JPH0942642A - Disposal equipment and use thereof - Google Patents
Disposal equipment and use thereofInfo
- Publication number
- JPH0942642A JPH0942642A JP18730995A JP18730995A JPH0942642A JP H0942642 A JPH0942642 A JP H0942642A JP 18730995 A JP18730995 A JP 18730995A JP 18730995 A JP18730995 A JP 18730995A JP H0942642 A JPH0942642 A JP H0942642A
- Authority
- JP
- Japan
- Prior art keywords
- fermentation
- incinerator
- treated
- drying tank
- tank
- 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
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/20—Waste processing or separation
Landscapes
- Incineration Of Waste (AREA)
- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、生ゴミがその代表
である水分を含有する醗酵処理可能な被処理物の処理設
備に関するとともに、このような処理設備の使用方法に
関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a facility for treating an object to be fermented which contains water, which is representative of garbage, and a method of using such a facility.
【0002】[0002]
【従来の技術】この種の生ゴミは、魚市場、野菜市場、
青果市場、農協、養鶏場、養豚場、ハム工場、缶詰工
場、スーパー等から発生する。従来、このような醗酵が
進んで分解処理できる被処理物は、その発生場所で集積
されて、例えば、農場等に搬送されて、堆肥として利用
されていた。2. Description of the Related Art This kind of garbage is used in fish markets, vegetable markets,
It is generated from fruit and vegetable markets, agricultural cooperatives, poultry farms, pig farms, ham factories, canning factories, supermarkets, etc. Heretofore, such substances to be treated that can be decomposed by the progress of fermentation have been accumulated at the place where they are generated, transported to, for example, a farm and used as compost.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、比較的
大量に生ゴミ等、醗酵を起こす被処理物が発生する事業
所にあっては、その定常的な処理場所(例えば農場等)
の確保が比較的困難であるとともに、発生物を事業所内
に一時的に集積しておく場合にあっても、その集積場所
の確保が難しく、集積に伴って発生する臭気の問題が大
きく、例えば、養鶏場、養豚場自体を、人口の少ない山
間にしか開設できない等の問題がある。従って、本発明
の目的は、臭気を伴うこととなりやすい生ゴミ等の減
量、無臭化処理を、環境に問題を発生しない状態で、比
較的簡便な設備で行える処理設備を得ることにある。However, in a business establishment where a relatively large amount of raw materials such as food wastes and the like that cause fermentation are generated, the regular processing place (eg, farm).
Is relatively difficult to secure, and even in the case of temporarily accumulating the generated substances in the business site, it is difficult to secure the accumulation place, and the problem of odor generated due to the accumulation is large. However, there is a problem that a poultry farm and a pig farm can be opened only in a mountain with a small population. Therefore, an object of the present invention is to obtain a treatment facility that can reduce the amount of raw garbage that is likely to be accompanied by an odor and deodorize it with relatively simple facilities without causing environmental problems.
【0004】[0004]
【課題を解決するための手段】この目的を達成するため
の本発明による請求項1に係わる処理設備の特徴構成
は、これが、水分を含有する醗酵処理可能な被処理物が
投入され、加温条件下で被処理物を醗酵乾燥する醗酵乾
燥槽と、醗酵乾燥槽で醗酵乾燥処理を受けた被処理物を
焼却処理する焼却炉とを備えるとともに、焼却炉から発
生する臭気を伴った排ガスを燃焼により脱臭する脱臭炉
を備え、脱臭炉から発生する脱臭処理済の排ガスを醗酵
乾燥槽に導いて加温用熱源とする熱回収路と、醗酵乾燥
槽で発生する臭気ガス及び水蒸気を脱臭炉もしくは焼却
炉に導く発生ガス導入路を備え、焼却炉を脱臭炉の下側
に設け、脱臭炉を醗酵乾燥槽の下側に設けることにあ
る。請求項1に係わる処理設備において、前記焼却炉が
ロータリーキルン式焼却炉であることが好ましい。これ
が、請求項2に係わる処理設備の特徴構成である。請求
項1または2に係わる処理設備において、前記被処理物
が投入される前記醗酵乾燥槽の処理物投入口が、開閉気
密操作自在に構成されるとともに、前記醗酵乾燥槽、前
記焼却炉、前記脱臭炉にわたる前記被処理物もしくは前
記排ガスの移動経路内を大気圧に対して低い圧力に維持
する減圧維持機構が備えられていることが、好ましい。
これが請求項3に係わる処理設備の特徴構成である。請
求項1〜3のいずれか1項に係わる処理設備において、
前記醗酵処理槽と前記焼却炉との間に、前記醗酵処理槽
で得られる醗酵乾燥処理済の被処理物を一旦貯留する貯
留槽と、前記貯留槽内より前記醗酵乾燥処理済の被処理
物を前記焼却炉内に所定量ずつ投入する定量供給装置を
備えることが好ましい。これが、請求項4に係わる処理
設備の特徴構成である。請求項4に係わる処理設備にお
いて、前記醗酵乾燥槽に於ける前記被処理物の醗酵乾燥
状態を検出する処理物状況検出手段を備え、前記処理物
状況検出手段による検出結果に基づいて、前記焼却炉に
於ける焼却処理量を制御する処理量調節手段を備えるこ
とが好ましい。これが、請求項5に係わる処理設備の特
徴構成である。請求項1〜5のいずれか1項に係わる処
理設備において、焼却処理可能な処理物を前記焼却炉に
直接投入できる処理物投入部を備えることが好ましい。
これが、請求項6に係わる処理設備の特徴構成である。
請求項1〜6のいずれか1項に係わる処理設備を使用す
るに、前記水分を含有する醗酵処理可能な被処理物を、
デンプンを主成分とする生分解性プラスチック袋に収納
して、前記醗酵乾燥槽に投入することが好ましい。これ
が、請求項7に係わる処理設備の使用方法の特徴であ
る。In order to achieve this object, the characteristic constitution of the treatment equipment according to claim 1 according to the present invention is as follows. Fermentation drying tank for fermenting and drying the object to be treated under conditions, and an incinerator for incinerating the object to be treated that has undergone fermentation and drying treatment in the fermentation drying tank, and exhaust gas with odor generated from the incinerator Equipped with a deodorizing furnace that deodorizes by combustion, a heat recovery path that guides the deodorized exhaust gas generated from the deodorizing furnace to the fermentation drying tank as a heat source for heating, and a deodorizing furnace that removes odorous gas and steam generated in the fermentation drying tank. Alternatively, it is provided with a generated gas introduction path leading to the incinerator, the incinerator is provided below the deodorizing furnace, and the deodorizing furnace is provided below the fermentation drying tank. In the treatment facility according to claim 1, it is preferable that the incinerator is a rotary kiln incinerator. This is a characteristic configuration of the processing equipment according to claim 2. The processing facility according to claim 1 or 2, wherein a processed material inlet of the fermentation drying tank into which the processed material is charged is configured to be open / closed in an airtight manner, and the fermentation drying tank, the incinerator, and It is preferable that a decompression maintaining mechanism that maintains a pressure lower than the atmospheric pressure in the moving path of the object to be treated or the exhaust gas passing through the deodorizing furnace is provided.
This is a characteristic configuration of the processing equipment according to claim 3. In the processing equipment according to any one of claims 1 to 3,
Between the fermentation treatment tank and the incinerator, a storage tank for temporarily storing the fermented and dried processed material obtained in the fermented treatment tank, and the fermented and dried processed material from the storage tank. It is preferable to provide a fixed amount supply device for charging a predetermined amount into the incinerator. This is a characteristic configuration of the processing equipment according to claim 4. The treatment facility according to claim 4, further comprising a treated substance status detecting means for detecting a fermentation dried state of the treated object in the fermentation drying tank, and the incineration based on a detection result by the treated substance status detecting means. It is preferable to provide a throughput adjusting means for controlling the incineration throughput in the furnace. This is the characteristic configuration of the processing equipment according to claim 5. In the treatment facility according to any one of claims 1 to 5, it is preferable that the treatment facility is provided with a treated substance charging unit capable of directly charging a treated substance capable of being incinerated into the incinerator.
This is the characteristic configuration of the processing equipment according to claim 6.
When using the treatment facility according to any one of claims 1 to 6, a fermentation-treatable substance containing the water is added,
It is preferable to store the product in a biodegradable plastic bag containing starch as a main component and put it in the fermentation drying tank. This is a feature of the method of using the processing equipment according to claim 7.
【0005】〔作用〕請求項1に係わる処理設備には、
醗酵乾燥槽、焼却炉、脱臭炉が備えられ、前記醗酵乾燥
槽で被処理物の醗酵乾燥が、焼却炉で醗酵乾燥済の被処
理物の焼却処理が、さらに、脱臭炉で、焼却炉から発生
する臭気付きの排ガスの脱臭が行われる。そして、脱臭
済の排ガスは、熱回収路を介して醗酵乾燥槽に於ける醗
酵乾燥用に熱源として利用される。醗酵乾燥槽で、処理
に伴って発生する臭気ガス及び水蒸気は、発生ガス導入
路を介して脱臭炉もしくは焼却炉に送られ、脱臭処理さ
れる。従って、本願の処理設備にあっては、被処理物の
焼却処理まで行って、充分な減量化を達成することがで
きる。さらに、装置が発生する熱を熱源とする醗酵乾燥
槽を備えるため、設備内での有効な熱利用が計られてお
り、省エネルギータイプの装置となっている。装置各機
器(醗酵乾燥槽及び焼却炉)から発生する臭気ガスも脱
臭炉で確実に処理できるため、臭気発生の問題は解消で
きる。さて、本願においては、醗酵乾燥槽、脱臭炉、焼
却炉が記載順に高位置(先に記載のものが後に記載のも
のより上側の位置)に来るように配置構成されている。
ここで、固形物の移動方向は、醗酵乾燥槽から焼却炉に
到り、炉出口から排出される格好となる。従って、固形
物の移動方向は、上から下へ移動する方向となり、例え
ば、装置内では重量のある固形物を投入以降、リフトア
ップする等の余分なエネルギーを必要とすることもな
い。一方、焼却炉から発生する排ガスの移動経路は、焼
却炉、脱臭炉、醗酵乾燥槽へと移動することとなり、下
から上方への移動となる。従って、この点でも、ガス移
動を誘起するためのブロア機構等の小容量化を達成で
き、この点でも好ましい設備を与えることとなる。請求
項2に係わる処理設備においては、焼却炉としてロータ
リーキルン式の焼却炉を採用する。この焼却炉は、横向
き傾斜配置のキルン内で被処理物を処理する形態である
ため、設備全体の高さを大きくすることなく、設備をコ
ンパクトに構成できる。さらに、図2に示すように、こ
のキルンの上部位置に、脱臭炉を備えるとともに、さら
に上方に同様に円筒状の醗酵乾燥槽を備えると、かなり
な処理容量を確保しながら、なお全体としての専有容積
の小さい処理設備を得ることができる。請求項3に係わ
る処理設備においては、醗酵乾燥槽の処理物投入口が気
密操作自在に構成されるとともに、醗酵乾燥槽、焼却
炉、脱臭炉にわたって、その内部圧力が減圧維持機構に
より減圧状態に保たれる。これらの機器内は、臭気ガス
が発生する部位であり、減圧状態に保つことで、臭気ガ
スの外部への漏れ出しが防止できる。さらに、この構成
で、減圧維持機構により醗酵乾燥槽、焼却炉内のガスを
最終的に、脱臭炉に導く構造(下記の実施の形態はこの
構造となっている)を採用しておくと、臭気ガスの処理
を確実に行える。請求項4に係わる処理設備において
は、醗酵乾燥済のある程度減量化された被処理物は、貯
留槽に一旦貯留され、その後、定量供給装置により、焼
却炉に供給される。従って、焼却炉に於ける焼却処理量
のコントロールを確実に行えるようになるとともに、一
方で、醗酵乾燥槽に於ける処理をおこないながら、且
つ、焼却処理物の安定供給状態を確保して、焼却炉に於
ける処理を安定的に進めることができる。請求項5に係
わる処理設備においては、設備に処理物状況検出手段と
処理量調節手段が備えられる。ここで、前者は醗酵乾燥
槽に於ける被処理物の状況を検出することにより、処理
量調節手段における処理量の決定基準を与える。本願の
処理設備にあっては、基本的には、醗酵乾燥槽に於ける
処理が比較的時間を要する処理であり、この槽からの処
理済被処理物が、所定量、定期的に得られる状況が実現
して始めて、設備の運転維持がスムーズに進む。そし
て、この醗酵処理槽にあっては、加温温度を醗酵が良好
に進む一定温度以上に常時維持することが好ましい。従
って、この構成により良好な操業状態を維持できる。請
求項6に係わる処理設備にあっては、以下のようにして
処理を進めることができる。一般の事業所にあっては、
生ゴミ等の醗酵処理できるものと、紙、プラスチック等
の醗酵には不適な被処理物が発生する。そして、このよ
うな醗酵に適さないものを、焼却炉に備えられた処理物
投入部から投入する。このようにすると、事業所から発
生するあらゆる種類の処理物に対応できる。請求項7に
係わる処理設備の使用方法にあっては、被処理物の醗酵
乾燥槽への投入を、デンプンを主成分とする生分解性プ
ラスチック袋に収納した状態で、槽内へ投入する。この
袋は、その組成から、醗酵乾燥槽内で醗酵分解乾燥され
る。従って、被処理物を好適に悪臭を外部に発散させる
ことなく移動搬送できる状態で、醗酵乾燥槽内に投入し
ながら、設備内で問題を起こすことなく、処理を順調に
進めることができる。[Operation] The processing equipment according to claim 1 includes:
Fermentation drying tank, incinerator, deodorizing furnace is provided, fermentation drying of the processed material in the fermentation drying tank, incineration of the fermented and dried processed material in the incinerator, further in the deodorizing furnace, from the incinerator The odorous exhaust gas that is generated is deodorized. The deodorized exhaust gas is used as a heat source for fermentation drying in the fermentation drying tank via the heat recovery passage. In the fermentation drying tank, the odorous gas and water vapor generated by the treatment are sent to a deodorizing furnace or an incinerator through a generated gas introduction passage to be deodorized. Therefore, in the treatment facility of the present application, it is possible to perform even the incineration treatment of the object to be treated and achieve sufficient reduction. Further, since the fermentation drying tank using the heat generated by the device as a heat source is provided, effective use of heat in the facility is measured, and the device is an energy saving type device. Since the odorous gas generated from each device (fermentation drying tank and incinerator) can be reliably treated in the deodorizing furnace, the problem of odor generation can be solved. By the way, in the present application, the fermentation drying tank, the deodorizing furnace, and the incinerator are arranged and arranged so as to come to the high position (the one described above is a position above the one described later) in the order of description.
Here, the moving direction of the solid matter is from the fermentation drying tank to the incinerator and is discharged from the furnace outlet. Therefore, the moving direction of the solid matter is from top to bottom, and for example, there is no need for extra energy such as lifting up after loading a heavy solid matter in the apparatus. On the other hand, the moving path of the exhaust gas generated from the incinerator moves to the incinerator, the deodorizing furnace, and the fermentation drying tank, and moves from the bottom to the top. Therefore, also in this respect, the capacity of the blower mechanism or the like for inducing gas movement can be reduced, and in this respect as well, preferable equipment can be provided. In the treatment facility according to claim 2, a rotary kiln type incinerator is used as the incinerator. Since this incinerator has a form in which the object to be treated is processed in the kiln having the laterally inclined arrangement, the equipment can be configured compactly without increasing the height of the entire equipment. Further, as shown in FIG. 2, if a deodorizing furnace is provided at the upper position of this kiln, and a cylindrical fermentation drying tank is also provided above the kiln, while maintaining a considerable processing capacity, the entire It is possible to obtain a processing facility with a small occupied volume. In the treatment facility according to claim 3, the treated product inlet of the fermentation drying tank is configured to be airtightly operable, and the internal pressure of the fermentation drying tank, the incinerator, and the deodorizing furnace is reduced by the reduced pressure maintaining mechanism. To be kept. The inside of these devices is a part where odorous gas is generated, and by keeping the depressurized state, it is possible to prevent the odorous gas from leaking to the outside. Furthermore, with this configuration, a structure that guides the gas in the fermentation drying tank and the incinerator to the deodorizing furnace by the depressurization maintaining mechanism (the following embodiment has this structure) is adopted. Reliable treatment of odorous gas. In the treatment facility according to the fourth aspect, the fermented and dried substance to be treated, which has been reduced to some extent, is temporarily stored in a storage tank and then supplied to an incinerator by a fixed amount supply device. Therefore, it becomes possible to reliably control the amount of incineration in the incinerator, and at the same time, while performing the treatment in the fermentation drying tank, while ensuring a stable supply state of the incineration treated product, The processing in the furnace can proceed stably. In the processing equipment according to the fifth aspect, the equipment is provided with a processed material status detecting means and a processing amount adjusting means. Here, the former provides a criterion for determining the throughput in the throughput adjusting means by detecting the condition of the object to be treated in the fermentation drying tank. In the processing equipment of the present application, basically, the processing in the fermentation drying tank is a processing that requires a relatively long time, and the processed material to be processed from this tank is regularly obtained in a predetermined amount. Only when the situation is realized will the operation and maintenance of the equipment proceed smoothly. Further, in this fermentation treatment tank, it is preferable that the heating temperature is always maintained at a certain temperature or higher at which the fermentation can proceed favorably. Therefore, this configuration can maintain a good operating condition. In the processing facility according to claim 6, the processing can be proceeded as follows. In general offices,
Some foods that can be fermented, such as raw garbage, and some materials that are unsuitable for fermentation, such as paper and plastic, are generated. And what is not suitable for such fermentation is thrown in from the processed material throwing part provided in the incinerator. In this way, it is possible to deal with all kinds of processed materials generated from business establishments. In the method of using the treatment facility according to claim 7, the material to be treated is put into the fermentation drying tank in a state where it is stored in a biodegradable plastic bag containing starch as a main component. Due to its composition, this bag is fermented, decomposed and dried in the fermentation drying tank. Therefore, it is possible to smoothly carry out the treatment without causing a problem in the equipment while being charged into the fermentation drying tank in a state in which the substance to be treated can be suitably transferred and conveyed without emitting a bad odor to the outside.
【0006】[0006]
【発明の実施の形態】以下、本願の処理設備の実施の形
態を図面に基づいて説明する。図1は処理設備1のシス
テム構成を示し、図2は処理設備1の概略正面図を、図
3は処理設備1の概略側面図を示している。さらに、図
4は、処理設備1の平面図を示している。この処理設備
1は、上下方向で2分割可能な構造となっているため、
図4においては、図上上側に醗酵乾燥槽2を主要機器と
する設備上段部200を、図上下側に脱臭炉4及び焼却
炉3を主要機器とする設備下段部300を示している。
図1〜4に示すように、処理設備1は、その主要機器と
して、例えば生ゴミ等の水分を含有する醗酵処理可能な
被処理物を加温条件下で醗酵乾燥する醗酵乾燥槽2と、
この醗酵乾燥槽2で醗酵乾燥処理を受けた被処理物を焼
却処理する焼却炉3とを備えるとともに、焼却炉3から
発生する臭気を伴った排ガスを燃焼により脱臭する脱臭
炉4を備えて構成されている。そして、脱臭炉4から発
生する脱臭処理済の排ガスを醗酵乾燥槽2に導いて加温
用熱源とする熱回収路5と、醗酵乾燥槽2で発生する臭
気ガス及び水蒸気を脱臭炉もしくは焼却炉3に導く発生
ガス導入路6を備えている。さらに、図2に示すよう
に、焼却炉3、脱臭炉4、醗酵乾燥槽2が記載順に上側
(後者程上側)に設けられている。BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the treatment facility of the present application will be described below with reference to the drawings. 1 shows a system configuration of the processing equipment 1, FIG. 2 shows a schematic front view of the processing equipment 1, and FIG. 3 shows a schematic side view of the processing equipment 1. Further, FIG. 4 shows a plan view of the processing equipment 1. Since this processing equipment 1 has a structure that can be divided into two parts in the vertical direction,
In FIG. 4, the upper part of the equipment 200 having the fermentation drying tank 2 as the main equipment is shown on the upper side of the drawing, and the lower part of the equipment 300 having the deodorizing furnace 4 and the incinerator 3 as the main equipment is shown on the upper and lower sides of the drawing.
As shown in FIGS. 1 to 4, the treatment equipment 1 has, as its main equipment, a fermentation drying tank 2 for fermenting and drying a fermentable material to be treated containing water, such as garbage, under heating conditions.
It is provided with an incinerator 3 for incinerating an object to be processed that has been subjected to fermentation and drying treatment in this fermentation and drying tank 2, and a deodorizing furnace 4 for deodorizing exhaust gas with odor generated from the incinerator 3 by burning. Has been done. Then, the heat recovery path 5 that guides the deodorized exhaust gas generated from the deodorization furnace 4 to the fermentation drying tank 2 to serve as a heat source for heating, and the odorous gas and steam generated in the fermentation drying tank 2 to the deodorization furnace or incinerator. A generated gas introduction path 6 that leads to 3 is provided. Further, as shown in FIG. 2, an incinerator 3, a deodorizing furnace 4, and a fermentation drying tank 2 are provided on the upper side in the order of description (the latter is on the upper side).
【0007】以下、さらに、詳細に各機器について説明
する。前記醗酵乾燥槽2は、所謂、円筒形処理槽7を備
えたものであり、被処理物を収容するための円筒形ドラ
ム8と、この処理槽7内に攪拌モータ9に連動されて回
転する攪拌機構10を備えている。この処理槽7には、
開閉密封操作自在な処理物投入口11が備えられるとと
もに、図3に示すように、処理槽7の下部位置より所定
量だけ高い位置に、処理物排出口12を備えている。こ
の処理物排出口12も開閉式に構成されており、処理槽
7内に於ける被処理物の処理が完了した状態で、ドラム
8内にある被処理物の大半(約70%程度)を、処理槽
7外に排出できる構成が採用されている。前記処理物投
入口11に対しては、リフター13が装備されており、
投入口11を開状態にしたまま、このリフター13によ
り地上側より被処理物を投入操作できるようになってい
る。この被処理物の投入操作にあたっては、後述するよ
うに、生ゴミ等をデンプンを主成分とする生分解性プラ
スチック袋14に収容した状態で、リフター13で投入
口11まで、上昇搬送して、醗酵乾燥槽2内への投入を
おこなうことができる。さらに、前記円筒形処理槽7の
外周部位には、後述するように、脱臭炉4により脱臭処
理済の排ガスが回流する加温ジャケット15を備えてお
り、この排ガスの保有する熱により処理槽7内に於ける
醗酵乾燥操作を促進できる構成が採用されている。ま
た、このような排ガスによる間接加熱では、充分な処理
が行えない状況に対応するために、脱臭処理済の排ガス
を直接処理槽7内に導いて、直接加熱することもできる
ようになっている。即ち、図1に示すように、前述の脱
臭炉4から醗酵乾燥槽2へ排ガスを導く熱回収路5は、
前述の加温ジャケット15に接続される間接加熱路5a
と、直接処理槽7内に排ガスを導入する直接加熱路5b
とを備えて構成されている。排ガスの流路に関しては、
後にさらに詳細に説明する。Each device will be described in more detail below. The fermentation drying tank 2 is provided with a so-called cylindrical processing tank 7, and a cylindrical drum 8 for accommodating an object to be processed and the processing tank 7 is rotated in association with a stirring motor 9. A stirring mechanism 10 is provided. In this processing tank 7,
A processed material inlet 11 that can be opened / closed and sealed is provided, and a processed material outlet 12 is provided at a position higher than a lower position of the processing tank 7 by a predetermined amount, as shown in FIG. This processed material discharge port 12 is also configured to be openable and closable so that most of the processed material in the drum 8 (about 70%) is completely processed in the processing tank 7. The structure that can be discharged to the outside of the processing tank 7 is adopted. A lifter 13 is provided for the processed material inlet 11,
The lifter 13 allows the object to be processed to be loaded from the ground side while the loading port 11 is kept open. In the operation of loading the object to be treated, as will be described later, in a state where raw garbage or the like is stored in the biodegradable plastic bag 14 containing starch as a main component, the lifter 13 moves up to the loading port 11, It can be put into the fermentation drying tank 2. Further, as will be described later, a heating jacket 15 for circulating the exhaust gas deodorized by the deodorizing furnace 4 is provided on the outer peripheral portion of the cylindrical processing tank 7, and the processing tank 7 is heated by the heat of the exhaust gas. The structure that can accelerate the fermentation drying operation inside is adopted. Further, in such indirect heating with exhaust gas, in order to deal with a situation where sufficient processing cannot be performed, the deodorized exhaust gas can be directly introduced into the processing tank 7 and directly heated. . That is, as shown in FIG. 1, the heat recovery path 5 for guiding the exhaust gas from the deodorizing furnace 4 to the fermentation drying tank 2 is
Indirect heating path 5a connected to the heating jacket 15 described above.
And a direct heating path 5b for directly introducing the exhaust gas into the treatment tank 7.
It is comprised including. Regarding the exhaust gas flow path,
This will be described in more detail later.
【0008】以上が、醗酵乾燥槽2に関する説明である
が、この槽2に於ける処理によって得られる醗酵乾燥処
理済の被処理物の流れを説明する。このような処理を経
た後にあっては、被処理物の容積は、約30%程度まで
減量化されており、その状態は、おから状になってい
る。前記処理物排出口12に対して、その出口位置に
は、醗酵処理槽2で得られる醗酵乾燥処理済の被処理物
を一旦貯留する貯留槽16と、この貯留槽16内より醗
酵乾燥処理済の被処理物を焼却炉3内に所定量ずつ投入
する定量供給装置17を備えている。前記定量供給装置
17は、切り出し側のスクリューコンベア18と投入側
のスクリューコンベア19との二段のスクリューコンベ
ア18、19から構成されている。そして、この定量供
給装置17に対して、これにより焼却炉3内に投入され
る被処理物の量を制御する処理量調節手段20を備えて
いる。そして、前記醗酵乾燥槽2に於ける被処理物の醗
酵乾燥状態を検出する処理物状況検出手段21を備え、
この処理物状況検出手段21又は焼却炉3内の燃焼状況
検出手段210による検出結果に基づいて、焼却炉3に
於ける焼却処理量を処理量調節手段20による定量供給
装置17の供給量制御により制御できるようになってい
る。ここで、処理物状況検出手段21とは、ドラム内の
温度、湿度、さらにドラム内に残っている被処理物の高
さ等の検出器22等と、これら検出器22の検出結果
を、予め記憶されている基準データとの比較することに
より、被処理物の処理状況を判断する判断手段23とか
ら構成されており、この判断手段23による判断結果
が、処理量調節手段20側へ送られる構成が採用されて
いる。The above is a description of the fermentation drying tank 2, and the flow of the fermented and dried processed material obtained by the processing in this tank 2 will be described. After such treatment, the volume of the object to be treated is reduced to about 30%, and the state is okara. At the outlet position of the treated product discharge port 12, a storage tank 16 for temporarily storing the fermented and dried processed product obtained in the fermented treatment tank 2, and a fermented and dried treatment from the storage tank 16 It is equipped with a constant amount supply device 17 for charging a predetermined amount of the object to be treated into the incinerator 3. The constant quantity supply device 17 is composed of two stages of screw conveyors 18, 19 including a cutting-side screw conveyor 18 and a charging-side screw conveyor 19. Then, the fixed amount supply device 17 is provided with a processing amount adjusting means 20 for controlling the amount of the object to be processed which is put into the incinerator 3. Then, a processed product status detection means 21 for detecting the fermented and dried state of the processed product in the fermentation and drying tank 2 is provided,
Based on the detection result by the treated material status detecting means 21 or the combustion status detecting means 210 in the incinerator 3, the incineration processing amount in the incinerator 3 is controlled by the supply amount control of the constant amount supply device 17 by the processing amount adjusting means 20. It can be controlled. Here, the processed material status detecting means 21 is a detector 22 for detecting the temperature and humidity in the drum, and the height of the processed material remaining in the drum, and the detection results of these detectors 22 in advance. It comprises a judgment means 23 for judging the processing status of the object to be processed by comparing it with the stored reference data, and the judgment result by this judgment means 23 is sent to the processing amount adjusting means 20 side. The configuration is adopted.
【0009】次に、焼却炉3について説明する。この焼
却炉3は、所謂、ロータリーキルン式の焼却炉である。
この焼却炉3は、被処理物が燃焼されるキルン24と、
このキルン24内に燃焼用空気を供給する送風機25
と、焼却炉操業開始時に使用される着火・予熱用のバー
ナ26と、先に説明した投入側のスクリューコンベア1
9を備えて構成されている。さらに、醗酵乾燥槽2にお
いて処理可能なものの焼却処理物とは別に、紙、廃棄プ
ラスチック等の醗酵処理できず、焼却処理可能な処理物
を、キルン24内に直接投入できる処理物投入部27
(図1参照)を備えている。この焼却炉3の下手側に
は、焼却処理物回収室28が設けられており、キルン2
4から回収される焼却灰29を設備外に取り出すことが
できる。Next, the incinerator 3 will be described. The incinerator 3 is a so-called rotary kiln type incinerator.
The incinerator 3 includes a kiln 24 in which an object to be processed is burned,
Blower 25 for supplying combustion air into this kiln 24
And a burner 26 for ignition / preheating used at the start of incinerator operation, and the screw conveyor 1 on the loading side described above.
9 is provided. Further, apart from the incineration products that can be processed in the fermentation drying tank 2, the fermentation products such as paper and waste plastic that cannot be fermented and can be incinerated directly can be inserted into the kiln 24.
(See FIG. 1). On the lower side of the incinerator 3, an incineration-processed material recovery chamber 28 is provided, and the kiln 2
The incinerated ash 29 collected from No. 4 can be taken out of the facility.
【0010】前記焼却処理物回収室28の上部には、排
ガス回収ダクト30が接続されており、この排ガス回収
ダクト30を介して、焼却炉3から発生する排ガスは、
脱臭炉4に導入される。この脱臭炉4は、脱臭処理用の
バーナ31を備えるとともに、800℃程度の高温環境
下で排ガスを1〜2秒以上処理して、完全脱臭をおこな
うに充分な脱臭室32を備える構成となっている。この
実施の形態の例においては、焼却炉3として横長のロー
タリーキルン式のものを採用するとともに、脱臭炉4を
この上部奥側に(図3参照)、同様に横長の脱臭室32
を備えた脱臭炉4を備えることにより、コンパクトな構
成で確実な焼却・脱臭が行えるようになっている。An exhaust gas recovery duct 30 is connected to the upper part of the incineration product recovery chamber 28, and the exhaust gas generated from the incinerator 3 is connected via the exhaust gas recovery duct 30.
It is introduced into the deodorizing furnace 4. This deodorizing furnace 4 is provided with a deodorizing burner 31 and a deodorizing chamber 32 that is sufficient for complete deodorization by treating exhaust gas for 1 to 2 seconds or more in a high temperature environment of about 800 ° C. ing. In the example of this embodiment, a horizontally long rotary kiln type is adopted as the incinerator 3, and the deodorizing furnace 4 is provided at the back of the upper part (see FIG. 3).
By providing the deodorizing furnace 4 provided with, it is possible to reliably incinerate and deodorize with a compact configuration.
【0011】脱臭炉4から醗酵乾燥槽2へ排ガスを導く
熱回収路5は、加温ジャケット15に接続される間接加
熱路5aと、直接ドラム8内に排ガスを導入する直接加
熱路5bとを備えている。これらの間接加熱路5aと直
接加熱路5bとの基端側には、夫々の路5a、5bを流
れて所定部位に供給される排ガスの温度を調節するため
の希釈空気吸引機構33(所定の配管33a、ダンパ3
3b及び吸引口33cから構成される)が設けられてい
る。ここで、間接加熱路5aを流れるガスの温度は30
0℃程度に調節し、直接加熱路5bを流れるガスの温度
は150℃程度に調節する。さて、醗酵乾燥槽2に備え
られる加温ジャケット15の下流側には、誘引ファン3
4が備えられるとともに、この排気が煙突35を介して
外部に放出される構成が取られている。ここで、この系
統を流れるガスは、脱臭炉4により脱臭処理済のもので
あるため、外部への臭気の漏れ出しを起こすことはな
い。前記直接加熱路5bを介してドラム8内に導かれる
ガスに関しては、このドラム8に対して設けられている
発生ガス導入路6を介して、これが焼却炉3のキルン2
4内に導かれる。発生ガス導入路6には、醗酵乾燥槽
2、キルン24、脱臭炉4を介するガスの循環を確保
し、焼却炉3に於ける燃焼用空気を確保するための循環
ファン36が備えられている。The heat recovery path 5 for guiding the exhaust gas from the deodorizing furnace 4 to the fermentation drying tank 2 includes an indirect heating path 5a connected to the heating jacket 15 and a direct heating path 5b for directly introducing the exhaust gas into the drum 8. I have it. At the base end sides of the indirect heating path 5a and the direct heating path 5b, a dilution air suction mechanism 33 (predetermined value) for adjusting the temperature of the exhaust gas flowing through the respective paths 5a and 5b and supplied to a predetermined part is provided. Pipe 33a, damper 3
3b and the suction port 33c). Here, the temperature of the gas flowing through the indirect heating path 5a is 30
The temperature of the gas flowing directly through the heating passage 5b is adjusted to about 150 ° C. Now, on the downstream side of the heating jacket 15 provided in the fermentation drying tank 2, the induction fan 3 is provided.
4 is provided, and the exhaust is discharged to the outside through the chimney 35. Here, since the gas flowing through this system has been deodorized by the deodorization furnace 4, it does not leak odor to the outside. Regarding the gas introduced into the drum 8 through the direct heating passage 5b, the gas is introduced into the kiln 2 of the incinerator 3 through the generated gas introduction passage 6 provided for the drum 8.
Guided within 4. The generated gas introduction path 6 is provided with a circulation fan 36 for ensuring the circulation of gas through the fermentation drying tank 2, the kiln 24, and the deodorizing furnace 4 and for ensuring the combustion air in the incinerator 3. .
【0012】以上が、設備1の概要であるが、以下、そ
の働きについて説明する。 1 被処理物である生ゴミ等を生分解性のプラスチック
袋14にいれたまま、リフター13によって、醗酵乾燥
槽2内に投入する。この投入時に、所謂、醗酵菌である
納豆菌、イースト菌等を同時に投入する。槽2内は、7
0〜80℃程度に保温維持され、約3時間程度で、1ト
ン程度の被処理物をオカラ状に減量、乾燥処理する。 2 所定の状態となった被処理物を、貯留槽16に排出
し、逐次、焼却炉3で焼却処理する。 3 焼却処理によって発生する排ガスは、脱臭炉4で脱
臭処理し、醗酵乾燥槽2に於ける処理に役立てた後、外
部に放出する。焼却灰29は、焼却処理物回収室28の
下部から回収する。The outline of the equipment 1 has been described above, and its function will be described below. (1) Raw garbage or the like to be treated is put into the fermentation drying tank 2 by the lifter 13 while being put in the biodegradable plastic bag 14. At this time, so-called fermentative bacteria such as natto and yeast are simultaneously introduced. 7 in tank 2
The temperature is maintained at 0 to 80 ° C., and the amount of about 1 ton of the object to be treated is reduced to an okara state and dried for about 3 hours. 2 The object to be processed in a predetermined state is discharged to the storage tank 16 and sequentially incinerated in the incinerator 3. 3. The exhaust gas generated by the incineration process is deodorized in the deodorization furnace 4, is used for the process in the fermentation drying tank 2, and is then discharged to the outside. The incineration ash 29 is collected from the lower part of the incineration treated material recovery chamber 28.
【0013】運転は、以上のように行われるが、この処
理設備1にあっては、充分な臭気対策が採られている。
この構成について説明する。先に説明したように、主な
臭気成分は、脱臭炉4により処理されるのであるが、本
願の設備にあっては、醗酵乾燥槽2の処理物投入口11
が、開閉気密操作自在に構成されている。さらに、先に
説明したように、醗酵乾燥槽2、焼却炉3、脱臭炉4に
わたる被処理物もしくは排ガスの移動経路は、閉構造と
されるとともに、この経路の最下流側が、前述の誘引フ
ァン34を介して、外気に接続される構造となってい
る。従って、このファン34の働きにより、上記の経路
内は、大気圧に対して低い圧力に維持されるため、臭気
ガスの外部への漏れだしも発生しない。即ち前記誘引フ
ァン34は、経路内を大気圧に対して低い圧力に維持す
る減圧維持機構の働きをしている。The operation is performed as described above, but the processing facility 1 takes sufficient measures against odor.
This configuration will be described. As described above, the main odorous components are processed by the deodorizing furnace 4. In the equipment of the present application, the processed product input port 11 of the fermentation drying tank 2 is used.
However, it can be opened and closed airtightly. Further, as described above, the moving route of the object to be treated or the exhaust gas passing through the fermentation drying tank 2, the incinerator 3, and the deodorizing furnace 4 has a closed structure, and the most downstream side of this route is the above-mentioned attraction fan. The structure is connected to the outside air via 34. Therefore, due to the function of the fan 34, the inside of the above-mentioned path is maintained at a pressure lower than the atmospheric pressure, so that the odorous gas does not leak to the outside. That is, the induction fan 34 functions as a decompression maintaining mechanism that maintains the inside of the passage at a pressure lower than the atmospheric pressure.
【0014】[0014]
【発明の効果】従って、本願の処理設備にあっては、比
較的コンパクトな構成で、悪臭を発生することなく、醗
酵処理可能な被処理物を、減量処理できる処理設備を得
ることができた。Therefore, in the treatment equipment of the present invention, it is possible to obtain the treatment equipment having a relatively compact structure and capable of reducing the amount of the fermentable material to be processed without generating a bad odor. .
【0015】尚、特許請求の範囲の項に図面との対照を
便利にするために符号を記すが、該記入により本発明は
添付図面の構成に限定されるものではない。It should be noted that reference numerals are given in the claims for convenience of comparison with the drawings, but the present invention is not limited to the configurations of the accompanying drawings by the entry.
【図1】処理設備のシステム構成を示す図FIG. 1 is a diagram showing a system configuration of a processing facility.
【図2】処理設備の正面図[Figure 2] Front view of processing equipment
【図3】処理設備の側面図[Figure 3] Side view of processing equipment
【図4】処理設備の分解平面図[Fig. 4] Exploded plan view of processing equipment
2 醗酵乾燥槽 3 焼却炉 4 脱臭炉 5 熱回収路 6 発生ガス導入路 11 処理物投入口 14 生分解性プラスチック袋 16 貯留槽 20 処理量調節手段 21 処理物状況検出手段 27 処理物投入部 34 減圧維持機構 2 Fermentation / drying tank 3 Incinerator 4 Deodorizing furnace 5 Heat recovery path 6 Emission gas introduction path 11 Treated material input port 14 Biodegradable plastic bag 16 Storage tank 20 Treated amount control means 21 Treated material status detection means 27 Treated material input part 34 Reduced pressure maintenance mechanism
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 F23G 5/00 108 F23G 5/20 ZABA 5/16 ZAB 5/50 ZABG 5/20 ZAB ZABQ 5/50 ZAB B09B 3/00 ZABD 303M (72)発明者 森本 三次 大阪府大阪市東成区中道一丁目4番2号 大阪ガスエンジニアリング株式会社内 (72)発明者 伊藤 拓仙 京都府舞鶴市字長浜920番地 けいはんな 環境株式会社内 (72)発明者 谷中 厳 京都府舞鶴市字長浜920番地 けいはんな 環境株式会社内 (72)発明者 都竹 節雄 愛知県一宮市神山2丁目2番1号 株式会 社オークス内 (72)発明者 鶴田 勝也 愛知県一宮市神山2丁目2番1号 株式会 社オークス内Continuation of the front page (51) Int.Cl. 6 Identification number Office reference number FI Technical display location F23G 5/00 108 F23G 5/20 ZABA 5/16 ZAB 5/50 ZABG 5/20 ZAB ZABQ 5/50 ZAB B09B 3/00 ZABD 303M (72) Inventor Mitsumoto Mitsumi Osaka Prefecture Osaka City, Higashisei-ku, 1-2-4 Nakamichi, Osaka Gas Engineering Co., Ltd. Co., Ltd. (72) Inventor, Yan Yan, 920, Nagahama, Maizuru City, Kyoto Prefecture, Keihanna Environment Co., Ltd. Inventor Katsuya Tsuruta 2-2-1 Kamiyama, Ichinomiya-shi, Aichi Stock Company Oaks
Claims (7)
が投入され、加温条件下で前記被処理物を醗酵乾燥する
醗酵乾燥槽(2)と、前記醗酵乾燥槽(2)で醗酵乾燥
処理を受けた前記被処理物を焼却処理する焼却炉(3)
とを備えるとともに、前記焼却炉(3)から発生する臭
気を伴った排ガスを燃焼により脱臭する脱臭炉(4)を
備え、 前記脱臭炉(4)から発生する脱臭処理済の排ガスを前
記醗酵乾燥槽(2)に導いて加温用熱源とする熱回収路
(5)と、前記醗酵乾燥槽(2)で発生する臭気ガス及
び水蒸気を前記脱臭炉(4)もしくは前記焼却炉(3)
に導く発生ガス導入路(6)を備え、 前記焼却炉(3)を前記脱臭炉(4)の下側に設け、前
記脱臭炉(4)を前記醗酵乾燥槽(2)の下側に設けた
処理設備。1. A fermentation drying tank (2) in which a fermentation-treatable substance to be treated containing water is introduced, and the substance to be treated is fermented and dried under a heating condition, and fermentation is performed in the fermentation dryer (2). An incinerator (3) for incinerating the object to be treated that has been dried
And a deodorizing furnace (4) for deodorizing the exhaust gas with odor generated from the incinerator (3) by burning, and the deodorized exhaust gas generated from the deodorizing furnace (4) is subjected to the fermentation drying. A heat recovery path (5) that leads to a tank (2) to be a heat source for heating, and odorous gas and steam generated in the fermentation drying tank (2) are deodorizing furnace (4) or incinerator (3).
The incinerator (3) is provided below the deodorizing furnace (4), and the deodorizing furnace (4) is provided below the fermentation drying tank (2). Treatment equipment.
焼却炉である請求項1記載の処理設備。2. The treatment facility according to claim 1, wherein the incinerator (3) is a rotary kiln incinerator.
槽(2)の処理物投入口(11)が、開閉気密操作自在
に構成されるとともに、前記醗酵乾燥槽(2)、前記焼
却炉(3)、前記脱臭炉(4)にわたる前記被処理物も
しくは前記排ガスの移動経路内を大気圧に対して低い圧
力に維持する減圧維持機構(34)を備えた請求項1ま
たは2記載の処理設備。3. A fermenting / drying tank (2) into which the to-be-treated material is put in is configured such that a treated material inlet (11) can be opened and closed in an airtight manner, and the fermentation / drying tank (2) and the incinerator are incinerated. The pressure reduction maintaining mechanism (34) according to claim 1 or 2, further comprising a decompression maintaining mechanism (34) for maintaining a pressure lower than atmospheric pressure in a moving path of the object to be treated or the exhaust gas passing through the furnace (3) and the deodorizing furnace (4). Processing equipment.
(3)との間に、前記醗酵処理槽(2)で得られる醗酵
乾燥処理済の被処理物を一旦貯留する貯留槽(16)
と、前記貯留槽(16)内より前記醗酵乾燥処理済の被
処理物を前記焼却炉(3)内に所定量ずつ投入する定量
供給装置(18)(19)を備えた請求項1〜3のいず
れか1項に記載の処理設備。4. A storage tank (16) for temporarily storing the fermented and dried processed material obtained in the fermentation treatment tank (2) between the fermentation treatment tank (2) and the incinerator (3). )
And a fixed amount supply device (18) (19) for charging the fermented and dried material to be processed from the storage tank (16) into the incinerator (3) by a predetermined amount. The processing equipment according to any one of 1.
理物の醗酵乾燥状態を検出する処理物状況検出手段(2
1)を備え、前記処理物状況検出手段(21)による検
出結果に基づいて、前記焼却炉(3)に於ける焼却処理
量を制御する処理量調節手段(20)を備えた請求項4
記載の処理設備。5. A processed product status detecting means (2) for detecting a fermentation dry condition of the object to be processed in the fermentation drying tank (2).
The process amount adjusting means (20) for controlling the incineration amount in the incinerator (3) on the basis of the detection result of the processed matter state detecting means (21).
The indicated processing equipment.
(3)に直接投入できる処理物投入部(27)を備えた
請求項1〜5のいずれか1項に記載の処理設備。6. The treatment facility according to claim 1, further comprising a treated substance charging section (27) capable of directly charging an incinerable treated substance to the incinerator (3).
理設備を使用するに、前記水分を含有する醗酵処理可能
な被処理物を、デンプンを主成分とする生分解性プラス
チック袋(14)に収納して、前記醗酵乾燥槽(2)に
投入する処理設備の使用方法。7. A biodegradable plastic bag containing starch as a main component, wherein the fermentable material to be treated containing the water is used in the treatment equipment according to any one of claims 1 to 6. A method of using the processing equipment, which is stored in (14) and put into the fermentation drying tank (2).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18730995A JPH0942642A (en) | 1995-07-24 | 1995-07-24 | Disposal equipment and use thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18730995A JPH0942642A (en) | 1995-07-24 | 1995-07-24 | Disposal equipment and use thereof |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0942642A true JPH0942642A (en) | 1997-02-14 |
Family
ID=16203748
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18730995A Pending JPH0942642A (en) | 1995-07-24 | 1995-07-24 | Disposal equipment and use thereof |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0942642A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001191059A (en) * | 1999-11-02 | 2001-07-17 | Taiheiyo Cement Corp | Fermenting processing method and method for manufacturing cement |
JP2001269652A (en) * | 2000-03-28 | 2001-10-02 | Unitika Ltd | Organic waste treating method |
WO2005044756A1 (en) * | 2003-11-11 | 2005-05-19 | Asuna Co., Ltd. | Method of composting organic waste and apparatus therefor |
JP2011083716A (en) * | 2009-10-16 | 2011-04-28 | Urayasu Densetsu Kk | Treatment system of wet organic waste |
JP2011206659A (en) * | 2010-03-29 | 2011-10-20 | Greening Laboratory Co Ltd | Device and method for treating hazardous substance |
KR101227689B1 (en) * | 2011-01-19 | 2013-01-29 | 에이치투더블유티이 주식회사 | Sludge supplying apparatus |
-
1995
- 1995-07-24 JP JP18730995A patent/JPH0942642A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001191059A (en) * | 1999-11-02 | 2001-07-17 | Taiheiyo Cement Corp | Fermenting processing method and method for manufacturing cement |
JP2001269652A (en) * | 2000-03-28 | 2001-10-02 | Unitika Ltd | Organic waste treating method |
JP4633222B2 (en) * | 2000-03-28 | 2011-02-16 | ユニチカ株式会社 | Organic waste treatment methods |
WO2005044756A1 (en) * | 2003-11-11 | 2005-05-19 | Asuna Co., Ltd. | Method of composting organic waste and apparatus therefor |
JP2011083716A (en) * | 2009-10-16 | 2011-04-28 | Urayasu Densetsu Kk | Treatment system of wet organic waste |
JP2011206659A (en) * | 2010-03-29 | 2011-10-20 | Greening Laboratory Co Ltd | Device and method for treating hazardous substance |
KR101227689B1 (en) * | 2011-01-19 | 2013-01-29 | 에이치투더블유티이 주식회사 | Sludge supplying apparatus |
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