JPS5925866Y2 - Composting equipment for sludge containing organic matter - Google Patents
Composting equipment for sludge containing organic matterInfo
- Publication number
- JPS5925866Y2 JPS5925866Y2 JP6705883U JP6705883U JPS5925866Y2 JP S5925866 Y2 JPS5925866 Y2 JP S5925866Y2 JP 6705883 U JP6705883 U JP 6705883U JP 6705883 U JP6705883 U JP 6705883U JP S5925866 Y2 JPS5925866 Y2 JP S5925866Y2
- Authority
- JP
- Japan
- Prior art keywords
- fermentation
- sludge
- fermentation bed
- beds
- rows
- 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
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Description
【考案の詳細な説明】
本考案は有機質を含んだ汚泥を好気的雰囲気のもとて好
気性菌により急速に醗酵、分解させて汚泥を堆肥化する
ための装置に係るものである。[Detailed Description of the Invention] The present invention relates to an apparatus for composting sludge by rapidly fermenting and decomposing sludge containing organic matter by aerobic bacteria in an aerobic atmosphere.
一般に有機質を多く含んだ汚泥としては、下水汚泥、し
尿処理汚泥、家畜排泄物若しくはその処理汚泥又は産業
排水処理汚泥等があり、これらの汚泥の堆肥化に関して
は種々の方法及び装置が開示されているが、汚泥の堆肥
化にあたっては汚泥の物理的な特性が取扱い面及び醗酵
、分解処理の過程に大きく影響するのであって、この汚
泥の特性に充分合致した最適の堆肥化装置となすことは
大変重要である。In general, sludge containing a large amount of organic matter includes sewage sludge, human waste treatment sludge, livestock excrement or its treatment sludge, industrial wastewater treatment sludge, etc., and various methods and devices have been disclosed for composting these sludges. However, when composting sludge, the physical characteristics of the sludge greatly affect the handling, fermentation, and decomposition processes, and it is important to create the optimal composting equipment that fully matches the characteristics of the sludge. Very important.
汚泥の物理的な特性のうち、堆肥化処理にあっては特に
対象となる汚泥の塑性的な流動特性が大きな問題となっ
ている。Among the physical characteristics of sludge, the plastic flow characteristics of sludge, which is the target of composting, are a major problem.
通常汚泥の堆肥化処理は好気的雰囲気のもとで行われる
ものであり、このためには通気性を充分に保つことと適
度な攪拌とが必要である。Composting treatment of sludge is usually carried out under an aerobic atmosphere, and for this purpose it is necessary to maintain sufficient air permeability and appropriate stirring.
しかし在米の手段による場合には汚泥に固有な塑性的な
流動特性のために、汚泥の醗酵、分解の障害となるよう
な、積層時の圧迫緊密化による窒息現象とが機械的攪拌
等による団塊化が起り易く、その結果通気性の不全及び
醗酵の均質性が損われる懸念が存したのである。However, in the case of methods based in the United States, due to the inherent plastic flow characteristics of sludge, suffocation due to pressure tightness during stacking, which hinders fermentation and decomposition of sludge, may occur due to mechanical agitation, etc. There was a concern that agglomeration was likely to occur, resulting in poor air permeability and loss of fermentation homogeneity.
このような難点を解消しようとして、たとえば特開昭5
4−80883号にみるごとき醗酵を上下に配設した複
数の棚段において行なわんとするものも提案されてはい
るが、これらのものは階段状の可動段で被処理汚泥を押
すように構成されており、このような手段による限りは
醗酵床を水平にしたときには汚泥は前方へ移行させるこ
とができず、却って団塊化をもたらすおそれが強かった
のである。In an attempt to resolve these difficulties, for example,
4-80883, in which fermentation is carried out in a plurality of shelves arranged above and below, has been proposed; However, as long as this method was used, the sludge could not be moved forward when the fermentation bed was leveled, and there was a strong possibility that it would lead to agglomeration.
本考案は斯かる現況に艦がみなされたもので、設置時の
占有スペースを効率よく活用すべく被処理汚泥を水平に
移行せしめつつ、汚泥の好気性雰囲気における醗酵、分
解に対する汚泥固有の塑性的な流動特性に起因する障害
をなくして、有機性汚泥の急速な堆肥化処理を効率よく
行うことができる装置を提供することを目的としている
。The present invention was developed based on this current situation, and in order to efficiently utilize the space occupied at the time of installation, the sludge to be treated is transferred horizontally, and the inherent plasticity of sludge with respect to fermentation and decomposition in an aerobic atmosphere is improved. The purpose of the present invention is to provide an apparatus that can efficiently perform rapid composting treatment of organic sludge by eliminating obstacles caused by its fluid flow characteristics.
以下、本考案に係る装置について詳述する。The apparatus according to the present invention will be described in detail below.
本考案装置における汚泥の堆肥化にあたっては、醗酵に
供する前処理として破砕、水分調整、pH調整又は製品
堆肥との混合等を施して醗酵、分解をし易くした原料汚
泥を醗酵室へ供給し、醗酵室内ではこのような原料汚泥
を、その積層厚さを通常1〜2m程度の層状にして堆積
することにより、在来例にみるような、うずたかい堆積
による圧迫緊密化若しくは団塊化を防ぎ、通気性を保ち
均質な醗酵が行われようにするのであり、このようにし
た原料汚泥層を、交互の向きの棚状の構成となした醗酵
床上を移行させ、各段ごとに原料汚泥層の底部から送気
し好気的醗酵、分解を促進させるのである。When composting sludge in the device of the present invention, raw material sludge that has been subjected to pretreatment such as crushing, moisture adjustment, pH adjustment, or mixing with product compost to make it easier to ferment and decompose is supplied to the fermentation chamber. In the fermentation chamber, such raw material sludge is piled up in layers, usually about 1 to 2 meters thick, to prevent compaction or agglomeration due to thick piles, as seen in conventional cases. This is to maintain air permeability and ensure homogeneous fermentation.The raw material sludge layer thus created is transferred over a fermentation bed that has a shelf-like configuration in alternating directions, and the raw material sludge layer is transferred at each stage. Air is introduced from the bottom to promote aerobic fermentation and decomposition.
そして各段の原料汚泥を上段から下段に遂次移動させて
いく際に、各段ごとに原料汚泥は落下により反転し攪拌
、混合がなされて均質化が進むと共に通気性が良好にな
る。When the raw material sludge in each stage is successively moved from the upper stage to the lower stage, the raw material sludge falls and is reversed in each stage, and is stirred and mixed, so that homogenization progresses and air permeability improves.
汚泥のごとく半固体基質の醗酵においては、連続的な攪
拌は不要であり、かえって機械的な連続攪拌は団塊化を
起し易く好気的な醗酵、分解を阻害するが、本考案に係
る堆肥化装置の構成によれば原料汚泥は各段において送
気による好気的雰囲気を伴いつつ生酔的に各股上を移動
し、更に各段より下段に落下する際に適度な混合攪拌が
なされ、原料汚泥の塑性的な流動特性による障害を防止
しながら有機質汚泥の醗酵、分解を促進するのである。Continuous stirring is not necessary in the fermentation of semi-solid substrates such as sludge, and continuous mechanical stirring tends to cause agglomeration and inhibits aerobic fermentation and decomposition. According to the structure of the oxidation equipment, the raw material sludge moves in an aerobic manner at each stage while being accompanied by an aerobic atmosphere due to air supply, and is further mixed and agitated appropriately as it falls from each stage to the lower stage. It promotes fermentation and decomposition of organic sludge while preventing problems caused by the plastic flow characteristics of raw sludge.
本考案の具体的装置について、その実施の1例を図面に
基づき説明すると、第1図以下に示すように、原料投入
口2より搬送機2′により送込まれる原料汚泥11が載
置されて移行していく移動式醗酵床3を水平に互に向き
を違えて複数段備えて醗酵室1を構成するのであって、
移動式醗酵床3は複数列の醗酵床構成列13を並列し、
これらの醗酵床構成列13,13は全部が一斉に一定の
ストローク前進し、次いで各醗酵床構成列13が1本又
は2本以上が前進したストロークだけ後退し更に残余の
醗酵床構成列13も同じような運動を行って何回かに分
けて全構成列13,13が元の位置に総べて回帰し、再
び全部が一斉に一定ストローク前進し、次いで何組かの
ブロックに分かれ、順次に全部が元の位置に回帰する動
作を反覆するような構造となすのである。An example of the implementation of the specific device of the present invention will be explained based on the drawings. As shown in FIG. The fermentation chamber 1 is constituted by a plurality of moving fermentation beds 3 arranged horizontally in different directions.
The mobile fermentation bed 3 has a plurality of fermentation bed configuration rows 13 arranged in parallel,
These fermentation bed configuration rows 13, 13 all move forward by a certain stroke at the same time, and then each fermentation bed configuration row 13 moves back by the stroke that one or more fermentation bed configuration rows 13 advanced, and then the remaining fermentation bed configuration rows 13 also move back. The same movement is carried out several times, and all the constituent rows 13, 13 return to their original positions, and then all of them move forward by a certain stroke at the same time, and then they are divided into several sets of blocks, and one after another. The structure is such that everything returns to its original position repeatedly.
そして同様な構造を有して、同様な機能を営む移動式醗
酵床3を1段ごとに対向するように複数段設置すること
により載置される原料汚泥を最上段より最下段へと円滑
に移送し得るのである。Then, by installing multiple stages of mobile fermentation beds 3 having the same structure and performing the same function so that each stage faces each other, the loaded raw material sludge can be smoothly transferred from the top stage to the bottom stage. It can be transported.
まず投入用搬送機2′から醗酵室1内に供給された原料
汚泥11は、最上段の移動式醗酵床3に1〜2mの積層
厚さに敷きつめられ、かきならし装置5で一定の層厚に
保ち、過度の層厚により圧迫緊密化する懸念をなくして
いる。First, the raw material sludge 11 supplied into the fermentation chamber 1 from the feeding conveyor 2' is spread on the uppermost movable fermentation bed 3 to a layer thickness of 1 to 2 m, and the leveling device 5 is used to flatten it into a certain layer. It is kept thick and eliminates the concern of pressure and tightness due to excessive layer thickness.
移動式醗酵床3上の原料汚泥11は、醗酵床構成列駆動
装置4の駆動により上記のような運動をする移動式醗酵
床3上をゆっくりと横方向に進み、移動式醗酵床3の先
端まで移行し、同時にこの移行中の全時間にわたり移動
式醗酵床3を形成する各醗酵床構成列13に設けられた
散気孔7より吐出される空気により好気性雰囲気となり
汚泥中の微生物は原料汚泥を培地とする好気性醗酵を盛
に営むのであり、また移動式醗酵床3への空気の供給は
、各構成列ごとに給気孔8へ可撓チューブ等を介して送
気すれば至便である。The raw material sludge 11 on the mobile fermentation bed 3 slowly moves laterally on the mobile fermentation bed 3, which moves as described above by the drive of the fermentation bed configuration train drive device 4, until it reaches the tip of the mobile fermentation bed 3. At the same time, during the entire time during this transition, the air discharged from the aeration holes 7 provided in each fermentation bed configuration row 13 forming the mobile fermentation bed 3 creates an aerobic atmosphere, and the microorganisms in the sludge become raw material sludge. Aerobic fermentation is actively carried out using the fermentation medium as a medium, and it is most convenient to supply air to the mobile fermentation bed 3 by supplying air to the air supply holes 8 in each constituent row through flexible tubes or the like. .
移動式醗酵床3上において、原料汚泥の積層厚さを一定
に保つためには、投入部又は落下受取部においては回転
式のかきならし装置5を設備すると共に、当該法先端で
は原料汚泥のドカ落ちを防ぎ汚泥の安息角以上の状態で
も、その下段の床において一定の積層厚さが保たれるよ
うにするために回転式のかき落し装置6を設備し、これ
により原料汚泥の崩れ落ちを防ぐと共に一定量をコンス
タントに落下せしめ、駆動装置4による機能に見合った
量で、順次に下の段へと原料汚泥を落下させる。In order to keep the layered thickness of the raw material sludge constant on the mobile fermentation bed 3, a rotary leveling device 5 is installed at the input section or the falling receiving section, and at the tip of the method, the layered thickness of the raw material sludge is A rotary scraping device 6 is installed to prevent the raw material sludge from falling down and to maintain a constant layer thickness on the lower floor even when the angle of repose of the sludge is exceeded. The raw material sludge is prevented from falling constantly, and the raw material sludge is caused to fall to the lower stage in an amount commensurate with the function of the drive device 4.
このようにして原料汚泥は最上段の移動式醗酵床から逐
次下の段に移行し、最下段に至るまでには通気と適度な
反転、攪拌又は混合により培地としては好条件のものと
なり醗酵、分解が促進され良好な堆肥となるのである。In this way, the raw material sludge is transferred from the top mobile fermentation bed to the lower stages one by one, and by the time it reaches the bottom stage, it has become suitable as a medium due to aeration, appropriate inversion, stirring, or mixing, and fermentation. This accelerates decomposition and makes good compost.
生成した堆肥は排出用搬送機10により醗酵室1外へ送
り出される。The generated compost is sent out of the fermentation chamber 1 by a discharge conveyor 10.
醗酵室1内で生ずる生成ガス及び余剰空気は各段ごとに
設けられた排気口9より排気し、この排気に関連して醗
酵室1内の温度を調整し得ることも本考案装置の有利な
点である。Another advantage of the device of the present invention is that the produced gas and surplus air generated in the fermentation chamber 1 are exhausted through the exhaust ports 9 provided in each stage, and the temperature within the fermentation chamber 1 can be adjusted in relation to this exhaust. It is a point.
このような実施の1例にみるごとく、原料汚泥を移動式
醗酵床上に好気的雰囲気のもとで積層し、且つその醗酵
床を縦方向に多段構築することにより、上段から下段へ
の移行時の適度な反転に伴う攪拌混合と各股上における
平静的な好気性醗酵条件とにより、在来の野積み又はコ
ンベアによる強制攪拌等に比較して省力化され或いはコ
ンパクトに装置化され同時に高速堆肥化をもたらすこと
ができるのである。As seen in one example of such implementation, raw material sludge is layered on a mobile fermentation bed in an aerobic atmosphere, and the fermentation bed is constructed in multiple stages in the vertical direction, thereby making it possible to transfer from the upper stage to the lower stage. Due to the agitation and mixing associated with appropriate reversal of the time and the static aerobic fermentation conditions at each rise, compared to conventional open piling or forced stirring using a conveyor, it is labor-saving or compact, and at the same time can be composted at high speed. It is possible to bring about change.
移動式醗酵床3を形成する醗酵床構成列13は、複数列
が並列しこれらが前記のような一斉前進又はグループご
との回帰を反復し原料汚泥を醗酵床の先端に向って移行
させるのであるが、この醗酵床構成列13の駆動装置4
としては各構成列ごとに油圧シリンダ、空気圧シリンダ
、電動シリンダ又は複数列全体の同軸カム機構ユニット
等を用いることにより円滑に運転をすることができる。The fermentation bed configuration rows 13 forming the mobile fermentation bed 3 are a plurality of rows in parallel, and these rows move forward all at once or repeat the regression for each group as described above, thereby moving the raw material sludge toward the tip of the fermentation bed. However, the drive device 4 of this fermentation bed configuration row 13
Therefore, smooth operation can be achieved by using a hydraulic cylinder, a pneumatic cylinder, an electric cylinder, or a coaxial cam mechanism unit for the entire plurality of rows for each constituent row.
各々の醗酵床構成列13の本体フレーム14は内部が中
空で、その上にこれと連通して複数個の散気”JL7,
7を備えた散気装置15を設け、この中空の本体フレー
ムには給気孔8を備えた空気供給管16と接続し、更に
この空気供給管16は醗酵床構成列駆動装置4の駆動軸
と連結するのであって、特にこの連結部は、醗酵床の移
動に不測の過負荷が生じた場合に駆動装置を保護し、又
は原料汚泥による偏荷重があって軸線不整が生じた等の
場合でも円滑に駆動力を伝達し得るように自在継手17
により連結することが望ましい。The main body frame 14 of each fermentation bed configuration row 13 has a hollow interior, and a plurality of air diffusers "JL7,
An air diffuser 15 equipped with an air diffuser 7 is provided, and this hollow main body frame is connected to an air supply pipe 16 equipped with an air supply hole 8. Furthermore, this air supply pipe 16 is connected to the drive shaft of the fermentation bed configuration row drive device 4. In particular, this connection part protects the drive device in the event of an unexpected overload during the movement of the fermentation bed, or in the case of an uneven load due to raw material sludge that causes axis misalignment. Universal joint 17 is used to smoothly transmit driving force.
It is desirable to connect by.
そして、醗酵に必要な空気は各醗酵床構成列ごとに送風
機及び可撓性の配管(いずれも図示せず)を経由して給
気孔8に供給され空気供給管16を通って中空の構成列
本体フレーム14中に導入され、散気装置15の散気孔
7より原料汚泥中に送気される。The air necessary for fermentation is supplied to the air supply hole 8 for each row of fermentation beds via a blower and flexible piping (none of which are shown), and then passes through the air supply pipe 16 to the hollow row of rows. The air is introduced into the main body frame 14 and sent into the raw material sludge through the air diffuser holes 7 of the air diffuser 15.
移動式醗酵床3は醗酵室1本体の構造支保も兼ねる支持
フレーム19によって支えられており、この支持フレー
ム19の上を駆動装置4により前後に往復運動を行うの
であり、この往復運動を円滑になすために各醗酵床構成
列13,13の本体フレーム14.14と支持フレーム
19との間にはスライドシュー18を装着するのである
。The movable fermentation bed 3 is supported by a support frame 19 that also serves as structural support for the main body of the fermentation chamber 1, and is reciprocated back and forth on this support frame 19 by a drive device 4. In order to achieve this, a slide shoe 18 is installed between the main frame 14, 14 and the support frame 19 of each fermentation bed configuration row 13, 13.
第4図は移動式醗酵床を形成する各構成列の動作を示す
説明図であり、この実施例では構成列が5本の場合を例
示しているが、醗酵室の規模、原料汚泥の性状等により
5本に限定されることなく必要に応じてその本数は最適
のものとなし得ることは勿論である。FIG. 4 is an explanatory diagram showing the operation of each constituent column forming a mobile fermentation bed. In this example, the case where there are five constituent columns is illustrated, but the scale of the fermentation chamber and the properties of the raw material sludge It goes without saying that the number is not limited to five, but can be set to an optimum number as necessary.
各構成列は説明図のごとく、動作■、動作II、動作I
II及び動作IVの4つの動作で1サイクルを構成し、
このサイクルを繰りかえすことにより原料汚泥を移動式
醗酵床の先端まで、一途に汚泥に無理な機械力を及ぼす
ことなくゆっくりと平静的に移行させることができる。Each configuration column is as shown in the explanatory diagram: action ■, action II, action I.
One cycle consists of four operations, II and IV,
By repeating this cycle, the raw material sludge can be slowly and calmly transferred to the tip of the mobile fermentation bed without applying excessive mechanical force to the sludge.
各動作の説明のために各醗酵床構成列に45口。45 bottles in each fermentation bed configuration row for explanation of each operation.
ハ、二、ホの符号を与えるものとすれば、動作Iでは先
づ両端のイとホとの構成列を所定のストロークで後退さ
せるが、このとき汚泥は分割された醗酵床の少部分のみ
の動きのため醗酵床上全体の汚泥体は後退する構成判面
と汚泥体底面との間に関しては滑りが生じて汚泥体は動
かずそのままの位置を保っている。Assuming that the signs C, 2, and E are given, in operation I, first, the constituent rows A and E at both ends are retreated with a predetermined stroke, but at this time, the sludge is collected only in a small part of the divided fermentation bed. Due to this movement, the entire sludge body on the fermentation bed slips between the receding constituent surface and the bottom surface of the sludge body, and the sludge body remains in the same position without moving.
次に動作IIでは口と二の構成列を所定のストロークで
後退させるのであり、このときも同様に汚泥体は動かな
い。Next, in operation II, the opening and second constituent rows are moved back by a predetermined stroke, and the sludge body does not move at this time as well.
更に動作IIIで残ったへの構成列を所定のストローク
で後退させても同様に汚泥体は動かない。Furthermore, even if the remaining constituent rows are moved back by a predetermined stroke in operation III, the sludge body does not move in the same way.
而して動作IVに至ってイ、o、ハ、二、ホの5本の醗
酵床構成列を同時に所定ストロークだけ一斉に前進させ
て、動作■が始まる直前の位置に各醗酵床構成列を回帰
させると、このときには汚泥体は醗酵床全体が動くため
に、滑りを生ずる部分がなく全汚泥体は移動式醗酵床に
載って所定ストローク分だけ前方へ移行させることがで
きるのであり、このストロークは約100〜300 m
mとなすのが実用上好ましい。Then, in operation IV, the five fermentation bed configuration rows A, O, C, 2, and E are simultaneously advanced by a predetermined stroke, and each fermentation bed configuration row is returned to the position immediately before the start of operation (■). At this time, since the entire fermentation bed moves, the entire sludge body is placed on the movable fermentation bed and can be moved forward by a predetermined stroke, and this stroke is Approximately 100-300 m
Practically preferred is m.
本考案によれば有機質汚泥の高速堆肥化処理において、
好気的雰囲気のもとで、汚泥の物理的特性による障害が
生ずることなく醗酵、分解が促進され、きわめて能率よ
く処理を行うことができるのであって、本考案の有機汚
泥の堆肥化装置は、(a) 縦形式に汚泥層を積層し
移行させていくことにより装置の占める用地面積が少な
くてすむ。According to the present invention, in high-speed composting treatment of organic sludge,
Under an aerobic atmosphere, fermentation and decomposition are promoted without any problems caused by the physical characteristics of sludge, and processing can be carried out extremely efficiently. (a) By stacking and transferring sludge layers in a vertical manner, the land area occupied by the equipment can be reduced.
(b) 無理な機械的攪拌を行わないため、汚泥の団
塊化や極端な微細化が生ぜず、均質で好気的な雰囲気の
もとての醗酵が促進される。(b) Since forced mechanical stirring is not performed, the sludge does not form into lumps or become extremely fine, and fermentation is promoted in a homogeneous and aerobic atmosphere.
(C)適度な汚泥積層厚さにて堆積することで、圧迫緊
密化を防止し、堆積汚泥の中間層部での水蒸気の凝縮が
起らず、醗酵の不均質が生じない。(C) By depositing the sludge with an appropriate layer thickness, pressure compaction is prevented, water vapor condensation does not occur in the middle layer of the deposited sludge, and non-uniform fermentation does not occur.
(d) 各段ごとの通気のため、吹気圧が低くてすみ
、通気むらを生じない。(d) Because each stage is ventilated, the blowing pressure is low and uneven ventilation does not occur.
(e)各段ごとで醗酵過程に合せた送気量調節が可能で
ある。(e) It is possible to adjust the amount of air supplied to each stage according to the fermentation process.
(f) 各段ごとで醗酵床の送り速度が調節でき、醗
酵過程に合せた滞留日数がとれる。(f) The feeding speed of the fermentation bed can be adjusted for each stage, and the residence time can be adjusted to suit the fermentation process.
(g) 醗酵室内での被処理汚泥の短絡が起らず、生
成堆肥も品質の安定したものが得られる。(g) Short-circuiting of the sludge to be treated in the fermentation chamber does not occur, and the quality of the produced compost is stable.
(h) 駆動が緩やかであるため機械的に安定してい
る。(h) It is mechanically stable because the drive is gradual.
(i) 醗酵室が殆んど密閉構造であるため、臭気の
飛散がなく二次公害を生ずる懸念がない。(i) Since the fermentation chamber has a nearly closed structure, there is no scattering of odors and there is no concern about secondary pollution.
(j)占有場所が短形となるため、多数設置する場合に
も敷地を有効に利用できる。(j) Since the occupied space is rectangular, the site can be used effectively even when a large number of units are installed.
等の利点ならびに効果を有しており、本考案は叙上の実
施例の1例に限定されることはなく、これらから導かれ
る変形又は応用等はすべて本考案の技術的思想に包含さ
れるものであることはいうまでもない。The present invention is not limited to one example of the embodiment described above, and all modifications or applications derived from these are included in the technical idea of the present invention. Needless to say, it is a thing.
第1図は本考案の方法に基づく装置の1実施例を示す縦
断説明図、第2図は移動式醗酵床部分の平面図、第3図
は同じく側面図、第4図は移動式醗酵床の動作状態を4
つに区分して示す説明図である。
1・・・・・・醗酵室、3・・・・・・移動式醗酵床、
4・・・・・・醗酵床構成列駆動装置、5・・・・・・
かきならし装置、6・・・・・・かき落し装置、7・・
・・・・散気孔、8・・・・・・給気孔、9・・・・・
・排気口、11・・・・・・原料汚泥、13・・・・・
・醗酵床構成列、14・・・・・・構成列本体フレーム
、15・・・・・・散気装置、16・・・・・・空気供
給管、17・・・・・・自在継手、18・・・・・・ス
ライドシュー、19・・・・・・支持フレーム。Fig. 1 is a longitudinal cross-sectional view showing one embodiment of the apparatus based on the method of the present invention, Fig. 2 is a plan view of the movable fermentation bed, Fig. 3 is a side view, and Fig. 4 is the movable fermentation bed. The operating status of 4
FIG. 1... Fermentation room, 3... Mobile fermentation bed,
4...Fermentation bed configuration train drive device, 5...
Scraping device, 6... Scraping device, 7...
... air diffuser hole, 8... air supply hole, 9...
・Exhaust port, 11... Raw material sludge, 13...
・Fermentation bed configuration row, 14...Configuration row main body frame, 15...Air diffuser, 16...Air supply pipe, 17...Universal joint, 18...Slide shoe, 19...Support frame.
Claims (1)
させて堆肥となす装置において、適宜の材料で構築され
上部には原料汚泥投入口を、下部には生成堆肥の排出用
搬送手段を偏見、また中間部には適当数の排気口を設け
た醗酵室内に、複数の醗酵床構成列を並列させて形成し
た移動式醗酵床を相対向する壁面より交互に水平な片持
式に突出させて、縦方向に少くとも二段以上の適当な段
数設けると共に、これらの移動式醗酵床を形成するそれ
ぞれ複数の醗酵床構成列にはいずれも空気を吐出する散
気機構を附帯させ、更に個々の醗酵床構成列には駆動装
置を装着して一定のストローク前進又は後退を所要速度
で行なうことを可能とし、これらの移動式醗酵床を形成
する醗酵床構成列が一定のストロークについて一斉に揃
って前進し、然る後いくつかのグループごとに何回かに
分かれて順次後退するような制御機構を設け、各移動式
醗酵床ごとに投入部若しくは落下受取部に回転式かきな
らし装置を、又先端部に回転式かき落し装置を配設した
構造となし、醗酵の進捗に随って原料汚泥を好適な積層
厚に保つ構成としたことを特徴とする有機質を含んだ汚
泥の堆肥化装置。A device that ferments and decomposes sludge containing organic matter in an aerobic atmosphere to produce compost.It is constructed of suitable materials, has a raw material sludge input port in the upper part, and a transport means for discharging the produced compost in the lower part. In addition, in a fermentation chamber with an appropriate number of exhaust ports in the middle, movable fermentation beds formed by aligning multiple rows of fermentation beds are placed horizontally cantilevered alternately from opposing walls. An appropriate number of protruding stages, at least two or more stages, are provided in the longitudinal direction, and each of the plurality of fermentation bed configuration rows forming these mobile fermentation beds is provided with an aeration mechanism for discharging air, Furthermore, each row of fermentation beds is equipped with a drive device to enable it to move forward or backward in a fixed stroke at the required speed, so that the rows of fermentation beds forming these mobile fermentation beds can be moved simultaneously for a fixed stroke. A control mechanism is provided so that the fermentation bed moves forward in unison, and then moves back in sequence in several groups. The apparatus has a structure in which a rotary scraping device is disposed at the tip, and the material sludge is kept at a suitable layer thickness as the fermentation progresses. Composting equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6705883U JPS5925866Y2 (en) | 1983-05-04 | 1983-05-04 | Composting equipment for sludge containing organic matter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6705883U JPS5925866Y2 (en) | 1983-05-04 | 1983-05-04 | Composting equipment for sludge containing organic matter |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59439U JPS59439U (en) | 1984-01-05 |
JPS5925866Y2 true JPS5925866Y2 (en) | 1984-07-28 |
Family
ID=30197264
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6705883U Expired JPS5925866Y2 (en) | 1983-05-04 | 1983-05-04 | Composting equipment for sludge containing organic matter |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5925866Y2 (en) |
-
1983
- 1983-05-04 JP JP6705883U patent/JPS5925866Y2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS59439U (en) | 1984-01-05 |
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