JPS6365637B2 - - Google Patents

Info

Publication number
JPS6365637B2
JPS6365637B2 JP59007266A JP726684A JPS6365637B2 JP S6365637 B2 JPS6365637 B2 JP S6365637B2 JP 59007266 A JP59007266 A JP 59007266A JP 726684 A JP726684 A JP 726684A JP S6365637 B2 JPS6365637 B2 JP S6365637B2
Authority
JP
Japan
Prior art keywords
organic matter
fermentation
stage
partition plate
fermentation chamber
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
Application number
JP59007266A
Other languages
Japanese (ja)
Other versions
JPS60155589A (en
Inventor
Hiroshi Etani
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.)
Japan Steel Works Ltd
Original Assignee
Japan Steel Works 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 Japan Steel Works Ltd filed Critical Japan Steel Works Ltd
Priority to JP59007266A priority Critical patent/JPS60155589A/en
Publication of JPS60155589A publication Critical patent/JPS60155589A/en
Publication of JPS6365637B2 publication Critical patent/JPS6365637B2/ja
Granted 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

Description

【発明の詳細な説明】 本発明は、都市ごみ、農村発棄物なの有機質物
の処理方法およびその装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for treating organic matter such as municipal waste and rural waste.

これらの有機質物の処理に際しては、埋立、焼
却などの方法がとられていたが、これらの方法で
は悪臭の発生、地下水の汚染、有害ガスの発生な
どの二次公害を伴い、環境面で社会問題となつて
いる。このため、これらの有機質物を発酵させて
堆肥を得る処理方式が、近年になつて採用されて
いる。堆肥を得る処理に際しては、従来は屋外に
おいてこれらの有機質物を野積に、適宜反覆切返
しを行つて自然の熟成を待つ方式が採られてきた
が、この方法では、依然として悪臭の発生や地下
水の汚染などの二次公害が避けられない。このた
めに、これらの有機質物を人工的につくられた好
気性条件下で発酵させて堆肥化する処理方法が採
られている。この処理方式には、ロータリーキル
ン(回転ドラム)式、パドル式、オーガ式、サイ
ロ式などの発酵槽を用いた機械式方法がある。し
かし、これらの既多の方法によるときには、いず
れも有機質物の含水率が、微生物発酵に適した50
〜65%の場合でなければ良好な好気性発酵をしな
い。そのために、有機質物を発酵槽に投入すると
きに、あらかじめもみがら、のこくずあるいはす
でに堆肥化した最終製品の一部を還元して使用す
るなどの水分調整材を有機質物中に混入して含水
率を50〜65%に調整して、槽内で好気性発酵をさ
せているのが実状である。含水率65%以上の有機
質物の場合には、嫌気性発酵が行われて、酢酸、
プロピオン酸、酪酸、吉草酸などの低級脂肪酸
や、硫化水素、硫化メチル、メチルメルカプタン
などの硫化物が生成され、強度の刺激臭と悪臭を
発生して二次公害を発生させるとともに、上記生
成物は、まだ有機質の十分な微生物分解が進行し
ていない。従つて、生成物の腐敗熟成度は農業に
施用するのに充分でない。堆肥化を完了するため
には、さらに長期間にわたつて、堆積場で堆積し
て、適宜切返し熟成させる必要があり、広い堆積
面積と長時間を要するなどの欠点がある。
Methods such as landfilling and incineration have been used to dispose of these organic materials, but these methods are associated with secondary pollution such as the generation of bad odors, groundwater contamination, and generation of harmful gases, and are socially harmful from an environmental perspective. It's becoming a problem. For this reason, in recent years, a treatment method has been adopted in which compost is obtained by fermenting these organic substances. Conventionally, the process of obtaining compost has been to pile up these organic materials outdoors and allow them to ripen naturally by turning over and over as needed. Secondary pollution such as these cannot be avoided. For this purpose, a treatment method has been adopted in which these organic substances are fermented under artificially created aerobic conditions and composted. This processing method includes mechanical methods using fermenters such as rotary kiln (rotating drum) type, paddle type, auger type, and silo type. However, when using these existing methods, the moisture content of the organic material is 50%, which is suitable for microbial fermentation.
Good aerobic fermentation only occurs in ~65% of cases. To this end, when adding organic matter to the fermentation tank, a moisture regulating material such as rice husks, sawdust, or reduced part of the final product that has already been composted is mixed into the organic matter in advance. In reality, the water content is adjusted to 50-65% and aerobic fermentation is carried out in a tank. In the case of organic substances with a moisture content of 65% or more, anaerobic fermentation is performed to produce acetic acid,
Lower fatty acids such as propionic acid, butyric acid, and valeric acid, and sulfides such as hydrogen sulfide, methyl sulfide, and methyl mercaptan are produced, producing strong pungent odors and bad odors, causing secondary pollution, and the above products. However, sufficient microbial decomposition of organic matter has not yet progressed. Therefore, the spoilage maturity of the product is not sufficient for agricultural applications. In order to complete composting, it is necessary to accumulate the material in a composting site for a longer period of time, and then turn it over and ripen it as appropriate, which has disadvantages such as requiring a large deposition area and a long time.

本発明は、上記欠点を解消し、含水率が65%以
上の高水分の有機質物を、もみがら、のこくずあ
るいはすでに堆肥化した最終製品の一部を還元し
て使用するなどの水分調整材を使用せずに、早期
に脱水し、好気性状況の下で発酵させて、臭気を
発生せずに堆肥が得られる有機質物の処理方法お
よびその装置を提供する。
The present invention solves the above-mentioned drawbacks and makes moisture adjustment by reducing the moisture content of rice husks, sawdust, or a part of the final product that has already been composted. To provide a method for processing organic matter and an apparatus thereof, capable of obtaining compost without generating odor by early dehydration and fermentation under aerobic conditions without using wood.

本発明に係る有機質物の処理方法および処理装
置を、図面に示す実施例に基づいて説明する。図
において、所要の内容量を有する縦形発酵槽1
は、その内部が仕切板2によつて、上下方向に2
以上に、段階状に分割されて多段式の複数の発酵
室A,B,C,…を構成する。仕切板2は、その
上に積載された都市ごみ、農村発棄物などの有機
質物3を支持し、かつ所定時間経過後にはこれら
の有機質物3を落下させるために、連動制御され
る任意適切な仕切板動作装置10により、それぞ
れ開閉あるいは滑動などの適宜な手段を用いて開
口部11を形成するように構成される。仕切板2
は、堆積された有機質物3の通気性を向上するた
めに、鋼製多孔板などを用いて形成する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A method and apparatus for treating organic substances according to the present invention will be explained based on embodiments shown in the drawings. In the figure, a vertical fermenter 1 with the required internal capacity
is divided into two parts in the vertical direction by the partition plate 2.
As described above, a plurality of multistage fermentation chambers A, B, C, . . . are constructed by being divided into stages. The partition plate 2 supports organic materials 3 such as municipal waste and rural discarded material loaded thereon, and allows the organic materials 3 to fall after a predetermined period of time. The partition plate operating device 10 is configured to form the opening 11 using appropriate means such as opening/closing or sliding. Partition plate 2
is formed using a perforated steel plate or the like in order to improve the air permeability of the deposited organic matter 3.

本発明の1態様によれば、仕切板2は、図のご
とく水平面に対して所定角度をもつて傾斜して設
置される。仕切板2の傾斜下方端縁、本実施例で
は発酵槽1の側壁への隣接縁は該側壁に沿つて縦
方向に設けられた汚水排出路4と連通し、汚水排
出路4は、各発酵室を形成する各階仕切板2の下
方端縁とそれぞれ連通しつつ下端において、外部
への排出手段を具備する汚水溜5に接続するよう
に構成される。
According to one aspect of the present invention, the partition plate 2 is installed so as to be inclined at a predetermined angle with respect to a horizontal plane as shown in the figure. The sloping lower edge of the partition plate 2, in this embodiment the edge adjacent to the side wall of the fermenter 1, communicates with a sewage discharge passage 4 provided vertically along the side wall. It is configured to communicate with the lower edge of each floor partition plate 2 forming the room, and to be connected at the lower end to a cesspool 5 provided with a means for discharging to the outside.

仕切板2の傾斜角度αは、上記の構成のごと
く、積載された有機質物中から自然に浸出する水
分、および後述するごとく、発酵処理中に各仕切
板の下面に生ずる結露水を、汚水排出路4に傾斜
を利用して排出させるためのものであり、有機質
物の性状、それが形成する安息角、有機質物から
出る水分の量、仕切板の材質などから定まるもの
であつて、一般に25゜〜45゜の範囲が適当である。
もし傾斜角度が25゜よりも小さくなると、有機質
物の性状、有機質物からの浸出水分、仕切板の形
状、仕切板の材質などが通常に考えられるいかな
るものであつても、この水分は流動摩擦、表面張
力などの影響により、仕切板に沿つて流れずに滞
留し、仕切板下方の発酵室内に所在する有機質物
の表面に落下してしまう。一方、傾斜角度が45゜
以上に大きい場合には、水分は有機質物3中を重
力によつて垂下、にじみ出るが、有機質物3の堆
積厚さは通常ほぼ300〜600mmであり、仕切板2の
傾斜角度が大きい程、傾斜角度の逆余弦である水
分の流れる垂直距離が長くなるから、必然的に水
分が流れにじみ出にくくなる。通常の含水率が65
%以上の都市ごみなどの有機質の場合には、仕切
板に沿つて有効に排水可能な角度αは45゜が上限
となる。
As with the above configuration, the inclination angle α of the partition plate 2 is set such that water that naturally leaches from the loaded organic matter and dew water that forms on the bottom surface of each partition plate during the fermentation process, as described later, are used to drain waste water. This is for draining the passageway 4 using the slope, and is determined by the properties of the organic matter, the angle of repose it forms, the amount of moisture coming out of the organic matter, the material of the partition plate, etc. A range of 45° to 45° is appropriate.
If the angle of inclination is smaller than 25°, this water will flow through the flow friction, regardless of the nature of the organic material, the water leached from the organic material, the shape of the partition plate, the material of the partition plate, etc. Due to the influence of surface tension, etc., the organic matter does not flow along the partition plate, but remains, and falls onto the surface of organic matter located in the fermentation chamber below the partition plate. On the other hand, if the inclination angle is greater than 45°, water will drip down and ooze out in the organic material 3 due to gravity, but the accumulated thickness of the organic material 3 is usually approximately 300 to 600 mm, and the thickness of the organic material 3 is usually approximately 300 to 600 mm. The larger the inclination angle is, the longer the vertical distance over which water flows, which is the inverse cosine of the inclination angle, naturally makes it more difficult for water to seep out. Normal moisture content is 65
% or more of organic matter such as municipal waste, the upper limit of the angle α that can effectively drain water along the partition plate is 45°.

さらに、送風装置6、送風ライン、排風ライン
および排風装置7をもつて構成した通気装置を設
け、ここにおいてこの送風系と排風系は図の矢印
で示すごとく、各段の発酵室について交互段に1
対として設けるものであり、これにより通気は1
対となつた上段階の発酵室内の有機質物から仕切
板2を経由して下段の有機質物を通つて排気され
て、発酵に必要な空気が供給される。空気の供給
量は、投入有機質物の量、性状などに応じて発酵
に適した量に定める。
Furthermore, an aeration system including a blower 6, a blower line, an exhaust line, and an exhauster 7 is provided, and the blower system and exhaust system are connected to each stage of the fermentation chamber as shown by the arrows in the figure. 1 in alternate rows
They are installed as a pair, and this allows for ventilation of 1
Air necessary for fermentation is supplied from the organic matter in the pair of upper stage fermentation chambers via the partition plate 2 and through the lower stage organic matter. The amount of air supplied is determined to be an amount suitable for fermentation depending on the amount and properties of the input organic material.

発酵槽1の最上段の発酵室Aの上方に有機質物
3を供給する供給コンベア8を設け、最下段の発
酵室下方に、発酵処理された生成堆肥を発酵槽外
へ排出する排出コンベア9を設ける。
A supply conveyor 8 for supplying organic matter 3 is provided above the fermentation chamber A at the top of the fermentation tank 1, and a discharge conveyor 9 for discharging the fermented compost out of the fermentation tank is provided below the fermentation chamber at the bottom. establish.

上述のごとく構成された処理装置を用いて、含
水率が65%以上の高水分の都市ごみ、農村廃棄物
などの有機質物を発酵させて堆肥化処理する方法
は、あらかじめ好気性発酵に適した粒度に破砕し
た有機質物を、供給コンベア8によつて、多段の
発酵槽1の最上段の発酵室Aに供給し、所要の厚
さに堆積する。この状態において、堆積された有
機質物3中の水分は、時間の経過とともに漸次、
傾斜した仕切板2に沿つて流れ出るから、有機質
物3の含水率は、堆肥化に有効な、好気性の細
菌、放線菌の増殖と活性化に適した65%程度まで
低下する。有機質物は上段室から下段室に落下さ
れる都度自動的に混合され、微生物の栄養源の均
一分散化が行なわれる。この間の所要日数は、有
機質物の性状によつて相違するが、通常1〜3日
前後である。含水率がほぼ65%に低下した状態に
おいて、発酵室内の有機物3は良好な好気性発酵
を行い、その温度は55〜65℃となつて、活発に水
分を蒸発し、これにより仕切板2の下側の表面、
すなわち下方室の天井に結露水が発生する。傾斜
した仕切板2に付着したこの結露水は、これに沿
つて流れて汚水排出路4を経由して汚水溜5に収
集されて槽外に排出処理される。従つて、その
際、下段の発酵室内に存在する有機質物中に結露
水が落下して該有機質物の水分低下を妨げる現象
は避けられる。その結果、このような好適な発酵
処理が各段の発酵室を逐次経過しつつ実施され、
当初投入された含水率が65%以上の高水分の有機
質物は、約5〜7日間経過することにより、充分
な発酵処理が終つて堆肥化され、そのC/N値が
低下し、還元糖態炭素割合が低下し、PH値がほぼ
8〜9となつて、最下段の発酵室内に堆積された
堆肥製品を、排出コンベア9により所定区域に送
出する。
A method of fermenting and composting high-moisture urban waste, rural waste, and other organic materials with a moisture content of 65% or more using a processing device configured as described above is a method that uses a processing device that is suitable for aerobic fermentation in advance. The organic matter crushed into particles is supplied to the fermentation chamber A at the top of the multi-stage fermenter 1 by a supply conveyor 8, and is deposited to a required thickness. In this state, the moisture in the deposited organic matter 3 gradually decreases over time.
Since it flows out along the inclined partition plate 2, the moisture content of the organic material 3 is reduced to about 65%, which is suitable for the growth and activation of aerobic bacteria and actinomycetes, which are effective for composting. Organic substances are automatically mixed each time they are dropped from the upper chamber to the lower chamber, thereby uniformly dispersing nutrients for microorganisms. The number of days required during this period varies depending on the properties of the organic material, but is usually around 1 to 3 days. In a state where the moisture content has decreased to approximately 65%, the organic matter 3 in the fermentation chamber undergoes good aerobic fermentation, and the temperature reaches 55 to 65°C, actively evaporating water, and as a result, the partition plate 2 the lower surface,
In other words, condensation water forms on the ceiling of the lower room. This condensed water adhering to the inclined partition plate 2 flows along the partition plate 2 and is collected in the sewage basin 5 via the sewage discharge channel 4, and is discharged to the outside of the tank. Therefore, in this case, a phenomenon in which condensed water falls into the organic matter existing in the lower fermentation chamber and prevents the moisture content of the organic matter from decreasing can be avoided. As a result, such a suitable fermentation process is carried out while passing through each stage of fermentation chambers sequentially,
After approximately 5 to 7 days, the initially input high-moisture organic matter with a moisture content of 65% or more will be fully fermented and composted, its C/N value will decrease, and reducing sugars will be produced. The compost product, which has a reduced carbon content and a pH value of approximately 8 to 9, is deposited in the bottom fermentation chamber and is delivered to a predetermined area by the discharge conveyor 9.

なお、発酵槽内の好気性条件を最適に保つため
には、発酵槽1の供給口部と排出口部は、送風装
置と排風装置の効果を十分に発揮するために、密
封性を高めた構造とすることが望ましい。
In addition, in order to maintain optimal aerobic conditions within the fermenter, the supply and discharge ports of fermenter 1 should be sealed tightly to fully utilize the effects of the blower and exhaust device. It is desirable to have a structure that

本発明により、縦形多段式発酵槽の最上段に投
入した含水率が65%以上の高水分の有機質物の早
期脱水と、好気性細菌類の微生物に増殖と活性化
の環境を与えて有機質物の発酵を促進させるとと
もに、発酵段階において有機質物からの蒸発水分
に起因する仕切板への結露を仕切板の傾斜特性に
より、発酵槽外に排除させることにより発酵中の
有機質物への落下に伴なう有機質物の含水率の低
下を防止でき、有機質物の効率の高い堆肥化処理
が遂行できる。
The present invention enables early dehydration of high-moisture organic matter with a water content of 65% or more, which is charged into the top stage of a vertical multi-stage fermenter, and provides an environment for the growth and activation of aerobic bacteria. In addition, during the fermentation stage, the sloping characteristics of the partition plates allow condensation on the partition plates caused by evaporated water from the organic substances to be removed from the fermentation tank, thereby preventing condensation from falling onto the organic substances during fermentation. This makes it possible to prevent the moisture content of the organic matter from decreasing, and to perform highly efficient composting of the organic matter.

さらに、本発明により、従来の機械式の方法に
よるごとき嫌気性発酵に伴なう強度の悪臭発生、
その他地下水汚染のごとき環境公害や、極めて長
い堆肥化所要期間が軽減され、有機質物の堆肥化
処理に極めて顕著な効果を奏する。
Furthermore, the present invention eliminates the generation of strong malodors associated with anaerobic fermentation as in conventional mechanical methods.
Other environmental pollution such as groundwater contamination and the extremely long time required for composting are reduced, and this has an extremely significant effect on the composting process of organic materials.

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

図面は本発明の一実施例を示す有機質物の処理
方法およびその装置を示す概略説明図である。 1……発酵槽、2……仕切板、3……有機質
物、4……汚水排出路、5……汚水溜、6……送
風装置、7……排風装置、8……供給コンベア、
9……排出コンベア、10……開閉動作装置。
The drawings are schematic explanatory diagrams showing a method for treating organic matter and an apparatus therefor, which represent an embodiment of the present invention. 1... Fermentation tank, 2... Partition plate, 3... Organic matter, 4... Sewage discharge channel, 5... Sewage pool, 6... Air blower, 7... Air exhaust device, 8... Supply conveyor,
9...Discharge conveyor, 10...Opening/closing operation device.

Claims (1)

【特許請求の範囲】 1 含水率が65%以上の高水分の公共廃棄物など
の有機質物を、水分調整を行わずに、これを多段
式発酵槽の最上段に供給し、該有機質物の含水率
を低下させつつ、順次下段に落下させて発酵さ
せ、最下段において堆肥を得ることを特徴とする
有機質物の処理方法。 2 有機質物を最上段の発酵室に定量ずつ供給す
る搬入手段と、最下段の発酵室に生成された堆肥
を排出する搬出手段を設け、かつ各段に通気性を
付与する通気手段を有する多段式発酵槽におい
て、各段の発酵室の仕切板を水平に対して角度
25゜〜45゜の範囲に傾斜させ、かつ各段の発酵室の
仕切板を開閉自在に構成して成る有機質物の処理
装置。
[Claims] 1. Organic matter such as high-moisture public waste with a moisture content of 65% or more is supplied to the top stage of a multistage fermenter without moisture adjustment, and the organic matter is A method for processing organic matter, which is characterized in that organic matter is allowed to fall into lower stages for fermentation while reducing its moisture content, and compost is obtained in the lowest stage. 2. A multi-tiered structure that is provided with a carrying-in means for supplying organic matter in fixed quantities to the fermentation chamber at the top level, a carrying-out means for discharging the produced compost to the fermentation chamber at the bottom level, and a ventilation means for imparting ventilation to each stage. In a type fermenter, the partition plate of each stage of fermentation chamber is set at an angle with respect to the horizontal.
An apparatus for treating organic matter, which is constructed by tilting the fermentation chamber at an angle of 25° to 45° and opening and closing the partition plates of each stage of the fermentation chamber.
JP59007266A 1984-01-20 1984-01-20 Organic matter treatment and device Granted JPS60155589A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59007266A JPS60155589A (en) 1984-01-20 1984-01-20 Organic matter treatment and device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59007266A JPS60155589A (en) 1984-01-20 1984-01-20 Organic matter treatment and device

Publications (2)

Publication Number Publication Date
JPS60155589A JPS60155589A (en) 1985-08-15
JPS6365637B2 true JPS6365637B2 (en) 1988-12-16

Family

ID=11661223

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59007266A Granted JPS60155589A (en) 1984-01-20 1984-01-20 Organic matter treatment and device

Country Status (1)

Country Link
JP (1) JPS60155589A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6467168A (en) * 1987-09-07 1989-03-13 Toshiko Osuga Fermentation treatment of fish

Also Published As

Publication number Publication date
JPS60155589A (en) 1985-08-15

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