JP3498025B2 - Organic waste treatment method and apparatus - Google Patents

Organic waste treatment method and apparatus

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Publication number
JP3498025B2
JP3498025B2 JP35466799A JP35466799A JP3498025B2 JP 3498025 B2 JP3498025 B2 JP 3498025B2 JP 35466799 A JP35466799 A JP 35466799A JP 35466799 A JP35466799 A JP 35466799A JP 3498025 B2 JP3498025 B2 JP 3498025B2
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JP
Japan
Prior art keywords
processing
chamber
processing chamber
treatment
organic 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.)
Expired - Fee Related
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JP35466799A
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Japanese (ja)
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JP2001170606A (en
Inventor
雄一 荘
Original Assignee
雄一 荘
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Priority to JP35466799A priority Critical patent/JP3498025B2/en
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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

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

Description

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

【0001】[0001]

【発明の属する技術分野】この発明は、生ごみ、汚泥、
家畜糞等の有機質廃棄物を連続して処理できる処理方法
及びその処理装置に関する。
TECHNICAL FIELD The present invention relates to garbage, sludge,
The present invention relates to a treatment method capable of continuously treating organic waste such as livestock manure and a treatment apparatus therefor.

【0002】[0002]

【従来の技術】例えば、一般家庭、業務用食品加工工
場、スーパーマーケット、レストラン等から出る水分を
含むごみ(例えば、賞味期限済みの廃棄食品、残飯、野
菜くず、魚のあら等)、畜産農家から出る畜糞、地方公
共団体等行政主体における終末処理場で生じる汚泥等の
有機質廃棄物は、含水率が高くてこれをそのまま焼却処
理ができないので、まず乾燥機で乾燥処理してから焼却
機で焼却していた。最近では、このような有機質廃棄物
を醗酵処理して有機肥料として利用する方法が提案され
ている。従来の醗酵処理装置では、単一の処理室からな
る処理槽又は2つの処理室を有する処理槽内に有機質廃
棄物を投入してバッチ方式によって醗酵処理している。
2. Description of the Related Art For example, water-containing wastes (eg, waste foods with expired dates, leftover foods, vegetable scraps, fish roe, etc.) from households, commercial food processing plants, supermarkets, restaurants, etc., from livestock farmers. Since organic waste such as sludge and sludge generated at the terminal treatment plants of administrative bodies such as local public bodies cannot be incinerated as it is because of high water content, first dry it with a dryer and then incinerate it with an incinerator. Was there. Recently, a method has been proposed in which such an organic waste is subjected to a fermentation treatment and used as an organic fertilizer. In a conventional fermentation treatment apparatus, organic waste is put into a treatment tank having a single treatment chamber or a treatment tank having two treatment chambers to perform fermentation treatment by a batch method.

【0003】[0003]

【発明が解決しようとする課題】このバッチ方式によっ
て含水率の高い有機質廃棄物(生ごみでは含水率85%
程度)を醗酵処理するためには、必ず、乾材(おが屑
等)を一緒に投入して被処理物の含水率を50%〜60
%位まで下げて水分調整してから醗酵処理している。こ
れは、含水率が高いと、微生物の働きが悪いためであ
る。投入する乾材の量としては、被処理物に対して30
%〜40%の乾材が必要となっている。そして処理槽に
対する有機質廃棄物の投入と取出しは24時間から48
時間の間隔で繰り返されている。また、処理槽から取り
出した被処理物は、十分熟成していないために取り出し
後に直ちに肥料として使うことが出来ず、二次醗酵して
から使うために長い時間と手間を要し、より速く醗酵処
理を可能にするには処理方法や処理装置に改善の必要が
あった。この発明の目的は、有機質廃棄物を連続して、
少ない手間で迅速に処理できるようにすることにある。
With this batch method, organic waste having a high water content (water content of 85% for garbage is obtained).
In order to carry out fermentation treatment, the dry matter (sawdust etc.) must be added together to make the water content of the treated material 50% to 60%.
Fermentation process is performed after lowering the water content to about%. This is because when the water content is high, the action of microorganisms is bad. The amount of dry material to be added is 30 for the material to be processed.
% -40% dry material is required. And the input and removal of organic waste from the treatment tank is from 24 hours to 48 hours.
It is repeated at intervals of time. In addition, the object to be treated taken out of the treatment tank cannot be used as a fertilizer immediately after taking it out because it is not matured sufficiently, it takes a long time and labor to use it after the secondary fermentation, and the fermentation is faster. It was necessary to improve the processing method and the processing equipment to enable the processing. The object of the present invention is to continuously treat organic waste,
It is to be able to process quickly with little effort.

【0004】[0004]

【課題を解決するための手段】この発明の処理方法の第
1の特徴は、有機質廃棄物を廃棄物醗酵処理槽内の複数
の処理室で加熱しながら回転攪拌移送手段の攪拌体で攪
拌し、攪拌体を正転と逆転を繰り返することにより、前
段の処理室から隣接している後段の処理室への移送と、
後段の処理室から隣接している前段の処理室へ後送(逆
送)とを行いながら処理し、醗酵処理された有機質廃棄
物が廃棄物醗酵処理槽外へ排出可能とするものである。
この発明の処理方法の第2の特徴は、前段処理室、少な
くとも3室を有する中段処理室及び後段処理室を備えて
いる廃棄物醗酵処理槽内で有機質廃棄物を加熱しながら
回転攪拌移送手段で攪拌し、上記前段処理室から後段処
理室まで移動させて処理する方法であり、上記有機質廃
棄物の移動工程では隣接する各中段処理室間で、隣接す
る中段処理室及び後段処理室間でそれぞれ上記有機質廃
棄物の移送と後送とが行われるものであり、上記各処理
室内の有機質廃棄物の移送と後送とは、上記回転攪拌移
送手段の攪拌体による正転と逆転とを通じて行われるも
のである。上記有機質廃棄物の移動方法として、前段処
理室からこの前段処理室に隣接している中段処理室への
移送はオーバーフローによるものであり、隣接している
中段処理室相互間、後段処理室とこれに隣接している中
段処理室相互間における有機質廃棄物の移送と後送と
、上記処理室を仕切る仕切壁に開けられている移行用
開口部である複数の通孔を通じて徐々に行われるもので
ある。上記各中間処理室内及び後段処理室内へ流入する
有機質廃棄物の量が室外へ流出する量よ りも大きいとき
は、上記中間処理室相互間、後段処理室とこれに隣接し
ている中間処理室相互間を仕切る各仕切壁の上部にそれ
ぞれ開けられているオーバーフロー移行用の開口部を通
じて処理室内の有機質廃棄物が隣接する処理室へ移動す
るものである。この発明の処理方法の第3の特徴は、前
段処理室である第1処理室、少なくとも3室からなる中
段処理室である第2処理室、第3処理室及び第4処理室
と、後段処理室である第5処理室とを備えている廃棄物
醗酵処理槽内の有機質廃棄物を加熱しかつ回転攪拌移送
手段によって攪拌しながら、上記第1処理室から第5処
理室まで移動させて処理する方法であり、上記有機質廃
棄物の移動工程では、上記第2処理室と第3処理室相互
間、第3処理室と第4処理室相互間、第4処理室と第5
処理室相互間でそれぞれ移送と後送とが上記回転攪拌移
送手段の攪拌体による正転と逆転とを通じて行われるも
のである。第1処理室内の有機質廃棄物の移動方法とし
ては、第2処理室へオーバーフローにより移送されるも
のであり、第2及び第3処理室相互間、第3及び第4処
理室相互間、第4処理室と第5処理室相互間における有
機質廃棄物の移送と後送とは、処理室を仕切る仕切壁に
開けられている移行用開口部である複数の通孔を通じて
行われるものである。この発明の処理装置の第4の特徴
は、廃棄物醗酵処理槽、加熱手段及び回転攪拌移送手段
を備えており、上記廃棄物醗酵処理槽は、その内部がそ
の長さ方向に仕切壁によって前段処理室と、複数の中段
処理室と、後段処理室とに連続状態に仕切られていると
共に、上記前段処理室及びこれに隣接している中段処理
室間、中段処理室相互間、後段処理室及びこれに隣接し
ている中段処理室間がそれぞれ互いに移行用開口部を介
して連通されており、上記中段処理室相互間、後段処理
室及びこれに隣接している中段処理室間がそれぞれ互い
にオーバーフロー移行用の開口部を介して連通されてお
り、上記前段処理槽は、有機質廃棄物の投入口を備えて
おり、上記各中段処理室間は仕切壁によって連続状態に
仕切られており、上記移行用開口部は各仕切壁に設けら
れており、上記回転攪拌移送手段は、前段処理室から後
段処理室に至る各処理室内を貫通している単一軸または
複数軸からなる回転軸と、この回転軸に取付けられ、上
記各処理室内の上記有機質廃棄物を攪拌すると共に、前
段処理室から後段処理室まで上記有機質廃棄物を攪拌す
るための攪拌体とを備えており、上記加熱手段は、各処
理室内の上記有機質廃棄物を加熱するものである。上記
移行用開口部の構成として、各移行用開口部のうち、
上記前段処理室とこれに隣接している中段処理室とを仕
切る仕切壁に設けられている移行用開口部として、例え
ば上記仕切壁の上部を切欠いたものであり、隣接してい
る中段処理室間、互いに隣接している中段処理室と後段
処理室間をそれぞれ仕切る各仕切壁に設けられている
移行用開口部として、例えば仕切壁に厚み方向に貫通
状態に開けた複数の通孔からなるものが選択される。
記各オーバーフロー移行用の開口部は、上記中段処理室
相互間、後段処理室及びこれに隣接している中段処理室
間をそれぞれ仕切る各仕切壁の上部に設けられ、上記他
の各移行用開口部の位置より高い位置に配置されてい
る。廃棄物醗酵処理槽は、有機質廃棄物の醗酵から熟
成、完熟及び乾燥を考慮すると、少なくとも第1、第
2、第3、第4及び第5処理室を備え、第1処理室は有
機質廃棄物の投入口を備えている前段処理室、第2、第
3及び第4処理室は中段処理室、第5処理室は最終処理
を行う後段処理室であることが望ましい。この発明にお
いて、処理の対象となる有機質廃棄物には、上述した食
品加工工場、スーパーマーケット、レストラン、家庭な
どから出る水分を含むごみの他に、業務用廃棄物食品工
場から出る食品残渣水処理後の汚泥、公共団体等の終末
処理場汚泥、畜産糞、鶏糞、木材工場から出る樹皮など
水分を含有する廃棄物が含まれる。
The first feature of the treatment method of the present invention is to stir the organic waste with the stirrer of the rotary stirring transfer means while heating the organic waste in a plurality of treatment chambers in the waste fermentation treatment tank. By repeating the forward rotation and the reverse rotation of the stirring body, the transfer from the processing chamber in the previous stage to the processing chamber in the next stage adjacent to the processing chamber,
The organic waste that has been subjected to fermentation processing can be discharged to the outside of the waste fermentation processing tank while performing processing while performing post-feeding (back-feeding) from the subsequent processing chamber to the adjacent preceding processing chamber.
The second aspect of the processing method of the present invention, the pretreatment chamber, small
While heating organic waste in a waste fermentation treatment tank equipped with at least three middle-stage treatment chambers and a second-stage treatment chamber
It is a method of stirring by a rotary stirring transfer means and moving it from the pre-treatment chamber to the post-treatment chamber for treatment.In the moving step of the organic waste, the adjacent middle treatment chambers and the rear treatment chambers are adjacent to each other. each between processing chambers all SANYO that the Koso and transport of the organic waste is performed, transfer the upper Symbol organic waste of the processing chamber and Koso, according agitation of the rotation stirred transport means It is performed through normal rotation and reverse rotation . As a method of moving the above-mentioned organic matter waste, pre-stage processing
Transfer to middle treatment chamber adjacent the physical chamber to the pretreatment chamber is due to overflow, between middle processing chamber mutual adjacent, in that adjacent thereto and post-processing chamber
The Koso the transfer of organic waste in interstage processing chamber cross, but gradually performed through multiple holes are transition opening which is opened in the partition wall for partitioning the upper Symbol processing chamber. Flows into each of the above intermediate processing chambers and post-processing chambers
When the amount of organic waste is also large Ri by the amount flowing out to the outdoor
Between the above-mentioned intermediate processing chambers,
It is located at the top of each partition wall that separates the intermediate processing chambers from each other.
Overflow openings are provided in each
Then, the organic waste in the treatment room moves to the adjacent treatment room.
It is something. The third feature of the processing method of the present invention is that the first processing chamber is a front processing chamber, the second processing chamber is a middle processing chamber including at least three chambers, the third processing chamber and the fourth processing chamber, and the second processing is And a fifth treatment chamber, which is a chamber, while heating the organic waste in the waste fermentation treatment tank and stirring it by a rotary stirring transfer means while moving it from the first treatment chamber to the fifth treatment chamber for treatment. In the step of moving the organic waste, the second treatment chamber and the third treatment chamber, the third treatment chamber and the fourth treatment chamber, the fourth treatment chamber, and the fifth treatment chamber in the moving step of the organic waste.
The transfer and the post-transfer between the processing chambers are respectively performed through the forward rotation and the reverse rotation by the stirring member of the rotary stirring transfer means. The method of moving the first processing organic waste chamber, which is transferred by the second processing chamber to overflow, the second and third treatment chamber therebetween, the third and fourth processing chamber therebetween, the 4 the transferred Koso of organic waste in the processing chamber and the fifth treatment chamber therebetween, are intended to be carried out through a plurality of holes is a transition opening which is opened in the partition wall for partitioning the processing chamber . A fourth characteristic of the treatment apparatus of the present invention is provided with a waste fermentation treatment tank, a heating means, and a rotary stirring transfer means, and the inside of the waste fermentation treatment tank is provided with a partition wall in the lengthwise direction. A processing chamber, a plurality of middle processing chambers, and a rear processing chamber are continuously partitioned, and the front processing chamber and the adjacent middle processing chambers, the middle processing chambers, and the rear processing chambers are adjacent to each other. and communicate with each other through a stepped process chamber between each transition openings from one another in that adjacent to this, the middle processing chamber therebetween, postprocessing
The chamber and the adjacent middle processing chambers are
To the overflow transfer opening.
The pretreatment tank is provided with an inlet for the organic waste, the middle treatment chambers are continuously partitioned by partition walls, and the transfer opening is provided in each partition wall. The rotary stirring and transporting means is provided on the rotary shaft, which comprises a single shaft or a plurality of shafts penetrating each processing chamber from the pre-processing chamber to the post-processing chamber, and is attached to this rotary shaft. The organic waste in the processing chamber is agitated, and a stirrer for agitating the organic waste from the pre-treatment chamber to the post-treatment chamber is provided, and the heating means includes the organic waste in each treatment chamber. Is to heat. the above
As the configuration of each transition opening, among each transition opening,
As a transfer opening provided in a partition wall for partitioning the front-stage processing chamber and a middle-stage processing chamber adjacent thereto, for example, the upper part of the partition wall is cut out, and the middle-stage processing chamber is adjacent. In addition, it is provided on each partition wall that separates the middle processing chamber and the second processing chamber that are adjacent to each other.
The transition opening is selected from, for example, a plurality of through holes formed in the partition wall in a through state in the thickness direction. Up
The openings for each overflow transfer are the above-mentioned middle processing chamber.
Between each other, the post-stage processing chamber and the adjacent mid-stage processing chamber
It is provided on the upper part of each partition wall that separates each space.
Located higher than the position of each transition opening in
It The waste fermentation treatment tank is provided with at least the first, second, third, fourth and fifth treatment chambers in consideration of fermentation, fermentation, maturation and drying of the organic waste, and the first treatment chamber has organic waste. It is desirable that the front-stage processing chamber, the second, third and fourth processing chambers provided with the above-mentioned inlets are the middle-stage processing chambers, and the fifth processing chamber is the latter-stage processing chamber for performing the final processing. In the present invention, the organic waste to be treated includes, in addition to the above-mentioned waste containing moisture from food processing plants, supermarkets, restaurants, households, etc. Includes water-containing waste such as sludge in Japan, end-of-life sludge from public organizations, livestock manure, chicken manure, and bark from wood factories.

【0005】[0005]

【作用】有機質廃棄物は、廃棄物醗酵処理槽内で加熱し
ながら攪拌され、上記複数の処理室間を移送と後送とが
繰り返されることにより、制限された処理スペースと時
間内で長い攪拌時間、醗酵時間及び移動距離が確保さ
れ、含有する水分が十分除去された状態で醗酵処理が可
能となる。
[Function] Organic waste is agitated while being heated in a waste fermentation treatment tank, and by repeating transfer and post-transfer between the plurality of treatment chambers, a long agitation is performed within a limited treatment space and time. The fermentation process can be performed in a state where the time, the fermentation time and the moving distance are secured and the water content is sufficiently removed.

【0006】[0006]

【発明の実施の形態】まず、この発明に係わる有機質廃
棄物の処理方法に使用する図1乃至図6に示す処理装置
について説明する。処理装置は、廃棄物醗酵処理槽1、
加熱手段2及び回転攪拌移送手段3を備えているもので
ある。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS First, the processing apparatus shown in FIGS. 1 to 6 used in the method for processing organic waste according to the present invention will be described. The processing equipment is a waste fermentation processing tank 1,
The heating means 2 and the rotary stirring transfer means 3 are provided.

【0007】廃棄物醗酵処理槽1について説明する。廃
棄物醗酵処理槽1は支持フレーム4内に設置されてお
り、その内部はその長さ方向(図1左右方向)に4枚の
仕切壁5a,5b,5c,5dによって、5つの処理室
6〜10に仕切られている。廃棄物醗酵処理槽1におけ
る処理室に関して、図1左側から右側に向けて第1、第
2、第3、第4及び第5の各処理室6,7,8,9,1
0が順次配置されている。第1処理室6は前段処理室、
第2、第3及び第4の処理室7,8,9は中段処理室、
第5処理室10は後段処理室である。図1の例では、第
1処理室6は初期処理室、第2、第3及び第4の各処理
室7,8,9は中間処理室、第5処理室10は最終処理
室の役割を有している。第1処理室6では投入された有
機質廃棄物が破砕され、水分調整による減量が行われ
る。第2処理室7では第1処理室6と同様の役割を有す
る他に、室内に供給される菌体(バクテリア)によって
醗酵処理が行われる。第3、第4及び第5の各処理室8
〜10では、第1及び第2の処理室6,7で粒状または
粉末状に処理された有機質廃棄物に対する醗酵処理が主
に行われる。仕切壁5a〜5dに関して説明する。第1
と第2の処理室6,7との間を仕切る仕切壁5aには移
送用開口部5a1が設けられており、移送用開口部5a
1は図1及び図2の例では仕切壁5aの上部を切欠くこ
とによって設けられている。また図3に示すように第2
と第3の処理室7,8との間を仕切る仕切壁5bには、
移送用開口部5b1が設けられており、移送用開口部は
図示の例では仕切壁を厚み方向に貫通して設けられた複
数の通孔で構成されている。さらに図4乃至図5に示す
ように第3と第4の処理室8,9との間を仕切る仕切壁
5c、第4と第5の処理室9,10との間を仕切る仕切
壁5dにも移送用開口部5b1と同様の移送用開口部5
c1,5d1がそれぞれ設けられている。第1及び第2
の処理室6,7、第2及び第3の処理室7,8、第3及
び第4の処理室8,9、第4及び第5の処理室9,10
がそれぞれ互いに移行用開口部5a1〜5d1を介して
連通されており、各移行用開口部が第1から第5の処理
室までの被処理用有機質廃棄物の通路となっている。ま
た図1に示すように、仕切壁5b〜5dの上部にも、仕
切壁5aの上部に設けてあるオーバーフロー用の移送用
開口部5a1と同様の移送用開口部5b2,5c2,5
d2が設けられている。移送用開口部5b2,5c2,
5d2は、必要に応じて移送用開口部5a1と併せて第
1から第5の処理室までの被処理用有機質廃棄物の通路
としての機能を持つ。第1処理室6は、図1及び図2に
示すように上部にホッパ状の有機質廃棄物の投入口11
を備えており、この投入口から有機質廃棄物が処理室6
内に投入される。投入口11の開口は蓋(図示せず。)
により開閉可能である。第5処理室10は、醗酵処理を
終えた有機質廃棄物を廃棄物醗酵処理槽1外に排出する
排出口12を備えている(図6)。排出口12には、図
1に示すように右下りに傾斜された排出管13の一端が
接続されている。第1乃至第5の処理室6〜10の上部
には、図1に示すように処理中の有機質廃棄物から排出
される蒸気及び臭気を処理室外へ排出するための排気室
14が設けられている。排気室14には、第2処理室
7、第3処理室8及び第5処理室10の側部側にそれぞ
れ対応して配管されている排気管15a,15b,15
cの一端が接続されている。各排気管15a〜15cの
他端は一個所に集められて、排気口部16に通じてい
る。各排気管15a〜15c内の排気はファン17によ
って排気口部16に吸引される。
The waste fermentation treatment tank 1 will be described. The waste fermentation processing tank 1 is installed in a support frame 4, and the inside thereof is divided into five processing chambers 6 by four partition walls 5a, 5b, 5c, 5d in the length direction (left and right direction in FIG. 1). It is divided into 10 parts. Regarding the treatment chambers in the waste fermentation treatment tank 1, the first, second, third, fourth, and fifth treatment chambers 6, 7, 8, 9, 1 from the left side to the right side in FIG.
0s are sequentially arranged. The first processing chamber 6 is the former processing chamber,
The second, third and fourth processing chambers 7, 8 and 9 are middle processing chambers,
The fifth processing chamber 10 is a post-processing chamber. In the example of FIG. 1, the first processing chamber 6 serves as an initial processing chamber, the second, third and fourth processing chambers 7, 8 and 9 serve as intermediate processing chambers, and the fifth processing chamber 10 serves as a final processing chamber. Have In the first processing chamber 6, the input organic waste is crushed and the water content is reduced by adjusting the water content. In addition to having the same role as the first processing chamber 6, the second processing chamber 7 also performs fermentation processing by the bacterial cells (bacteria) supplied in the room. Third, fourth and fifth processing chambers 8
In Nos. 10 to 10, fermentation treatment is mainly performed on the organic waste treated in the first and second treatment chambers 6 and 7 in a granular or powder form. The partition walls 5a to 5d will be described. First
A transfer opening 5a1 is provided in the partition wall 5a that separates the transfer opening 5a from the second processing chambers 6 and 7.
1 is provided by notching the upper part of the partition wall 5a in the example of FIGS. Also, as shown in FIG.
The partition wall 5b for partitioning between the third processing chambers 7 and 8 is
The transfer opening 5b1 is provided, and the transfer opening is constituted by a plurality of through holes provided in the illustrated example so as to penetrate the partition wall in the thickness direction. Further, as shown in FIGS. 4 to 5, a partition wall 5c for partitioning between the third and fourth processing chambers 8 and 9 and a partition wall 5d for partitioning between the fourth and fifth processing chambers 9 and 10 are provided. Is the same as the transfer opening 5b1.
c1 and 5d1 are provided respectively. First and second
Processing chambers 6, 7, second and third processing chambers 7, 8, third and fourth processing chambers 8, 9, fourth and fifth processing chambers 9, 10
Are communicated with each other through the transfer openings 5a1 to 5d1, and each transfer opening serves as a passage for the organic waste to be processed from the first to the fifth processing chambers. Further, as shown in FIG. 1, transfer openings 5b2, 5c2, 5 similar to the overflow transfer opening 5a1 provided at the upper part of the partition wall 5a are also provided above the partition walls 5b to 5d.
d2 is provided. Transfer openings 5b2, 5c2
5d2 has a function as a passage for the organic waste to be processed from the first to the fifth processing chambers, together with the transfer opening 5a1 if necessary. As shown in FIGS. 1 and 2, the first processing chamber 6 has a hopper-shaped inlet 11 for the organic waste at the top.
It is equipped with and the organic waste is discharged from the input port to the treatment room 6
It is thrown in. The opening of the charging port 11 is a lid (not shown).
Can be opened and closed by. The fifth treatment chamber 10 is provided with an outlet 12 for discharging the organic waste that has undergone the fermentation treatment to the outside of the waste fermentation treatment tank 1 (FIG. 6). As shown in FIG. 1, one end of a discharge pipe 13 that is inclined downward to the right is connected to the discharge port 12. As shown in FIG. 1, an exhaust chamber 14 is provided above the first to fifth processing chambers 6 to 10 for discharging steam and odor emitted from the organic waste being processed to the outside of the processing chamber. There is. In the exhaust chamber 14, exhaust pipes 15a, 15b, 15 are provided which are arranged so as to correspond to the side portions of the second processing chamber 7, the third processing chamber 8 and the fifth processing chamber 10, respectively.
One end of c is connected. The other ends of the exhaust pipes 15a to 15c are collected in one place and communicate with the exhaust port portion 16. The exhaust gas in each of the exhaust pipes 15a to 15c is sucked into the exhaust port portion 16 by the fan 17.

【0008】加熱手段2について説明する。加熱手段2
は図1乃至図6に示すように、各第1から第5の処理室
6〜10の外側に設けられており、図示の例では角筒内
に電線を配線したヒーター18で構成されている(図2
参照)。ヒーター18は、第1乃至第5の処理室6〜1
0の外側でこれらを囲むように設けられている。このた
めに各ヒーター18から生じる熱は、各処理室6〜10
内で処理される有機質廃棄物に対してこれらを囲む方向
から均等に加熱可能となって、室内の有機質廃棄物の乾
燥とバクテリア増殖の促進とが図られる。図1及び図2
に示す第1から第5までの各処理室6〜10の外周側面
(図2左右側面)並びに第1処理室6の外周前面(図1
左側面)及び第5処理室10の外周前面(図1右側面)
は保温材19a,19bで被覆されており、処理室内の
加熱状態を維持するようにしている。ヒーター18は各
第1から第5の処理室6〜10の外側面と保温材19a
との間に配置されている。なお、加熱手段の構成はこの
例に限られない。
The heating means 2 will be described. Heating means 2
As shown in FIGS. 1 to 6, is provided outside each of the first to fifth processing chambers 6 to 10. In the illustrated example, the heater is formed by a heater 18 in which electric wires are wired in a rectangular tube. (Fig. 2
reference). The heater 18 includes the first to fifth processing chambers 6 to 1
It is provided so as to surround these outside 0. For this reason, the heat generated from each heater 18 is applied to each processing chamber 6-10.
The organic wastes to be treated inside can be heated evenly from the direction surrounding them, and drying of the organic wastes in the room and promotion of bacterial growth can be achieved. 1 and 2
1 to 5, the outer peripheral side surfaces of the first to fifth processing chambers 6 to 10 (left and right side surfaces in FIG. 2) and the outer peripheral front surface of the first processing chamber 6 (see FIG. 1).
(Left side surface) and the outer peripheral front surface of the fifth processing chamber 10 (right side surface in FIG. 1)
Is covered with heat insulating materials 19a and 19b so as to maintain the heating state in the processing chamber. The heater 18 is a heat insulating material 19a and the outer surface of each of the first to fifth processing chambers 6 to 10.
It is located between and. The configuration of the heating means is not limited to this example.

【0009】回転拌移送手段3について説明する。回
拌移送手段3は、図1及び図2に示すように、第1
乃至第5の処理室6〜10内を貫通している回転軸2
0,21と、これらの回転軸の周囲から起立している複
数の拌体22,23,24,25,26と、各回転軸
を回転させる駆動モータ27,28と、例えばチェーン
29,30とスプロケット31,32とを備えている駆
動力伝達手段とで構成されている(図1)。各拌体2
2〜26は、各第1から第5の処理室6〜10に収納し
た有機質廃棄物を拌しながら、図1左方から右方へ移
送したり、反対に右方から左方へ後送したりする機能を
持つものである。回転軸の構成に関して、図1の例では
回転軸は2分割され、一方(左方)の回転軸20は第1
処理室6から第2処理室7内を貫通し、他方(右方)の
回転軸21は第3処理室8から第5処理室10内を貫通
している。一方の回転軸20は、その両側が第1処理室
6の側板に取付けられている座板33と仕切壁5bに取
付けられている軸受34とによって回転可能に軸受けさ
れている。回転軸20の一端側(図1左端側)は第1処
理室6外へ伸ばされて、端部にスプロケット31が取付
けられている。回転軸20にはチェーン29及びスプロ
ケット31を通じて駆動モータ27の駆動力が伝達され
る。回転軸20の最先端部は受台35に軸受けされてい
る。他方の回転軸21はその両側が仕切壁5bに取付け
られている軸受34と第5処理室10の側板に取付けら
れている座板36とによって回転可能に軸受けされてい
る。回転軸21の一端側(図1右端側)は第5処理室1
0外へ伸ばされて、端部にスプロケット32が取付けら
れている。回転軸21にはチェーン30及びスプロケッ
ト32を通じて駆動モータ28の駆動力が伝達される。
回転軸21の最先端部は受台37に軸受けされている。
拌体22〜26は、図1及び図2の例によれば、第
1処理室6乃至第5処理室10内の回転軸20,21に
取付けられている。各攪拌体22〜26の先端部に攪拌
パドル22a,23a,24a,25a,26aが設け
られている。攪拌パドル22a〜26aは攪拌体22〜
26に対して回転方向に所定角度傾けて取付けられてい
る。攪拌パドル22aは、図2では矢印方向(時計方
向)を上向きにして、所定角度(例えば45度)傾斜さ
せて取付けられている(図3)。攪拌パドル23aも攪
拌パドル22aと同様な状態で取付けられている。また
攪拌パドル24aは、図4では矢印方向(時計方向)を
上向きにして、所定角度(例えば60度)傾斜させて取
付けられている。攪拌パドル25a,26aも攪拌パド
ル24aと同様な状態で取付けられている(図5,図
6)。攪拌パドル22a〜26aが上記のように攪拌体
22〜26に取付けられているので、後述するように正
転(例えば図2時計方向の回転)により第1乃至第5の
処理室6〜10内の有機質廃棄物を隣接する処理室に移
送可能となり、また逆転により第3乃至第5の処理室8
〜10内の有機質廃棄物を隣接する処理室へ後送(逆
送)することができる。図1に示すように、第1処理室
6及び第2処理室7内の各攪拌体22,23の本数はそ
れぞれ5本、第3処理室8内の各攪拌体24の本数は4
本、第4処理室9及び第5処理室10内の各攪拌体2
5,26の本数はそれぞれ3本であるが、その本数は上
例に限定されない。攪拌体の形状や本数は、処理室の処
理容積、処理能力及び処理する有機質廃棄物の種類など
に応じて適宜選択される。駆動モータ27,28は正逆
回転可能である。このために駆動モータ27,28の双
方をそれぞれ駆動させて、回転軸20,21の双方を同
時に正転(例えば図2乃至図6時計方向)に、また逆転
(反時計方向)にさせることができる。回転軸20,2
1の双方を同時に正転させると、攪拌体22〜26は各
第1乃至第5の処理室6〜10内の有機質廃棄物を、順
次前段の処理室から後段の処理室へ移送用開口部5a1
〜5d1を通じて移送可能にする。図1の例では、回転
軸20,21の正転により、有機質廃棄物は、第1処理
室6から第2処理室7へ、第2処理室7から第3処理室
8へ、第3処理室8から第4処理室9、第4処理室9か
ら第5処理室10へ移送される。また回転軸21を逆転
させることにより、攪拌体24〜26は各第3乃至第5
の処理室8〜10内の有機質廃棄物を、順次後段の処理
室から前段の処理室へ通孔からなる移送用開口部5b
1,5c1,5d1を通じて後送可能となる。図1の例
では、回転軸21の逆転により、第3処理室8から第2
処理室7へ、第4処理室9から第3処理室8へ、第5処
理室10から第4処理室9へそれぞれ後送可能である。
[0009] describes rotation 拌移feeding means 3. Rotation 拌移feed means 3, as shown in FIGS. 1 and 2, the first
To the rotary shaft 2 penetrating the inside of the fifth processing chambers 6 to 10.
And 0,21, a plurality of 拌体22,23,24,25,26 are erected from the periphery of the rotating shaft, a drive motor 27, 28 for rotating the rotary shafts, for example the chain 29, 30 And driving force transmission means including sprocket 31, 32 (FIG. 1). Each 拌体2
2-26, the rear of the organic waste from the first housed in the fifth treatment chamber 6 to 10 with 拌, or transported to the right in FIG. 1 the left, to the left from the right side to the opposite It has a function of sending. Regarding the configuration of the rotary shaft, in the example of FIG. 1, the rotary shaft is divided into two, and one (left side) rotary shaft 20 is the first.
The processing chamber 6 penetrates the inside of the second processing chamber 7, and the rotating shaft 21 on the other side (the right side) penetrates the inside of the third processing chamber 8 through the fifth processing chamber 10. One side of the rotary shaft 20 is rotatably supported by a seat plate 33 attached to the side plate of the first processing chamber 6 and a bearing 34 attached to the partition wall 5b on both sides. One end side (the left end side in FIG. 1) of the rotary shaft 20 is extended to the outside of the first processing chamber 6, and a sprocket 31 is attached to the end portion. The driving force of the drive motor 27 is transmitted to the rotary shaft 20 through the chain 29 and the sprocket 31. The tip of the rotary shaft 20 is supported by the pedestal 35. The other rotary shaft 21 is rotatably supported on both sides by a bearing 34 mounted on the partition wall 5b and a seat plate 36 mounted on a side plate of the fifth processing chamber 10. One end side (the right end side in FIG. 1) of the rotating shaft 21 is the fifth processing chamber 1.
It is extended to the outside of 0 and the sprocket 32 is attached to the end. The driving force of the drive motor 28 is transmitted to the rotary shaft 21 through the chain 30 and the sprocket 32.
The tip of the rotary shaft 21 is supported by the pedestal 37.
Each 拌体22-26, according to the example of FIGS. 1 and 2, is attached to the first processing chamber 6 through the rotation axis 20, 21 of the fifth process chamber 10. Stirring paddles 22a, 23a, 24a, 25a, and 26a are provided at the tips of the stirring bodies 22 to 26, respectively. The stirring paddles 22a to 26a are the stirring members 22 to
It is attached so as to be inclined at a predetermined angle with respect to the rotation direction 26. The stirring paddle 22a is attached with the arrow direction (clockwise direction) facing upward in FIG. 2 and inclined at a predetermined angle (for example, 45 degrees) (FIG. 3). The stirring paddle 23a is also attached in the same state as the stirring paddle 22a. Further, the stirring paddle 24a is attached with the arrow direction (clockwise direction) facing upward in FIG. 4 and inclined at a predetermined angle (for example, 60 degrees). The stirring paddles 25a and 26a are also attached in the same state as the stirring paddle 24a (FIGS. 5 and 6). Since the stirring paddles 22a to 26a are attached to the stirring bodies 22 to 26 as described above, the insides of the first to fifth processing chambers 6 to 10 are rotated by forward rotation (for example, clockwise rotation in FIG. 2) as described later. Of the organic waste can be transferred to the adjacent processing chamber, and the third to fifth processing chambers 8 can be reversed by reversing.
The organic waste in 10 to 10 can be post-transferred (back-sent) to the adjacent processing chamber. As shown in FIG. 1, the number of the stirring bodies 22 and 23 in the first processing chamber 6 and the second processing chamber 7 is 5, and the number of the stirring bodies 24 in the third processing chamber 8 is 4 respectively.
Each stirring body 2 in the book, the fourth processing chamber 9 and the fifth processing chamber 10
The numbers of 5 and 26 are three, respectively, but the number is not limited to the above example. The shape and the number of the stirring bodies are appropriately selected according to the processing volume of the processing chamber, the processing capacity, the type of organic waste to be processed, and the like. The drive motors 27 and 28 can rotate in the forward and reverse directions. For this purpose, both the drive motors 27 and 28 can be driven to simultaneously rotate both the rotary shafts 20 and 21 in the forward direction (for example, clockwise direction in FIGS. 2 to 6) and in the reverse direction (counterclockwise direction). it can. Rotating shaft 20,2
When both of them are rotated in the normal direction at the same time, the stirring members 22 to 26 sequentially open the organic wastes in the first to fifth processing chambers 6 to 10 from the first processing chamber to the second processing chamber. 5a1
~ Transmit through 5d1. In the example of FIG. 1, the organic waste is transferred from the first processing chamber 6 to the second processing chamber 7, the second processing chamber 7 to the third processing chamber 8, and the third processing by the forward rotation of the rotating shafts 20 and 21. Transferred from the chamber 8 to the fourth processing chamber 9 and from the fourth processing chamber 9 to the fifth processing chamber 10. Further, by rotating the rotating shaft 21 in the reverse direction, the agitating members 24 to 26 are set to the third to fifth parts.
Of the organic waste in the processing chambers 8 to 10 from the processing chamber in the subsequent stage to the processing chamber in the preceding stage, which is a transfer opening 5b formed of a through hole.
Post-delivery is possible through 1, 5c1 and 5d1. In the example of FIG. 1, the rotation of the rotary shaft 21 causes the third processing chamber 8 to move to the second
It is possible to post-transfer to the processing chamber 7, the fourth processing chamber 9 to the third processing chamber 8, and the fifth processing chamber 10 to the fourth processing chamber 9.

【0010】次に、本装置を用いて有機質廃棄物を醗酵
処理する方法について説明する。有機質廃棄物の醗酵処
理は、回転軸20,21の攪拌体22〜26を使用して
第1乃至第5の処理室6〜10内の有機質廃棄物を移動
させることによって行われる。有機質廃棄物の移動工程
には移送工程と後送工程が含まれる。移送工程時には、
双方の回転軸20,21は図7(A)矢印に示すように
同時に同一方向に回転(正転)され、攪拌体22〜26
もすべて正転される。有機質廃棄物は、攪拌体22〜2
6の正転によって、図7(A)左側から右側方向に換言
すれば、前段の処理室から後段の処理室へ移送される。
後送工程時には、双方の回転軸20,21は図7(B)
矢印に示すように同時に逆転され、攪拌体22〜26も
すべて逆転される。有機質廃棄物は、攪拌体22〜26
の逆転によって、図7(B)右側から左側方向に換言す
れば、後段の処理室から前段の処理室へ後送(逆方向に
移動)される。ただし、第2処理室7から第1処理室6
への後送は、仕切壁5aの存在により行われない。この
発明の処理方法では、両回転軸20,21を同時に同一
方向の回転とその反対方向の回転すなわち正転と逆転と
を繰り返し、攪拌体22〜26を通じて有機質廃棄物の
移送と後送(前進と後退)を行い、有機質廃棄物が第2
処理室7から第5処理室10へ直線的に移動するのでは
なく、移動過程で前段の処理室へ戻る過程を組入れるこ
とによって処理室内における有機質廃棄物の攪拌と移動
時間を長くして醗酵から熟成、完熟及び乾燥を可能とし
て、有機肥料を製造するものである。有機質廃棄物は、
第1処理室6へ投入されてから、第5処理室10から処
理を終えて出るまで、第2処理室7から第5処理室10
までの間を前進と後退が繰り返されながら醗酵処理され
る。ここで、回転軸20,21(攪拌体22〜26)の
動作に伴う有機質廃棄物の処理を説明する。まず、回転
軸20,21の正転過程における処理について説明す
る。回転軸20,21が正転している場合には、攪拌体
22〜26は図2乃至図6矢印方向に回転する。このた
めに、第1処理室6内における有機質廃棄物は、ヒータ
ー18により加熱されながら破砕され、水分調整され
る。有機質廃棄物は、第1処理室6内の処理によって減
量されると共に、細く破砕される。第1処理室6内の有
機質廃棄物は、新たに投入口11から投入された有機質
廃棄物によって第1処理室6内の容積を越えた分量だけ
オーバーフローされて移送用開口部5a1から第2処理
室7内へ移送される。第2処理室7内の有機質廃棄物
は、攪拌体23によって加熱されながら破砕され、水分
調整され、第1処理室6内の処理に比較してより一層減
量されると共に、細く破砕され、醗酵処理される。同時
に、第2処理室7内の有機質廃棄物は拌体23によっ
て仕切壁5bに設けた通孔5b1より第3処理室8へ少
量ずつ移送される。また第3乃至第5の処理室8〜10
内の有機質廃棄物もそれぞれ加熱されながら拌体24
〜26で攪拌されて、さらに水分調整されながら減量さ
れ、醗酵処理され、第3処理室8内の有機質廃棄物は仕
切壁5cに設けた通孔5c1から第4処理室9へ、第4
処理室9内の有機質廃棄物は、仕切壁5dに設けた通孔
5d1から第5処理室10へ、それぞれ少量ずつ移送さ
れる。このように、正転時には、第1乃至第5の処理室
6〜10内では、既に収納されている有機質廃棄物と、
投入された又は隣室から移送されてきた有機質廃棄物と
が攪拌され処理される。つぎに、回転軸20,21の逆
転過程における処理について説明する。回転軸20,2
1が逆転されている場合には、攪拌体22〜26は図2
乃至図6矢印方向とは反対方向に回転する。第1及び第
2の処理室6,7内における有機質廃棄物は、正転時と
同様に、ヒーター18により加熱されながら破砕され、
水分調整されて、減量される。第2処理室7内で醗酵処
理された有機質廃棄物は第1処理室6へ後送されない。
また第3乃至第5の処理室8〜10内における醗酵処理
された有機質廃棄物は、逆転によってそれぞれ前段の処
理室へその一部が戻される(後送される)。すなわち、
第3処理室8内の有機質廃棄物は、通孔5b1から第2
処理室7へ、少量ずつ移送され、同様に第4処理室9内
の有機質廃棄物は、通孔5c1から第3処理室7へ、第
5処理室10内の有機質廃棄物は、通孔5d1から第4
処理室9へ、それぞれ少量ずつ後送される。このよう
に、逆転時には、第1及び第2の処理室6,7では、内
部の有機質廃棄物を正転時と同様に、ヒーター18の加
熱と攪拌体22,23の攪拌とを通じて、水分除去によ
る減量と破砕が行われる。ただし、第2処理室7では、
後段の第3処理室8から逆送された有機質廃棄物を加え
た状態で処理が行われる。また第3乃至第5の処理室8
〜10では、有機質廃棄物を攪拌しながら、その一部を
一側で前段の処理室へ戻し、他側で後段の処理室から流
入した有機質廃棄物も混合処理する。具体例で説明す
る。ヒーター18の加熱により、廃棄物醗酵処理槽1の
第1乃至第5の処理室6〜10内の室温を約60〜70
°C程度に保温しておく。まず、有機質廃棄物の例えば
10tを投入口11から廃棄物醗酵処理槽1の第1処理
室6へ投入する。投入された有機質廃棄物は、第1処理
室6内においてヒーター18により加熱されつつ、
体22の正転と逆転の繰り返しにより破砕され、投入後
24時間経過すると、約1/3が水分調整され、減量さ
れる。投入後24時間経過後、再度上記と同量の有機質
廃棄物を投入口11から第1処理室6へ投入すると、第
1処理室6内の処理容積を越えた分量の有機質廃棄物が
オーバーフローされて仕切壁5aの上部に設けてある移
送用開口部5a1から第2処理室7内へ移送される。第
2処理室7内の有機質廃棄物も第1処理室6内の有機質
廃棄物と同様にヒーター18により加熱されつつ、
体23の正転と逆転の繰り返しにより粒状に破砕され、
水分調整され、減量され、菌体による醗酵処理が行われ
る。第2処理室7内の有機質廃棄物は拌体22の正転
によって通孔5b1より第3処理室8へ少量ずつ移送さ
れる。第3処理室8内の有機質廃棄物も第2処理室7内
の有機質廃棄物と同様にヒーター18により加熱されつ
つ、回転軸21の拌体24の正転と逆転の繰り返しに
より、水分調整され、減量され、さらに醗酵処理が図ら
れる共に、拌体24の正転によって通孔5c1より
第4処理室9へ少量ずつ移送され、逆転によって通孔5
b1より第3処理室8へ少量ずつ後送される。第4乃至
第5の処理室9,10内の有機質廃棄物についても、回
転軸21の拌体24の正転と逆転の繰り返しにより、
水分調整され、減量され、醗酵が一層促進されてより細
粒状または粉末状になると共に、拌体24の正転によ
って通孔5c1より第4処理室9へ少量ずつ移送され、
逆転によって通孔5b1より第3処理室8へ少量ずつ後
送される。処理を終えた第5処理室10内の細粒状また
は粉末状になった醗酵状態にある有機質廃棄物は回転軸
21の拌体24の正転により排出口12から排出され
る。投入から24時間後に、排出量は投入量の1/3に
減量され、含水率も約25%となり、有機質廃棄物の醗
酵から熟成、完熟、乾燥が連続して行うことができ、有
機肥料が生産可能となった。そしてこの有機肥料は、バ
クテリアを含むから、使用時に土壌でバクテリアが有効
な作用をし、有効な肥料となる。加熱されている第2処
理室乃至第5処理室7〜10内の有機質廃棄物は、攪拌
体23〜26の回転により攪拌と移動に伴って、バクテ
リアの醗酵が促進され、しかも正逆回転により長い攪拌
と移動の作業が継続されるために熟成、完熟、乾燥が効
果的に行える。上例では、日量50Kgから30tまで
の有機質廃棄物の醗酵処理が24日周期で連続処理がで
きた。第3乃至第5処理室8〜10内へ流入する有機質
廃棄物の量が流出するものより大きい場合には、仕切壁
5b,5c,5dの上部に設けてあるオーバーフロー移
行用の開口部5b2,5c2,5d2から隣接する処理
室に移行される。各処理室6〜10内の有機質廃棄物か
らの臭気や加熱により生じた水蒸気は排気管15a,1
5b,15cを経て排気口部16へ排出される。
Next, a method of fermenting an organic waste by using this apparatus will be described. The fermentation treatment of the organic waste is performed by moving the organic waste in the first to fifth processing chambers 6 to 10 using the stirring bodies 22 to 26 of the rotating shafts 20 and 21. The transfer process of organic waste includes a transfer process and a post-transfer process. During the transfer process,
Both rotary shafts 20 and 21 are simultaneously rotated in the same direction (normal rotation) as shown by the arrow in FIG.
Are all rotated normally. Organic waste is agitator 22-2
By the normal rotation of 6, in other words, from the left side to the right side in FIG. 7A, the process chamber is transferred from the front process chamber to the rear process chamber.
During the post-delivery process, both rotary shafts 20 and 21 are shown in FIG. 7 (B).
At the same time, the stirring bodies 22 to 26 are all reversed as indicated by the arrow. Stirrers 22-26 for organic waste
7B, in other words, from the right side to the left side in FIG. 7B, in other words, the post-processing chamber is post-transferred (moved in the reverse direction) from the post-processing chamber. However, from the second processing chamber 7 to the first processing chamber 6
The post-delivery to is not performed due to the presence of the partition wall 5a. In the processing method of the present invention, both rotary shafts 20 and 21 are simultaneously rotated in the same direction and rotation in the opposite direction, that is, forward rotation and reverse rotation, to transfer and post-transfer (forward) the organic waste through the stirring members 22 to 26. And organic waste is second.
Rather than moving linearly from the treatment chamber 7 to the fifth treatment chamber 10, by incorporating a process of returning to the previous treatment chamber in the movement process, the stirring and movement time of the organic waste in the treatment chamber can be lengthened and fermentation can be performed. It is an organic fertilizer that can be matured, matured and dried. Organic waste is
From the second processing chamber 7 to the fifth processing chamber 10 until the processing is completed and exits from the fifth processing chamber 10 after being input to the first processing chamber 6.
Fermentation treatment is performed while repeating forward and backward movements up to. Here, the processing of the organic waste accompanying the operation of the rotary shafts 20 and 21 (stirring bodies 22 to 26) will be described. First, the process in the forward rotation process of the rotary shafts 20 and 21 will be described. When the rotating shafts 20 and 21 are rotating in the normal direction, the stirring bodies 22 to 26 rotate in the directions of the arrows in FIGS. Therefore, the organic waste in the first processing chamber 6 is crushed while being heated by the heater 18, and the water content is adjusted. The organic waste is reduced in amount by the treatment in the first treatment chamber 6 and is crushed into fine pieces. The organic waste in the first processing chamber 6 is overflowed by the amount of organic waste newly input from the input port 11 in an amount exceeding the volume in the first processing chamber 6, and the second processing is performed from the transfer opening 5a1. Transferred into the chamber 7. The organic waste in the second processing chamber 7 is crushed while being heated by the agitator 23, the water content is adjusted, the amount is further reduced as compared with the processing in the first processing chamber 6, and the organic waste is finely crushed and fermented. It is processed. At the same time, organic waste in the second processing chamber 7 is transferred little by little from the through hole 5b1 formed in the partition wall 5b by 拌体23 into the third process chamber 8. Also, the third to fifth processing chambers 8 to 10
Each while being heated also organic waste inner 拌体24
It is stirred at ~ 26, further reduced in volume while adjusting the water content, and subjected to fermentation treatment, and the organic waste in the third treatment chamber 8 is transferred from the through hole 5c1 provided in the partition wall 5c to the fourth treatment chamber 9 to the fourth treatment chamber 9.
The organic waste in the processing chamber 9 is transferred little by little from the through hole 5d1 provided in the partition wall 5d to the fifth processing chamber 10. Thus, at the time of normal rotation, the organic waste already stored in the first to fifth processing chambers 6 to 10
The organic waste that has been input or transferred from the adjacent chamber is agitated and processed. Next, the process in the reverse rotation process of the rotary shafts 20 and 21 will be described. Rotating shaft 20,2
1 is reversed, the agitators 22-26 are shown in FIG.
6 to 6 rotate in the direction opposite to the arrow direction. The organic waste in the first and second processing chambers 6 and 7 is crushed while being heated by the heater 18 as in the normal rotation,
The water content is adjusted and the weight is reduced. The organic waste that has been fermented in the second processing chamber 7 is not sent to the first processing chamber 6 later.
Further, the fermentation-treated organic wastes in the third to fifth processing chambers 8 to 10 are partially returned (post-sent) to the preceding processing chambers by reversing. That is,
The organic waste in the third processing chamber 8 is discharged from the through hole 5b1 to the second
The organic waste in the fourth processing chamber 9 is transferred from the through hole 5c1 to the third processing chamber 7 and the organic waste in the fifth processing chamber 10 is transferred through the through hole 5d1 in the same manner. To 4th
A small amount of each is sent to the processing chamber 9 later. Thus, in reverse rotation, in the first and second processing chambers 6 and 7, the organic waste inside is removed by heating the heater 18 and stirring the stirring members 22 and 23 as in the normal rotation. Weight loss and crushing are performed. However, in the second processing chamber 7,
The treatment is performed in a state where the organic waste sent back from the third treatment chamber 8 in the latter stage is added. Also, the third to fifth processing chambers 8
In Nos. 10 to 10, while agitating the organic waste, a part of the organic waste is returned to the former treatment chamber on one side, and the organic waste flowing from the latter treatment chamber is mixed on the other side. A specific example will be described. By heating the heater 18, the room temperature in the first to fifth treatment chambers 6 to 10 of the waste fermentation treatment tank 1 is increased to about 60 to 70.
Keep it at about ° C. First, for example, 10 t of organic waste is introduced into the first treatment chamber 6 of the waste fermentation treatment tank 1 through the inlet 11. Introduced organic matter waste, while being heated by the heater 18 in the first treatment chamber 6, disrupted by repeated reverse and forward rotation of 拌体22 to 24 hours after the addition, about one-third water Adjusted and reduced. After the lapse of 24 hours from the charging, when the same amount of the organic waste as above is again charged into the first processing chamber 6 from the charging port 11, the amount of the organic waste exceeding the processing volume in the first processing chamber 6 overflows. And is transferred into the second processing chamber 7 from the transfer opening 5a1 provided in the upper portion of the partition wall 5a. While being heated by the organic waste as well as the heater 18 of the organic waste also within the first process chamber 6 in the second processing chamber 7, it is crushed to a granular by repeated reverse and forward rotation of 拌体23,
The water content is adjusted, the amount is reduced, and the fermentation treatment with bacterial cells is performed. Organic waste in the second processing chamber 7 is transferred in portions to the third process chamber 8 from the through hole 5b1 by the forward rotation of 拌体22. While it is heated by the organic waste as well as the heater 18 in the third processing chamber organic waste also within the second processing chamber 7 in 8, by the repetition of reverse and normal rotation of 拌体24 of the rotary shaft 21, the moisture adjustment It is, is reduced, both the further fermentation process is achieved, is transferred little by little from the through hole 5c1 by the forward rotation of the 拌体24 to fourth processing chamber 9, through-hole 5 by reversing
It is sent to the third processing chamber 8 little by little from b1. For even fourth through organic waste fifth treatment chamber 9, by the repetition of reverse and normal rotation of 拌体24 of the rotary shaft 21,
Is moisture control, is reduced, fermentation can be transported further together is promoted becomes more finely divided or powdered, portionwise than the through hole 5c1 by the forward rotation of the 拌体24 to fourth processing chamber 9,
By the reverse rotation, the toner is sent from the through hole 5b1 to the third processing chamber 8 little by little. Organic wastes in the fermentation condition that the fine granular or powdered fifth treatment chamber 10 which have been processed is discharged from the discharge port 12 by the forward rotation of the 拌体24 of the rotary shaft 21. Twenty-four hours after the input, the discharge amount is reduced to 1/3 of the input amount, the water content is also about 25%, and the fermentation, ripening, and drying of the organic waste can be continuously performed, and the organic fertilizer is Production is now possible. Since this organic fertilizer contains bacteria, the bacteria act effectively in the soil when used, and become an effective fertilizer. The heated organic wastes in the second to fifth processing chambers 7 to 10 are stirred and moved by the rotation of the stirring members 23 to 26, and the fermentation of bacteria is promoted by the rotation of the stirring members 23 to 26. Since the work of long stirring and moving is continued, aging, complete ripening and drying can be effectively performed. In the above example, the fermentation treatment of the organic waste having a daily dose of 50 kg to 30 t could be continuously performed in a 24-day cycle. When the amount of the organic waste flowing into the third to fifth processing chambers 8 to 10 is larger than the amount of the organic waste flowing out, the overflow transfer opening 5b2 provided at the upper portion of the partition walls 5b, 5c, 5d. Transferred from 5c2, 5d2 to the adjacent processing chamber. The odor from the organic waste in each processing chamber 6-10 and the steam generated by heating are exhaust pipes 15a, 1
It is discharged to the exhaust port 16 through 5b and 15c.

【0011】上例では第2乃至第5処理室7〜10を醗
酵処理室としたが、第1処理室6を含めたすべて処理
室を醗酵処理室としてもよい。回転軸の構成は、図1で
は2本からなるものを使用したが、単一であってもよ
い。処理室は5室を設けているが、第2乃至第4室の中
段処理室は増設してもよく、室数は例示のものに限定さ
れない。
In the above example, the second to fifth processing chambers 7 to 10 are fermentation processing chambers, but all the processing chambers including the first processing chamber 6 may be fermentation processing chambers. Although the rotating shaft used in FIG. 1 has two, it may have a single rotating shaft. Although five processing chambers are provided, the middle processing chambers of the second to fourth chambers may be added, and the number of chambers is not limited to the example.

【0012】[0012]

【発明の効果】この発明によれば、有機質廃棄物を加熱
しながら攪拌してかつ移動工程として移送と後送とを含
むので、限られたスペースと時間内で処理室内における
有機質廃棄物の攪拌時間と移動距離を十分確保でき、醗
酵から熟成、完熟及び乾燥が可能となり、この作業を連
続して行うことができ、手間数を従来例に比較して少な
くでき、有機質廃棄物を速やかに処理することができ
る。
According to the present invention, since the organic waste is agitated while being heated and the transfer process and the post-delivery are included as a moving step, the agitation of the organic waste in the processing chamber is performed within a limited space and time. Sufficient time and moving distance can be secured, fermentation, ripening, ripening and drying are possible, this work can be performed continuously, the labor time can be reduced compared with the conventional example, and organic waste can be treated promptly. can do.

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

【図1】この発明の一実施形態を示す処理装置の一部切
欠正面図である。
FIG. 1 is a partially cutaway front view of a processing apparatus showing an embodiment of the present invention.

【図2】図1のII−II線拡大断面図である。FIG. 2 is an enlarged sectional view taken along line II-II of FIG.

【図3】図1のIII−III線拡大断面図である。FIG. 3 is an enlarged sectional view taken along line III-III of FIG.

【図4】図1のIV−IV線拡大断面図である。FIG. 4 is an enlarged sectional view taken along line IV-IV of FIG.

【図5】図1のV−V線拡大断面図である。5 is an enlarged cross-sectional view taken along line VV of FIG.

【図6】図1のVI−VI線拡大断面図である。6 is an enlarged cross-sectional view taken along line VI-VI of FIG.

【図7】有機質廃棄物の移動工程を説明するための構成
図であり、(A)は移送工程を、(B)は後送工程をそ
れぞれ示す図である。
7A and 7B are configuration diagrams for explaining a moving process of organic waste, in which FIG. 7A is a transfer process and FIG. 7B is a post-transfer process.

【符号の説明】[Explanation of symbols]

1 廃棄物醗酵処理槽 2 加熱手段 3 回転攪拌移送手段 5a 仕切壁 5a1 移送用開口部 5b 仕切壁 5b1 移送用開口部 5b2 オーバーフロー移送用の開口部 5c 仕切壁 5c1 移送用開口部 5c2 オーバーフロー移送用の開口部 5d 仕切壁 5d1 移送用開口部 5d2 オーバーフロー移送用の開口部 6 第1処理室(前段処理室) 7 第2処理室(中段処理室) 8 第3処理室(中段処理室) 9 第4処理室(中段処理室) 10 第5処理室(後段処理室) 11 投入口 12 排出口 13 排出管 14 排気室 18 ヒーター 20 回転軸 21 回転軸 22 攪拌体 22a 攪拌パドル 23 攪拌体 23a 攪拌パドル 24 攪拌体 24a 攪拌パドル 25 攪拌体 25a 攪拌パドル 26 攪拌体 26a 攪拌パドル 27 駆動モータ 28 駆動モータ DESCRIPTION OF SYMBOLS 1 Waste fermentation treatment tank 2 Heating means 3 Rotating stirring transfer means 5a Partition wall 5a1 Transfer opening 5b Partition wall 5b1 Transfer opening 5b2 Overflow transfer opening 5c Partition wall 5c1 Transfer opening 5c2 Overflow transfer Opening 5d Partition wall 5d1 Transfer opening 5d2 Overflow transfer opening 6 First processing chamber (pre-processing chamber) 7 Second processing chamber (middle processing chamber) 8 Third processing chamber (middle processing chamber) 9 Fourth Processing chamber (middle processing chamber) 10 Fifth processing chamber (latter processing chamber) 11 Input port 12 Discharge port 13 Discharge pipe 14 Exhaust chamber 18 Heater 20 Rotating shaft 21 Rotating shaft 22 Stirring body 22a Stirring paddle 23 Stirring body 23a Stirring paddle 24 Stirrer 24a Stirrer Paddle 25 Stirrer 25a Stirrer Paddle 26 Stirrer 26a Stirrer Paddle 27 Drive Motor 28 Drive Motor

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 前段処理室と、少なくとも3室に連続し
て仕切られている中段処理室と、後段処理室とが連続状
態に仕切られている廃棄物醗酵処理槽の各処理室内で有
機質廃棄物を加熱しながら回転攪拌移送手段によって攪
拌し、上記前段処理室から後段処理室まで移動させて処
理する方法であって、 上記有機質廃棄物の移動工程では、上記回転攪拌移送手
段の攪拌体による正転と逆転とを通じて、上記中間処理
室相互間、後段処理室とこれに隣接している中間処理室
相互間でそれぞれ移送と後送とが行われるものであり、 上記前段処理室内の有機質廃棄物は、上記前段処理室と
これに隣接している中間処理室とを仕切る仕切壁の上部
に開けられている移行用開口部を介してオーバーフロー
により隣接している上記中間処理室へ移送されるもので
あり、 上記中間処理室相互間、後段処理室とこれに隣接してい
る中間処理室相互間における有機質廃棄物の移送と後送
とは、隣接している両処理室を仕切る各仕切壁にそれぞ
れ開けられている複数の通孔からなる移行用開口部を通
じて行われるものであり、 上記各中間処理室内及び後段処理室内へ流入する有機質
廃棄物の量が室外へ流出する量よりも大きいときは、上
記中間処理室相互間、後段処理室とこれに隣接している
中間処理室相互間を仕切る各仕切壁の上部にそれぞれ開
けられているオーバーフロー移行用の開口部を通じて処
理室内の有機質廃棄物が隣接する処理室へ移動するもの
である ことを特徴とする有機質廃棄物の処理方法。
1. A pretreatment chamber and at least three chambers in succession
The middle processing chamber and the rear processing chamber, which are separated by
In each processing chamber of the waste fermentation tanks
While heating the mechanical waste, it is agitated by the rotary stirring transfer means.
Stir and move from the above processing chamber to the following processing chamber.
In the moving step of the organic waste, the rotary stirring transfer hand is used.
The above intermediate processing is performed through normal rotation and reverse rotation by the stirrer of the stage.
Between each room, the latter processing room and the intermediate processing room adjacent to it
Transfer and post-transfer are performed between each other, and the organic waste in the pre-treatment chamber is the same as that in the pre-treatment chamber.
The upper part of the partition wall that separates the intermediate processing chamber adjacent to this
Overflow through a transition opening that is opened in
Is transferred to the intermediate processing chamber adjacent to
Yes, between the above intermediate processing chambers, adjacent to the latter processing chamber
Transfer and post-delivery of organic waste between two intermediate treatment chambers
Means that each partition wall separates the two adjacent processing chambers.
Through the transition opening, which consists of
Flip and is intended to be performed, organic flowing said each intermediate processing chamber and post-processing chamber
If the amount of waste is greater than the amount discharged to the outside,
Between the intermediate processing chambers, adjacent to the latter processing chamber
Opened at the top of each partition wall that separates the intermediate processing chambers.
Through the overflow transfer openings in the
Organic waste in the processing room moves to the adjacent processing room
The method for treating organic waste according to claim 1.
【請求項2】 前段処理室が第1処理室であり、中段処
理室が少なくとも3室からなる第2、第3及び第4処理
室であり、後段処理室が第5処理室であり、上記第1処
理室内の有機質廃棄物は第2処理室へオーバーフローに
より移送されるものであり、上記第2処理室と第3処理
室相互間、上記第3処理室と第4処理室相互間及び第4
処理室と第5処理室相互間における有機質廃棄物の移送
と後送とは、上記第2処理室と第3処理室間、第3処理
室と第4処理室間及び第4処理 室と第5処理室間を仕切
る仕切壁の移行用開口部を通じて行われ、第2処理室乃
至第5処理室それぞれの有機質廃棄物のオーバーフロー
はオーバーフロー移行用の開口部を通じて処理される
とを特徴とする請求項1記載の有機質廃棄物の処理方
法。
2. The pretreatment chamber is the first treatment chamber, and the middle treatment is performed.
2nd, 3rd and 4th treatments with at least 3 treatment rooms
Chamber, the post-treatment chamber is the fifth treatment chamber, and the first treatment chamber
Organic waste in the processing room overflows into the second processing room
The second processing chamber and the third processing
Between the chambers, between the third processing chamber and the fourth processing chamber, and between the fourth processing chamber
Transfer of organic waste between the treatment room and the fifth treatment room
And post-delivery means between the second processing chamber and the third processing chamber, and the third processing.
Partition between chamber and fourth processing chamber and between fourth processing chamber and fifth processing chamber
The second processing room
Overflow of organic waste in each of the 5th treatment room
The method for treating organic waste according to claim 1 , wherein the organic waste is treated through an opening for overflow transfer .
【請求項3】 廃棄物醗酵処理槽、加熱手段及び回転攪
拌移送手段を備えており、 上記廃棄物醗酵処理槽は、その内部がその長さ方向に仕
切壁によって前段処理室と、中段処理室と、後段処理室
とに連続状態に仕切られていると共に、上記中段処理室
が複数室に連続状態に仕切られており、上記前段処理
及びこれに隣接している中段処理室間、中段処理室相互
間、後段処理室及びこれに隣接している中段処理室間が
それぞれ互いに移行用開口部を介して連通されており、
上記中段処理室相互間、後段処理室及びこれに隣接して
いる中段処理室間がそれぞれ互いにオーバーフロー移行
用の開口部を介して連通されており、 上記前段処理は、有機質廃棄物の投入口を備えてお
り、上記複数室の中段処理室は少なくとも3室が上記仕切壁
によって仕切られているものであり、 上記各移行用開口部のうち、上記前段処理室とこれに隣
接している中段処理室とを仕切る仕切壁に設けられてい
る移行用開口部は、上記仕切壁の上部を切欠いたもので
あって、かつ他の各移行用開口部の位置よりも高い位置
に配置されており、上記他の各移行用開口部は隣接して
いる上記中段処理室間を仕切る仕切壁、後段処理室とこ
れに隣接している中段処理室間を仕切る仕切壁に仕切壁
の厚み方向に貫通状態に開けられた複数の通孔からなる
ものであり、 上記各オーバーフロー移行用の開口部は、上記中段処理
室相互間、後段処理室及びこれに隣接している中段処理
室間をそれぞれ仕切る各仕切壁の上部に設けられ、上記
他の各移行用開口部の位置より高い位置に配置されてお
り、 上記回転攪拌移送手段は、上記前段処理室から後段処理
室に至る各処理室内を貫通している正逆回転可能である
回転軸と、この回転軸に取付けられ、上記各処理室内の
上記有機質廃棄物を攪拌すると共に、前段処理室から後
段処理室まで上記有機質廃棄物を移送するための攪拌体
とを備えており、上記回転軸は中段処理室の仕切壁の位置で軸心方向に二
分割されており、 上記加熱手段は、各処理室内の上記有機質廃棄物を加熱
するものであることを特徴とする有機質廃棄物の処理装
置。
3. A waste fermentation treatment tank provided with a heating means and rotary stirring transfer means, the waste fermentation treatment tank, a pretreatment chamber inside thereof by its length to the partition wall, the middle stage process The chamber and the post-stage processing chamber are partitioned into a continuous state, and the above-mentioned middle-stage processing chamber
Are partitioned into a plurality of chambers in a continuous state, and the preceding processing chamber and the intermediate processing chambers adjacent thereto, between the intermediate processing chambers, the downstream processing chamber and the intermediate processing adjacent thereto. The chambers are communicated with each other through the transition openings,
Between the above middle processing chambers, adjacent to the latter processing chamber
The middle processing chambers are overflowing each other
Are connected to each other through an opening for water, the pretreatment chamber is provided with an input port for organic waste, and the middle treatment chambers of the plurality of chambers have at least three chambers as the partition walls.
Among the above-mentioned transfer openings , it is divided by
It is provided on the partition wall that separates the middle-stage processing chamber that is in contact with
The transition opening is a cutout at the top of the partition wall.
Position that is higher than the position of each of the other transition openings
And the other transition openings are adjacent to each other.
There is a partition wall that separates the above middle processing chambers,
A partition wall that separates the intermediate processing chambers adjacent to it
It consists of a plurality of through holes opened in the thickness direction of the
The openings for the above-mentioned overflow transitions are the same as those in the middle-stage processing.
Between the chambers, the post-treatment chamber and the middle treatment adjacent to it
It is installed at the top of each partition wall that separates each room,
Located higher than the position of each of the other transition openings.
Ri, said rotary stirring transfer means, and <br/> rotary shaft can be normal and reverse rotation extending through the treatment chamber reaches the post-processing chamber from the pretreatment chamber, mounted on the rotary shaft, each of While stirring the organic waste in the processing chamber, a stirring body for transferring the organic waste from the pre-treatment chamber to the post-treatment chamber is provided, and the rotary shaft is at the position of the partition wall of the middle-stage treatment chamber. Two in the axial direction
An apparatus for treating organic waste, wherein the heating means is divided, and the heating means heats the organic waste in each treatment chamber.
【請求項4】 廃棄物醗酵処理槽は、前段処理室が第1
処理室であり、中段処理室が少なくとも3室からなる第
2、第3及び第4処理室であり、後段処理室が第5処理
室であることを特徴とする請求項3記載の有機質廃棄物
の処理装置。
4. The waste fermentation tank has a first- stage processing chamber as a first stage.
It is a processing chamber, and the middle-stage processing chamber consists of at least three
There are 2, 3 and 4 processing chambers, and the latter processing chamber is the 5th processing chamber.
The apparatus for treating organic waste according to claim 3, which is a room .
JP35466799A 1999-12-14 1999-12-14 Organic waste treatment method and apparatus Expired - Fee Related JP3498025B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP35466799A JP3498025B2 (en) 1999-12-14 1999-12-14 Organic waste treatment method and apparatus

Publications (2)

Publication Number Publication Date
JP2001170606A JP2001170606A (en) 2001-06-26
JP3498025B2 true JP3498025B2 (en) 2004-02-16

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7449330B2 (en) * 2002-08-30 2008-11-11 Bouldin Corporation Bioreactor vessel and shaft assembly
JP2006167561A (en) * 2004-12-15 2006-06-29 Yuichi So Apparatus for treatment of organic waste
JP4884013B2 (en) * 2006-01-26 2012-02-22 キヤノン電子株式会社 Waste treatment equipment
KR101898269B1 (en) * 2018-06-28 2018-09-12 마이크로맥스 영농조합법인 ferment treat apparatus of organic wastes

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