JPH07184635A - Fermentation of organic waste and fermentation apparatus - Google Patents

Fermentation of organic waste and fermentation apparatus

Info

Publication number
JPH07184635A
JPH07184635A JP33188293A JP33188293A JPH07184635A JP H07184635 A JPH07184635 A JP H07184635A JP 33188293 A JP33188293 A JP 33188293A JP 33188293 A JP33188293 A JP 33188293A JP H07184635 A JPH07184635 A JP H07184635A
Authority
JP
Japan
Prior art keywords
organic waste
fermentation
fermenter
air
blower
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.)
Granted
Application number
JP33188293A
Other languages
Japanese (ja)
Other versions
JP2932921B2 (en
Inventor
Koji Toda
孝司 戸田
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.)
Niigata Engineering Co Ltd
Original Assignee
Niigata Engineering Co 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 Niigata Engineering Co Ltd filed Critical Niigata Engineering Co Ltd
Priority to JP33188293A priority Critical patent/JP2932921B2/en
Publication of JPH07184635A publication Critical patent/JPH07184635A/en
Application granted granted Critical
Publication of JP2932921B2 publication Critical patent/JP2932921B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/20Sludge processing
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/40Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

Landscapes

  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)
  • Fertilizers (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)

Abstract

PURPOSE:To provide a fermentation method capable of performing uniform aerobic fermentation of an organic waste without causing excessively moistened state or hard-dried state of the bottom sediment generated in a fixed bottom fermentation tank furnished with a fixed bottom plate for precipitating the organic waste and to provide a fermentation apparatus for performing the fermentation method. CONSTITUTION:This fermentation method alternately performs an upward aeration to pass air upward from the bottom of the sediment of an organic waste and a downward aeration to pass air from the top toward the sedimentation bottom of the organic waste. The characteristic of the fermentation apparatus for performing the fermentation method comprises connecting a blower 4 with an aeration chamber 3 under the bottom plate 2 of the fermentation tank 1 through a channel-switching means composed of automatic valve V1 and V4 and a dust and selectively connecting the aeration chamber to the exhaustion side or the suction side of the blower by the automatic control of the channel-switching means with a timer.

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、有機質廃物を好気性発
酵させる発酵方法および発酵装置に関し、さらに詳しく
は、発酵槽内の有機質廃物堆積層への酸素含有気体の通
気方式を改良した発酵方法および発酵装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fermentation method and a fermentation apparatus for aerobically fermenting an organic waste, and more specifically, a fermentation method in which an oxygen-containing gas aeration method is improved in an organic waste accumulation layer in a fermenter. And a fermenter.

【0002】[0002]

【従来の技術】馬、牛、豚、鶏等の家畜糞、家畜の敷わ
ら、厨芥、汚泥、農林廃棄物、都市ごみ等の有機質廃物
を好気的条件で発酵させて堆肥化する発酵装置は、従来
から各種の型式のものが知られている。例えば、落し戸
を並べて棚段を構成した構造や、つめ状、板状あるいは
鋭角状の突起部を外周に備えた回転棒の複数本を互いに
平行に間隔を置いて並列させた構造等の竪型多段落し戸
式の堆肥化発酵装置が知られている。この多段落し戸式
の堆肥化発酵装置は、各段の落し戸を開くことあるいは
回転棒を回転させることによって棚段上の有機質廃物の
堆積物を下方の次段へ落下させるので、棚段上の堆積物
全体が撹拌され比較的均一に好気性発酵を行うことがで
きると共に、敷地面積が少なくてすむという利点があ
る。
Fermentation apparatus for fermenting organic wastes such as horse droppings, cows, pigs, chickens and other livestock manure, livestock straws, kitchen waste, sludge, agricultural and forestry wastes, and municipal wastes under aerobic conditions to compost them. Conventionally, various types are known. For example, a vertical structure such as a structure in which trapdoors are arranged to form a shelf or a structure in which a plurality of rotating rods provided with claw-shaped, plate-shaped, or acute-angled protrusions on the outer periphery are arranged in parallel at intervals. A multi-stage, door-type composting and fermentation apparatus is known. This multi-paragraph door-to-door type composting fermenter drops organic waste deposits on the tray to the next lower tray by opening the trapdoor on each stage or rotating the rotating rod. There is an advantage that the whole sediment above can be agitated and relatively aerobically fermented, and the site area can be reduced.

【0003】しかし、この竪型多段落し戸式の堆肥化発
酵装置は、多数の機械要素を必要とし、高価であるた
め、底部が固定式の堆肥化発酵装置も多く採用されてい
る。この底部固定式の堆肥化発酵装置は、一般に上方が
開放された直方体形状の発酵槽が多く採用され、さらに
は、切欠部分を有する固定底板を多段に配して各段の有
機質廃物堆積物を移動させて切欠部分から下方の段に落
下させるようにしたものがある。また、これらの底部固
定式の堆肥化発酵装置は、均一に好気性発酵を行うため
に有機質廃物の堆積物を上下に撹拌するための種々の切
返機が設けられている。例えば、螺旋状のスクリューに
よって堆積物を上方に掻き上げるオーガータイプ、回転
する跳ね上げパドルによって堆積物をパドルの進行方向
と反対側に跳ね返すパドルタイプ、チェーンコンベアに
掻き取り板やバケットを取付けた形状のスクープにより
堆積物を後方に掻き上げるスクープタイプ等の種々の切
返装置がある。
However, since this vertical type multi-paragraph door type composting and fermenting apparatus requires a large number of mechanical elements and is expensive, a fixed bottom type composting and fermenting apparatus is often employed. In this bottom fixed type composting fermentation apparatus, generally, a rectangular parallelepiped fermenter with an open upper part is generally adopted.Furthermore, a fixed bottom plate having a cutout portion is arranged in multiple stages to collect organic waste deposits at each stage. There is one that is moved and dropped from the notch to the lower step. Further, these bottom fixed type composting and fermenting devices are provided with various cutting machines for vertically stirring the organic waste deposits in order to uniformly perform aerobic fermentation. For example, an auger type that scrapes the deposit upwards with a spiral screw, a paddle type that flips the deposit back to the side opposite to the direction of movement of the paddle with a rotating flip-up paddle, and a shape with a scraping plate or bucket attached to the chain conveyor. There are various cutting devices such as a scoop type which scoops up the deposit backward by the scoop.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、上記底
部固定式の堆肥化発酵装置においては、種々の切返機で
有機質廃物の堆積層を切返しても、どうしても機械的に
発酵槽底部まで掻き取れないので、切返しがあまり行わ
れない堆積部分が発酵槽底部に生じてしまう。つまり、
実際に発酵処理を行うと、あるタイプの底部固定式堆肥
化発酵装置では、発酵槽底部に生じる切返しが難しい堆
積部分は、べとべとの過湿状態となり、害虫が発生した
り、異臭を発したり、さらには、これらがたまに切返機
で掻き取られ発酵製品中に塊となって混入するといった
弊害が生じる。また、別のタイプの底部固定式堆肥化発
酵装置では、発酵槽底部に生じる切返しが難しい堆積部
分は、乾燥状態になって、発酵が停止して固くなってお
り、前述と同様にこれらがたまに切返機で掻き取られ発
酵製品中に塊となって混入するといった弊害が生じる。
However, in the above-mentioned fixed bottom type composting and fermentation apparatus, even if the organic waste accumulation layer is cut back by various cutting machines, it cannot be mechanically scraped to the bottom of the fermentation tank. As a result, a piled-up portion that is not cut back occurs at the bottom of the fermenter. That is,
When the fermentation process is actually performed, in a certain type of bottom fixed type composting fermenter, the piled-up part that is difficult to turn over at the bottom of the fermenter becomes sticky and sticky, causing pests and giving off a strange odor. Further, there is an adverse effect that these are occasionally scraped off by a turning machine and mixed into the fermented product as a lump. Further, in another type of bottom fixed type composting fermenter, the piled up part that is difficult to turn over at the bottom of the fermenter is in a dry state and fermentation is stopped and hardened. The scraper is scraped off by a cutting machine, and the fermented product is contaminated in the form of lumps.

【0005】子細に調べると、発酵槽内の有機質廃物の
堆積底部から吸気して該有機質廃物の堆積表面から空気
を取り入れる下向流通気方式の底部固定式堆肥化発酵装
置においては、発酵槽底部に生じる堆積部分がべとべと
の過湿状態となり、一方、発酵槽内の有機質廃物の堆積
底部から空気を供給して該有機質廃物の堆積表面から排
出放散させる上向流通気方式の底部固定式堆肥化発酵装
置においては、発酵槽底部に生じる堆積部分が固い乾燥
状態になっていることを知見した。
Upon close examination, in the bottom fixed composting fermenter of the downward circulating air system, which sucks air from the bottom of the organic waste deposit in the fermenter and takes in air from the surface of the organic waste deposit, the bottom of the fermenter is used. The part that accumulates at the bottom becomes sticky and over-humidified, while air is supplied from the bottom of the organic waste stack in the fermenter to discharge and disperse from the surface of the organic waste stack. In the fermenter, it was found that the accumulated portion at the bottom of the fermenter was in a hard and dry state.

【0006】また、本願と同一出願人等により出願され
た実公昭63−27839号には、図4に示したよう
に、多数の孔を長手方向に穿設した吸気管20を、発酵
槽内の有機質廃物の堆積層中間位置の発酵槽側壁21に
配設した底部固定式発酵装置が記載されている。この装
置においては、多数の空気送入孔を穿設した固定底板2
2からブロワー23により空気を送入し、同時に吸気管
20を介して吸引ブロワー24により空気を吸引して脱
臭装置25で処理する。これによって、図中の矢印で示
されるように、吸気管20より上方の堆積層では下向流
通気方式となるが、吸気管20より下方の堆積層では上
向流通気方式となって、やはり発酵槽底部に生じる堆積
部分では固い乾燥状態が生じてしまう。
Further, in Japanese Utility Model Publication No. 63-27839 filed by the same applicant as the present application, as shown in FIG. 4, an intake pipe 20 having a large number of holes in the longitudinal direction is provided in the fermentation tank. There is described a bottom fixed fermentation apparatus arranged on the side wall 21 of the fermenter at an intermediate position of the sedimentary layer of the organic waste. In this device, a fixed bottom plate 2 having a large number of air inlet holes is formed.
Air is sent from 2 by a blower 23, and at the same time, air is sucked by a suction blower 24 via an intake pipe 20 and treated by a deodorizing device 25. As a result, as shown by the arrow in the figure, the downward flow air system is used in the deposition layer above the intake pipe 20, but the upward flow air system is used in the deposition layer below the intake pipe 20, At the bottom of the fermenter, a hard, dry state occurs at the deposit.

【0007】そこで本発明は、底部固定式の発酵槽に固
有の上記したごとき問題を解消すべくなされたものであ
って、有機質廃物を均一に好気性発酵を行える発酵方法
およびその方法を実施するための発酵装置を提供するこ
とを目的とする。
Therefore, the present invention has been made to solve the above-mentioned problems peculiar to a fixed bottom type fermenter, and implements a fermentation method and a method for uniformly aerobic fermentation of organic waste. It is an object of the present invention to provide a fermentation device for

【0008】[0008]

【課題を解決するための手段】上記の目的を達成するた
めの第1の発明である有機質廃物の発酵方法は、有機質
廃物を堆積させる固定底板を備えた発酵槽で有機質廃物
を好気性発酵させる方法において、酸素含有気体を有機
質廃物の堆積底部から上方に向けて通気する上向流通気
と、酸素含有気体を上方から有機質廃物の堆積底部に向
けて通気する下向流通気とを交互に行うことを特徴とす
るものである。
The method for fermenting organic waste according to the first aspect of the present invention for achieving the above object comprises aerobically fermenting the organic waste in a fermenter equipped with a fixed bottom plate for depositing the organic waste. In the method, an upflow gas that ventilates an oxygen-containing gas upward from the bottom of the organic waste deposit and a downflow air that vents the oxygen-containing gas from above to the bottom of the organic waste deposit are alternately performed. It is characterized by that.

【0009】また、第2の発明である有機質廃物の発酵
装置は、有機質廃物を堆積させる固定底板の近傍に通気
手段を配設した発酵装置において、該通気手段はタイマ
ーにより切替えられる通路切替手段を介して気体送風手
段の吐出側と吸引側とに選択的に連絡され、該通気手段
と該気体送風手段の吐出側とが連絡されているときは、
該気体送風手段の吸引側が酸素含有気体源と連絡されて
いることを特徴とするものである。
The organic waste fermenter according to the second aspect of the present invention is a fermenter in which a ventilating means is provided in the vicinity of a fixed bottom plate for accumulating the organic waste, and the ventilating means includes a passage switching means that is switched by a timer. When the discharge side and the suction side of the gas blowing means are selectively communicated with each other and the ventilation means and the discharge side of the gas blowing means are communicated with each other,
The suction side of the gas blowing means is connected to an oxygen-containing gas source.

【0010】本明細書中で“有機質廃物”という用語は
広義に解するものとし、好気的条件で発酵させて堆肥化
することができる馬、牛、豚、鶏等の家畜糞、家畜の敷
わら、厨芥、汚泥、農林廃棄物、都市ごみ等の有機質廃
物の他に、これらを好気性発酵させて得られた製品とし
ての堆肥も含むものとする。また“酸素含有気体”と
は、好気性発酵に不可欠な酸素を含有する気体であれば
いかなる種類の気体でもよいが、一般には空気(大気)
が使用できる。
In the present specification, the term "organic waste" is to be understood in a broad sense, and it can be fermented under aerobic conditions to be composted, and the dung of horses, cattle, pigs, chickens, etc. In addition to organic wastes such as straw, kitchen waste, sludge, agricultural and forestry wastes, and municipal wastes, compost as a product obtained by aerobically fermenting these is also included. The "oxygen-containing gas" may be any kind of gas as long as it contains oxygen essential for aerobic fermentation, but it is generally air (atmosphere).
Can be used.

【0011】[0011]

【作用】上記した構成を有する本発明によれば、上向流
通気と下向流通気とが交互に行われるため、従来の上向
流通気方式の底部固定式発酵装置の発酵槽底部堆積部分
に生じていたような固い乾燥状態や、従来の下向流通気
方式の底部固定式発酵装置の発酵槽底部堆積部分で生じ
ていたようなべとべとの過湿状態が発生することがな
い。その結果、機械的な切返しや掻き取りの難しい発酵
槽底部堆積部分がどうしても生じてしまう底部固定式の
発酵装置を使用しても、発酵槽底部堆積部分まで均一な
好気性発酵を行うことができる。
According to the present invention having the above-mentioned structure, since the upward air flow and the downward air flow are alternately performed, the fermentation tank bottom deposition portion of the conventional bottom fixed fermentation apparatus of the upward air flow system. There is no occurrence of a hard dry condition such as that which occurs in the above, or a sticky and over-humidified condition which occurs in the bottom part of the fermentation tank of the conventional fixed bottom type bottom-fermented fermentation apparatus. As a result, even when using a fixed bottom type fermenter that causes mechanical flipping or scraping of the fermenter bottom that is difficult to scrape, uniform aerobic fermentation can be performed up to the bottom of the fermenter. .

【0012】上向流通気と下向流通気とを交互に行う場
合の切替時間は特に限定されることはなく、発酵槽内の
堆積物、特に底部堆積部分の乾燥と過湿を防止して、堆
積物全体にわたって均一な発酵が得られるように適宜切
替えればよいが、好ましくは1時間以上、通常は3〜4
時間以上、より好ましくは12時間毎に切替えることが
望ましい。
There is no particular limitation on the switching time in the case where the upward air flow and the downward air flow are alternately performed, and the drying and overhumidity of the sediment in the fermenter, especially the bottom sedimentation part, is prevented. It may be appropriately switched so that uniform fermentation can be obtained over the whole sediment, but preferably 1 hour or more, usually 3 to 4
It is desirable to switch over every hour or more, more preferably every 12 hours.

【0013】[0013]

【実施例】以下に本発明の実施例について説明する。図
1および図2は、本発明による発酵装置の第1実施例を
示しており、発酵槽1の底板2には多数の孔が穿設され
ていて、この底板2の下方に通気室3が設けられてい
る。給気ブロワー4の吸引側4aには、自動弁V1を有
する空気吸引ダクトが接続されている。一方、給気ブロ
ワーの吐出側4bは、自動弁V2を有するダクトを介し
て発酵槽1の通気室3と、さらには自動弁V3を有する
ダクトを介して脱臭装置5と接続されている。給気ブロ
ワー4の吸引側4aはさらに、自動弁V4を有するダク
トを介して発酵槽1の通気室3と接続されている。発酵
槽1は全体が建屋6内に設置され、発酵槽1上方の建屋
内にフード7が設けられ、自動弁V5を有するダクトを
介して脱臭ファン8さらには脱臭装置5と接続されてい
る。建屋の屋上には換気扇9と自動弁V6が設置されて
いる。各自動弁V1〜V6の切替動作はすべて制御盤に
おけるタイマー設定により自動的に制御することができ
る。
EXAMPLES Examples of the present invention will be described below. 1 and 2 show a first embodiment of a fermentation apparatus according to the present invention, in which a bottom plate 2 of a fermenter 1 has a large number of holes, and a ventilation chamber 3 is provided below the bottom plate 2. It is provided. An air suction duct having an automatic valve V1 is connected to the suction side 4a of the air supply blower 4. On the other hand, the discharge side 4b of the air supply blower is connected to the ventilation chamber 3 of the fermentation tank 1 via a duct having an automatic valve V2, and further to the deodorizing device 5 via a duct having an automatic valve V3. The suction side 4a of the air supply blower 4 is further connected to the aeration chamber 3 of the fermenter 1 via a duct having an automatic valve V4. The fermentation tank 1 is entirely installed in a building 6, a hood 7 is provided in the building above the fermentation tank 1, and is connected to a deodorizing fan 8 and a deodorizing device 5 via a duct having an automatic valve V5. A ventilation fan 9 and an automatic valve V6 are installed on the roof of the building. The switching operation of each automatic valve V1 to V6 can be automatically controlled by the timer setting in the control panel.

【0014】この発酵装置の動作を以下に説明する。図
1は昼間運転の状態を示しており、自動弁V1とV2は
閉とし、V3とV4は開とする。この状態で給気ブロワ
ー4を運転することにより通気室3から空気が自動弁V
4を通して吸引され、有機質廃物の堆積層表面から堆積
層中に空気が取り入れられることになる。有機質廃物の
堆積層中を通過して給気ブロワーによって吸引された高
濃度臭気を含む空気は、自動弁V3を通して脱臭装置5
へ送られて脱臭処理される。堆積層表面からの臭気の放
散は、堆積層表面から堆積中に空気が取り入れられるの
で極めて少なく、建屋6内の低濃度臭気は単に作業環境
を考慮して、自動弁V6を開とし換気扇9を運転して屋
外に放出すればよく、特に脱臭処理する必要はない。従
って、自動弁V5は閉とし脱臭ファン8は運転しない。
The operation of this fermenter will be described below. FIG. 1 shows a state of daytime operation, in which automatic valves V1 and V2 are closed and V3 and V4 are opened. By operating the air supply blower 4 in this state, the air from the ventilation chamber 3 is automatically controlled by the automatic valve V.
4 will be sucked in and air will be taken into the sedimentary layer from the surface of the organic waste depositing layer. The air containing the high-concentration odor that has been sucked by the air supply blower after passing through the deposited layer of the organic waste passes through the automatic valve V3 and the deodorizing device 5
Sent to and deodorized. Emission of odor from the surface of the deposited layer is extremely small because air is taken in from the surface of the deposited layer during the deposition, and low-concentration odor in the building 6 is simply taken into consideration in the working environment and the automatic valve V6 is opened to turn the ventilation fan 9 on. It suffices to drive it and release it outdoors, and there is no particular need for deodorizing treatment. Therefore, the automatic valve V5 is closed and the deodorizing fan 8 is not operated.

【0015】図2は夜間運転状態を示すものであり、自
動弁V1とV2は開とし、V3とV4は閉とする。この
状態で給気ブロワー4を運転することにより自動弁V1
を通して吸引された新鮮空気が自動弁V2を通して通気
室3へ送られ、さらに底板2を通して有機質廃物の堆積
層下部より堆積層中に供給されることになる。堆積層中
を通過した高濃度臭気を含む空気は、自動弁V5を開と
して脱臭ファン8を運転することにより、フード7から
吸引され脱臭装置5で処理される。建屋6屋上の自動弁
V6は閉として換気扇9の運転は停止する。
FIG. 2 shows a nighttime operation state in which the automatic valves V1 and V2 are opened and V3 and V4 are closed. By operating the air supply blower 4 in this state, the automatic valve V1
The fresh air sucked through is sent to the ventilation chamber 3 through the automatic valve V2, and further supplied through the bottom plate 2 from the lower part of the organic waste accumulation layer to the accumulation layer. The air containing the high-concentration odor that has passed through the accumulated layer is sucked from the hood 7 and processed by the deodorizing device 5 by operating the deodorizing fan 8 by opening the automatic valve V5. The automatic valve V6 on the roof of the building 6 is closed and the operation of the ventilation fan 9 is stopped.

【0016】一般に底部固定式の発酵装置は、槽上面が
開放状態の開放横型発酵槽を使用するものが多い。図示
した第1実施例でも開放横型発酵槽1を使用しており、
槽の表面積が広いため、建屋6内に臭気が拡散すること
になる。特に昼間は作業員が建屋内に入ることが多く、
換気を兼ねた脱臭対策が必要となり、多量な換気と脱臭
処理が必要となる。そのため臭気対策用の脱臭設備が大
型化するという問題もある。そこで図示した第1実施例
においては、給気ブロワー4によって発酵槽1底面より
空気を供給する上向流通気方式と、発酵槽1底面より給
気ブロワー4によって吸引して堆積層表面から空気を取
り入れる下向流通気方式とを交互に行って、堆積層底部
が乾燥状態となりあるいは過湿状態となるのを防止して
堆積層全体にわたって均一な発酵を得るとと共に、昼間
は下向流通気方式を行うことにより建屋内の臭気濃度を
抑え、建屋が無人化する夜間には上向流通気方式を行う
ことにより建屋内の最小限の脱臭を行えるようにしてあ
るため、脱臭設備の小型化を図ることができる。
In general, a fixed bottom type fermenter often uses an open horizontal fermenter having an open upper surface. Also in the illustrated first embodiment, the open horizontal fermentor 1 is used,
Since the surface area of the tank is large, the odor will diffuse into the building 6. Especially during the daytime, workers often enter the building,
Deodorization measures that combine ventilation are required, and a large amount of ventilation and deodorization processing are required. Therefore, there is also a problem that the deodorizing equipment for odor control becomes large. Therefore, in the illustrated first embodiment, an upward flow air system in which air is supplied from the bottom surface of the fermenter 1 by the air supply blower 4, and air is sucked from the bottom surface of the fermenter tank 1 by the air supply blower 4 to suck air from the surface of the deposition layer. Alternately with the downward circulation air system to take in, the bottom of the sedimentary layer is prevented from becoming dry or overhumid and uniform fermentation is obtained throughout the sedimentary layer. By reducing the odor concentration inside the building, and by performing an upward circulation air system at night when the building becomes unattended, it is possible to minimize the deodorization inside the building. Can be planned.

【0017】図3は本発明による発酵装置の第2実施例
を示しており、図4に示した実公昭63−27839号
に記載された従来の発酵装置を改造して本発明方法を実
施できるようにしたものである。図中、図4と同じ部材
には同じ参照番号を付すことによって説明を省略する。
図3に示した本発明の発酵装置が、図4の従来装置と異
なる点は、ブロワー23に自動弁V21〜V24とダク
トから構成される通路切替手段を組み入れて、有機質廃
物堆積層中に下向流通気と上向流通気とを交互に行わせ
るようにした点である。第2実施例における自動弁V2
1〜24とダクトの構成は、第1実施例における自動弁
V1〜4とダクトの構成と同じであるので説明を省略す
る。下向流通気方式とする場合には、自動弁V21とV
22を閉、V23とV24を開としてブロワー23を運
転する。これによって、堆積層表面から堆積層中に空気
が取り入れられ、図中の点線矢印で示されるような下向
流通気がなされる。ブロワー23で吸引された臭気を含
む空気は自動弁V23を通って脱臭装置25で処理され
る。このとき、吸引ブロワー24は停止させておいても
よく、あるいは運転状態としてもよい。吸引ブロワー2
4を運転状態とすれば、堆積層表面から堆積層中に取り
入れられた空気の一部は吸気管20を介して吸引ブロワ
ー24から吸引される。
FIG. 3 shows a second embodiment of the fermentation apparatus according to the present invention, and the method of the present invention can be carried out by modifying the conventional fermentation apparatus described in JP-B-63-27839 shown in FIG. It was done like this. In the figure, the same members as those in FIG. 4 are designated by the same reference numerals, and the description thereof will be omitted.
The fermentation apparatus of the present invention shown in FIG. 3 is different from the conventional apparatus of FIG. 4 in that the blower 23 is equipped with a passage switching means composed of automatic valves V21 to V24 and a duct so that the blower 23 can be installed in the organic waste deposit layer. This is a point that the upflow air and the upflow air are alternately performed. Automatic valve V2 in the second embodiment
The configurations of the ducts 1 to 24 and the duct are the same as the configurations of the automatic valves V1 to V4 and the duct in the first embodiment, and therefore the description thereof will be omitted. When using the downward flow system, automatic valves V21 and V
The blower 23 is operated by closing 22 and opening V23 and V24. As a result, air is taken into the deposition layer from the surface of the deposition layer, and downward airflow as shown by the dotted arrow in the figure is made. The air containing the odor sucked by the blower 23 passes through the automatic valve V23 and is processed by the deodorizing device 25. At this time, the suction blower 24 may be stopped or may be in an operating state. Suction blower 2
When 4 is set in the operating state, part of the air taken into the deposit layer from the deposit layer surface is sucked from the suction blower 24 through the intake pipe 20.

【0018】上向流通気方式とする場合には、自動弁V
21とV22を開、V23とV24を閉としてブロワー
23および吸引ブロワー24を運転する。これによっ
て、自動弁21を通して吸引された新鮮空気は堆積層底
部から堆積層中に供給され、吸気管20を介して吸引ブ
ロワー24から吸引され、かくして吸気管20より下方
の堆積層では上向流通気(図中の実線矢印)が形成され
る。一方、吸引ブロワー24を運転状態としてあるた
め、堆積層表面から吸引管20へ向かう下向流通気(図
中の実線矢印)が形成される。従って、堆積層を通過し
た臭気を含む空気流はすべて吸引管20から吸引されて
脱臭装置25で脱臭処理がなされることになり、堆積層
の開放表面からの臭気の放散を効果的に防止することが
できる。特に図示していないが、自動弁V21〜V24
の切替はタイマー設定により自動制御されている。
When the upward circulating air system is used, an automatic valve V
21 and V22 are opened and V23 and V24 are closed to operate the blower 23 and the suction blower 24. As a result, the fresh air sucked through the automatic valve 21 is supplied into the sediment layer from the bottom of the sediment layer, is sucked from the suction blower 24 through the intake pipe 20, and thus flows upward in the sediment layer below the intake pipe 20. Qi (solid arrow in the figure) is formed. On the other hand, since the suction blower 24 is in the operating state, downward flowing air (solid line arrow in the figure) from the surface of the deposited layer toward the suction pipe 20 is formed. Therefore, all the odor-containing air flow that has passed through the deposited layer is sucked from the suction pipe 20 and deodorized by the deodorizing device 25, effectively preventing the odor emission from the open surface of the deposited layer. be able to. Although not particularly shown, automatic valves V21 to V24
Switching of is automatically controlled by the timer setting.

【0019】なお、図示した第1実施例および第2実施
例においてはいずれも、多数の孔を穿設した発酵槽底板
の下方に設けた通気室を通気手段として使用し、この通
気室に空気を送入しあるいはこの通気室から空気を吸引
する構成によって発酵槽内の有機質廃物堆積層に通気を
行っている。しかしながら、本発明の発酵装置における
通気手段はこれに限定されるものではなく、例えば多数
の孔を長手方向に穿設した配管を通気手段として発酵槽
底板の上面近傍に配設し、この配管を介して空気を送入
あるいは吸引するような構成も採用することができる。
In each of the illustrated first and second embodiments, an aeration chamber provided below the fermenter bottom plate having a large number of holes is used as an aeration means, and air is supplied to the aeration chamber. Is introduced or air is sucked from the ventilation chamber to ventilate the organic waste deposit layer in the fermenter. However, the ventilation means in the fermentation apparatus of the present invention is not limited to this, for example, a pipe having a large number of holes bored in the longitudinal direction is arranged near the upper surface of the fermenter bottom plate as the ventilation means, and this pipe is It is also possible to employ a configuration in which air is introduced or sucked through.

【0020】さらに、図示の第1実施例および第2実施
例ではいずれも発酵槽底板を1段のみ備えた型式の発酵
槽を使用しているが、底板を多段に配設して発酵槽内部
に複数の棚段を形成するような型式の発酵槽とすること
も可能である。
Further, in both the illustrated first and second embodiments, the type of fermenter having only one fermenter bottom plate is used. It is also possible to have a type of fermenter in which a plurality of trays are formed.

【0021】また、通路切替手段は一般に自動弁とダク
トないし配管系とから構成できるが、自動弁としてはダ
ンパーや、電磁式、油圧式、気体式等の二方弁あるいは
三方弁等が採用することができる。
Further, the passage switching means can be generally constituted by an automatic valve and a duct or a piping system, but as the automatic valve, a damper, a two-way valve such as an electromagnetic type, a hydraulic type, a gas type or a three-way valve is adopted. be able to.

【0022】[0022]

【発明の効果】以上説明したところからわかるように本
発明においては、有機質廃物の堆積底部から上方に向け
て通気する上向流通気方式と、上方から堆積底部へ向け
て通気する下向流通気方式とを交互に組み合わせること
によって、上向流通気のみの場合に見られる堆積底部の
乾燥状態や、下向流通気のみの場合に見られる堆積底部
の過湿状態の発生を効果的に防止することができる。従
って、堆積底部の機械的切返しや掻き取りの難しい底部
固定式の発酵槽においても、発酵槽内の有機質廃物堆積
層の水分を堆積層底部から上面にわたって全体的に均一
に保つことができ、均質な好気性発酵を行なわせること
ができる。
As can be seen from the above description, in the present invention, an upward flowing air system in which air is vented upward from the bottom of the organic waste deposit, and a downward air flow in which air is vented from above to the bottom of the deposit. By alternately combining these methods, it is possible to effectively prevent the occurrence of a dry condition at the bottom of the pile, which can be seen only when the air flows upward, and an over-humidity condition at the bottom of the deposit, which can be seen only when the air flows downward. be able to. Therefore, even in a bottom fixed type fermenter where it is difficult to mechanically cut off the bottom of the pile or scrape it off, it is possible to keep the water content of the organic waste sedimentary layer in the fermenter uniform from the bottom to the top of the sedimentary layer. Aerobic fermentation can be performed.

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

【図1】 本発明による発酵装置の第1実施例におい
て、下向流通気方式の運転状態を示す説明図。
FIG. 1 is an explanatory diagram showing an operating state of a downward circulation air system in a first embodiment of a fermentation apparatus according to the present invention.

【図2】 図1に示した本発明による発酵装置の第1実
施例において、上向流通気方式の運転状態を示す説明
図。
FIG. 2 is an explanatory view showing an operating state of an upward circulation air system in the first embodiment of the fermentation apparatus according to the present invention shown in FIG.

【図3】 本発明による発酵装置の第2実施例を示す説
明図。
FIG. 3 is an explanatory view showing a second embodiment of the fermentation apparatus according to the present invention.

【図4】 従来の底部固定式発酵装置の一例を示す説明
図。
FIG. 4 is an explanatory view showing an example of a conventional bottom fixed fermentation apparatus.

【符号の説明】[Explanation of symbols]

1: 発酵槽 2: 底板 3: 通気室 4: 給気ブロワー V1〜V4: 自動弁 22: 底板 23: ブロワー V21〜V24: 自動弁 1: Fermenter 2: Bottom plate 3: Ventilation chamber 4: Air supply blower V1 to V4: Automatic valve 22: Bottom plate 23: Blower V21 to V24: Automatic valve

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C05F 7/00 7537−4H 9/04 7537−4H 17/00 7537−4H C12M 1/00 H ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location C05F 7/00 7537-4H 9/04 7537-4H 17/00 7537-4H C12M 1 / 00H

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 有機質廃物を堆積させる固定底板を備え
た発酵槽で有機質廃物を好気性発酵させる方法におい
て、酸素含有気体を有機質廃物の堆積底部から上方に向
けて通気する上向流通気と、酸素含有気体を上方から有
機質廃物の堆積底部に向けて通気する下向流通気とを交
互に行うことを特徴とする有機質廃物の発酵方法。
1. A method of aerobically fermenting an organic waste in a fermenter equipped with a fixed bottom plate for depositing the organic waste, in which an oxygen-containing gas is upwardly ventilated from the bottom of the organic waste to be aerated. A method for fermenting an organic waste, which comprises alternately performing downward flow air in which an oxygen-containing gas is aerated from above toward the bottom of the organic waste accumulation.
【請求項2】 有機質廃物を堆積させる固定底板の近傍
に通気手段を配設した発酵装置において、該通気手段は
タイマーにより切替えられる通路切替手段を介して気体
送風手段の吐出側と吸引側とに選択的に連絡され、該通
気手段と該気体送風手段の吐出側とが連絡されていると
きは、該気体送風手段の吸引側が酸素含有気体源と連絡
されていることを特徴とする有機質廃物の発酵装置。
2. A fermenter in which a ventilating means is disposed in the vicinity of a fixed bottom plate for accumulating organic waste, the ventilating means being provided on a discharge side and a suction side of a gas blowing means via a passage switching means switched by a timer. The organic waste is characterized in that the ventilation side and the discharge side of the gas blowing means are communicated selectively and the suction side of the gas blowing means is communicated with the oxygen-containing gas source. Fermentation equipment.
JP33188293A 1993-12-27 1993-12-27 Organic waste fermentation method and fermentation apparatus Expired - Fee Related JP2932921B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33188293A JP2932921B2 (en) 1993-12-27 1993-12-27 Organic waste fermentation method and fermentation apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33188293A JP2932921B2 (en) 1993-12-27 1993-12-27 Organic waste fermentation method and fermentation apparatus

Publications (2)

Publication Number Publication Date
JPH07184635A true JPH07184635A (en) 1995-07-25
JP2932921B2 JP2932921B2 (en) 1999-08-09

Family

ID=18248681

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33188293A Expired - Fee Related JP2932921B2 (en) 1993-12-27 1993-12-27 Organic waste fermentation method and fermentation apparatus

Country Status (1)

Country Link
JP (1) JP2932921B2 (en)

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KR100475554B1 (en) * 2002-05-24 2005-03-16 강윤식 Automatic air supply and drainage system for compost fermenting chamber
JP2005170743A (en) * 2003-12-11 2005-06-30 Digi I's Ltd Method and apparatus for composting organic waste material
CN100371440C (en) * 2005-09-30 2008-02-27 华南理工大学 Submerged solid fermentation method of fungus fermentation lacquer producing enzyme and its device
CN102807402A (en) * 2012-08-07 2012-12-05 深圳市东森环境技术有限公司 Bio-aeration automatic control device of sludge aerobic fermentation and control method for sludge aerobic fermentation
JP2016077961A (en) * 2014-10-16 2016-05-16 隆史 中下 Composting method and composting device
CN108405561A (en) * 2018-03-13 2018-08-17 庐江绿世代生态农业科技有限公司 A kind of kitchen garbage recovery processing technique
CN109929740A (en) * 2019-04-28 2019-06-25 王毅 Excrement sludge aerobic fermentation unit and its multilayer aerobic fermentation system
CN115197008A (en) * 2022-08-23 2022-10-18 湖北问心农业科技有限公司 Grape fertilizer fermentation device and fermentation process for preventing and treating root pests

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100475554B1 (en) * 2002-05-24 2005-03-16 강윤식 Automatic air supply and drainage system for compost fermenting chamber
JP2005170743A (en) * 2003-12-11 2005-06-30 Digi I's Ltd Method and apparatus for composting organic waste material
CN100371440C (en) * 2005-09-30 2008-02-27 华南理工大学 Submerged solid fermentation method of fungus fermentation lacquer producing enzyme and its device
CN102807402A (en) * 2012-08-07 2012-12-05 深圳市东森环境技术有限公司 Bio-aeration automatic control device of sludge aerobic fermentation and control method for sludge aerobic fermentation
JP2016077961A (en) * 2014-10-16 2016-05-16 隆史 中下 Composting method and composting device
CN108405561A (en) * 2018-03-13 2018-08-17 庐江绿世代生态农业科技有限公司 A kind of kitchen garbage recovery processing technique
CN109929740A (en) * 2019-04-28 2019-06-25 王毅 Excrement sludge aerobic fermentation unit and its multilayer aerobic fermentation system
CN115197008A (en) * 2022-08-23 2022-10-18 湖北问心农业科技有限公司 Grape fertilizer fermentation device and fermentation process for preventing and treating root pests
CN115197008B (en) * 2022-08-23 2024-03-12 问心农业科技(宜昌)有限公司 Fertilizer fermentation device and fermentation process

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