JPH06199586A - Method for composting organic sludge and device therefor - Google Patents

Method for composting organic sludge and device therefor

Info

Publication number
JPH06199586A
JPH06199586A JP4361473A JP36147392A JPH06199586A JP H06199586 A JPH06199586 A JP H06199586A JP 4361473 A JP4361473 A JP 4361473A JP 36147392 A JP36147392 A JP 36147392A JP H06199586 A JPH06199586 A JP H06199586A
Authority
JP
Japan
Prior art keywords
organic sludge
fermentation
sludge
temperature
organic
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
JP4361473A
Other languages
Japanese (ja)
Inventor
Eiko Hayashi
栄港 林
Taijirou Morita
泰治郎 森田
Muneyoshi Obara
宗義 小原
Toshinori Inoue
敏則 井上
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.)
HIGASHI NIPPON YUUGOU KK
Original Assignee
HIGASHI NIPPON YUUGOU KK
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 HIGASHI NIPPON YUUGOU KK filed Critical HIGASHI NIPPON YUUGOU KK
Priority to JP4361473A priority Critical patent/JPH06199586A/en
Publication of JPH06199586A publication Critical patent/JPH06199586A/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

Landscapes

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

Abstract

PURPOSE:To shorten the time in producing org. manure by fermentation of an org. sludge. CONSTITUTION:The org. sludge having 60-75% water content is made to the small lump having 3-20mm max. diameter, and the lump is housed into a fermentation tank provided with a feed/exhaust device and a heating device, and heated up to >=40 deg.C to promote the start of fermentation, then, the oxygen content in the fermentation tank is maintained in 5-20% and the temp. of the org. sludge is maintained at 55-65 deg.C, and after fermentation is almost finished, the org. sludge is dryed and the compost as a product is obtained. In this way, the fermentation is finished for the period one several that of the conventional method and a perfectly fermented org. manure is obtained.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は下水汚泥、生ゴミ、家畜
糞尿、油絞りカス等の有機性廃棄物(以下有機汚泥と記
す)をコンポスト(堆肥)化する方法とその装置に関す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and apparatus for composting organic waste (hereinafter referred to as organic sludge) such as sewage sludge, raw garbage, livestock excrement, and oil squeezing waste. .

【0002】[0002]

【従来の技術】上記有機汚泥、特に下水汚泥や生ゴミ等
は年々増え続けており、これらを何らかの形で処理する
ことは急務となっている。そこで従来このような有機汚
泥は焼却して灰とし容積を圧縮して廃棄場所に廃棄し
たり、高温で処理してレンガやタイル等を製造した
り、又は微生物を利用して発酵させ堆肥化して有機肥
料として利用する等が行なわれていた。
2. Description of the Related Art The organic sludge, particularly sewage sludge and raw garbage, has been increasing year by year, and it is an urgent need to treat them in some form. Therefore, conventionally, such organic sludge is incinerated into ash to reduce the volume and to be disposed of at a disposal site, or treated at high temperature to manufacture bricks and tiles, or fermented by using microorganisms to be composted. It was used as an organic fertilizer.

【0003】しかしながら上記の処理では廃棄するこ
とに変りはなく、いずれ廃棄場所の問題が顕在化してく
る問題があり、またの処理はその設備が大がかり且つ
高価であることから得られるレンガ等も高価であってと
ても採算が採れないものであった。
However, in the above treatment, disposal is still the same, and there is a problem that the problem of the disposal site will become apparent, and in the other treatment, the bricks and the like obtained are expensive because the equipment is large and expensive. But it was very unprofitable.

【0004】そこで比較的簡単な方法としての処理方
法が注目されており、種々の検討が行なわれている。そ
の最も簡単な方法としては、従来より農家などで行なわ
れている方法で、有機汚泥を野積みにして自然発酵を行
なわせるものであるが、数カ月もの長期間にわたるため
上記大量の有機汚泥を処理するには現実的でない。そこ
でこの方式を大規模化して大型の発酵槽の中にこれら有
機汚泥を積み上げ、積極的に微生物を添加し、発酵中の
有機汚泥を機械的に攪拌したりする装置や、又は発酵槽
内に積み上げた有機汚泥中に給気管を設置して微生物の
発酵を活発化させる試み等が実施されているが、それで
も発酵の完了までには2カ月程度必要であった。しかも
発酵の終了時点は作業者の感に頼るものであるため発酵
が完全に終わって完熟有機肥料となっていない場合もあ
るといった問題もあった。
Therefore, attention has been paid to a processing method as a relatively simple method, and various studies have been made. The simplest method is a method that has been conventionally used by farmers, etc., in which organic sludge is piled up in a field and naturally fermented. Unrealistic to do. Therefore, this method is scaled up to stack these organic sludges in a large fermentation tank, actively add microorganisms, mechanically stir the organic sludge during fermentation, or in the fermentation tank. Attempts have been made to activate the fermentation of microorganisms by installing an air supply pipe in the stacked organic sludge, but it still took about two months to complete the fermentation. In addition, there is also a problem that the fermentation may not be completed and it may not be a fully-ripened organic fertilizer because the end of fermentation depends on the feeling of the operator.

【0005】[0005]

【課題を解決するための手段】本発明はこれに鑑み種々
検討の結果、有機汚泥を発酵槽に投入する前段階で短時
間発酵が可能なように有機汚泥に前処理を施しておくこ
とにより、従来と比較して数分の一の期間で完熟有機肥
料を製造できる有機汚泥のコンポスト化方法とその装置
を開発したものである。
As a result of various investigations in view of the above, the present invention provides a pretreatment of organic sludge so that fermentation can be performed for a short time before the organic sludge is put into a fermenter. , A method of composting organic sludge and a device therefor capable of producing a fully-ripened organic fertilizer in a fraction of a time compared with the conventional method.

【0006】即ち本発明の方法は、含水率60〜75%の有
機汚泥を最大径が3〜20mmの小塊とし、該小塊を給排気
装置と加熱装置を備えた発酵槽に収納して加熱装置によ
り有機汚泥の温度を40℃以上に昇温して発酵開始を促進
させた後給排気装置により発酵槽内の酸素量を5〜20%
に、同時に有機汚泥の温度を55〜65℃に保持し、発酵が
ほぼ終了した後にその有機汚泥を乾燥して製品コンポス
トを得ることを特徴とするものである。
That is, according to the method of the present invention, organic sludge having a water content of 60 to 75% is made into a small mass having a maximum diameter of 3 to 20 mm, and the small mass is stored in a fermentation tank equipped with an air supply / exhaust device and a heating device. The heating device raises the temperature of the organic sludge to 40 ° C or more to accelerate the start of fermentation, and then the supply / exhaust device increases the oxygen content in the fermentation tank to 5-20%.
At the same time, the temperature of the organic sludge is kept at 55 to 65 ° C, and after the fermentation is almost completed, the organic sludge is dried to obtain a product compost.

【0007】そしてこの本発明において、有機汚泥を圧
延して圧延方向に断続するのしいか状とし、これを圧延
方向に対して横方向に細断することにより小塊とした
り、小塊化した有機汚泥に製品コンポスト、有機汚泥の
焼却灰、硬質の通過性材料の1種以上を単に分散した状
態に混ぜて発酵槽に収納したり、小塊化した有機汚泥を
発酵槽内に収納するに際して、該有機汚泥の最大積み高
さを50cm以内とした段を複数段としたり、又は発酵終了
後の乾燥を、発酵槽内にてその給排気装置及び加熱装置
を作動させて行なうのは有効である。
According to the present invention, the organic sludge is rolled into a squid-like shape which is intermittent in the rolling direction, and the sludge is shredded in the lateral direction with respect to the rolling direction to form small lumps or lumps. When storing product compost, incinerator ash of organic sludge, or one or more of hard permeable materials in an organic sludge in a simply dispersed state and storing it in a fermentation tank, or when storing small-sized organic sludge in a fermentation tank It is effective to use a plurality of stages with the maximum stacking height of the organic sludge within 50 cm, or to perform drying after completion of fermentation by operating the air supply / exhaust device and heating device in the fermentation tank. is there.

【0008】また本発明の装置は、含水率60〜75%の有
機汚泥を圧延して圧延方向に断続するのしいか状とする
少なくとも1対の回転圧延ローラーと、該のしいか状の
有機汚泥を圧延方向に対して横方向に細断することによ
り最大径が3〜20mmの小塊とする横方向に凹凸を形成し
て互いに噛み合う一対の回転溝ローラーとを備えた前処
理装置を有し、さらに小塊化した有機汚泥を50cm以内の
高さに積み上げた段を複数段設置し、かつ積み上げた有
機汚泥を40℃以上に加熱して有機汚泥の発酵開始を促進
させる加熱装置を有し、さらに該積み上げた有機汚泥内
に空気を流通させる給排気装置と、該有機汚泥の温度を
測定する温度センサーと、雰囲気中の酸素濃度を測定す
る酸素濃度計とを備えて雰囲気の酸素濃度を5〜20%、
有機汚泥の温度を55〜65℃に上記給排気装置により自動
調節する発酵槽を有することを特徴とするものであり、
この際給排気装置として排気側を吸引することにより発
酵槽内に給気するのがより効果が大きい。
Further, the apparatus of the present invention comprises at least one pair of rotary rolling rollers for rolling organic sludge having a water content of 60 to 75% so as to be intermittent in the rolling direction, and the organic matter in the form of watermelon. It has a pretreatment device equipped with a pair of rotary groove rollers that mesh with each other by cutting the sludge laterally with respect to the rolling direction to form small pieces with a maximum diameter of 3 to 20 mm and forming unevenness in the lateral direction. In addition, there are multiple stages of stacked organic sludge in a height of 50 cm or less, and there is a heating device that heats the stacked organic sludge to 40 ° C or higher to accelerate the start of fermentation of the organic sludge. In addition, an air supply / exhaust device for circulating air in the stacked organic sludge, a temperature sensor for measuring the temperature of the organic sludge, and an oxygen concentration meter for measuring the oxygen concentration in the atmosphere are used to provide the oxygen concentration in the atmosphere. 5-20%,
It is characterized by having a fermentation tank that automatically adjusts the temperature of the organic sludge to 55 to 65 ° C by the air supply and exhaust device.
At this time, it is more effective to supply air into the fermentation tank by sucking the exhaust side as a supply / exhaust device.

【0009】[0009]

【作用】上記のように本発明の対象となる有機汚泥の含
水率をあらかじめ60〜75%とするのは、コンポスト化を
実行する好気性の微生物が最も活発に活動でき、さらに
有機汚泥を小塊化処理しやすい水分量だからである。
As described above, the water content of the organic sludge targeted by the present invention is set to 60 to 75% in advance so that the aerobic microorganisms that carry out composting can be the most active and the organic sludge can be reduced to a small amount. This is because the water content is easy to agglomerate.

【0010】またこのような有機汚泥を最大径が3〜20
mmの小塊とするのは、この大きさであれば好気性微生物
が有機汚泥を均一に且つ万遍なく発酵させることがで
き、従って完熟肥料を短時間で得ることができるからで
ある。そして小塊の大きさが3mm 未満では発酵槽内に積
み上げた際に空気の流通が悪くなってしまい、好気性微
生物による発酵が充分進行しなくなってしまい、発酵終
了まで長時間を要してしまう。またその大きさが20mmを
越えると粒状体の内部まで充分発酵が進行しなくなり、
やはり発酵終了まで長時間必要となる。なお小塊の形状
としては小球形、小偏平形又は不定形等どのような形で
もよく、それらの個々の最大の差し渡し寸法が3〜20mm
であればよいが、望ましくは5〜10mm程度がより良好で
ある。
The maximum diameter of such organic sludge is 3 to 20.
The reason for making a small lump of mm is that the aerobic microorganisms can ferment the organic sludge uniformly and evenly if it has this size, and thus a mature fertilizer can be obtained in a short time. And if the size of the nodules is less than 3 mm, the air flow will be poor when piled up in the fermentor, fermentation by aerobic microorganisms will not progress sufficiently, and it will take a long time to complete the fermentation. . If the size exceeds 20 mm, fermentation will not proceed to the inside of the granules,
After all, it takes a long time to complete the fermentation. The shape of the small lumps may be any shape such as a small sphere, a small flat shape, or an indeterminate shape, and the maximum crossover dimension of each of them is 3 to 20 mm.
However, about 5 to 10 mm is more preferable.

【0011】そしてこのような小塊を得るのには、有機
汚泥を圧延して圧延方向に断続するのしいか状とする一
対の回転圧延ローラーと、該のしいか状の有機汚泥を圧
延方向に対して横方向に細断する横方向に凹凸を形成し
て互いに噛み合う一対の回転溝ローラーとからなる前処
理装置を用いる。
In order to obtain such small lumps, a pair of rotary rolling rollers that rolls the organic sludge into a squid-like shape and is intermittent in the rolling direction, and the squid-like organic sludge in the rolling direction. On the other hand, a pretreatment device is used which is composed of a pair of rotary groove rollers which are formed by forming unevenness in the lateral direction by shredding in the lateral direction and meshing with each other.

【0012】即ち図1に示すように表面が平滑又は粗面
で互いに10mm程度の間隙(図中A)を有する一対の回転
圧延ローラー(1)で、有機汚泥を圧延する。この圧延
された有機汚泥は圧延方向にところどころ切れ目の入っ
たのしいか状有機汚泥(2)となる。次に上記回転圧延
ローラー(1)の下方に、横方向に10mm程度の幅(図中
B)の凹凸を設け、これら凹凸が図2のように互いに噛
み合っている回転溝ローラー(3)を設置しておき、こ
の溝ローラー(3)に上記のしいか状有機汚泥(2)を
供給する。この回転溝ローラー(3)によりのしいか状
有機汚泥(2)は横方向に細断され、該ローラー(3)
から排出された際にはそれ自身の切れ目及び自重により
小塊となって落下する。
That is, as shown in FIG. 1, the organic sludge is rolled by a pair of rotary rolling rollers (1) having smooth or rough surfaces and having a gap of about 10 mm (A in the figure). This rolled organic sludge becomes squid-like organic sludge (2) with some breaks in the rolling direction. Next, below the above-mentioned rotary rolling roller (1), unevenness having a width of about 10 mm (B in the figure) is provided in the lateral direction, and a rotating groove roller (3) in which these unevenness meshes with each other as shown in FIG. 2 is installed. Then, the squid-like organic sludge (2) is supplied to the groove roller (3). The squid-like organic sludge (2) is laterally shredded by the rotating groove roller (3), and the roller (3)
When it is discharged from, it breaks into small pieces due to its own cut and its own weight.

【0013】次にこの小塊を発酵槽に収納するが、この
とき同時に製品コンポスト、有機汚泥の焼却灰、硬質の
通気性材料を混入することもできる。このように製品コ
ンポストを一部混合することにより発酵を担う好気性微
生物を多量に添加することとなり、発酵が促進される。
また焼却灰は有機汚泥の水分量を調整するものであり、
硬質の通気性材料は小塊の有機汚泥を積み上げた際に内
部まで空気の流通を良好ならしめて発酵を促進させるた
めのものである。なおこの通気性材料としては、積み上
げた際に押し潰されないような硬質のもので、その大き
さは径が20mm以上のものが良好である。一例としては硬
質多孔プラスチックボール等があげられる。
Next, the small lumps are stored in a fermenter, but at the same time, product compost, incineration ash of organic sludge, and hard breathable material can be mixed. In this way, by partially mixing the product compost, a large amount of aerobic microorganisms responsible for fermentation are added, and fermentation is promoted.
In addition, incineration ash adjusts the water content of organic sludge,
The hard breathable material is for facilitating the fermentation by smoothing the air flow to the inside when a small amount of organic sludge is piled up. The breathable material is preferably a hard material that is not crushed when stacked and has a diameter of 20 mm or more. An example is a hard porous plastic ball.

【0014】発酵槽はその内部に空気の流通が良好にな
るように多数の穴の開いた板で作られた段を複数段設け
たものであり、さらにこの複数段を断熱性の外枠で覆っ
たものがよい。そして各段に積み上げる上記小塊の有機
汚泥はその積み高さを50cm以下とする。これが50cmを超
えると底部の小塊は重量で圧縮されて互いに密接・密着
し合ってより大きな塊となってしまい、空気が流通しず
らくなる。
The fermenter is provided with a plurality of stages made of a plate having a large number of holes so that the air can flow well inside the fermenter. The one covered is good. The small sludge of organic sludge stacked on each stage has a stacking height of 50 cm or less. If this exceeds 50 cm, the small lumps at the bottom are compressed by weight and come into close contact with each other to form larger lumps, making it difficult for air to flow.

【0015】また発酵槽の内部を加熱する装置としては
電気ヒーターやガスバーナーでもよいが、槽内を速く且
つ均一に加熱するため、ブロアーにより加熱空気を供給
し、同時に槽内雰囲気を攪拌できるようにするとより有
効である。さらに給排気装置としては、槽の天井部から
吸引し、同時に槽の下部あるいは底部から上記吸引力に
より外部空気を供給する方式のものが良好である。この
ように槽内を負圧として外部から空気を吸入すれば、槽
の隙間から有機汚泥の悪臭が外部に漏れるという不具合
がなくなり、環境衛生上も優れたものとなる。
An electric heater or a gas burner may be used as a device for heating the inside of the fermentation tank, but in order to heat the inside of the tank quickly and uniformly, heated air is supplied by a blower and at the same time the atmosphere in the tank can be stirred. It is more effective when set to. Further, as the air supply / exhaust device, it is preferable to use a system that sucks air from the ceiling of the tank and at the same time supplies external air from the bottom or bottom of the tank by the suction force. By sucking air from the outside with a negative pressure in the tank as described above, the problem that the malodor of the organic sludge leaks to the outside from the gap of the tank is eliminated, which is excellent in environmental hygiene.

【0016】次に発酵槽内雰囲気コントロールについて
説明する。前処理済の小塊状有機汚泥を発酵槽内の各段
に積み上げた後、加熱装置により積み上げた有機汚泥の
堆積物の温度を約45℃に昇温する。この昇温までの時間
は槽の大きさや加熱装置の容量等により異なるが、最長
24時間あれば十分である。この昇温によって微生物の活
動は活発となり発酵を開始する。この発酵により積み上
げた有機汚泥の温度は自然に上昇すると共に、発酵開始
により雰囲気中の酸素を消費するので雰囲気中の酸素濃
度は次第に低下する。
Next, the control of the atmosphere in the fermenter will be described. After stacking the pretreated small organic sludge on each stage in the fermenter, the temperature of the accumulated organic sludge deposits is raised to about 45 ° C by the heating device. The time until this temperature rise depends on the size of the tank and the capacity of the heating device, but
24 hours is enough. This temperature rise activates the activity of microorganisms and starts fermentation. The temperature of the organic sludge piled up by this fermentation naturally rises, and since oxygen in the atmosphere is consumed by the start of fermentation, the oxygen concentration in the atmosphere gradually decreases.

【0017】このとき最適発酵温度は約60℃であるが、
発酵が進むにつれて温度はさらに上昇し、堆積物の温度
が65℃を超えると発酵を担う好気性微生物の活動が急激
に低下してしまう。そこで、このときは給排気装置によ
り外気を導入して温度を60℃付近まで下げる。また雰囲
気の酸素濃度が5%未満になると、やはり微生物の発酵
が停滞してしまうのでこのときも給排気装置により外気
を導入して酸素濃度を上昇させる。このような温度と酸
素濃度との調整を同時に、かつ繰り返し実施することに
より、小塊状の有機汚泥の発酵は順調に進行する。なお
本発明によれば堆積物の温度が約60℃に上ってから発酵
の終了までの時間は約48時間である。
At this time, the optimum fermentation temperature is about 60 ° C.,
As the fermentation progresses, the temperature rises further, and when the temperature of the sediment exceeds 65 ° C, the activity of the aerobic microorganisms responsible for the fermentation suddenly decreases. Therefore, at this time, the outside air is introduced by the air supply / exhaust device to lower the temperature to around 60 ° C. Further, when the oxygen concentration in the atmosphere is less than 5%, fermentation of microorganisms is also stagnation. Therefore, also at this time, the outside air is introduced by the air supply / exhaust device to raise the oxygen concentration. By simultaneously and repeatedly adjusting such temperature and oxygen concentration, fermentation of the small sludge-like organic sludge proceeds smoothly. According to the present invention, the time from when the temperature of the sediment rises to about 60 ° C to the end of fermentation is about 48 hours.

【0018】そして発酵が終了すると堆積物の温度が60
℃付近から自然に低下してくるので、その時点で発酵の
終了した堆積物は乾燥工程に移す。なお乾燥は発酵槽内
で加熱装置と給排気装置とを同時に作動させて実施する
こともできるが、外部に取り出して独立の乾燥装置によ
り行なってもよい。本発明では発酵槽内での乾燥は最大
24時間行なえばよく、これにより完熟した製品コンポス
トが得られる。以上のように有機汚泥を原料として完熟
した有機肥料を製品化するまでは約4日あればよく、従
来に比べてはるかに短時間である。
When the fermentation is completed, the temperature of the sediment becomes 60
Since the temperature will naturally decrease from around 0 ° C, the fermented sediment at that point is transferred to the drying process. The drying can be carried out by operating the heating device and the air supply / exhaust device at the same time in the fermentation tank, but may be carried out by an external drying device. In the present invention, the maximum drying in the fermenter is
It only needs to be done for 24 hours, which results in a ripe product compost. As described above, it takes about 4 days to commercialize a fully-ripened organic fertilizer using organic sludge as a raw material, which is much shorter than in the past.

【0019】[0019]

【実施例】次に本発明を実施例によりさらに説明する。EXAMPLES The present invention will be further described with reference to examples.

【0020】含水率75〜85%とした下水汚泥を前記の前
処理装置により粒径10mm前後の小塊とした。そして含水
率15〜25%の汚泥焼却灰及び返送製品コンポスト、多孔
プラスチックボールを上記小塊に混ぜて全体の含水率が
60〜65%になるように調整した試料を表1に示すように
A〜Eの5種類作った。なお下水汚泥 100%の試料は、
所定の含水率60〜65%にまで乾燥するのが時間的費用的
に非常に困難なために採用しなかった。また市販の微生
物も促進剤として加えたが、微量であるため量としては
無視した。
Sewage sludge having a water content of 75 to 85% was made into small pieces having a particle size of about 10 mm by the above pretreatment device. Then, the sludge incineration ash with a water content of 15 to 25%, the returned product compost, and the porous plastic balls are mixed with the above-mentioned small lumps so that the total water content is
As shown in Table 1, five types of samples A to E were prepared so as to have a concentration of 60 to 65%. The sample of 100% sewage sludge is
It was not adopted because it is very difficult in terms of time and cost to dry it to a predetermined water content of 60 to 65%. A commercially available microorganism was also added as a promoter, but the amount was neglected because of its small amount.

【0021】[0021]

【表1】 [Table 1]

【0022】これら配合物の配合方法は表2の3種類と
し、また発酵槽内の初期の環境温度を10℃以下、25℃及
び45℃の3種類として、これらを表3のように組合わせ
てコンポスト化を実施した。なおこれら配合物が60℃に
達して発酵が活発化した後は配合物の温度は約60℃、か
つ槽内の酸素濃度は約5%となるように給排気装置を作
動させて調整した。
The blending method of these blends is the three types shown in Table 2, and the initial environmental temperature in the fermenter is 10 ° C or less, 25 ° C and 45 ° C, and these are combined as shown in Table 3. It was composted. After the temperature of these compounds reached 60 ° C and the fermentation was activated, the temperature of the compounds was adjusted to about 60 ° C and the oxygen concentration in the tank was adjusted to about 5% by operating the air supply / exhaust device.

【0023】[0023]

【表2】 [Table 2]

【0024】[0024]

【表3】 [Table 3]

【0025】このように条件を組み合わせて各配合形式
の配合物を発酵槽内に、底面の寸法が 1.5m角で積み高
さ約40cmとした段を棚状に7段積み上げて前記の条件で
発酵を行なわせ、それらの結果を表4〜表6に示す。
By combining the conditions as described above, the compound of each compounding type is piled up in a fermenter in the form of a shelf having seven steps with a bottom size of 1.5 m square and a stacking height of about 40 cm. Fermentation was performed and the results are shown in Tables 4-6.

【0026】[0026]

【表4】 [Table 4]

【0027】[0027]

【表5】 [Table 5]

【0028】[0028]

【表6】 [Table 6]

【0029】表中16Hr等の数字は、配合物を発酵槽内に
投入後配合物の温度が60℃に達するまでの時間を示し、
最終的に全体が良好な発酵状態の場合に(全体)と記
し、配合物の 1/3近くが嫌気性発酵と判断される場合に
(ムラ大)と記し、さらに目標としている好気性発酵
(60℃)に到達せず、いわゆる腐る状態になってしまっ
たものを(嫌気性発酵)と表記した。なお表中*は実施
条件以外の条件を表わし、また発酵の状態は目視および
臭いで判断した。
Numbers such as 16 Hr in the table indicate the time until the temperature of the compound reaches 60 ° C. after the compound is put into the fermenter.
Finally, when the whole is in a good fermentation state, it is described as (overall), and when approximately 1/3 of the formulation is judged to be anaerobic fermentation (mura is large), it is further described as the target aerobic fermentation ( Those that did not reach 60 ° C and became so-called rotten were described as (anaerobic fermentation). In addition, * in the table represents conditions other than the implementation conditions, and the state of fermentation was judged visually and by smell.

【0030】表より以下のことが明らかとなった。 均一に混ぜようとして、試料を人為的に攪拌し、又
は練り合わせると、通気性を良くするために小塊化細粒
化した試料が団塊状になり、配合方法としては最も悪
い。 小塊化された試料に、返送コンポストなど水分調節
及び発酵促進剤を振りかけてやる(単に分散した状態に
混ぜたもの)のが最も良い結果を与えた。 配合形式(添加物の多少)よりも環境温度による影
響が大きい。特に、48時間以内に60℃昇温が達成されな
いと好気性発酵へは移行しない。 初期の環境温度が微生物交代の生じる45度に保たれ
ておれば、16〜24時間で好気性発酵に移行し、その後は
60℃前後の試料温度を保つことができる。
The following is clear from the table. If the sample is artificially stirred or kneaded in an attempt to mix it uniformly, the sample that has been made into agglomerated and finely divided particles for improving air permeability becomes a nodule-like shape, which is the worst compounding method. The best results were obtained by sprinkling the agglomerated sample with water control and fermentation accelerators such as returning compost (simply mixed in a dispersed state). The effect of environmental temperature is greater than that of the compounding type (some additives). In particular, if the temperature rise of 60 ° C is not achieved within 48 hours, aerobic fermentation does not occur. If the initial environmental temperature is maintained at 45 degrees where microbial change occurs, it will shift to aerobic fermentation in 16 to 24 hours, and thereafter
The sample temperature around 60 ℃ can be maintained.

【0031】このように発酵槽内の初期環境温度が40℃
以上で、攪拌等をせずに混ぜた配合物であれば配合形式
に無関係に、発酵槽に投入してから18時間以内で発酵に
最適な60℃となり、さらに全体が良好な発酵状態となっ
て発酵が終了するまでの時間はいずれも48時間以内であ
った。
As described above, the initial environmental temperature in the fermenter is 40 ° C.
With the above, if it is a blended mixture without stirring, regardless of the blending format, the temperature will be 60 ° C, which is optimal for fermentation within 18 hours after being added to the fermenter, and the whole will be in a good fermentation state. The fermentation time was 48 hours or less in all cases.

【0032】[0032]

【発明の効果】このように本発明によれば、有機汚泥の
発酵時間が従来に比べて非常に短くなり、且つ完熟した
有機肥料が得られる。従って有機汚泥から堆肥を数日で
得ることが可能となったので、従来主として廃棄されて
いた有機性廃棄物の肥料としての利用が容易に実現でき
る等工業上顕著な効果を奏する。
As described above, according to the present invention, it is possible to obtain an organic fertilizer in which the fermentation time of the organic sludge is much shorter than in the conventional case and the organic fertilizer is fully ripe. Therefore, since compost can be obtained from the organic sludge within a few days, the industrially significant effect is achieved such that the organic waste that has been mainly discarded conventionally can be easily used as a fertilizer.

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

【図1】本発明に係る前処理装置の概略を示す斜視図で
ある。
FIG. 1 is a perspective view showing an outline of a pretreatment apparatus according to the present invention.

【図2】本発明に係る前処理装置の回転溝ローラーを示
す平面図である。
FIG. 2 is a plan view showing a rotary groove roller of the pretreatment device according to the present invention.

【符号の説明】[Explanation of symbols]

1 回転圧延ローラー 2 のしいか状有機汚泥 3 回転溝ローラー 1 rotary rolling roller 2 squid-like organic sludge 3 rotary groove roller

───────────────────────────────────────────────────── フロントページの続き (72)発明者 井上 敏則 埼玉県所沢市小手指町4丁目13番地の1 東日本融合株式会社内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Toshinori Inoue 1-13-4 Koteshi-cho, Tokorozawa, Saitama Prefecture East Japan Fusion Co., Ltd.

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 含水率60〜75%の有機汚泥を最大径が3
〜20mmの小塊とし、該小塊を給排気装置と加熱装置を備
えた発酵槽に収納して加熱装置により有機汚泥の温度を
40℃以上に昇温して発酵開始を促進させた後給排気装置
により発酵槽内の酸素量を5〜20%に、同時に有機汚泥
の温度を55〜65℃に保持し、発酵がほぼ終了した後にそ
の有機汚泥を乾燥して製品コンポストを得ることを特徴
とする有機汚泥のコンポスト化方法。
1. An organic sludge having a water content of 60 to 75% has a maximum diameter of 3
A small lump of ~ 20 mm is stored in a fermentation tank equipped with an air supply / exhaust device and a heating device, and the temperature of the organic sludge is controlled by the heating device.
After raising the temperature to 40 ° C or higher to accelerate the start of fermentation, the oxygen amount in the fermenter is kept at 5 to 20% by the air supply / exhaust device, and at the same time, the temperature of the organic sludge is kept at 55 to 65 ° C, and the fermentation is almost completed. After that, the organic sludge is dried to obtain a product compost, which is a method for composting an organic sludge.
【請求項2】 有機汚泥を圧延して圧延方向に断続する
のしいか状とし、これを圧延方向に対して横方向に細断
することにより小塊とする請求項1記載のコンポスト化
方法。
2. The composting method according to claim 1, wherein the organic sludge is rolled into a caustic shape that is intermittent in the rolling direction, and the sludge is shredded in the lateral direction with respect to the rolling direction to form small pieces.
【請求項3】 小塊化した有機汚泥に製品コンポスト、
有機汚泥の焼却灰、硬質の通気性材料の1種以上を単に
分散した状態に混ぜて発酵槽に収納する請求項1又は2
記載のコンポスト化方法。
3. A small-sized organic sludge, product compost,
The incineration ash of organic sludge and one or more hard breathable materials are simply mixed and stored in a fermenter.
The composting method described.
【請求項4】 小塊化した有機汚泥を発酵槽内に収納す
るに際して、該有機汚泥の最大積み高さを50cm以内とし
た段を複数段とする請求項1〜3のいずれか1項記載の
コンポスト化方法。
4. When storing the lumped organic sludge in a fermenter, a plurality of stages having a maximum stacking height of the organic sludge of not more than 50 cm are provided. How to compost.
【請求項5】 発酵終了後の乾燥を、発酵槽内にてその
給排気装置及び加熱装置を作動させて行なう請求項1〜
4のいずれか1項記載のコンポスト化方法。
5. Drying after completion of fermentation is performed by operating the air supply / exhaust device and heating device in the fermentation tank.
4. The composting method according to any one of 4 above.
【請求項6】 含水率60〜75%の有機汚泥を圧延して圧
延方向に断続するのしいか状とする少なくとも1対の回
転圧延ローラーと、該のしいか状の有機汚泥を圧延方向
に対して横方向に細断することにより最大径が3〜20mm
の小塊とする横方向に凹凸を形成して互いに噛み合う一
対の回転溝ローラーとを備えた前処理装置を有し、さら
に小塊化した有機汚泥を50cm以内の高さに積み上げた段
を複数段設置し、かつ積み上げた有機汚泥を40℃以上に
加熱して有機汚泥の発酵開始を促進させる加熱装置を有
し、さらに該積み上げた有機汚泥内に空気を流通させる
給排気装置と、該有機汚泥の温度を測定する温度センサ
ーと、雰囲気中の酸素濃度を測定する酸素濃度計とを備
えて雰囲気の酸素濃度を5〜20%、有機汚泥の温度を55
〜65℃に上記給排気装置により自動調節する発酵槽を有
することを特徴とする有機汚泥のコンポスト化装置。
6. At least one pair of rotary rolling rollers for rolling an organic sludge having a water content of 60 to 75% in the rolling direction and intermittently in the rolling direction, and the water-dried organic sludge in the rolling direction. On the other hand, the maximum diameter is 3 to 20 mm by laterally chopping.
It has a pretreatment device equipped with a pair of rotating groove rollers that form unevenness in the lateral direction and mesh with each other, and there are multiple steps in which the small lumps of organic sludge are piled up within a height of 50 cm. The organic sludge is installed in stages and has a heating device that heats the stacked organic sludge to 40 ° C. or more to accelerate the start of fermentation of the organic sludge, and a supply / exhaust device that circulates air in the stacked organic sludge, and the organic material. Equipped with a temperature sensor to measure the temperature of sludge and an oxygen concentration meter to measure the oxygen concentration in the atmosphere, the oxygen concentration in the atmosphere is 5 to 20%, and the temperature of the organic sludge is 55
An apparatus for composting organic sludge, comprising a fermentation tank which is automatically adjusted to a temperature of up to 65 ° C by the air supply and exhaust device.
【請求項7】 給排気装置として排気側を吸引すること
により発酵槽内に給気する請求項6記載のコンポスト化
装置。
7. The composting device according to claim 6, wherein air is supplied to the fermentation tank by sucking the exhaust side as a supply / exhaust device.
JP4361473A 1992-12-28 1992-12-28 Method for composting organic sludge and device therefor Pending JPH06199586A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4361473A JPH06199586A (en) 1992-12-28 1992-12-28 Method for composting organic sludge and device therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4361473A JPH06199586A (en) 1992-12-28 1992-12-28 Method for composting organic sludge and device therefor

Publications (1)

Publication Number Publication Date
JPH06199586A true JPH06199586A (en) 1994-07-19

Family

ID=18473733

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4361473A Pending JPH06199586A (en) 1992-12-28 1992-12-28 Method for composting organic sludge and device therefor

Country Status (1)

Country Link
JP (1) JPH06199586A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006111572A1 (en) * 2005-04-22 2006-10-26 Martin Fuchs Method for the aerobic-thermophilic stabilization and decontamination of sludge
JP2010069477A (en) * 2008-08-22 2010-04-02 Chubu Shiryo Kk Fermentation apparatus for food residue

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006111572A1 (en) * 2005-04-22 2006-10-26 Martin Fuchs Method for the aerobic-thermophilic stabilization and decontamination of sludge
US7531093B2 (en) 2005-04-22 2009-05-12 Leonhard Fuchs Process for the aerobic-thermophilic stabilization and disinfection of sludge
JP2010069477A (en) * 2008-08-22 2010-04-02 Chubu Shiryo Kk Fermentation apparatus for food residue

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