JP2632227B2 - Organic waste fermentation treatment system - Google Patents
Organic waste fermentation treatment systemInfo
- Publication number
- JP2632227B2 JP2632227B2 JP2064913A JP6491390A JP2632227B2 JP 2632227 B2 JP2632227 B2 JP 2632227B2 JP 2064913 A JP2064913 A JP 2064913A JP 6491390 A JP6491390 A JP 6491390A JP 2632227 B2 JP2632227 B2 JP 2632227B2
- Authority
- JP
- Japan
- Prior art keywords
- fermentation
- organic waste
- fermentation treatment
- tank
- processing tank
- 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 - Fee Related
Links
- 238000000855 fermentation Methods 0.000 title claims description 71
- 230000004151 fermentation Effects 0.000 title claims description 71
- 239000010815 organic waste Substances 0.000 title claims description 28
- 238000003756 stirring Methods 0.000 claims description 29
- 238000012545 processing Methods 0.000 claims description 28
- 238000001035 drying Methods 0.000 claims description 14
- 239000000463 material Substances 0.000 claims description 12
- 239000000203 mixture Substances 0.000 description 15
- 239000002699 waste material Substances 0.000 description 13
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- 241000894006 Bacteria Species 0.000 description 4
- 241000287828 Gallus gallus Species 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000010828 animal waste Substances 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 235000013405 beer Nutrition 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 235000013311 vegetables Nutrition 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 241000283690 Bos taurus Species 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 241000282898 Sus scrofa Species 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 230000003698 anagen phase Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 210000000988 bone and bone Anatomy 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 239000010908 plant waste Substances 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/145—Feedstock the feedstock being materials of biological origin
Landscapes
- Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)
- Fertilizers (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は、廃鶏などの動物性廃棄物や漢方薬やビール
や酒の搾り糟などの植物性廃棄物を発酵処理する有機廃
棄物の発酵処理システムに関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to fermentation of organic waste for fermenting animal waste such as waste chicken and vegetable waste such as Chinese medicine, beer and sake squeezer. It relates to a processing system.
[従来の技術] 一般に、廃鶏を発酵処理する装置としては、有機廃棄
物を攪拌発酵する発酵槽と攪拌発酵した混合物を乾燥す
る乾燥槽の2バッチで構成されており、発酵槽で発酵処
理された発酵処理物は乾燥槽に移し替えて乾燥させてい
た。そして一度に大量の有機廃棄物を発酵処理するため
には、発酵槽及び乾燥槽を大型化しなければならなかっ
た。しかし、かかる構成だと構造が複雑な上に発酵条件
の設定が面倒になり、また発酵槽および乾燥槽の強度を
アップしなければならず設備費も高くなり、さらに発酵
処理物の移し替え作業も大変に面倒なものとなってい
た。[Prior art] In general, an apparatus for fermenting waste chicken is composed of two batches, a fermenter for stirring and fermenting organic waste and a drying tank for drying a mixture obtained by stirring and fermenting. The fermented product was transferred to a drying tank and dried. In order to ferment a large amount of organic waste at a time, the fermenter and the drying tank had to be enlarged. However, with this configuration, the structure is complicated and the setting of fermentation conditions is complicated, the strength of the fermentation tank and drying tank must be increased, the equipment cost increases, and the work of transferring the fermentation processed material Was also very troublesome.
[発明が解決しようとする課題] 本発明は、発酵槽と乾燥槽を一体化させてワンバッチ
で発酵から乾燥までの処理を可能にした小容量の発酵処
理槽を列設して有機廃棄物を並行処理することにより、
発酵処理槽が大型化することがなく有機廃棄物を大量に
処理することができ、発酵条件の設定が容易となる有機
廃棄物の発酵処理システムを提供することを目的とす
る。[Problems to be Solved by the Invention] The present invention is to integrate a fermentation tank and a drying tank and arrange a small-capacity fermentation treatment tank that enables processing from fermentation to drying in a single batch. By processing in parallel,
An object of the present invention is to provide an organic waste fermentation treatment system that can treat a large amount of organic waste without increasing the size of a fermentation treatment tank and that facilitates setting of fermentation conditions.
[課題を解決するための手段] 上記問題点を解決するために提案される本発明の有機
廃棄物の発酵処理システムは、外周に発酵・乾燥用ヒー
ターを取付けた断面U形の処理槽を有し、その上部にム
ロ化室を設けるとともに、上記処理槽本体内には槽底部
曲面に沿って鉛直方向に回動するパドル型の攪拌羽根を
設け、かつ上記処理槽本体の上部及び下部に材料投入口
および発酵処理物排出口を設けた複数の発酵処理装置
を、横方向に、かつそれぞれが取り外し可能となるよう
に列設するとともに、これら発酵処理装置の上部にガイ
ドレールを連続して敷設し、更に上記ガイドレールの上
には、上方から投入された有機廃棄物を破砕して下方に
排出するように構成された前処理機を、各発酵処理装置
の材料投入口の上で停止可能となるように走行自在に取
付けた構成としている。[Means for Solving the Problems] A fermentation treatment system for organic waste of the present invention proposed to solve the above problems has a treatment tank having a U-shaped cross section equipped with a fermentation / drying heater on the outer periphery. In addition, a mulling chamber is provided on the upper part, paddle-type stirring blades that rotate vertically along the tank bottom curved surface are provided in the processing tank body, and material is provided on the upper and lower parts of the processing tank body. A plurality of fermentation treatment devices with an inlet and a fermentation treatment product outlet are arranged side by side and detachably, and guide rails are continuously laid on top of these fermentation treatment devices. In addition, on the above guide rail, a pretreatment machine configured to crush organic waste input from above and discharge it downward can be stopped above the material input port of each fermentation treatment device Traveling to be It is configured to be freely mounted.
[作用] 本発明の有機廃棄物の発酵処理システムによると、各
々の発酵処理装置においては、処理物の水分が多い発酵
工程では処理物は処理槽の底部において攪拌羽根にて攪
拌され、処理物の水分が少なくなる乾燥工程では処理物
は攪拌羽根に絡まって持ち上げられたのち自重で落下し
て崩れ、攪拌羽根の稼働中は以上の動作が繰り返される
ことにより乾燥効率が促進される。[Action] According to the organic waste fermentation treatment system of the present invention, in each fermentation treatment apparatus, in the fermentation step in which the treated matter has a large amount of water, the treated matter is stirred by the stirring blade at the bottom of the treatment tank, In the drying step in which the water content is reduced, the treated material is entangled with the stirring blades, lifted up, falls under its own weight and collapses, and the above operation is repeated during the operation of the stirring blades, whereby the drying efficiency is promoted.
このように攪拌羽根の回動によって処理物の乾燥を効
率的に行なうことができるので、材料を移動させること
なくワンバッチで発酵、乾燥が可能となる。As described above, the processed material can be efficiently dried by rotating the stirring blade, so that fermentation and drying can be performed in one batch without moving the material.
したがって、かかる発酵処理槽を小容量にして複数配
設して有機廃棄物を各発酵処理槽で並行処理することに
より、発酵処理槽が大型化することがなく有機廃棄物を
大量に処理することができる。Therefore, by disposing a plurality of such fermentation treatment tanks in a small capacity and treating the organic waste in parallel in each fermentation treatment tank, it is possible to treat a large amount of organic waste without increasing the size of the fermentation treatment tank. Can be.
また発酵処理槽を横方向におのおの取り外し可能とな
るように列設したので、廃棄物の処理量に応じて発酵処
理槽の増減が可能となる。In addition, since the fermentation tanks are arranged side by side so that they can be removed, the number of fermentation tanks can be increased or decreased according to the amount of waste to be treated.
[実施例] 以下、本発明を図示の実施例に基づいて説明する。[Example] Hereinafter, the present invention will be described based on an illustrated example.
有機廃棄物の発酵処理システムは、第1図のように発
酵処理槽1を複数個列設し、各発酵処理槽1の天板には
上蓋13で閉塞される処理物投入口14が形成され、処理槽
1の底部曲板15には下蓋16で閉塞される排出口17が設け
られている。発酵処理槽1は横方向に複数列設され、こ
れら発酵処理槽1の上にはガイドレール(ラックレー
ル)94が敷設され、粗砕機(前処理機)9は有機廃棄物
を破砕して下方に排出するように構成されていて、ガイ
ドレール94上を走行して各発酵処理槽1の投入口14の上
で停止可能となっている。各発酵処理槽1の排出口17の
下方にはベルトコンベア12を配設してあり、各発酵処理
槽1の排出口17から自由落下により排出される発酵処理
物はこのベルトコンベア12,12A,12Bにて搬送され、貯留
槽(ステージホッパタンク)1A、定量供給装置(スクリ
ュウコンベア)1Bを通って後処理機(粉砕機、ペレット
化装置)1Cで粉砕され、最後に自動袋詰め装置1Dで袋詰
めされる。As shown in FIG. 1, the organic waste fermentation treatment system includes a plurality of fermentation treatment tanks 1 arranged in a row, and a top plate of each fermentation treatment tank 1 is provided with a treatment material inlet 14 closed by an upper lid 13. The bottom curved plate 15 of the processing tank 1 is provided with a discharge port 17 closed by a lower lid 16. The fermentation tanks 1 are arranged in a plurality of rows in the horizontal direction, and guide rails (rack rails) 94 are laid on the fermentation tanks 1. A crusher (pre-treatment machine) 9 crushes organic waste and lowers it. The fermentation tank 1 can be stopped on the inlet 14 of each fermentation treatment tank 1 while traveling on the guide rail 94. A belt conveyor 12 is provided below the outlet 17 of each fermentation tank 1, and the fermentation products discharged by the free fall from the outlet 17 of each fermentation tank 1 are the belt conveyors 12, 12A, It is transported by 12B, pulverized by a post-processing machine (pulverizer, pelletizing device) 1C through a storage tank (stage hopper tank) 1A, a quantitative supply device (screw conveyor) 1B, and finally by an automatic bagging device 1D. Bagged.
1Eは粗砕機9に有機廃棄物を供給する投入移送装置で
あって、この投入移送装置1Eは粗砕機9にともなって粗
砕機9の上方まで移動して粗砕機9に有機廃棄物を投入
するものであり、投入移送装置1Eとしてはバケットコウ
ベアやベルトコンベアやバケットリフトなどが考えられ
る。1E is an input / transfer device for supplying organic waste to the crusher 9, and the input / transfer device 1E is moved together with the crusher 9 to above the crusher 9 and inputs the organic waste to the crusher 9. The input transfer device 1E may be a bucket conveyor, a belt conveyor, a bucket lift, or the like.
なお、前処理機としては粗砕機9には限られず、スク
リュープレスやシュレッダーであっても良い。The pretreatment device is not limited to the crusher 9 but may be a screw press or a shredder.
粗砕機9は回転カッター91、92を上下2段にして箱体
95内に納めるとともに、粗砕用モータ(不図示)にて回
転駆動するように構成され、上段には粗目の回転カッタ
ー91が、下段に細目の回転カッター92が配設されてい
る。箱体95の上部および下部には廃棄物の投入孔96およ
び落下孔97が形成されている。また粗砕機9の両側には
駆動モータ(不図示)にて回動するピニオン93が取り付
けられ、このピニオン93は処理槽1の天板に敷設された
ラックレール94と歯合している。なお、粗砕機9は手動
で走行させるようにしても良い。The crusher 9 is a box body with the rotary cutters 91 and 92 in two stages
It is configured to be housed in a housing 95 and driven to rotate by a crushing motor (not shown). A coarse rotary cutter 91 is provided in an upper stage, and a fine rotary cutter 92 is provided in a lower stage. In the upper and lower parts of the box 95, a waste input hole 96 and a drop hole 97 are formed. A pinion 93 which is rotated by a drive motor (not shown) is attached to both sides of the crusher 9, and the pinion 93 meshes with a rack rail 94 laid on the top plate of the processing tank 1. The crusher 9 may be run manually.
粗砕機9の停止手段としては、粗砕機9が自動走行の
場合には粗砕機9の停止位置にリミットスイッチやセン
サなどを設けて自動停止させる構成を採用することが考
えられる。As the stopping means of the crusher 9, when the crusher 9 is traveling automatically, it is conceivable to adopt a configuration in which a limit switch, a sensor or the like is provided at a stop position of the crusher 9 to automatically stop.
発酵処理槽1は、処理槽本体1aと機械室2を一体化し
て構成されている。処理槽本体1aは金属板製であって底
部が断面U状に形成されており、処理槽本体1aの底部に
は攪拌羽根3が配設され、この攪拌羽根3の上方にはム
ロ化空間4が形成されている。処理槽本体1aの外周には
パネル状のヒーター11が配設されている。一方、機械式
2にはモータ(不図示)、ブロワー(不図示)が配設さ
れ、機械室の外壁には制御盤6が取り付けられている。
攪拌羽根3はパドル型であって、第4図のように角材製
の横羽根31と一対の縦羽根32とで構成されている。攪拌
羽根3は水平回転軸5に2枚取着されており、水平回転
軸5の回動により処理槽1の底部曲面に沿って回転する
ようになっており、一方の攪拌羽根3の横羽根31aは水
平回転軸5に対して僅かに傾斜し、他方の攪拌羽根3の
横羽根31は水平回転軸5と平行となるように配設され、
よって傾斜横羽根31aと水平横羽根31とで混合物Aを交
互に攪拌することができ、攪拌効率を一層向上させるこ
とができる。攪拌羽根3の一対の縦羽根32は攪拌羽根3
の回転方向にずらせて(例えば15゜)、横羽根31を攪拌
羽根3の回転方向にねじれ配置しており、よって横羽根
31は水平回転軸5に対して斜めに位置した状態で回動す
ることとなり、攪拌羽根3を正転・反転させると、混合
物は処理槽1内を横方向(水平回転軸5の軸方向)に往
復移動して攪拌効率を一層向上させている。The fermentation treatment tank 1 is configured by integrating a treatment tank main body 1a and a machine room 2. The processing tank main body 1a is made of a metal plate and has a bottom formed in a U-shaped cross section. A stirring blade 3 is disposed at the bottom of the processing tank main body 1a. Are formed. A panel-shaped heater 11 is provided on the outer periphery of the processing tank body 1a. On the other hand, the mechanical type 2 is provided with a motor (not shown) and a blower (not shown), and a control panel 6 is attached to the outer wall of the machine room.
The stirring blade 3 is of a paddle type, and includes a horizontal blade 31 and a pair of vertical blades 32 made of a square material as shown in FIG. Two stirring blades 3 are attached to the horizontal rotation shaft 5, and are rotated along the bottom curved surface of the processing tank 1 by the rotation of the horizontal rotation shaft 5. 31a is slightly inclined with respect to the horizontal rotation shaft 5, and the horizontal blade 31 of the other stirring blade 3 is disposed so as to be parallel to the horizontal rotation shaft 5,
Therefore, the mixture A can be alternately stirred by the inclined horizontal blades 31a and the horizontal horizontal blades 31, and the stirring efficiency can be further improved. The pair of vertical blades 32 of the stirring blade 3 is the stirring blade 3
(For example, 15 °), and the horizontal blades 31 are twisted and arranged in the rotation direction of the stirring blade 3, so that the horizontal blades
The rotation of the stirring blade 3 in the forward and reverse directions causes the mixture to move in the processing tank 1 in the horizontal direction (the axial direction of the horizontal rotation shaft 5). The stirring efficiency is further improved by reciprocating.
ムロ化空間4は、発酵時に生じる二酸化炭素が滞留す
る空間であって、廃棄物と水分調整剤と発酵菌との混合
物を二酸化炭素に接触させるためのものである。処理槽
1と機械室2の間の仕切壁7には、上記ブロワーに接続
される空気吹出口71がムロ化空間4よりも上方に形成さ
れ、水平回転軸5よりも下方には温度コントロールセン
サー72が処理槽1内に向けて突出している。処理槽1の
外壁8には排気口81がムロ化空間4よりも上方に形成さ
れている。82は覗き窓である。The mulling space 4 is a space in which carbon dioxide generated during fermentation stays, and is for bringing a mixture of waste, a moisture regulator and fermentation bacteria into contact with carbon dioxide. An air outlet 71 connected to the blower is formed in the partition wall 7 between the processing tank 1 and the machine room 2 above the mulling space 4, and a temperature control sensor is provided below the horizontal rotating shaft 5. 72 project into the processing tank 1. An exhaust port 81 is formed on the outer wall 8 of the processing tank 1 above the mulling space 4. 82 is a viewing window.
以上のようにして構成される処理装置は、制御盤6の
操作スイッチをオンにすれば、温度コントロールセンサ
ー72およびタイマー(不図示)にてヒーター11、上記ブ
ロワーおよび攪拌羽根3を自動制御して、発酵処理工程
を全自動で行えるようになっている。When the operation switch of the control panel 6 is turned on, the processing apparatus configured as described above automatically controls the heater 11, the blower, and the stirring blade 3 with the temperature control sensor 72 and a timer (not shown). The fermentation process can be performed fully automatically.
次に、有機廃棄物の発酵処理システムの動作を説明す
る。Next, the operation of the organic waste fermentation treatment system will be described.
まず粗砕・投入工程においては、上蓋を開いてヌカお
よびフスマ等の水分調整剤を処理槽1に投入したのち、
粗砕機9を処理槽1の投入口14の上方で停止させ、廃鶏
を粗砕機9で粗砕処理しつつ投入口14から処理槽1内に
落下させた後、粗砕機を隣の発酵処理槽に移動させ、そ
の後発酵菌も処理槽1に投入してから投入口14を閉じ
る。First, in the crushing / charging step, after opening the upper lid and charging the moisture adjusting agent such as bran and bran into the processing tank 1,
The crusher 9 is stopped above the input port 14 of the processing tank 1, and the waste chicken is dropped into the processing tank 1 from the input port 14 while being crushed by the crusher 9, and then the crusher is moved to the next fermentation processing. Then, the fermentation bacteria are also charged into the processing tank 1 and then the inlet 14 is closed.
各発酵処理槽1では、攪拌羽根3が停止を挟んで正転
・逆転して有機廃棄物と水分調整剤と発酵菌の混合物を
得る。その後処理槽1の攪拌羽根3およびヒーター11の
作動を停止させて二酸化炭素を混合物Aに接触させた状
態で放置してムロ化する。その後撹拌羽根3が再び停止
を挟んで正転・逆転する一方上記ブロワーにて空気吹出
口71から処理槽1内に酸素を供給して排気口81から排出
し、これにより発酵菌が対数増殖期に入り、発酵・分解
が活発に進行する。その後ヒーターとブロワーにて混合
物Aを高温乾燥する。In each of the fermentation treatment tanks 1, the stirring blades 3 rotate forward and reverse with the stop interposed therebetween to obtain a mixture of the organic waste, the water regulator and the fermenting bacteria. Thereafter, the operations of the stirring blades 3 and the heater 11 of the processing tank 1 are stopped, and the mixture is left in a state where carbon dioxide is in contact with the mixture A to form the mixture. Thereafter, the stirring blade 3 rotates forward and backward again with the stop again interposed therebetween, while the blower supplies oxygen from the air outlet 71 into the processing tank 1 and discharges it from the exhaust port 81, whereby the fermentation bacteria grow in the logarithmic growth phase. And fermentation and decomposition proceed actively. Thereafter, the mixture A is dried at a high temperature using a heater and a blower.
発酵処理槽1の攪拌羽根3は、混合物の水分が多い発
酵工程では、処理槽1の底部において攪拌羽根3は混合
物を攪拌し、それと同時に角材製の横羽根31にて、廃棄
物の骨や羽根など硬質のものをすりつぶしながら撹拌で
きる。In the fermentation process in which the mixture has a high moisture content, the stirring blade 3 of the fermentation treatment tank 1 stirs the mixture at the bottom of the treatment tank 1, and at the same time, the horizontal blades 31 made of square wood, and the waste bone and the like. Agitation can be performed while grinding hard objects such as blades.
また、攪拌羽根3はスクレーバー機能を有し、混合物
Aが半流動化しても攪拌が可能である。次に混合物Aの
水分が少なくなる乾燥工程では、攪拌羽根3の横羽根31
で混合物Aを絡めて持ち上げ、その後廃棄物を自重で落
下させて水平回転軸5に当てて崩す。このように攪拌羽
根の回動によって処理物の乾燥を効率的に行なうことが
できるので、材料を移動させることなくワンバッチで発
酵、乾燥が可能となる。Further, the stirring blade 3 has a scraper function, and can stir even if the mixture A becomes semi-fluidized. Next, in the drying step in which the water content of the mixture A is reduced, the horizontal blade 31 of the stirring blade 3 is used.
Then, the mixture A is entangled and lifted, and then the waste is dropped by its own weight and hit against the horizontal rotating shaft 5 to break it. As described above, the processed material can be efficiently dried by rotating the stirring blade, so that fermentation and drying can be performed in one batch without moving the material.
このようにして発酵処理槽1を複数配設して有機廃棄
物を各発酵処理槽1で平行処理することにより、発酵処
理槽が大型化することがなく有機廃棄物を大量に処理す
ることができる。By arranging a plurality of fermentation treatment tanks 1 and treating organic waste in each fermentation treatment tank 1 in parallel in this manner, a large amount of organic waste can be treated without increasing the size of the fermentation treatment tank. it can.
なお、有機廃棄物の処理量が増えればその分だけ発酵
処理槽1を増やすとともにガイドレール94を継ぎ足せば
良く、逆に有機廃棄物の処理量が減ればその分だけ発酵
処理槽1を減らすとともにガイドレール94を取り外せば
良い。If the amount of organic waste increases, the fermentation tank 1 may be increased by that amount and the guide rail 94 may be added. Conversely, if the amount of organic waste decreases, the number of fermentation tanks 1 decreases. At the same time, the guide rail 94 may be removed.
本発明の有機廃棄物の発酵処理システムは、廃鶏の他
に、魚、牛、豚などの動物性廃棄物や、漢方薬、ビー
ル、酒の搾り糟など植物性廃棄物、畜糞,有機汚泥類、
動物性廃棄物と植物性廃棄物の混合物の発酵処理にも使
用できる。The organic waste fermentation treatment system of the present invention can be used for animal waste such as fish, cattle and pig, vegetable waste such as Chinese medicine, beer and sake squeezer, animal dung, and organic sludge, in addition to waste chicken. ,
It can also be used for fermentation treatment of a mixture of animal waste and plant waste.
[効 果] 本発明の有機廃棄物の発酵処理システムによれば、発
酵処理槽を小容量にして複数配設して有機廃棄物を各発
酵処理槽で並行処理することにより、発酵処理槽を大型
化することがなく有機廃棄物を大量に処理することがで
きるので、発酵条件の設定が容易となり、構造も複雑化
しない。[Effect] According to the organic waste fermentation treatment system of the present invention, a plurality of fermentation treatment tanks are arranged in a small capacity, and the organic waste is processed in parallel in each fermentation treatment tank. Since a large amount of organic waste can be treated without increasing the size, the fermentation conditions can be easily set and the structure is not complicated.
また廃棄物の処理量に応じて発酵処理槽の増減が可能
となるので、廃棄物の処理量の変化に迅速に対処でき
る。In addition, since the number of fermentation treatment tanks can be increased or decreased according to the amount of waste processed, a change in the amount of waste processed can be quickly dealt with.
第1図は本発明の実施例の有機廃棄物の発酵処理システ
ムの全体斜視図、第2図は発酵処理槽の斜視図、第3図
(a)(b)は粗砕機の縦断面図および横断面図、第4
図および第5図は発酵処理槽の正断面図および側断面図
である。 (符号の説明) 1……発酵処理槽 1a……処理槽本体 3……攪拌羽根 9……粗砕機 11……ヒーター 12……ベルトコンベア 14……投入口 17……排出口 94……ガイドレールFIG. 1 is an overall perspective view of an organic waste fermentation treatment system according to an embodiment of the present invention, FIG. 2 is a perspective view of a fermentation treatment tank, and FIGS. 3 (a) and (b) are longitudinal sectional views of a crusher and Cross section, fourth
FIG. 5 and FIG. 5 are a front sectional view and a side sectional view of the fermentation tank. (Explanation of reference numerals) 1... Fermentation treatment tank 1a... Treatment tank body 3... Stirring blade 9... Crusher 11... Heater 12... Belt conveyor 14... Inlet 17... rail
───────────────────────────────────────────────────── フロントページの続き (72)発明者 山田 潤 大阪府富田林市木戸山町579―1 リメ インズKハイツ202号 (56)参考文献 特開 平1−145388(JP,A) 特開 昭60−71584(JP,A) 特開 昭58−3695(JP,A) 特開 昭62−52194(JP,A) 特開 昭54−54878(JP,A) ────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Jun Yamada 579-1 Kidoyama-cho, Tondabayashi-shi, Osaka Remains K Heights 202 (56) References JP-A-1-145388 (JP, A) JP-A-60 -71584 (JP, A) JP-A-58-3695 (JP, A) JP-A-62-52194 (JP, A) JP-A-54-54878 (JP, A)
Claims (1)
面U形の処理槽を有し、その上部にムロ化室を設けると
ともに、上記処理槽本体内には槽底部曲面に沿って鉛直
方向に回動するパドル型の攪拌羽根を設け、かつ上記処
理槽本体の上部及び下部に材料投入口および発酵処理物
排出口を設けた複数の発酵処理装置を、横方向に、かつ
それぞれが取り外し可能となるように列設するととも
に、これら発酵処理装置の上部にガイドレールを連続し
て敷設し、更に上記ガイドレールの上には、上方から投
入された有機廃棄物を破砕して下方に排出するように構
成された前処理機を、各発酵処理装置の材料投入口の上
で停止可能となるように走行自在に取付けたことを特徴
とする有機廃棄物の発酵処理システム。1. A processing tank having a U-shaped cross section with a heater for fermentation and drying mounted on the outer periphery thereof, a roasting chamber provided above the processing tank, and a vertical direction along the curved surface at the bottom of the tank inside the processing tank body. A plurality of fermentation processing devices provided with paddle-type stirring blades that rotate in a horizontal direction, and provided with a material input port and a fermentation product discharge port at the upper and lower parts of the processing tank body can be detached in the horizontal direction, and each can be removed. In addition, the guide rails are continuously laid on the top of these fermentation treatment apparatuses, and the organic waste input from above is crushed and discharged downward on the guide rails. The fermentation treatment system for organic waste, wherein the pretreatment machine configured as described above is mounted so as to be able to run on the material inlet of each fermentation treatment device so as to be able to stop.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2064913A JP2632227B2 (en) | 1990-03-15 | 1990-03-15 | Organic waste fermentation treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2064913A JP2632227B2 (en) | 1990-03-15 | 1990-03-15 | Organic waste fermentation treatment system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03265589A JPH03265589A (en) | 1991-11-26 |
| JP2632227B2 true JP2632227B2 (en) | 1997-07-23 |
Family
ID=13271763
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2064913A Expired - Fee Related JP2632227B2 (en) | 1990-03-15 | 1990-03-15 | Organic waste fermentation treatment system |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2632227B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103653213B (en) * | 2013-11-27 | 2015-08-19 | 河南宏翔生物科技有限公司 | A kind of production system of biological feedstuff |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5454878A (en) * | 1977-10-12 | 1979-05-01 | Emu Esu Kk | Method and apparatus for producing fermented fertilizer |
| JPS607958B2 (en) * | 1981-06-26 | 1985-02-28 | 日立機電工業株式会社 | Fermentation treatment equipment for sludge, etc. |
| JPS6071584A (en) * | 1983-09-28 | 1985-04-23 | 株式会社荏原製作所 | Operation of composting device |
| JPS6252194A (en) * | 1985-08-30 | 1987-03-06 | 株式会社ヒューマン・ソサエテイ. | Method of quickly fermenting organic waste such as mowed lawn or fallen leaves and apparatus therefor |
| JPH01145388A (en) * | 1987-11-30 | 1989-06-07 | Nippon Steel Corp | Apparatus for high-speed fermentation of organic material |
-
1990
- 1990-03-15 JP JP2064913A patent/JP2632227B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03265589A (en) | 1991-11-26 |
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