 | Raw refuse treatment device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0788460A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH10305269A (en) * | 1997-05-01 | 1998-11-17 | Kii & Craft:Kk | Treatment device of waste product or the like |
WO2000037188A1 (en) * | 1998-12-18 | 2000-06-29 | Mihara Co., Ltd. | Food waste treating device |
JP2003024906A (en) * | 2001-07-13 | 2003-01-28 | Canon Electronics Inc | Waste disposal device and method |
JP2007203167A (en) * | 2006-01-31 | 2007-08-16 | Nichirei Foods:Kk | Garbage disposer |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4970560U (en) * | 1972-10-03 | 1974-06-19 | ||
JPS62252815A (en) * | 1986-04-23 | 1987-11-04 | Itoo Yookadou:Kk | Garbage incineration and fermentation device |
JPH01123684A (en) * | 1987-11-06 | 1989-05-16 | Harman Co Ltd | Crude refuse treating device |
-
1993
- 1993-07-30 JP JP5208718A patent/JPH0788460A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4970560U (en) * | 1972-10-03 | 1974-06-19 | ||
JPS62252815A (en) * | 1986-04-23 | 1987-11-04 | Itoo Yookadou:Kk | Garbage incineration and fermentation device |
JPH01123684A (en) * | 1987-11-06 | 1989-05-16 | Harman Co Ltd | Crude refuse treating device |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH10305269A (en) * | 1997-05-01 | 1998-11-17 | Kii & Craft:Kk | Treatment device of waste product or the like |
WO2000037188A1 (en) * | 1998-12-18 | 2000-06-29 | Mihara Co., Ltd. | Food waste treating device |
JP2003024906A (en) * | 2001-07-13 | 2003-01-28 | Canon Electronics Inc | Waste disposal device and method |
JP2007203167A (en) * | 2006-01-31 | 2007-08-16 | Nichirei Foods:Kk | Garbage disposer |
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