JP2003047941A - Organic waste composting apparatus - Google Patents

Organic waste composting apparatus

Info

Publication number
JP2003047941A
JP2003047941A JP2001240998A JP2001240998A JP2003047941A JP 2003047941 A JP2003047941 A JP 2003047941A JP 2001240998 A JP2001240998 A JP 2001240998A JP 2001240998 A JP2001240998 A JP 2001240998A JP 2003047941 A JP2003047941 A JP 2003047941A
Authority
JP
Japan
Prior art keywords
tank
fermentation
primary
compost
mixing
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
JP2001240998A
Other languages
Japanese (ja)
Other versions
JP3595290B2 (en
Inventor
Yosuke Tamura
陽右 田村
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.)
Soken Co Ltd
Original Assignee
Soken 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 Soken Co Ltd filed Critical Soken Co Ltd
Priority to JP2001240998A priority Critical patent/JP3595290B2/en
Publication of JP2003047941A publication Critical patent/JP2003047941A/en
Application granted granted Critical
Publication of JP3595290B2 publication Critical patent/JP3595290B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock
    • Y02P20/145Feedstock the feedstock being materials of biological origin
    • 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

  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)
  • Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)
  • Fertilizers (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an organic waste composting apparatus capable of manufacturing fully ripened high quality compost at a low cost by simple and highly durable equipment. SOLUTION: A mixing tank 2, a two-stage primary fermentation tank 3, a secondary fermentation tank 4 and a compost storage tank 5 are successively formed from an organic waste charging port 1a and demarcated by partition walls 6-1-6-4 in a composting tank 1. Pressure air blow means are provided to the mixing tank 2 and the primary and secondary fermentation tanks 3 and 4 to blow pressure air from the lower ends of those tanks and an air blow means for aerobic fermentation are provided to the mixing tank 2, the primary and secondary fermentation tanks 3 and 4 and the compost storage tank 5. The heights of the partition walls 6-1-6-4 are set so that a material to be treated can be successively transferred from the mixing tank 2 to the primary and secondary fermentation tanks 3 and 4 and the compost storage tank 5 by blowing in pressure air.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、脱水した有機汚泥
や生ゴミ及び食品残滓等の有機性廃棄物をコンポスト化
するための有機性廃棄物のコンポスト化装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an organic waste composting device for composting dehydrated organic sludge, organic waste such as food waste and food waste.

【0002】[0002]

【従来の技術】従来から、工場廃液や下水汚泥等の有機
汚泥は脱水してコンポスト化することにより処理されて
いる。このような処理のためのコンポスト化装置には堆
積式と機械式のものが通常使用されている。
2. Description of the Related Art Conventionally, organic sludge such as industrial waste liquid and sewage sludge has been treated by dehydration and composting. Stacking and mechanical composting devices are commonly used for such processes.

【0003】堆積式のコンポスト化装置は、三方を囲っ
た発酵槽内に脱水汚泥と返送コンポストを混合後に高く
堆積させ、底部からの空気の供給により発酵させるとい
うものである。そして、均一な発酵促進のため定期的に
ショベルローダで他の槽に移し替えながら混合汚泥を切
り返してコンポストを製造することができる。
The stacking type composting device is one in which dehydrated sludge and return compost are mixed and highly deposited in a fermenter surrounded by three sides and fermented by supplying air from the bottom. Then, the compost can be manufactured by cutting back the mixed sludge while periodically transferring it to another tank with a shovel loader in order to promote uniform fermentation.

【0004】このような堆積式のコンポスト化装置で
は、発酵日数を十分に確保できることと、被処理材を高
く堆積させるため、内部に発酵熱が蓄熱され、加温する
ことなく高い発酵温度が維持でき、完熟した高品質のコ
ンポストが製造できる。
In such a stacking type composting device, it is possible to secure a sufficient number of fermentation days and to accumulate the material to be treated at a high level, so that the heat of fermentation is stored inside and a high fermentation temperature is maintained without heating. It is possible to produce a ripe, high-quality compost.

【0005】一方、機械式のコンポスト化装置は、発酵
槽内に設置した機械装置で混合・切り返しを連続的に行
いながら高カロリーの副資材の添加または加温で発酵温
度を維持して、好気性発酵によりコンポストを製造可能
としたものである。
On the other hand, the mechanical composting device is preferable because the mechanical device installed in the fermentation tank maintains the fermentation temperature by continuously adding and heating high calorie auxiliary materials while continuously mixing and cutting. The compost can be produced by aerobic fermentation.

【0006】この機械式のコンポスト化装置では、自動
運転ができるとともに処理槽を密閉化できるので臭気や
防塵対策のための構造が簡単になる。また、乾燥機能と
相まって発酵時間を短縮できる。
In this mechanical type composting device, the operation tank can be automatically operated and the processing tank can be hermetically sealed, so that the structure for preventing odor and dust is simplified. Further, the fermentation time can be shortened in combination with the drying function.

【0007】[0007]

【発明が解決しようとする課題】ところが、堆積式のコ
ンポスト化装置では、時期をみてショベルローダによる
処理物の移し替え作業が必要なので、オペレータの労力
と熟練を必要とする。また、発酵槽を密閉化できないの
で、臭気及び防塵のための設備を必要とし、装置全体の
設置面積が大きくなってしまう。
However, in the pile-up type composting device, it is necessary to transfer the processed products by the shovel loader depending on the time, so the labor and skill of the operator are required. Further, since the fermenter cannot be hermetically sealed, equipment for odor and dust prevention is required, and the installation area of the entire apparatus becomes large.

【0008】一方、機械式のコンポスト化装置では、混
合・切り返し装置の構造に制限されるので、被処理物の
堆積高さと発酵日数を十分に確保することができない。
このため、装置の構造上乾燥が促進されやすいため、未
完熟のコンポストが製造される傾向がある。また、混合
・切り返しのための機構が腐食性のガスに接触するの
で、腐食防止のための対策が必要となりその耐用性が低
い。
On the other hand, in the mechanical composting device, since the structure of the mixing / cutting-back device is limited, it is not possible to sufficiently secure the deposition height of the object to be treated and the number of fermentation days.
For this reason, drying is likely to be promoted due to the structure of the apparatus, and thus unfinished compost tends to be produced. Moreover, since the mechanism for mixing and turning back comes into contact with corrosive gas, it is necessary to take measures to prevent corrosion, and its durability is low.

【0009】本発明は、完熟した高品質のコンポストを
簡単で且つ耐用性の高い設備でしかも低コストで製造で
きる有機性廃棄物のコンポスト化装置を提供することを
目的とする。
It is an object of the present invention to provide a composting device for organic waste, which is capable of producing ripe, high-quality compost with simple and highly durable equipment and at low cost.

【0010】[0010]

【課題を解決するための手段】本発明は、コンポスト化
槽に、有機性廃棄物の投入口から順に混合槽と少なくと
も2段の発酵槽とコンポスト貯槽とを仕切り壁によって
区画形成し、前記混合槽と発酵槽には、被処理材の混合
・切り返し及び移送を行わせるための圧力空気を下端か
ら吹き込む手段を備えるとともに、前記混合槽と発酵槽
及びコンポスト貯槽には、好気性発酵用の空気を吹き込
む手段を備え、前記仕切り壁の高さを、前記圧力空気の
吹き込みにより前記混合槽から発酵槽及びコンポスト貯
槽の順に被処理材を移送可能となるように設定したこと
を特徴とする。
According to the present invention, in a composting tank, a mixing tank, at least two stages of a fermentation tank and a compost storage tank are partitioned and formed in order from an input port of an organic waste, and the mixing is performed. The tank and the fermenter are equipped with a means for blowing pressurized air from the lower end for mixing, turning back and transferring the material to be treated, and the mixing tank, the fermenter and the compost storage tank are equipped with air for aerobic fermentation. And a height of the partition wall is set so that the material to be treated can be transferred in order from the mixing tank to the fermentation tank and the compost storage tank by blowing the pressure air.

【0011】このような構成において、前記混合槽及び
発酵槽のそれぞれに連通する開閉用の電動弁を配置し、
前記圧力空気を供給する単一のコンプレッサーを前記電
動弁に接続したものとすることができる。
In such a structure, an electric valve for opening and closing, which communicates with each of the mixing tank and the fermentation tank, is arranged,
A single compressor that supplies the pressurized air may be connected to the motor-operated valve.

【0012】なお、本明細書においていう「切り返し」
とは混合槽及び発酵槽内の被処理材を上下に移動させな
がら攪拌することを意味する。
The term "cutback" as used in this specification
Means to stir while moving the material to be treated in the mixing tank and the fermentation tank up and down.

【0013】[0013]

【発明の実施の形態】本発明では、コンポスト化槽に設
ける有機性廃棄物の投入口から順に混合槽と少なくとも
2段の発酵槽とコンポスト貯槽を仕切り壁により区画形
成し、混合槽と発酵槽には下端から圧力空気を吹き込む
手段を備えている。このため、混合槽では投入口から投
入された有機性廃棄物と後段の発酵槽から切り返された
発酵物とを混合させることができる。そして、空気を吹
き込む手段によって混合槽に空気を供給することで、有
機性廃棄物と発酵物の混合物を予備発酵させることがで
きる。なお、好気性発酵を促すため、空気を吹き込む手
段からの空気を加熱したものとしてもよい。
BEST MODE FOR CARRYING OUT THE INVENTION In the present invention, a mixing tank, at least two stages of a fermentation tank and a compost storage tank are sequentially formed from a partition wall in order from the organic waste charging port provided in the composting tank, and the mixing tank and the fermentation tank are formed. Is equipped with means for blowing pressurized air from the lower end. Therefore, in the mixing tank, it is possible to mix the organic waste charged from the charging port and the fermented material cut back from the subsequent fermentation tank. Then, by supplying air to the mixing tank by means of blowing air, the mixture of the organic waste and the fermented product can be pre-fermented. In addition, in order to promote aerobic fermentation, the air from the means for blowing air may be heated.

【0014】混合槽内の混合物は混合槽の下端からの圧
力空気の瞬間的な上昇流によって混合されると同時に仕
切り壁を越えて発酵槽に移送される。この発酵槽は少な
くとも2段として設けられ、それぞれに圧力空気を吹き
込む手段及び好気性発酵用の空気(または加熱空気)を
吹き込む手段を備えている。このため、第1段の発酵槽
では圧力空気による切り返しと次の第2段の発酵槽への
処理物の移送が行われると同時に空気により発酵が促進
される。したがって、発酵槽どうしの間の仕切り壁を越
えて次段の発酵槽に送られるにつれて発酵物の発酵が促
され、発酵槽の段数を適切にすることにより被処理物を
完熟したコンポストとすることができる。
The mixture in the mixing tank is mixed by the instantaneous rising flow of the pressurized air from the lower end of the mixing tank, and at the same time, it is transferred over the partition wall to the fermentation tank. This fermenter is provided as at least two stages, and each has a means for blowing pressurized air and a means for blowing air (or heated air) for aerobic fermentation. For this reason, in the first-stage fermenter, turning back by pressure air and transfer of the processed product to the next second-stage fermenter are performed, and at the same time fermentation is promoted by air. Therefore, the fermentation of the fermented product is promoted as it is sent to the next-stage fermenter over the partition wall between the fermenters, and the compost to be processed is made fully mature by appropriately adjusting the number of stages of the fermenter. You can

【0015】ここで、混合槽と発酵槽及びコンポスト貯
槽を区画する仕切り壁の高さは、混合槽と発酵槽に供給
され瞬間的な圧力空気による流動化によって各仕切り壁
を越えて移送できるように設定されている。このため、
混合槽から各段の発酵槽へ順に移送されながら被処理物
はコンポスト化され、最終段のコンポスト貯槽に供給さ
れる。そして、このコンポスト貯槽には好気性発酵用の
空気を吹き込む手段が設けられているので、前段の発酵
槽でコンポスト化された処理物を更に仕上げ発酵させる
ことができる。したがって、コンポスト貯槽内の処理物
を完熟したコンポストとして回収することができる。空
気吹き込み手段からの空気は好気性発酵を促すために加
熱された空気としてもよい。
Here, the height of the partition wall that divides the mixing tank, the fermentation tank, and the compost storage tank is set so that the partition wall can be transferred across each partition wall by the fluidization by the instantaneous pressurized air supplied to the mixing tank and the fermentation tank. Is set to. For this reason,
The material to be treated is composted while being sequentially transferred from the mixing tank to the fermentation tanks of the respective stages, and is supplied to the compost storage tank of the final stage. Since the compost storage tank is provided with a means for blowing air for aerobic fermentation, it is possible to further finish and ferment the processed product composted in the former fermentation tank. Therefore, the processed material in the compost storage tank can be collected as fully-ripened compost. The air from the air blowing means may be heated air to promote aerobic fermentation.

【0016】なお、発酵槽とコンポスト槽との間の仕切
り壁の上端には高さと角度を変更可能な機構によって連
接したガイドを設けることができる。このようなガイド
を設けることによって、各仕切り壁を越えて移送される
被処理材の移送量を調節することができるとともに逆流
を防止することができる。
A guide connected by a mechanism whose height and angle can be changed can be provided at the upper end of the partition wall between the fermentation tank and the compost tank. By providing such a guide, it is possible to adjust the transfer amount of the material to be processed transferred across each partition wall and prevent backflow.

【0017】また、混合槽及び発酵槽のそれぞれに連通
する開閉用の電動弁を配置し、圧力空気を供給する単一
のコンプレッサーを電動弁に接続したものでは、単一の
コンプレッサーによって混合槽及び発酵槽のそれぞれに
圧力空気を供給することができるので、設備を簡単にす
ることができる。
Further, in the case where a motor-operated valve for opening and closing, which communicates with each of the mixing tank and the fermentation tank, is arranged and a single compressor for supplying pressurized air is connected to the motor-operated valve, the mixing tank and the single tank are connected by a single compressor. Since pressurized air can be supplied to each of the fermenters, the equipment can be simplified.

【0018】[0018]

【実施例】以下、本発明の実施例を図面に基づいて説明
する。
Embodiments of the present invention will be described below with reference to the drawings.

【0019】図1は本発明のコンポスト化装置の概略図
である。
FIG. 1 is a schematic view of a composting device of the present invention.

【0020】図において、コンポスト化装置はコンポス
ト化槽1によって構成されたものである。このコンポス
ト化槽1の左側壁の上端部には脱水された有機汚泥を投
入するための投入口1aを開けるとともに右側壁の下端
側には製造されたコンポストを回収するための回収口1
bを設けている。また、コンポスト化槽1の上端には内
部で発生するベーパーを排気するための除塵機能を有し
た排気室1cを設け、その下流には脱臭装置1dを配置
している。このような排気室1cと脱臭装置1dを設け
ることにより、コンポスト化槽1内で発生するベーパー
の塵が取り除かれるとともに臭気を脱臭して大気に放出
することができる。
In the figure, the composting device is composed of a composting tank 1. At the upper end of the left side wall of the composting tank 1, an input port 1a for inputting dehydrated organic sludge is opened, and at the lower end side of the right side wall, a recovery port 1 for collecting the produced compost.
b is provided. Further, an exhaust chamber 1c having a dust removing function for exhausting vapor generated inside is provided at the upper end of the composting tank 1, and a deodorizing device 1d is disposed downstream thereof. By providing the exhaust chamber 1c and the deodorizing device 1d as described above, the dust of the vapor generated in the composting tank 1 can be removed and the odor can be deodorized and released to the atmosphere.

【0021】コンポスト化槽1の内部は投入口1a側の
上流から回収口1b側の下流にかけて混合槽2,一次発
酵槽3,二次発酵槽4,コンポスト貯槽5がそれぞれ形
成されている。これらの各槽は仕切り壁6−1,6−
3,6−4によって区画されたものである。そして、一
次発酵槽3は仕切り壁6−2により一次発酵槽第一室3
−1と一次発酵槽第二室3−2に区画されている。仕切
り壁6−3,6−4の上端にはそれぞれガイド6−3
a,6−4aをそれぞれ設ける。これらのガイド6−3
a,6−4aはそれぞれ高さと角度を調整できる機構
(図示せず)によって仕切り壁6−3,6−4の上端に
連接されたものである。
Inside the composting tank 1, a mixing tank 2, a primary fermentation tank 3, a secondary fermentation tank 4, and a compost storage tank 5 are formed from the upstream side on the input port 1a side to the downstream side on the recovery port 1b side. Each of these tanks has partition walls 6-1, 6-
It is divided by 3, 6-4. The primary fermentation tank 3 is separated by the partition wall 6-2 into the primary fermentation tank first chamber 3
-1 and the second chamber 3-2 of the primary fermentation tank. Guides 6-3 are provided at the upper ends of the partition walls 6-3 and 6-4, respectively.
a and 6-4a are provided respectively. These guides 6-3
Reference characters a and 6-4a are connected to the upper ends of the partition walls 6-3 and 6-4 by a mechanism (not shown) capable of adjusting the height and the angle.

【0022】ここで、仕切り壁6−1〜6−4において
は、仕切り壁6−3が最も高い。そして、混合槽2に投
入された脱水汚泥と一次発酵槽3内に堆積する脱水汚泥
及び発酵物のレベルはこの仕切り壁6−3よりも少し低
い。仕切り壁6−1は脱水汚泥及び発酵物のレベルより
も低く設定され、投入口1aから投入された脱水汚泥及
び一次発酵槽3内からの切り返された発酵物の混合物は
仕切り壁6−1を越えて一次発酵槽3内に移動すること
ができる。仕切り壁6−2は最も低く一次発酵槽第一室
3−1と二次発酵槽第二室3−2を区画し、発酵物を一
次発酵槽3内の全体で後述する圧力空気により流動化さ
せることができる。仕切り壁6−4は前段の仕切り壁6
−3よりも少し低い高さを持ち、二次発酵槽4内の発酵
物が圧力空気により流動化されて押し上げられた分が仕
切り壁6−4を越えてコンポスト貯槽5に供給される。
なお、仕切り壁6−3,6−4にはそれぞれ高さと角度
を調節可能なガイド6−3a,6−4aを設けているの
で、一次発酵槽3から二次発酵槽4、及び二次発酵槽4
からコンポスト槽5へのそれぞれの移動量を調節できる
とともに、二次発酵槽4から一次発酵槽3及びコンポス
ト槽5から二次発酵槽4への逆流が防止される。
Here, among the partition walls 6-1 to 6-4, the partition wall 6-3 is the highest. The levels of the dehydrated sludge charged in the mixing tank 2, the dehydrated sludge accumulated in the primary fermentation tank 3 and the fermented material are slightly lower than those of the partition wall 6-3. The partition wall 6-1 is set lower than the level of the dehydrated sludge and the fermented product, and the mixture of the dehydrated sludge injected from the input port 1a and the fermented product cut back from the inside of the primary fermentation tank 3 is applied to the partition wall 6-1. It can be moved over and moved into the primary fermentation tank 3. The partition wall 6-2 is the lowest and partitions the primary fermentation tank first chamber 3-1 and the secondary fermentation tank second chamber 3-2, and the fermented product is fluidized in the primary fermentation tank 3 as a whole by the pressure air described later. Can be made. The partition wall 6-4 is the front partition wall 6
The height of the fermented material in the secondary fermentation tank 4 is slightly lower than -3, and the fermented material in the secondary fermentation tank 4 is fluidized by the pressure air and pushed up, and is supplied to the compost storage tank 5 over the partition wall 6-4.
Since the partition walls 6-3 and 6-4 are provided with guides 6-3a and 6-4a whose height and angle can be adjusted, respectively, the primary fermentation tank 3 to the secondary fermentation tank 4 and the secondary fermentation tank 4 can be used. Tank 4
It is possible to adjust the amount of transfer from the fermenter to the compost tank 5 and prevent backflow from the secondary fermentation tank 4 to the primary fermentation tank 3 and from the compost tank 5 to the secondary fermentation tank 4.

【0023】混合槽2,一次発酵槽第一室3−1,一次
発酵槽第二室3−2,二次発酵槽4,コンポスト貯槽5
のそれぞれには2本ずつの空気供給管7が配置されてい
る。また、混合槽2,一次発酵槽第一室3−1,一次発
酵槽第二室3−2,二次発酵槽4には圧力空気供給管8
がそれぞれ配置されている。混合槽2,一次発酵槽第一
室3−1,一次発酵槽第二室3−2,二次発酵槽4の圧
力空気供給管8はそれぞれ開閉式の電動弁9−1,9−
2,9−3,9−4に接続されている。これらの開閉式
の電動弁9−1〜9−4は圧力タンク10を介してコン
プレッサー11に接続されている。また、空気供給管7
は中途に発酵温度を補うためのヒータ12を設けた送風
機13からの流路に接続されている。
Mixing tank 2, primary fermentation tank first chamber 3-1, primary fermentation tank second chamber 3-2, secondary fermentation tank 4, compost storage tank 5
Two air supply pipes 7 are arranged in each of the above. In addition, a pressure air supply pipe 8 is provided in the mixing tank 2, the primary fermentation tank first chamber 3-1, the primary fermentation tank second chamber 3-2, and the secondary fermentation tank 4.
Are arranged respectively. The pressure air supply pipes 8 of the mixing tank 2, the primary fermentation tank first chamber 3-1, the primary fermentation tank second chamber 3-2, and the secondary fermentation tank 4 are open / close motorized valves 9-1, 9-, respectively.
2, 9-3, 9-4 are connected. These open / close type electric valves 9-1 to 9-4 are connected to a compressor 11 via a pressure tank 10. Also, the air supply pipe 7
Is connected to a flow path from a blower 13 provided with a heater 12 for supplementing the fermentation temperature midway.

【0024】空気供給管7にはヒータ12によって加熱
された空気が供給され、脱水汚泥の予備発酵や一次,二
次の発酵槽3,4及びコンポスト貯槽5内での最終発酵
を行わせる。また、圧力空気供給管8は下側から上に向
けて圧力空気を供給するもので、脱水汚泥及び発酵物の
混合及び切り返しと下流側への移送を行わせる。
Air heated by a heater 12 is supplied to the air supply pipe 7 to perform pre-fermentation of dehydrated sludge and final fermentation in the primary and secondary fermentation tanks 3 and 4 and the compost storage tank 5. Further, the pressurized air supply pipe 8 supplies pressurized air from the lower side to the upper side, and mixes and cuts back the dehydrated sludge and the fermented product and transfers it to the downstream side.

【0025】なお、電動弁9−1〜9−4,コンプレッ
サー11,ヒータ12及び送風機13は図示しないコン
トローラによって制御されるものとする。
The electric valves 9-1 to 9-4, the compressor 11, the heater 12 and the blower 13 are controlled by a controller (not shown).

【0026】以上の構成において、コンポスト化槽1内
の混合槽2には投入口1aから脱水汚泥aが投入され、
一次発酵槽3内では一次発酵物bが創成され、二次発酵
槽4内では二次発酵物cが創成され、コンポスト貯槽5
内では最終製品としてのコンポストdが創成され、コン
ポストdは回収口1bから排出コンポストとして回収さ
れる。このような脱水汚泥aの投入から排出コンポスト
の回収までは連続的に処理されるもので、この処理は図
1から図4の工程により順次行われる。
In the above construction, the dehydrated sludge a is charged into the mixing tank 2 in the composting tank 1 through the charging port 1a,
The primary fermentation product b is created in the primary fermentation tank 3, the secondary fermentation product c is created in the secondary fermentation tank 4, and the compost storage tank 5 is created.
A compost d as a final product is created therein, and the compost d is recovered as a discharge compost from the recovery port 1b. From the input of such dehydrated sludge a to the collection of discharged compost, the treatment is performed continuously, and this treatment is sequentially performed by the steps of FIGS. 1 to 4.

【0027】図1において、投入口1aから投入された
脱水汚泥aは混合槽2内に収容される。このとき、仕切
り壁6−1は混合槽2内及び一次発酵槽3内の一次発酵
物bのレベルよりも低いので、電動弁9−1を開弁して
圧力空気供給管8から圧力空気を上昇流として瞬間的に
且つ断続的に供給すると流動化によって脱水汚泥aと一
次発酵物bは混合される。すなわち、一次発酵槽第一室
3−1での切り返し操作によって一部が混合槽2側に返
送された一次発酵物bが脱水汚泥aと混合されると同時
に、この混合物の一部は一次発酵槽第一室3−1に移送
される。また、混合槽2内の脱水汚泥aと一次発酵物b
の混合物は空気供給管7からの空気の吹き込みにより予
備発酵させられる。なお、圧力空気供給管8からの圧力
空気の吹き込みは脱水汚泥aを投入している期間で適正
な回数だけ行うものとする。
In FIG. 1, the dehydrated sludge a charged through the charging port 1a is stored in the mixing tank 2. At this time, since the partition wall 6-1 is lower than the level of the primary fermented product b in the mixing tank 2 and the primary fermentation tank 3, the motor-operated valve 9-1 is opened and pressurized air is supplied from the pressurized air supply pipe 8. When it is instantaneously and intermittently supplied as an upward flow, the dehydrated sludge a and the primary fermented product b are mixed by fluidization. That is, the primary fermented product b, part of which has been returned to the mixing tank 2 side by the turning operation in the primary fermentation tank first chamber 3-1, is mixed with the dehydrated sludge a, and at the same time, part of this mixture is subjected to primary fermentation. It is transferred to the tank first chamber 3-1. In addition, dehydrated sludge a and primary fermented product b in the mixing tank 2
The mixture of 1 is pre-fermented by blowing air from the air supply pipe 7. The pressure air is blown from the pressure air supply pipe 8 a proper number of times during the period in which the dehydrated sludge a is charged.

【0028】図2は図1の工程に続いて、一次発酵槽第
一室3−1に配置した圧力空気供給管8に接続した電動
弁9−2だけを開弁させて一次発酵槽第一室3−1内で
脱水汚泥aと一次発酵物bを混合している状態を示す。
この工程では、含まれている脱水汚泥aに対しても空気
供給管7からの空気によって好気性発酵による発酵が促
され、時間の経過とともに全体が一次発酵物bに変化し
ていく。
FIG. 2 shows that, following the process of FIG. 1, only the motor-operated valve 9-2 connected to the pressure air supply pipe 8 arranged in the primary fermenter first chamber 3-1 is opened to open the primary fermenter first chamber. The state where the dehydrated sludge a and the primary fermentation product b are mixed in the chamber 3-1 is shown.
In this process, the dehydrated sludge a contained therein is also aerobically fermented by the air from the air supply pipe 7, and the whole is changed to the primary fermented product b over time.

【0029】図3は図2の工程に続いて一次発酵槽第二
室3−2に配置した圧力空気供給管8に接続した電動弁
9−3だけを開弁させた状態を示すものである。この工
程では、一次発酵槽第一室3−1で発酵処理された一次
発酵物bを更に空気供給管7からの空気によって均一に
好気性発酵させると同時に圧力空気供給管8からの圧力
空気によって切り返して発酵を促している。そして、圧
力空気の上昇流によって切り返された一次発酵物bの一
部が仕切り壁6―3を越えて二次発酵槽4へ移動する。
FIG. 3 shows a state in which only the motor-operated valve 9-3 connected to the pressure air supply pipe 8 arranged in the second chamber 3-2 of the primary fermentation tank is opened following the process of FIG. . In this step, the primary fermented product b fermented in the primary fermenter first chamber 3-1 is further aerobically fermented uniformly with air from the air supply pipe 7, and at the same time with pressurized air from the pressure air supply pipe 8. It is turned back to promote fermentation. Then, a part of the primary fermented product b cut back by the upward flow of the pressure air moves to the secondary fermentation tank 4 over the partition wall 6-3.

【0030】以上までの工程で、発酵を促された一次発
酵物bが創成され、コンポストに近い状態にまで変化さ
せることができる。
Through the above steps, the primary fermented product b in which the fermentation is promoted is created and can be changed to a state close to compost.

【0031】図4は図3の工程に続くもので、電動弁9
−4だけを開弁させた状態を示すものである。この工程
では、一次発酵物bが更に空気供給管7からの空気によ
って好気性発酵が促されて二次発酵物cに変化する。そ
して、圧力空気供給管8からの圧力空気の上昇流によっ
て、均一発酵のために切り返されると同時に二次発酵物
cが仕切り壁6−4を乗り越えてコンポスト貯槽5に移
送される。
FIG. 4 is a continuation of the process of FIG.
It shows a state in which only -4 is opened. In this step, the primary fermented product b is further promoted aerobic fermentation by the air from the air supply pipe 7, and is converted into the secondary fermented product c. Then, due to the upward flow of the pressurized air from the pressurized air supply pipe 8, the secondary fermented product c is transferred back to the compost storage tank 5 over the partition wall 6-4 while being cut back for uniform fermentation.

【0032】コンポスト貯槽5内に移動してきた二次発
酵物cは空気供給管7からの空気によって更に好気性発
酵させられて仕上げ発酵が促される。すなわち、コンポ
スト貯槽5内に移送されてきた二次発酵物cは仕上げ発
酵によって完熟したコンポストdとなる。そして、貯留
されたコンポストdは定期的に回収口1bから取り出す
ことにより製品として回収される。
The secondary fermented product c that has moved into the compost storage tank 5 is further aerobically fermented by the air from the air supply pipe 7 to promote finish fermentation. That is, the secondary fermented material c transferred to the compost storage tank 5 becomes the compost d that has been matured by the finish fermentation. Then, the stored compost d is recovered as a product by periodically taking out from the recovery port 1b.

【0033】このように、電動弁9−1〜9−4を順に
開弁していくことによって、混合槽2,一次発酵槽第一
室3−1,一次発酵槽第二室3−2,二次発酵槽4内の
処理物を混合しながら下流側に移送することができる。
そして、混合槽2内では脱水汚泥aと一次発酵物bの混
合物が空気供給管7からの空気によって予備発酵され、
一次発酵槽第一室3−1,一次発酵槽第二室3−2及び
二次発酵槽4においても空気供給管7からの空気によっ
て発酵が促される。したがって、電動弁9−1〜9−4
を順次開閉していくことにより、二次発酵槽4内の二次
発酵物cはほぼコンポスト状態とすることができる。そ
して、電動弁9−4が開弁して二次発酵物cがコンポス
ト貯槽5に移送された後には、空気供給管7からの空気
により二次発酵物cが更に発酵処理されてコンポストd
を得ることができる。
In this way, by sequentially opening the motor-operated valves 9-1 to 9-4, the mixing tank 2, the primary fermentation tank first chamber 3-1, the primary fermentation tank second chamber 3-2. The processed material in the secondary fermentation tank 4 can be transferred to the downstream side while being mixed.
Then, in the mixing tank 2, the mixture of the dehydrated sludge a and the primary fermentation product b is pre-fermented by the air from the air supply pipe 7,
In the primary fermentation tank first chamber 3-1, the primary fermentation tank second chamber 3-2, and the secondary fermentation tank 4 as well, fermentation is promoted by the air from the air supply pipe 7. Therefore, the motor operated valves 9-1 to 9-4
By sequentially opening and closing, the secondary fermented product c in the secondary fermenter 4 can be almost composted. Then, after the motor-operated valve 9-4 is opened and the secondary fermented product c is transferred to the compost storage tank 5, the secondary fermented product c is further fermented by the air from the air supply pipe 7 to compost d.
Can be obtained.

【0034】本発明のコンポスト化装置では、コンポス
ト化槽に圧力空気と空気を供給するだけの操作でコンポ
ストdを得ることができる。したがって、コンポスト化
槽1内に脱水汚泥や発酵物を移送したり混合したりする
機構が不要となり、脱水汚泥やベーパー等と接触する可
動部材がなくて済む。このため、可動部材の腐食対策等
が不要となり設備を簡単にすることができる。また、圧
力空気を供給する手段は各電動弁9−1〜9−4に接続
した単一のコンプレッサー11なので、各槽ごとにコン
プレッサーを備える場合に比べると設備がより簡単にな
る。
In the composting apparatus of the present invention, the compost d can be obtained by simply supplying pressurized air and air to the composting tank. Therefore, a mechanism for transferring or mixing dehydrated sludge or fermented material in the composting tank 1 is not required, and a movable member that comes into contact with the dehydrated sludge or vapor is unnecessary. Therefore, it is not necessary to take measures against corrosion of the movable member and the facility can be simplified. Further, since the means for supplying the compressed air is the single compressor 11 connected to each of the motor-operated valves 9-1 to 9-4, the equipment becomes simpler than the case where a compressor is provided for each tank.

【0035】なお、実施例では脱水有機汚泥のコンポス
ト化について説明したが、その他の各種の有機性廃棄物
についても本発明のコンポスト化装置によってコンポス
ト化が可能である。また、発酵槽は一次発酵槽3と二次
発酵槽4の2段としたがこれ以上の段数としてもよく、
要するにコンポスト貯槽5に至るまでに処理物が十分に
コンポスト化される段数であればよい。
In the examples, the composting of dehydrated organic sludge was described, but other various kinds of organic waste can also be composted by the composting device of the present invention. Further, the fermenter has two stages of the primary fermenter 3 and the secondary fermentor 4, but the number of stages may be more than this,
In short, the number of stages is sufficient as long as the processed product is sufficiently composted before reaching the compost storage tank 5.

【0036】[0036]

【発明の効果】請求項1の発明では、コンポスト化槽の
投入口から有機性廃棄物を投入するだけで、混合槽から
発酵槽にかけてコンポスト化の処理ができ、この処理は
圧力空気の供給と空気または加熱空気の送り込みの操作
により実現できるので、簡単な装置での処理が可能とな
る。このため、従来の機械式コンポスト化装置に比べて
構造が簡単になるほか、発酵物及びベーパーに駆動部が
接触しないので、腐食対策が不要となる。また、コンポ
スト化槽を高くすることによって、処理物を高く堆積さ
せることができるので設置面積を小さくすることができ
るとともに処理物の蓄熱効果により加熱発酵のための動
力費を安価にすることができる。さらに、コンポスト化
槽を密閉式とすることができるので、保温性を高く維持
でき処理物の発酵を効率的に行うことができる。
According to the first aspect of the present invention, the composting process can be performed from the mixing tank to the fermentation tank only by adding the organic waste from the charging port of the composting tank. Since it can be realized by the operation of feeding air or heated air, the processing can be performed with a simple device. Therefore, the structure is simpler than that of the conventional mechanical composting device, and the fermented material and the vapor are not brought into contact with the drive unit, so that no corrosion countermeasure is required. In addition, by increasing the height of the composting tank, it is possible to deposit the processed material at a high level, so that it is possible to reduce the installation area and to reduce the power cost for heating fermentation due to the heat storage effect of the processed material. . Furthermore, since the composting tank can be of a closed type, the heat retaining property can be maintained high and the fermented product can be efficiently fermented.

【0037】請求項2の発明では、単一のコンプレッサ
ーにより混合槽及び発酵槽に圧力空気を供給できるの
で、設備をより簡単にすることができる。
According to the second aspect of the invention, the compressed air can be supplied to the mixing tank and the fermentation tank by a single compressor, so that the equipment can be simplified.

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

【図1】 本発明のコンポスト化装置の概略図であっ
て、混合槽に圧力空気を供給して槽内の混合汚泥を流動
させて混合と一次発酵槽への一部移動が行われている状
態を示す。
FIG. 1 is a schematic view of a composting apparatus of the present invention, in which pressurized air is supplied to a mixing tank to cause the mixed sludge in the tank to flow to perform mixing and partial transfer to the primary fermentation tank. Indicates the status.

【図2】 一次発酵槽第一室に圧力空気を供給して槽内
の一次発酵物を流動させて切り返しが行われている状態
を示す説明図。
FIG. 2 is an explanatory view showing a state in which pressurized air is supplied to the first chamber of the primary fermentation tank to cause the primary fermentation product in the tank to flow and to be cut back.

【図3】 一次発酵槽第二室に圧力空気を供給して槽内
の一次発酵物を流動させて切り返しと二次発酵槽への一
部移動が行われている状態を示す説明図。
FIG. 3 is an explanatory view showing a state in which pressurized air is supplied to the second chamber of the primary fermentation tank to flow the primary fermented material in the tank to cut it back and partially move it to the secondary fermentation tank.

【図4】 二次発酵槽に圧力空気を供給して槽内の二次
発酵物を流動させて切り返しとコンポスト貯槽への一部
移動が行われている状態を示す説明図。
FIG. 4 is an explanatory view showing a state in which pressurized air is supplied to the secondary fermentation tank to cause the secondary fermented material in the tank to flow and to be cut back and partially moved to the compost storage tank.

【符号の説明】[Explanation of symbols]

1 コンポスト化槽 1a 投入口 1b 回収口 1c 排気室 1d 脱臭装置 2 混合槽 3 一次発酵槽 3−1 一次発酵槽第一室 3−2 一次発酵槽第二室 4 二次発酵槽 5 コンポスト貯槽 6−1,6−2,6−3,6−4 仕切り壁 6−3a,6−4a ガイド 7 空気供給管 8 圧力空気供給管 9−1,9−2,9−3,9−4 電動弁 10 圧力室 11 コンプレッサー 12 ヒータ 13 送風機 a 脱水汚泥 b 一次発酵物 c 二次発酵物 d コンポスト 1 Composting tank 1a Input port 1b Collection port 1c Exhaust chamber 1d deodorizing device 2 mixing tanks 3 Primary fermenter 3-1 Primary fermentation tank first room 3-2 Primary fermentation tank second room 4 Secondary fermenter 5 Compost storage tank 6-1, 6-2, 6-3, 6-4 Partition wall 6-3a, 6-4a guide 7 Air supply pipe 8 Pressure air supply pipe 9-1, 9-2, 9-3, 9-4 Motorized valve 10 Pressure chamber 11 compressor 12 heater 13 blower a Dewatered sludge b Primary fermentation product c Secondary fermentation d compost

フロントページの続き Fターム(参考) 4D004 AA02 AA03 AC04 CA19 CA48 CB04 CB06 CB21 CB47 4D059 AA05 AA07 BA03 BA44 BA48 BA51 BJ09 CA16 CB01 CB07 4G035 AB48 AE13 AE15 4G036 AC13 4H061 AA03 CC42 CC51 CC55 EE03 FF06 GG12 GG14 GG41 GG49 GG69 Continued front page    F-term (reference) 4D004 AA02 AA03 AC04 CA19 CA48                       CB04 CB06 CB21 CB47                 4D059 AA05 AA07 BA03 BA44 BA48                       BA51 BJ09 CA16 CB01 CB07                 4G035 AB48 AE13 AE15                 4G036 AC13                 4H061 AA03 CC42 CC51 CC55 EE03                       FF06 GG12 GG14 GG41 GG49                       GG69

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 コンポスト化槽に、有機性廃棄物の投入
口から順に混合槽と少なくとも2段の発酵槽とコンポス
ト貯槽とを仕切り壁によって区画形成し、前記混合槽と
発酵槽には、被処理材の混合・切り返し及び移送を行わ
せるための圧力空気を下端から吹き込む手段を備えると
ともに、前記混合槽と発酵槽及びコンポスト貯槽には、
好気性発酵用の空気を吹き込む手段を備え、前記仕切り
壁の高さを、前記圧力空気の吹き込みにより前記混合槽
から発酵槽及びコンポスト貯槽の順に被処理材を移送可
能となるように設定したことを特徴とする有機性廃棄物
のコンポスト化装置。
1. A composting tank is formed by partitioning a mixing tank, at least two stages of fermentation tanks and a compost storage tank in order from an organic waste charging port, and the mixing tank and the fermentation tank are covered with With a means for blowing pressure air from the lower end for mixing, turning back and transferring the processing material, the mixing tank, the fermentation tank and the compost storage tank,
A means for blowing air for aerobic fermentation is provided, and the height of the partition wall is set so that the material to be treated can be transferred in order from the mixing tank to the fermentation tank and the compost storage tank by blowing the pressure air. A composting device for organic waste.
【請求項2】 前記混合槽及び発酵槽のそれぞれに連通
する開閉用の電動弁を配置し、前記圧力空気を供給する
単一のコンプレッサーを前記電動弁に接続したことを特
徴とする請求項1記載の有機性廃棄物のコンポスト化装
置。
2. A motor-operated valve for opening and closing, which communicates with each of the mixing tank and the fermentation tank, is arranged, and a single compressor for supplying the compressed air is connected to the motor-operated valve. The described apparatus for composting organic waste.
JP2001240998A 2001-08-08 2001-08-08 Organic waste composting equipment Expired - Fee Related JP3595290B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001240998A JP3595290B2 (en) 2001-08-08 2001-08-08 Organic waste composting equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001240998A JP3595290B2 (en) 2001-08-08 2001-08-08 Organic waste composting equipment

Publications (2)

Publication Number Publication Date
JP2003047941A true JP2003047941A (en) 2003-02-18
JP3595290B2 JP3595290B2 (en) 2004-12-02

Family

ID=19071523

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001240998A Expired - Fee Related JP3595290B2 (en) 2001-08-08 2001-08-08 Organic waste composting equipment

Country Status (1)

Country Link
JP (1) JP3595290B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006218384A (en) * 2005-02-09 2006-08-24 Mitsui Eng & Shipbuild Co Ltd Method for drying hydrous material and method for manufacturing compost
JP2006219332A (en) * 2005-02-09 2006-08-24 Mitsui Eng & Shipbuild Co Ltd Compost manufacturing device
WO2008099227A1 (en) * 2007-02-12 2008-08-21 Ingenieurgemeischaft Luxemburg Sarl Method and device for producing biogas from a biomass
JP2011157238A (en) * 2010-02-02 2011-08-18 Mitsui Zosen Environment Engineering Corp Compost production apparatus and method therefor

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006218384A (en) * 2005-02-09 2006-08-24 Mitsui Eng & Shipbuild Co Ltd Method for drying hydrous material and method for manufacturing compost
JP2006219332A (en) * 2005-02-09 2006-08-24 Mitsui Eng & Shipbuild Co Ltd Compost manufacturing device
JP4553746B2 (en) * 2005-02-09 2010-09-29 三井造船環境エンジニアリング株式会社 Method for drying hydrous material and method for producing compost
WO2008099227A1 (en) * 2007-02-12 2008-08-21 Ingenieurgemeischaft Luxemburg Sarl Method and device for producing biogas from a biomass
JP2011157238A (en) * 2010-02-02 2011-08-18 Mitsui Zosen Environment Engineering Corp Compost production apparatus and method therefor

Also Published As

Publication number Publication date
JP3595290B2 (en) 2004-12-02

Similar Documents

Publication Publication Date Title
CN2609925Y (en) Closed compost fermentation device
US2929688A (en) Composting apparatus
CN108191189A (en) Multilayer sludge aerobic installation for fermenting and method
CN104289497B (en) A kind of multi-stage Semi-continuous Organic Refuse Bioreactor and method
CN105062876A (en) Solid state fermentation device, system and fermentation method of movable material distribution
CN1970507A (en) Full-automatic negative pressure fermentation and deodorization device and production process for organic fertilizer
JP2003047941A (en) Organic waste composting apparatus
EP1431262B1 (en) A method and a plant for the aerobic treatment of materials having a highly fermentable organic component
CN105062875A (en) Solid-state fermentation device with uniform material distribution function and fermentation method
JP2000354897A (en) Aerobic fermentation method and apparatus of organic solid waste
EP0707559B1 (en) Plant and process for composting organic material
JPH06304542A (en) Treating device for solid organic waste
CN204918580U (en) Remove solid state fermentation device and system of cloth
CN208680137U (en) Kitchen garbage after-treatment system
JPWO2007083379A1 (en) Cement production raw fuel production facility, cement production plant, and waste cement raw fuel conversion method
CN115231966B (en) Integrated aerobic fermentation equipment and fermentation process thereof
CN204918406U (en) Remove working bin robot of stirring and cloth suitable for solid state fermentation
JP2003335594A (en) Composting facility
JPS5829145Y2 (en) Fermentation equipment that produces fully ripened compost
JPH07241540A (en) Fermentation treatment apparatus for organic material
JP3481109B2 (en) Composting of garbage
JP2000119083A (en) Composting of both garbage and organic matter residue
JP2005034041A (en) Method for producing methane gas and fermentation product by combined use of anaerobic bacterium methane gas fermentation and aerobic bacterium fermentation and apparatus therefor
JP2007176756A (en) Apparatus and method of manufacturing compost
JPS5942100A (en) Fermentation device for organic waste

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20040720

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20040803

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20040902

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20070910

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080910

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080910

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100910

Year of fee payment: 6

LAPS Cancellation because of no payment of annual fees