JPH09278570A - Fermentation processing apparatus - Google Patents

Fermentation processing apparatus

Info

Publication number
JPH09278570A
JPH09278570A JP8095543A JP9554396A JPH09278570A JP H09278570 A JPH09278570 A JP H09278570A JP 8095543 A JP8095543 A JP 8095543A JP 9554396 A JP9554396 A JP 9554396A JP H09278570 A JPH09278570 A JP H09278570A
Authority
JP
Japan
Prior art keywords
fermentation
organic waste
bottom plate
air supply
air
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP8095543A
Other languages
Japanese (ja)
Inventor
Munehiro Kondo
宗浩 近藤
Kazuto Takahashi
一人 高橋
Kenichi Shibamoto
賢一 柴本
Toshimitsu Ishida
敏光 石田
Noritoshi Taniguchi
範敏 谷口
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ISHIDA KOGYO KK
Hitachi Chemical Techno Plant Ltd
Resonac Corp
Original Assignee
ISHIDA KOGYO KK
Hitachi Chemical Co Ltd
Hitachi Chemical Techno Plant Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by ISHIDA KOGYO KK, Hitachi Chemical Co Ltd, Hitachi Chemical Techno Plant Ltd filed Critical ISHIDA KOGYO KK
Priority to JP8095543A priority Critical patent/JPH09278570A/en
Publication of JPH09278570A publication Critical patent/JPH09278570A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

Abstract

PROBLEM TO BE SOLVED: To provide a fermentation processing apparatus which enables uniform fermentation without agitation and flow turning and enables the processing of the fermentation product with a reduced amount of water. SOLUTION: This fermentation processing apparatus comprises a frame stand 21, a storage housing 20 which is set on the frame stand 21 and is opened only at its one side wall, a bottom plate 6 which is arranged on the frame 21 and beneath the storage housing 20, divided into a plurality of sheets and equipped with a plurality of air-feeding pipes having a plurality of outputs embedded in and is made horizontally movable, the wall face 19 which is made horizontally movable to close the opened side wall of the housing 20, and a moving means 8 which moves the bottom plate 6 and the wall face 19 horizontally. An auxiliary plate 22 is attached to the wall face 19 corresponding to the storage side face, a sucking pipe 11 having a plurality of sucking inlets 12 is set inside the storage housing to communicate the sucking tube 11 through a blower 9 to the air-feeding tube.

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】本発明は、有機性廃棄物を発
酵処理し、減量化、堆肥化、飼料化を図るための発酵処
理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fermentation treatment apparatus for fermenting an organic waste to reduce its weight, compost it, and feed it.

【0002】[0002]

【従来の技術】従来より、有機性廃棄物を投入口側から
投入し、投入した有機性廃棄物を取り出し口側に移送す
る過程で有機性廃棄物を発酵させる発酵処理装置として
は、斜面を利用して有機性廃棄物を移動させながら発酵
させるもの、コンベア方式で床を移動させ有機性廃棄物
を移送する過程で発酵させるもの、キルン−スクリュー
方式のもの、切り返しにより有機性廃棄物を移送する過
程で発酵させるもの等が使用されていた。
2. Description of the Related Art Conventionally, as a fermentation treatment apparatus for fermenting organic waste in the process of inputting organic waste from the input side and transferring the input organic waste to the output side, a slope is used. Fermentation while moving organic waste by using it, fermenting in the process of moving the floor by conveyor method to transfer organic waste, kiln-screw method, transferring organic waste by turning back What was fermented during the process was used.

【0003】又、これとは別に、有機性廃棄物を発酵槽
に入れバッチ方式で処理する発酵処理装置や、発酵槽を
回転させながら発酵させる装置も従来より使用されてい
る。
In addition to this, a fermentation treatment apparatus for putting organic waste into a fermenter to treat it in a batch system, and an apparatus for fermenting while rotating the fermenter have been conventionally used.

【0004】前記何れの方式においても、その発酵は、
有機性廃棄物に空気を供給し、好気的な環境で有機性廃
棄物を生物分解させ、その分解熱により有機性廃棄物の
温度を高めて生物分解をより活発に進行させると共に、
有機性廃棄物中の雑菌等を死滅させ無害化するものであ
る。発酵が進み有機性廃棄物の温度が一定以上になった
後は、堆積された有機性廃棄物中に空気を通過させるこ
とによって、蒸発した水分が持ち出され、発酵生成物は
有機物が安定化し且つ水分が低下した取扱易い資材とし
て土壌改良剤等の用途で再利用可能となる。
In any of the above methods, the fermentation is
Air is supplied to the organic waste, the organic waste is biodegraded in an aerobic environment, and the heat of decomposition raises the temperature of the organic waste to promote biodegradation more actively.
It is intended to kill and detoxify various bacteria in organic waste. After the fermentation progresses and the temperature of the organic waste reaches a certain temperature or higher, the evaporated moisture is taken out by passing air through the accumulated organic waste, and the fermentation product stabilizes the organic matter and It can be reused as a soil-remediating agent as a material with reduced water content and easy to handle.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、これら
従来の発酵処理装置では、発酵槽内の有機性廃棄物中に
未発酵の部分が残り発酵生成物の品質が安定しなかっ
た。これは、有機性廃棄物に供給した空気は、酸素供給
の他に有機性廃棄物の堆積層を通過する過程で有機性廃
棄物から水分を奪ってこれを系外に持ち出す役割を果た
すが、有機性廃棄物の上部表面が相対的に温度の低い空
気と接触するために、水分を含んだ空気が有機性廃棄物
の上部に結露して部分的に水分過剰となり発酵が充分に
進行しないことによるものである。当然のことながら、
このような場合には、水分の多い発酵生成物が生成さ
れ、取扱性が悪いものとなってしまう。
However, in these conventional fermentation treatment apparatuses, the unfermented portion remains in the organic waste in the fermenter and the quality of the fermentation product is not stable. This is because the air supplied to the organic waste plays a role in removing water from the organic waste and taking it out of the system in the process of passing through the sedimentary layer of the organic waste in addition to supplying oxygen. Since the upper surface of the organic waste comes into contact with the air having a relatively low temperature, the air containing water condenses on the upper part of the organic waste to cause partial excess of water and the fermentation does not proceed sufficiently. It is due to. As a matter of course,
In such a case, a fermented product having a high water content is produced, resulting in poor handleability.

【0006】また別の問題として、空気の供給量が少な
い場合は、発酵初期の昇温は起こるが蒸発した水分の持
出し量が少なく発酵生成物の水分が低下することなく、
発酵が充分に進行しないことや、逆に空気供給量が多い
場合には、外気温の低い時期において空気供給によって
発酵素材が冷却されて温度が上昇せずに発酵が進行しな
い等の問題があった。
Another problem is that when the amount of air supplied is small, the temperature rise in the early stage of fermentation occurs but the amount of evaporated water taken out is small and the water content of the fermentation product does not decrease.
Fermentation does not proceed sufficiently, or conversely, when the air supply is large, there is a problem that the fermentation material is cooled by the air supply and the temperature does not rise and the fermentation does not proceed in a period when the outside temperature is low. It was

【0007】本願発明では、前記問題点に鑑み品質の安
定した発酵生成物、即ち発酵槽全体で発酵が均一に進行
し、再利用品として適切な水分に低下した発酵生成物が
得られる発酵処理装置を提供することを目的としてい
る。
In the present invention, in view of the above problems, a fermentation product having a stable quality, that is, a fermentation product in which fermentation uniformly progresses throughout the fermenter and the water content is reduced to an appropriate level as a recycled product The purpose is to provide a device.

【0008】[0008]

【課題を解決するための手段】本発明は、架台と、該架
台上面に設置する1側壁のみ開放された収納部と、前記
架台上面で且つ前記収納部の下部に複数枚に分割され且
つ複数の送気口を有した送気管を埋設した水平方向移動
自在な底板と、前記収納部の開放側面を閉塞させる水平
方向移動自在な壁面と、前記底板及び壁面を水平方向に
移動させる移動手段とからなり、前記壁面には収納部側
面に対応する補助板を設け、前記収納部内部に複数の吸
引口を有する吸引管を設置し、該吸引管をブロワを介し
て送気管と連通させたことを特徴とする。
SUMMARY OF THE INVENTION According to the present invention, a gantry, a storage portion installed on the top surface of the pedestal and having only one side wall opened, and a plurality of divided portions on the top surface of the pedestal and below the storage portion. A horizontally movable bottom plate in which an air supply pipe having an air supply port is embedded, a horizontally movable wall surface that closes the open side surface of the storage section, and a moving means that horizontally moves the bottom plate and the wall surface. An auxiliary plate corresponding to the side surface of the storage portion is provided on the wall surface, a suction pipe having a plurality of suction ports is installed inside the storage portion, and the suction pipe is connected to an air supply pipe through a blower. Is characterized by.

【0009】上記構成としたのは、発酵槽内の有機性廃
棄物の発酵過程を種々検討した結果、有機性廃棄物を撹
拌、切り返しをした場合、発酵による有機性廃棄物の温
度上昇が妨げられ望ましい発酵温度に達することが困難
となり、これが発酵生成物の品質安定化に悪影響を与え
る原因であることを見出したことによる。
[0009] The above-mentioned constitution is made as a result of various studies on the fermentation process of the organic waste in the fermenter, and as a result, when the organic waste is agitated and cut back, the temperature rise of the organic waste due to fermentation is hindered. It is difficult to reach the desired fermentation temperature, and it has been found that this is a cause of adversely affecting the stabilization of the quality of the fermentation product.

【0010】本発明の構成を簡単に換言すれば、発酵過
程において撹拌、切り返しを行なわずに有機性廃棄物を
発酵させるものである。
In other words, the constitution of the present invention is to ferment the organic waste without stirring and turning back in the fermentation process.

【0011】[0011]

【発明の実施の形態】本発明を図1を用いて説明する
と、移動装置8を駆動させ油圧シリンダ18を介して接
続させた複数の底板6及び壁面19を同時に投入口2側
に引き出し、前記底板6及び壁面19を引き出すことに
よって形成された投入口2より壁面19、底板6及び補
助板22に囲まれた空間部16に投入コンベア4により
有機性廃棄物1を充填する。そして、投入口2直下にあ
る空間部16に有機性廃棄物1が高さ方向に対して充填
されると、図2に示すように移動装置8を駆動させ油圧
シリンダ18により複数の底板6及び壁面19とを同時
に押出し有機性廃棄物1を発酵槽17内に収納する。こ
の時点において、発酵槽17内の有機性廃棄物1は投入
口2側の壁面19及び底板6に押されながら発酵槽17
に収納されるため、壁面19及び底板6が完全に発酵槽
17に収納された時点において有機性廃棄物1は発酵槽
17の入口に存在する。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described with reference to FIG. 1. A plurality of bottom plates 6 and wall surfaces 19 which are driven by a moving device 8 and connected to each other through hydraulic cylinders 18 are simultaneously pulled out to the insertion port 2 side. The space 16 surrounded by the wall surface 19, the bottom plate 6 and the auxiliary plate 22 is filled with the organic waste 1 from the charging port 2 formed by drawing the bottom plate 6 and the wall surface 19. Then, when the organic waste 1 is filled in the space 16 just below the charging port 2 in the height direction, the moving device 8 is driven as shown in FIG. The wall surface 19 and the organic waste material 1 are extruded at the same time, and the organic waste 1 is stored in the fermentation tank 17. At this point, the organic waste 1 in the fermenter 17 is being pushed by the wall surface 19 and the bottom plate 6 on the input port 2 side while being fermented.
The organic waste 1 is present at the inlet of the fermenter 17 when the wall surface 19 and the bottom plate 6 are completely accommodated in the fermenter 17.

【0012】次に、有機性廃棄物1を更に投入するには
図3に示すように、移動装置8を駆動させ油圧シリンダ
18により複数の底板6及び壁面19とを発酵槽17内
から引き出して投入口2を出現させる。この時点におい
て、有機性廃棄物1の堆積層は、壁面19の両側部に対
向して立設させた補助板22と底板6に接触しており、
分割された複数の底板6を移動装置8によって個々に引
き出すことによって、また壁面19を引き出すことによ
って有機性廃棄物1の堆積層は補助板22、底板6、壁
面19から分離され、投入口2下方に空間が生じる。そ
して投入口2より下方の空間部16に有機性廃棄物1を
投入して充填させ、順次この動作を繰り返して有機性廃
棄物1を継続的に投入する。尚、投入口2を出現させる
には、底板6上に乗っている有機性廃棄物1を移動させ
る必要があるが、単に底板6を移動させただけでは有機
性廃棄物を移動させることはできない。そこで底板6を
複数に分割し、底板6を同時ではなく各々別々に移動さ
せることにより有機性廃棄物1を底板6から引き剥がし
移動させている。
Next, in order to further add the organic waste 1, as shown in FIG. 3, the moving device 8 is driven to pull out the plurality of bottom plates 6 and the wall surface 19 from the fermentation tank 17 by the hydraulic cylinder 18. The input port 2 appears. At this point, the deposited layer of the organic waste 1 is in contact with the auxiliary plate 22 and the bottom plate 6 that are erected upright on both sides of the wall surface 19,
By pulling out the divided bottom plates 6 individually by the moving device 8 and pulling out the wall surface 19, the deposited layer of the organic waste 1 is separated from the auxiliary plate 22, the bottom plate 6, and the wall surface 19, and the charging port 2 There is a space below. Then, the organic waste 1 is charged into the space 16 below the charging port 2 to fill it, and this operation is sequentially repeated to continuously charge the organic waste 1. It is necessary to move the organic waste 1 on the bottom plate 6 in order to make the input port 2 appear, but it is not possible to move the organic waste simply by moving the bottom plate 6. . Therefore, the bottom plate 6 is divided into a plurality of parts, and the bottom plates 6 are moved separately, not simultaneously, so that the organic waste 1 is peeled from the bottom plate 6 and moved.

【0013】上記のような有機性廃棄物1の投入及び移
送を行なうことにより、投入物の撹拌、切り返しを伴わ
ないので、有機性廃棄物1の分解による反応熱を蓄熱で
き、温度上昇が促進され、発酵が良好に進行する。
By performing the input and transfer of the organic waste 1 as described above, the reaction heat due to the decomposition of the organic waste 1 can be stored because the input waste is not stirred and cut back, and the temperature rise is promoted. The fermentation proceeds well.

【0014】発酵槽17が一杯になり投入が完了した後
は、図4に示すようにブロワ9を稼働させて吸引管11
より発酵槽17内の空気を前記吸引管11に設けられた
複数の吸引口12から吸引する。吸引した空気は、その
一部又は全部をブロワ9より吐出した後、2方向に分配
する。一方は、投入口側送気管14によって発酵槽17
中央部から投入口2側の発酵初期の有機性廃棄物1また
は発酵生成物10に対して供給される。他方は、取り出
し口側送気管15によって発酵槽17中央部から取り出
し口3側の発酵後期の有機性廃棄物1または発酵生成物
10に対して供給される(図8参照)。2方向への配分
割合は、発酵初期の方より発酵後期の方により多く送気
するようにすることが好ましい。これは、発酵初期には
温度上昇を確実に行なわせるため、温度低下を招く空気
供給量を抑えるためであり、発酵後期では水分を低下さ
せるため発酵初期に比べ多くの空気を供給したいためで
ある。
After the fermenter 17 is full and the addition is completed, the blower 9 is operated to move the suction pipe 11 as shown in FIG.
The air in the fermenter 17 is sucked through a plurality of suction ports 12 provided in the suction pipe 11. The sucked air is partly or wholly discharged from the blower 9 and then distributed in two directions. One is the fermenter 17 with the inlet side air pipe 14.
It is supplied from the central part to the organic waste 1 or the fermentation product 10 at the beginning of fermentation on the side of the input port 2. The other is supplied from the central part of the fermentation tank 17 to the organic waste 1 or the fermentation product 10 at the latter stage of fermentation on the side of the outlet 3 by the outlet side air pipe 15 (see FIG. 8). As for the distribution ratio in the two directions, it is preferable to supply more air in the latter half of the fermentation than in the first half of the fermentation. This is because in order to surely raise the temperature in the early stage of fermentation, it is necessary to suppress the air supply amount that causes a temperature decrease, and in the latter half of fermentation to reduce the water content, it is desirable to supply a larger amount of air than in the initial stage of fermentation. .

【0015】本発明の場合、吸引管11によって、有機
性廃棄物1または発酵生成物10の堆積層内から直接高
温多湿の空気を吸引するため、堆積層上部の結露帯が大
幅に減少し、送気による水分の持ち出しが効果的に行な
われる。また、送気管の分割によって、発酵初期の温度
上昇を確実に進行させ、且つ、発酵生成物10の水分を
低下させることができる。
In the case of the present invention, since the suction pipe 11 directly sucks the hot and humid air from the inside of the sediment layer of the organic waste 1 or the fermentation product 10, the dew zone above the sediment layer is greatly reduced, The removal of water by insufflation is effectively performed. Further, by dividing the air supply pipe, it is possible to reliably advance the temperature rise in the initial stage of fermentation and reduce the water content of the fermentation product 10.

【0016】発酵生成物10を取り出す場合には、図5
に示すように、移動装置8を駆動させ、油圧シリンダ1
8により分割された複数の底板6を発酵槽17内から個
々に引き出すことにより取り出し口3の直上に位置する
発酵生成物10が自重により自然落下し取り出しコンベ
ア5で移送される。
When the fermentation product 10 is taken out, the process shown in FIG.
As shown in FIG.
By pulling out the plurality of bottom plates 6 divided by 8 from the fermentation tank 17, the fermentation product 10 located immediately above the take-out port 3 is naturally dropped by its own weight and transferred by the take-out conveyor 5.

【0017】[0017]

【実施例】本発明の実施例を図1乃至図8を用いて説明
する。本発明の発酵処理装置は、図1に示すように、主
に架台21と収納部20からなる発酵槽17と、水平方
向移動自在な複数の底板6と、該底板6とは別体として
移動し且つ対向する2枚の補助板22を設けた壁面19
と、底板6及び壁面19とを移動させる油圧シリンダ1
8を設けた移動装置(移動手段)8と、発酵槽17内の
空気を吸引する吸引管11と、該吸引管11とブロワ9
を介して連通する投入口側送気管14及び取り出し口側
送気管15(図7参照)により構成される。吸引管11
は、図6及び図7に示してあるように、有機性廃棄物1
を発酵槽17に挿入した際に、前記有機性廃棄物1中に
埋もれるように設ける。
Embodiments of the present invention will be described with reference to FIGS. As shown in FIG. 1, the fermentation treatment apparatus of the present invention comprises, as shown in FIG. 1, a fermentation tank 17 mainly composed of a pedestal 21 and a storage section 20, a plurality of horizontally movable bottom plates 6, and the bottom plate 6 as a separate body. Wall surface 19 provided with two auxiliary plates 22 facing each other
And a hydraulic cylinder 1 for moving the bottom plate 6 and the wall surface 19
A moving device (moving means) 8 provided with 8, a suction pipe 11 for sucking air in the fermenter 17, a suction pipe 11 and a blower 9
It is composed of an inlet side air supply pipe 14 and an outlet side air supply pipe 15 (see FIG. 7) which are communicated with each other through. Suction tube 11
As shown in FIGS. 6 and 7, the organic waste 1
When it is inserted into the fermenter 17, it is provided so as to be buried in the organic waste 1.

【0018】架台21の一端には、開口部を設け発酵生
成物10の取り出し口3が形成され、他端には、有機性
廃棄物1の投入口2を形成してある。底板6は、架台2
1上を水平方向、換言すれば長手方向に移動可能であ
り、前記底板6の収納部20に設けられた開口側面側に
該開口側面を閉塞する壁面19が底板6とは別体に立設
されている。図7に示すように壁面19には、有機性廃
棄物1のこぼれを防止するために補助板22が2枚対向
して接合されている。
An opening is provided at one end of the gantry 21 to form an outlet 3 for the fermentation product 10, and an inlet 2 for the organic waste 1 is formed at the other end. The bottom plate 6 is a pedestal 2
1 is movable in the horizontal direction, in other words, in the longitudinal direction, and a wall surface 19 that closes the opening side surface provided on the storage portion 20 of the bottom plate 6 is provided separately from the bottom plate 6. Has been done. As shown in FIG. 7, two auxiliary plates 22 are joined to the wall surface 19 so as to prevent the organic waste 1 from spilling.

【0019】壁面19近傍には、油圧シリンダ18を動
かすための移動装置8を設け、該移動装置8と壁面1
9、移動装置8と複数の底板6とをそれぞれ油圧シリン
ダ18によって接続し、壁面19及び複数の底板6を水
平方向に移動可能にする。
A moving device 8 for moving the hydraulic cylinder 18 is provided near the wall surface 19, and the moving device 8 and the wall surface 1 are provided.
9. The moving device 8 and the plurality of bottom plates 6 are connected by hydraulic cylinders 18, respectively, so that the wall surface 19 and the plurality of bottom plates 6 can be moved in the horizontal direction.

【0020】吸引管11は、収納部内に設けられ、その
位置は有機性廃棄物1によって埋設される個所が好まし
い。埋設される位置に設けることにより、吸引する空気
は高温多湿なものとなり、結露を効果的に防止すること
ができる。吸引管11は、前述したようにブロワ9を介
して投入口側送気管14及び取り出し口側送気管15に
連通されており、吸引された空気は、その全部又は一部
を外気と混合した後、前記送気管14、15の送気口7
より発酵槽17内に送気される。投入口側送気管14及
び取り出し口側送気管15は、底板6の上面に付設さ
れ、底板6と接する面が開放されている。ブロワ6によ
って吐出された空気は、投入口側送気管14及び取り出
し口側送気管15によって移送され、底板6に設けられ
た複数の送気口7を介して発酵槽17内に供給される。
The suction pipe 11 is provided in the storage portion, and the position thereof is preferably a place where the organic waste 1 is buried. By providing it in a position where it is buried, the air to be sucked becomes hot and humid, and it is possible to effectively prevent dew condensation. The suction pipe 11 is connected to the inlet side air supply pipe 14 and the outlet side air supply pipe 15 via the blower 9 as described above, and the sucked air is mixed with the outside air in whole or in part. The air supply port 7 of the air supply pipes 14 and 15
More air is fed into the fermenter 17. The inlet-side air supply pipe 14 and the outlet-side air supply pipe 15 are attached to the upper surface of the bottom plate 6, and the surfaces in contact with the bottom plate 6 are open. The air discharged by the blower 6 is transferred by the inlet side air supply pipe 14 and the outlet side air supply pipe 15, and is supplied into the fermenter 17 through the plurality of air supply ports 7 provided in the bottom plate 6.

【0021】一例として、有機性廃棄物1である浄化槽
汚泥の脱水汚泥を水分調整剤と混合し、投入コンベア4
によって発酵槽17内に投入した。投入量は、発酵槽1
7の中央部から投入口2側を埋める容積、即ち発酵槽1
7全体の半分程度の容積となる量である。前記投入物に
対し、ブロワ9を稼動して投入口側送気管14によって
送気を行った。投入物は、投入した日から7日以内に汚
泥中の有機物の分解反応熱によって摂氏60〜70度ま
で温度上昇した。その後、再び浄化槽汚泥を前回と同様
に発酵槽17に投入した。この操作は、先ず複数の底板
6を同時にではなく個別に動かすことにより、底板6に
貼り付いた有機性廃棄物1及び発酵生成物10を引き剥
がし、その後に壁面19を移動させることで投入口2の
下部に空間部16を出現させた。前記空間部16に投入
物を投入することにより、空間部16が満たされた後、
複数の底板6及び壁面19を同時に取り出し口3側に移
動することで投入物を発酵槽17内に収納した。以上の
操作を繰返し、発酵槽17内の中央部から投入口側を新
しい投入物が、中央部から取り出し口側を古い投入物が
占める状態とした。更に、ブロワ9を稼動させ、投入口
側送気管14によって新しい投入物に対して送気を行
い、取り出し口側送気管15によって古い投入物に送気
を行った。この時、投入口側送気管14の送気量は投入
物の温度上昇を妨げないように少量とし、取り出し口側
送気管15の送気量は、水分蒸発を促進するために投入
口側送気管14からの送気量よりも多量の送気を行っ
た。
As an example, the dehydrated sludge of the septic tank sludge, which is the organic waste 1, is mixed with a water content adjusting agent, and the feeding conveyor 4 is used.
Was charged into the fermenter 17. Input amount is 1 fermenter
Volume of filling the inlet 2 side from the central part of 7, that is, fermenter 1
The volume is about half of the total volume of 7. The blower 9 was operated to supply air to the above-mentioned input material by the input port side air supply pipe 14. The temperature of the charged material increased to 60 to 70 degrees Celsius due to the heat of decomposition reaction of organic matter in sludge within 7 days from the day of charging. Then, the septic tank sludge was again charged into the fermentation tank 17 as in the previous case. In this operation, first, the plurality of bottom plates 6 are not moved at the same time but individually, so that the organic waste 1 and the fermentation product 10 attached to the bottom plate 6 are peeled off, and then the wall surface 19 is moved to move the charging port. The space portion 16 appeared at the bottom of 2. After the space 16 is filled by charging the space 16 with the charge,
The plurality of bottom plates 6 and the wall surface 19 were moved to the outlet 3 side at the same time to store the input material in the fermenter 17. By repeating the above operation, a new charge occupies the center of the fermenter 17 from the center to the input side, and an old charge occupies the center to the outlet side. Further, the blower 9 was operated, air was supplied to the new charge by the inlet side air supply pipe 14, and air was supplied to the old charge by the outlet side air supply pipe 15. At this time, the amount of air supplied to the inlet-side air supply pipe 14 is set small so as not to hinder the temperature rise of the input material, and the amount of air supplied to the outlet-side air supply pipe 15 is set to the inlet-side air supply in order to promote water evaporation. A larger amount of air was supplied than the amount of air sent from the trachea 14.

【0022】最初の投入物の温度が低下した後、発酵生
成物10の取り出しを行った。この操作は、先ず取り出
しコンベア5を稼動し、底板6を移動装置8側へ移動さ
せて取り出し口3を出現させた。取り出し口3上に位置
する発酵生成物10は取り出しコンベア5上に落下して
搬送される。発酵生成物10の水分を測定した結果は、
投入時51パーセントだったものが42パーセントとな
っていた。しかも、結露帯が極めて少なく、発酵槽17
全体で均一な発酵が進行した。一方、吸引管11、投入
口側送気管14及び取り出し口側送気管15の運転を停
止した状態で前記同様の運転を行うと、投入時51パー
セントの水分が46パーセントの水分比率にまでしか低
下しなかった上に、結露帯が大きく、均一な発酵を行え
なかった。
After the temperature of the initial charge dropped, the fermentation product 10 was taken out. In this operation, first, the take-out conveyor 5 was operated, the bottom plate 6 was moved to the moving device 8 side, and the take-out port 3 appeared. The fermentation product 10 located on the take-out port 3 falls on the take-out conveyor 5 and is conveyed. The result of measuring the water content of the fermentation product 10 is
What was 51% at the time of input was 42%. Moreover, the dew zone is extremely small, and the fermentation tank 17
Uniform fermentation proceeded throughout. On the other hand, when the same operation as described above is performed with the suction pipe 11, the inlet side air supply pipe 14 and the outlet side air supply pipe 15 stopped, the water content of 51% at the time of supply is reduced to only 46%. In addition, the dew zone was large and uniform fermentation could not be performed.

【0023】[0023]

【発明の効果】本発明は、以上説明してきた通り、発酵
槽内で有機性廃棄物の撹拌や切り返しを行わずに搬送す
るため、有機性廃棄物の分解熱を蓄熱して高温下での発
酵が安定して行われる。また、発酵槽内に投入された有
機性廃棄物によって埋設される位置に吸引管を設け、ま
た発酵槽内の有機性廃棄物に空気を供給する送気管を発
酵槽中央部から投入口側と、発酵槽中央部から取り出し
口側の2つに分割して設けたことによって、発酵初期の
温度上昇が確実に行われるとともに、発酵生成物からの
蒸発水分の持ち出しが促進され、水分の低い取扱性に優
れた発酵生成物が得られる。
INDUSTRIAL APPLICABILITY As described above, the present invention conveys the organic waste in the fermenter without stirring or turning it back. Therefore, the heat of decomposition of the organic waste is stored and stored at high temperature. Fermentation is stable. In addition, a suction pipe is provided at a position where it is buried by the organic waste put in the fermenter, and an air supply pipe for supplying air to the organic waste in the fermenter is connected to the inlet side from the central part of the fermenter. By dividing the fermentation tank from the center to the outlet side, the temperature of the fermentation can be surely raised at the beginning of fermentation and the evaporation of moisture from the fermentation product can be promoted. A fermentation product having excellent properties is obtained.

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

【図1】本発明の実施例による発酵処理装置の側方断面
図である。
FIG. 1 is a side sectional view of a fermentation treatment apparatus according to an embodiment of the present invention.

【図2】本発明の実施例による発酵処理装置の説明図で
ある。
FIG. 2 is an explanatory diagram of a fermentation treatment apparatus according to an embodiment of the present invention.

【図3】本発明の実施例による発酵処理装置の底板の動
きを説明する断面図である。
FIG. 3 is a cross-sectional view illustrating the movement of the bottom plate of the fermentation treatment apparatus according to the embodiment of the present invention.

【図4】本発明の実施例による発酵処理装置の底板と有
機性廃棄物の関係を説明する断面図である。
FIG. 4 is a cross-sectional view illustrating the relationship between the bottom plate of the fermentation treatment apparatus and the organic waste according to the embodiment of the present invention.

【図5】本発明の実施例による発酵処理装置の有機性廃
棄物と取り出しコンベアの関係を説明する断面図であ
る。
FIG. 5 is a cross-sectional view illustrating the relationship between the organic waste and the takeout conveyor of the fermentation treatment apparatus according to the embodiment of the present invention.

【図6】本発明の要部である底板の平面図である。FIG. 6 is a plan view of a bottom plate which is a main part of the present invention.

【図7】図6に示す発酵処理装置のA−A断面図であ
る。
7 is a cross-sectional view taken along the line AA of the fermentation treatment apparatus shown in FIG.

【図8】本発明の要部である底板と送気管の関係を示す
平面図である。
FIG. 8 is a plan view showing a relationship between a bottom plate and an air supply pipe, which is an essential part of the present invention.

【符号の説明】[Explanation of symbols]

1.有機性廃棄物 2.投入口 3.取り出し口 4.
投入コンベア 5.取り出しコンベア 6.底板 7.
送気口 8.移動装置 9.ブロワ 10.発酵生成物
11.吸引管 12.吸引口 13.吸引管固定管
14.投入口側送気管 15.取り出し口側送気管 1
6.空間部 17.発酵槽 18.油圧シリンダ 1
9.壁面 20.収納部 21.架台 22.補助板
1. Organic waste 2. Input port 3. Outlet 4.
Input conveyor 5. Take-out conveyor 6. Bottom plate 7.
Air outlet 8. Mobile device 9. Blower 10. Fermentation product 11. Suction tube 12. Suction port 13. Suction tube Fixed tube
14. Inlet side air pipe 15. Air outlet tube 1
6. Space section 17. Fermenter 18. Hydraulic cylinder 1
9. Wall surface 20. Storage section 21. Stand 22. Auxiliary plate

───────────────────────────────────────────────────── フロントページの続き (72)発明者 高橋 一人 茨城県下館市大字下江連1250番地 日立化 成工業株式会社結城工場内 (72)発明者 柴本 賢一 茨城県下館市大字下江連1250番地 日立化 成工業株式会社結城工場内 (72)発明者 石田 敏光 鳥取県倉吉市瀬崎町2736番地 石田工業株 式会社内 (72)発明者 谷口 範敏 鳥取県倉吉市瀬崎町2736番地 石田工業株 式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) One inventor Takahashi 1250 Shimoeden, Shimodate-shi, Ibaraki Inside the Yuki factory of Hitachi Chemical Co., Ltd. (72) Kenichi Shibamoto 1250 Shimoedren, Shimodate, Ibaraki Hitachi Seikou Co., Ltd.Yuki Factory (72) Inventor Toshimitsu Ishida 2736 Sezaki-cho, Kurayoshi-shi, Tottori Prefecture Ishida Industry Co., Ltd. (72) Inventor Noritoshi Taniguchi 2736 Sezaki-cho, Kurayoshi-shi, Tottori Ishida Industry Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 架台と、該架台上面に設置する1側壁の
み開放された収納部と、前記架台上面で且つ前記収納部
の下部に複数枚に分割され且つ複数の送気口を有した送
気管を埋設した水平方向移動自在な底板と、前記収納部
の開放側面を閉塞させる水平方向移動自在な壁面と、前
記底板及び壁面を水平方向に移動させる移動手段とから
なり、前記壁面には収納部側面に対応する補助板を設
け、前記収納部内部に複数の吸引口を有する吸引管を設
置し、該吸引管をブロワを介して送気管と連通させたこ
とを特徴とする発酵処理装置。
1. A gantry, an accommodating section which is installed on the gantry upper surface and has only one side wall opened, and a feeding unit which is divided into a plurality of sheets and has a plurality of air supply ports on the gantry upper surface and below the accommodating section. It comprises a horizontally movable bottom plate with a trachea buried therein, a horizontally movable wall surface that closes the open side surface of the storage section, and a moving means that horizontally moves the bottom plate and the wall surface. A fermentation treatment apparatus, characterized in that an auxiliary plate corresponding to the side surface of the unit is provided, a suction pipe having a plurality of suction ports is installed inside the storage unit, and the suction pipe is connected to an air supply pipe via a blower.
【請求項2】 底板に埋設した送気管が、複数本であり
且つその一部が底板長手方向に対し半分の長さのみに送
気口を有し、その他の送気管が残り半分の長さにのみに
送気口を有している請求項1記載の発酵処理装置。
2. A plurality of air supply pipes embedded in the bottom plate, a part of which has an air supply port only in a half length with respect to the longitudinal direction of the bottom plate, and the other air supply pipes have a remaining half length. The fermentation treatment apparatus according to claim 1, wherein the fermentation treatment apparatus has an air supply port only at the end.
JP8095543A 1996-04-17 1996-04-17 Fermentation processing apparatus Pending JPH09278570A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8095543A JPH09278570A (en) 1996-04-17 1996-04-17 Fermentation processing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8095543A JPH09278570A (en) 1996-04-17 1996-04-17 Fermentation processing apparatus

Publications (1)

Publication Number Publication Date
JPH09278570A true JPH09278570A (en) 1997-10-28

Family

ID=14140489

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8095543A Pending JPH09278570A (en) 1996-04-17 1996-04-17 Fermentation processing apparatus

Country Status (1)

Country Link
JP (1) JPH09278570A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010137593A1 (en) * 2009-05-28 2010-12-02 岩手コンポスト株式会社 Fermentation method
CN103102193A (en) * 2013-03-14 2013-05-15 上海交通大学 Movable microbial fermentation system based on farmland straw wastes

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010137593A1 (en) * 2009-05-28 2010-12-02 岩手コンポスト株式会社 Fermentation method
CN103102193A (en) * 2013-03-14 2013-05-15 上海交通大学 Movable microbial fermentation system based on farmland straw wastes

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