JPH02229587A - Fermenting device for organic waste - Google Patents
Fermenting device for organic wasteInfo
- Publication number
- JPH02229587A JPH02229587A JP1049453A JP4945389A JPH02229587A JP H02229587 A JPH02229587 A JP H02229587A JP 1049453 A JP1049453 A JP 1049453A JP 4945389 A JP4945389 A JP 4945389A JP H02229587 A JPH02229587 A JP H02229587A
- Authority
- JP
- Japan
- Prior art keywords
- fermentation
- chamber
- waste
- hot air
- far
- 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
Links
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
- Processing Of Solid Wastes (AREA)
- Treatment Of Sludge (AREA)
- Fertilizers (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、家庭や食品関係産業或いは農林水産更には畜
産関係の各種加工工場等から排出される有機性廃棄物を
水分調整し且つ醗酵させ、堆肥や肥料、飼料に転換する
有機性廃棄物の醗酵化装置に関する。[Detailed Description of the Invention] (Industrial Application Field) The present invention is a method for adjusting the moisture content of organic waste discharged from households, food-related industries, agriculture, forestry and fisheries, and livestock-related various processing plants, and fermenting it. , concerning fermentation equipment for organic waste that is converted into compost, fertilizer, and feed.
(従来の技術)
従来、農林水産関連の各種加工工場から排出される間引
き野菜や鋸くず、おから、魚の頭や内蔵、又家庭・レス
トラン等の厨房或いは食品加工工場等から排出される残
飯、料理かす等は大部分が埋立てられたり、焼却炉で焼
却されて処理されていた。(Conventional technology) Conventionally, thinned vegetables, sawdust, okara, fish heads and internal organs discharged from various processing factories related to agriculture, forestry and fisheries, and leftovers discharged from kitchens of homes, restaurants, food processing factories, etc. Most of the cooking scraps were disposed of by being landfilled or incinerated in incinerators.
(発明が解決しようとする課題)
ところで、上記のような有機性廃棄物は、腐敗し易くす
ぐに悪臭を発生させたり、又放置されると有害昆虫やね
ずみ等の餌になり非衛生な状態になる等環境破壊の原因
となる。しかも、斯かる有機性廃棄物は益々増大する傾
向にあり,その有効且つ合理的な処理方法の開発が待望
されていた。(Problems to be Solved by the Invention) Organic waste as described above is easily putrefied and immediately generates a bad odor, and if left unattended, it becomes food for harmful insects and rats, resulting in unsanitary conditions. It causes environmental destruction such as Moreover, the amount of such organic waste is increasing, and there has been a long-awaited development of an effective and rational treatment method for it.
本発明は,上記に鑑みなされたものであり、水分を多量
に含む各種有機性廃棄物を効率良く水分調整し、良好な
醗酵条件の下で且つ衛生的に醗酵させて有用な堆肥,肥
料或いは飼料に転換するコンパクト且つ新規な有機性廃
棄物の醗酵化装置を提供することを目的とする。The present invention has been made in view of the above, and it is possible to efficiently adjust the moisture content of various organic wastes containing a large amount of water, ferment them hygienically under good fermentation conditions, and turn them into useful compost, fertilizer, or fertilizer. The purpose of the present invention is to provide a compact and novel fermentation device for organic waste that is converted into feed.
(課題を解決するための手段)
上記目的を達成する本発明の有機性廃棄物の醗酵化装置
を添付図面に基づき説明する.第1図は本発明醗酵化装
置の一例を示す縦断面図、第2図は第1図における■−
■線断面図、第3図は回動軸の部分切欠斜視図である。(Means for Solving the Problems) The organic waste fermentation apparatus of the present invention which achieves the above object will be explained based on the attached drawings. FIG. 1 is a vertical cross-sectional view showing an example of the fermentation apparatus of the present invention, and FIG.
3 is a partially cutaway perspective view of the rotating shaft.
即ち、本発明の有機性廃棄物の醗酵化装置は、有機性廃
棄物の投入口12、投入廃棄物の攪拌手段20及び遠赤
外線加熱手段30を備え且つ熱風が室内に導入されるよ
うにした乾燥処理室10と、攪拌手段50、遠赤外線加
熱手段30及び醗酵処理物の排出口62を備え、予め添
加された醗酵菌により上記処理室10からの乾燥処理物
を醗酵促進する醗酵室60とより成ることを要旨とする
。That is, the organic waste fermentation apparatus of the present invention includes an organic waste inlet 12, an input waste stirring means 20, and a far-infrared heating means 30, and hot air is introduced into the room. A fermentation chamber 60 comprising a drying chamber 10, a stirring means 50, a far-infrared heating means 30, and an outlet 62 for the fermented product, and promotes fermentation of the dried product from the processing chamber 10 using fermentation bacteria added in advance. The gist is to consist of:
上記乾燥処理室10と醗酵室60との間に移送手段40
を設け、乾燥処理室10に於ける乾燥処理物を連続的に
或いは間欠的(処理室10でバッチ式に処理したものを
移送する場合も含む)醗酵室60に移送させるようにす
ることが望ましく、該移送手段40としてはパイプスク
リューコンベアが一例として挙げられる。A transfer means 40 is provided between the drying chamber 10 and the fermentation chamber 60.
It is desirable to provide a fermentation chamber 60 so that the dried product in the drying chamber 10 is transferred continuously or intermittently (including when transferring batch-processed products in the processing chamber 10). An example of the transfer means 40 is a pipe screw conveyor.
上記攪拌手段2oとしては、左右一対の平行回動軸22
、22と、該回動軸22、22の周体に固設された複数
のパドル21…とを備えたものが望ましく採用される。The stirring means 2o includes a pair of left and right parallel rotation shafts 22.
, 22, and a plurality of paddles 21 fixed to the circumferential body of the rotating shafts 22, 22.
そして、該回動軸22、22及びパドル21…には,軸
端のロータリジョイント23を介し熱風発生手段70よ
り供給される熱風を乾燥処理室10内に噴出させる為の
通路22a、21a及び吐出孔22b、2lbを設け、
攪拌中の被処理物に直接熱風を吹き付けるようにするこ
とが効果的である。上記パドル21…をスクリュープロ
ペラの如き形状にすれば、攪拌効果が大きく且つ推進力
も付与される。The rotation shafts 22, 22 and the paddles 21 are provided with passages 22a, 21a and discharge ports for spouting hot air supplied from the hot air generating means 70 into the drying processing chamber 10 via the rotary joint 23 at the end of the shaft. Holes 22b and 2lb are provided,
It is effective to blow hot air directly onto the object being stirred. If the paddles 21 are shaped like a screw propeller, the stirring effect will be large and the propulsive force will also be provided.
亦、上記遠赤外線加熱手段30は、乾燥処理室10及び
醗酵室60内の天井部に設けることが望ましい。Furthermore, it is desirable that the far-infrared heating means 30 be provided on the ceiling of the drying chamber 10 and the fermentation chamber 60.
更に、上記乾燥処理室1o及び醗酵室60に排気管71
を連結し、該排気管71からの多湿ガスを凝縮器73に
より凝縮・脱水した後上記熱風発生手段7oに導入する
ことにより,熱風供給・排気の循環システムを確立し、
悪臭ガスの逸散を防止するようになすことが望ましい。Furthermore, an exhaust pipe 71 is connected to the drying chamber 1o and the fermentation chamber 60.
The humid gas from the exhaust pipe 71 is condensed and dehydrated by the condenser 73 and then introduced into the hot air generating means 7o, thereby establishing a hot air supply/exhaust circulation system.
It is desirable to prevent the escape of foul-smelling gas.
加えて、乾燥及び醗酵を更に促進し且つ適正条件に保つ
よう、上記乾燥処理室10及び醗酵室60の周囲に加熱
用ジャケット75.76を設けることも可能である。In addition, heating jackets 75 and 76 may be provided around the drying chamber 10 and fermentation chamber 60 to further accelerate drying and fermentation and maintain proper conditions.
(作用)
上記構成の本発明装置に於ける有機性廃棄物の醗酵化要
領を述べる。投入口12から投入された含有水分の多い
有機性廃棄物は、この時同時に醗酵菌が添加され、攪拌
手段20によりほぐされるように攪拌される.この攪拌
中、乾燥処理室10に熱風が供給され、また遠赤外線加
熱手段30より遠赤外線が照射される.遠赤外線のエネ
ルギーとその特性により廃棄物は内部から加熱され、供
給熱風の作用と相俟って廃棄物中の含有水分は速やかに
蒸散する.乾燥処理室10の周囲に加熱用ジャケット7
5を設けた場合,更にこの蒸散が促進される。投入され
る有機性廃棄物の含有水分量(通常、80〜90%)、
性状或いは処理量等に応じ、供給熱風量及び遠赤外線加
熱手段30のパワーを調整し更には加熱用ジャケット7
5を使用することにより含有水分を45〜55%にまで
下げる。攪拌手段2oが、回動軸22、22とパドル2
1…とよりなる場合、これを適宜正逆転させることによ
り加熱効率のアップを図ることが出来る.そして、廃棄
物の温度が70±10℃に維持されると、添加された醗
酵菌により一部が醗酵を開始する。(Operation) The procedure for fermenting organic waste in the apparatus of the present invention having the above configuration will be described. At this time, fermentation bacteria are simultaneously added to the organic waste containing a large amount of water, which is inputted from the input port 12, and is stirred by the stirring means 20 so as to be loosened. During this stirring, hot air is supplied to the drying chamber 10, and far-infrared rays are irradiated from the far-infrared heating means 30. The waste is heated from the inside by far infrared energy and its properties, and together with the action of the supplied hot air, the moisture contained in the waste evaporates quickly. A heating jacket 7 is installed around the drying chamber 10.
5, this transpiration is further promoted. Moisture content of input organic waste (usually 80-90%),
The amount of hot air supplied and the power of the far-infrared heating means 30 are adjusted according to the properties or processing amount, etc., and the heating jacket 7 is adjusted.
By using No. 5, the water content can be lowered to 45-55%. The stirring means 2o includes the rotating shafts 22, 22 and the paddle 2.
1..., heating efficiency can be increased by appropriately reversing this direction. Then, when the temperature of the waste is maintained at 70±10° C., a portion of the waste begins to ferment due to the added fermentation bacteria.
次いで、上記の如く水分調整され且つ一部醗酵した乾燥
処理物は醗酵室60に移される。上記移送手段40が設
けられている場合、該移送手段40を連続駆動すれば乾
燥処理物は乾燥処理室1oから醗酵室60に逐次移送さ
れる。乾燥を十分に行なう必要がある場合、該移送手段
40を間欠駆動しバッチ毎に移送させることも可能であ
る.醗酵室60に移送された乾燥処理物は,攪拌手段5
0の作用を受けて更に攪拌されほぐされると共に,遠赤
外線加熱手段30の遠赤外線照射によりその内部から加
熱され、醗酵菌の醗酵・増殖に好適な条件(70±10
℃)に維持されると共にここでも含有水分の蒸散がなさ
れる。醗酵室60の周囲に加熱用,ジャケット76が設
けられている場合は、必要によって該ジャケット76を
作動させ上記条件の維持を図り且つ水分の蒸散を促進す
る。斯くして、上記乾燥処理物は、醗酵菌の醗酵・増殖
作用を受けて醗酵し、排出口62から含有水分が20%
程度で堆肥、肥料或いは飼料として好適な最終処理物と
して排出される。Next, the dried product, whose moisture content has been adjusted as described above and which has been partially fermented, is transferred to the fermentation chamber 60. When the transfer means 40 is provided, the dried product is sequentially transferred from the drying chamber 1o to the fermentation chamber 60 by continuously driving the transfer means 40. If sufficient drying is required, the transfer means 40 may be driven intermittently to transfer each batch. The dried product transferred to the fermentation chamber 60 is stirred by the stirring means 5.
It is further stirred and loosened by the action of 0, and is heated from inside by far infrared rays irradiated by the far infrared heating means 30, under conditions suitable for fermentation and proliferation of fermentation bacteria (70±10
℃), and the moisture contained therein is also evaporated. If a heating jacket 76 is provided around the fermentation chamber 60, the jacket 76 is operated as necessary to maintain the above conditions and promote water evaporation. In this way, the dried product is fermented by the fermentation and multiplication action of fermentation bacteria, and the water content is reduced to 20% from the discharge port 62.
It is discharged as a final treated product suitable for use as compost, fertilizer or feed.
(実施例)
次に実施例について述べる。図において、乾燥処理室1
oはケーシング11によって形成され、該ケーシング1
1の基部側上部に開閉蓋12aを有する廃棄物投入口1
2が形設されている。この乾燥処理室ケーシング11内
にはその長手方向に沿って水平な攪拌手段20が設けら
れており,該攪拌手段20は、両端が軸受Bで支承され
且つ内部に熱風通路22a、22aを外周面に吐出孔2
2b…を各々形成した左右一対の回動軸22、22と、
該回動軸22、22の周体に適宜間隔毎に固設された複
数のスクリュープロペラ状パドル21…とから構成され
ている。上記熱風通路22a,22aは、一方の軸端に
おいてロータリジョイント23を介して後述する熱風発
生手段70の供給管74aに連通され、該通路22a.
22aから供給された熱風は上記吐出孔22b…及びパ
ドル21…の周縁に開設された吐出孔2lb…から攪拌
中の処理廃棄物に直接吹き付けられるようになされてい
る.回動軸22、22は矢印の如き対向回転を正回転と
し、パドル21…はこの正回転中廃棄物を攪拌すると共
に廃棄物に小さな推力を付与すべく図の如く湾曲形成さ
れている。回転方向は、後述の可逆転式電動モータによ
って適宜或いは所定時間毎に繰返し正逆転されるように
構成され、攪拌効率の向上と過重負荷の緩和を図るよう
になされている。(Example) Next, an example will be described. In the figure, drying chamber 1
o is formed by a casing 11, said casing 1
A waste inlet 1 having an opening/closing lid 12a on the upper part of the base side of the waste inlet 1
2 is set up. A horizontal stirring means 20 is provided in the drying chamber casing 11 along its longitudinal direction, and the stirring means 20 is supported by bearings B at both ends and has hot air passages 22a, 22a formed on its outer peripheral surface. Discharge hole 2
A pair of left and right rotation shafts 22, 22 each forming a 2b...
It is composed of a plurality of screw propeller-shaped paddles 21 fixed to the circumferential body of the rotating shafts 22, 22 at appropriate intervals. The hot air passages 22a, 22a are communicated with a supply pipe 74a of a hot air generating means 70, which will be described later, via a rotary joint 23 at one shaft end, and the passages 22a.
The hot air supplied from 22a is blown directly onto the waste being stirred through the discharge holes 22b and 2lb formed on the periphery of the paddles 21. The rotating shafts 22, 22 rotate in a forward direction as shown by the arrows, and the paddles 21 are curved as shown in the figure in order to agitate the waste and apply a small thrust to the waste during this forward rotation. The direction of rotation is configured to be rotated forward and reverse repeatedly as needed or at predetermined time intervals by a reversible electric motor, which will be described later, in order to improve stirring efficiency and alleviate excessive loads.
になされている。is being done.
乾燥処理室ケーシング11の天井には、攪拌されている
廃棄物に向って遠赤外線を照射する遠赤外線加熱手段3
0が複数組長手方向に亘って設けられている.遠赤外線
は、被加熱物に対する浸透性に優れ、内部から加熱する
作用を行い、上記熱風の廃棄物に対する直接吹き付けと
相俟って極めて効率珀に水分の蒸散がなされる。乾燥処
理室ケーシング11の少なくとも一方の側壁上部には、
水分を多量に含んだ空気を排出する排気口78が開設さ
れている。On the ceiling of the drying chamber casing 11, there is a far-infrared heating means 3 that irradiates far-infrared rays toward the waste being stirred.
0 are provided in multiple sets in the longitudinal direction. Far-infrared rays have excellent permeability to the object to be heated and have the effect of heating the object from the inside, and in combination with the above-mentioned direct blowing of the hot air to the waste, moisture is evaporated extremely efficiently. At the top of at least one side wall of the drying chamber casing 11,
An exhaust port 78 is provided to exhaust air containing a large amount of moisture.
醗酵室60は上記乾燥処理室ケーシング11に隣接して
設けられたケーシング61内に形成され、該ケーシング
61内にその長手力向に沿って水平な攪拌手段50が設
けられている。該攪拌手段50は,上記攪拌手段2oと
同様軸受Bで支承された回動軸52、52と、該回動軸
52、52の周体に適宜間隔毎に固設された複数のスク
リュープロペラ状パドル51…とより成る。図例では、
該回動軸52、52及びパドル51…に上記のような熱
風供給手段を設けていないが、醗酵室60内での乾燥及
び醗酵条件維持の為に同様のものを設けることも除外す
るものではない。乾燥処理室10の回動軸22、22と
醗酵室60内の回動軸52、52とは、夫々同軸的に連
結され、一個の駆動ユニットUにより同時に駆動するよ
うになされているが、完熟醗酵させる観点からは回動軸
52、52の方が低速であることが望ましく、その為両
回動軸22、52間に増速機Aが介設されている。The fermentation chamber 60 is formed within a casing 61 provided adjacent to the drying chamber casing 11, and a horizontal stirring means 50 is provided within the casing 61 along its longitudinal direction. The stirring means 50 includes rotating shafts 52, 52 supported by bearings B, similar to the above-mentioned stirring means 2o, and a plurality of screw propeller-shaped screw propellers fixed to the circumferential bodies of the rotating shafts 52, 52 at appropriate intervals. It consists of a paddle 51... In the example,
Although the rotating shafts 52, 52 and the paddles 51 are not provided with hot air supply means as described above, it is not excluded that similar devices may be provided in order to maintain drying and fermentation conditions within the fermentation chamber 60. do not have. The rotating shafts 22, 22 in the drying chamber 10 and the rotating shafts 52, 52 in the fermentation chamber 60 are coaxially connected, respectively, and are driven simultaneously by one drive unit U. From the viewpoint of fermentation, it is desirable that the rotating shafts 52, 52 have lower speeds, and therefore a speed increaser A is interposed between the rotating shafts 22, 52.
しかし、これに限定されず両者を別個に駆動させるよう
になすことも可能であることは云うまでもない。尚、符
号Gは左右の回動軸2 2(5 2)、22(52)を
1個の駆動源により互いに対向或いは反対向回転させる
為の歯車ユニットである。However, it goes without saying that the invention is not limited to this, and it is also possible to drive both separately. Incidentally, reference numeral G designates a gear unit for rotating the left and right rotation shafts 22 (5 2), 22 (52) in opposite directions or opposite directions to each other by one driving source.
醗酵室用ケーシング61の天井にも、乾燥処理室10内
のものと同様の遠赤外線加熱手段30が設けられている
.この遠赤外線の照射により醗酵室60内の被処理物は
内部から加熱され、更にその含有水分が蒸゜散され且つ
醗酵に好適な条件に維持される。醗酵室ケーシング61
の一方の側壁上部には、水分及び醗酵ガスを含んだ空気
を排出する排気口79が開設されている。A far infrared heating means 30 similar to that in the drying chamber 10 is also provided on the ceiling of the fermentation chamber casing 61. By this irradiation with far-infrared rays, the material to be processed in the fermentation chamber 60 is heated from within, and the moisture contained therein is evaporated and conditions suitable for fermentation are maintained. Fermentation chamber casing 61
An exhaust port 79 for discharging air containing moisture and fermentation gas is provided at the upper part of one side wall of the chamber.
移送手段40は、乾燥処理室ケーシング11の前方底壁
に設けられた開口部と醗酵室ケーシング61の基部側底
壁に設けられた開口部間に連架されたパイプスクリュー
コンベア41より成り、電動モータ42の駆動力を得て
乾燥処理室10内の乾燥処,理物を逐次成いは間欠的に
醗酵室60に移行させるべく機能する。また、醗酵室ケ
ーシング61の前方底壁には排出口62が設けられ、該
排出口62にはスクリュー式フィーダー63が連設され
ている.該スクリューフィダー63により醗酵され堆肥
、肥料或いは飼料として好適な最終処理物が逐次成いは
間欠的に排出される。該スクリューフィーダー63と上
記スクリューコンベア41とを同じ駆動源で作動させる
こともまたこれを別個とすることも自由である。The transfer means 40 consists of a pipe screw conveyor 41 connected between an opening provided in the front bottom wall of the drying chamber casing 11 and an opening provided in the base side bottom wall of the fermentation chamber casing 61, and is electrically operated. It functions to obtain the driving force of the motor 42 to transfer the drying process and processed material in the drying process chamber 10 to the fermentation chamber 60 sequentially or intermittently. Further, a discharge port 62 is provided on the front bottom wall of the fermentation chamber casing 61, and a screw type feeder 63 is connected to the discharge port 62. The screw feeder 63 sequentially or intermittently discharges a final product that is fermented and suitable as compost, fertilizer, or feed. The screw feeder 63 and the screw conveyor 41 can be operated by the same drive source or can be operated separately.
乾燥処理室10内の被処理物に熱風を吹き付ける熱風発
生手段70は,熱風発生炉74と、該熱風発生炉74か
ら導出され前記ロータリジョイント23に連結された熱
風供給管74aと、余剰ガスの排気塔74bとより成る
.一方,前記排気口78、79には排気管71が連結さ
れ、該排気管71は途中電動吸引ファン72及び凝縮器
73を配設具備して熱風発生炉74に連結されている。The hot air generating means 70 that blows hot air onto the workpiece in the drying processing chamber 10 includes a hot air generating furnace 74, a hot air supply pipe 74a led out from the hot air generating furnace 74 and connected to the rotary joint 23, and a hot air generating means 70 that blows hot air onto the workpiece in the drying processing chamber 10. It consists of an exhaust tower 74b. On the other hand, an exhaust pipe 71 is connected to the exhaust ports 78 and 79, and the exhaust pipe 71 is connected to a hot air generating furnace 74 with an electric suction fan 72 and a condenser 73 disposed therebetween.
而して、乾燥処理室1o及び醗酵室60内の多湿ガスは
、吸引ファン72により吸引され、凝縮器73により凝
縮・脱水されて熱風発生炉74に導入される。ここに導
入されたガスは,該熱風発生炉74により加熱され、供
給管74aを経て前記吐出口22b…,21b…より処
理排気物に吹き付けられる.このような循環システムを
確立することにより、乾燥処理室10及び醗酵室60内
の悪臭が装置外に逸散することを防止することが出来,
これにより設置場所等の制約が緩和される。The humid gas in the drying chamber 1o and the fermentation chamber 60 is sucked by the suction fan 72, condensed and dehydrated by the condenser 73, and introduced into the hot air generating furnace 74. The gas introduced here is heated by the hot air generating furnace 74, passes through the supply pipe 74a, and is blown onto the process exhaust from the discharge ports 22b..., 21b.... By establishing such a circulation system, it is possible to prevent the bad odor in the drying chamber 10 and the fermentation chamber 60 from escaping outside the apparatus.
This eases restrictions on installation locations, etc.
尚、加熱されたガスは一部排気塔74bより装置外に排
出されるが、凝縮器73により脱水されしかも加熱によ
り脱臭される為、これにより周囲に悪臭を放つことがな
い。A portion of the heated gas is discharged to the outside of the apparatus from the exhaust tower 74b, but since it is dehydrated by the condenser 73 and deodorized by heating, it does not emit any bad odor to the surroundings.
更に、図例では乾燥処理室ケーシング11及び醗酵室ケ
ーシング61の側壁から底壁にかけてこれを包囲するよ
う加熱用ジャケット75、76が設けられている。該加
熱用ジャケット75.76としては、電熱式、温水循環
式或いは温熱オイル循環式等公知のものが採用可能であ
り、乾燥処理室1o及び醗酵室60内の処理物を水分蒸
散及び醗酵に適正な温度に維持すべく機能する。従って
、処理物の温度を検出しながら該加熱用ジャケット75
、76をオン・オフ制御して常時適正温度に維持するよ
うなすことが望ましい。Further, in the illustrated example, heating jackets 75 and 76 are provided from the side walls to the bottom walls of the drying chamber casing 11 and the fermentation chamber casing 61 so as to surround them. As the heating jackets 75 and 76, known ones such as an electric heating type, a hot water circulation type, or a hot oil circulation type can be adopted, and the heating jackets 75 and 76 can be used to properly heat the processed materials in the drying chamber 1o and the fermentation chamber 60 for water evaporation and fermentation. It functions to maintain a certain temperature. Therefore, while detecting the temperature of the processed material, the heating jacket 75
, 76 are preferably controlled on and off to maintain a proper temperature at all times.
尚、上記実施例では攪拌手段として左右一対の二軸式回
動軸による場合を示したが、一軸或いはその他の多軸の
ものも除外するものではない。亦、乾燥処理室と醗酵室
とを前後に連設した例を示したが、これらを夫々別個に
配置し(例えば、上下に)他の移送手段(例えば、パケ
ットコンベアや空気輸送手段等)により乾燥処理物を移
送させるようにすることも可能である.その他、本発明
を逸脱しない限り変更が可能であることは云うまでもな
い。In the above embodiments, a pair of left and right biaxial rotating shafts are used as the stirring means, but a single shaft or other multi-shafts are not excluded. In addition, although we have shown an example in which the drying processing chamber and the fermentation chamber are connected in front and behind each other, they can be placed separately (e.g., upper and lower) and transported by other transport means (e.g., packet conveyor, pneumatic transport means, etc.). It is also possible to transport the dried product. It goes without saying that other changes may be made without departing from the invention.
(発明の効果)
以上述べた如く構成された有機性廃棄物の醗酵化装置に
よれば、乾燥処理室内においては熱風による加熱の他に
遠赤外線による廃棄物内部からの加熱によって攪拌中極
めて短時間に乾燥を行い速やかに醗酵に好適な含水量に
調整を行うと共に、醗酵室内においては少なくとも遠赤
外線によって廃棄物の内部から極めて効率的に加熱する
ことによって醗酵速度を早めることができ、小形の装置
でありながら多量の有機性廃棄物を再利用価値の高い堆
肥、肥料或いは飼料として再生処理することができる。(Effects of the Invention) According to the organic waste fermentation apparatus configured as described above, in addition to heating with hot air in the drying treatment chamber, heating from inside the waste with far infrared rays is used to heat the waste for an extremely short period of time during stirring. In addition to quickly adjusting the moisture content to a suitable level for fermentation by drying the waste, the fermentation speed can be accelerated by extremely efficiently heating the waste from within, using at least far infrared rays in the fermentation chamber. However, a large amount of organic waste can be recycled into compost, fertilizer, or feed with high reuse value.
このように特筆すべき効果を有する本発明は、近年大き
な社会問題とされている有機性廃棄物処理の懸案を一掃
するもので、その社会的価値は極めて大である。The present invention, which has such remarkable effects, eliminates the problem of organic waste disposal, which has become a major social problem in recent years, and has extremely great social value.
第1図は本発明醗酵化装置の一例を示す縦断面図、第2
図は第1図における■一■線断面図、第3図は回動軸の
部分切欠斜視図である。
(符号の説明)
1o…乾燥処理室、 12…投入口、 2o、50…
攪拌手段、 21、51…パドル、 22、52…回動
軸, 21a、22a…熱風通路,2lb、22b…吐
出孔、 23…ロータリジョイント、30…遠赤外線
加熱手段、 40…移送手段、 41…パイプスクリュ
ーコンクベア、
60…醗酵室、、 62…排出口、 71…排気管、
73…凝縮器、75、76…加熱用ジャケット・ット・
一以上一Fig. 1 is a longitudinal sectional view showing an example of the fermentation apparatus of the present invention, Fig. 2
The figure is a sectional view taken along the line 1-2 in FIG. 1, and FIG. 3 is a partially cutaway perspective view of the rotation shaft. (Explanation of symbols) 1o...drying chamber, 12...inlet, 2o, 50...
Stirring means, 21, 51... Paddle, 22, 52... Rotating shaft, 21a, 22a... Hot air passage, 2lb, 22b... Discharge hole, 23... Rotary joint, 30... Far infrared heating means, 40... Transfer means, 41... Pipe screw conveyer, 60... fermentation chamber, 62... discharge port, 71... exhaust pipe,
73... Condenser, 75, 76... Heating jacket, one or more, one
Claims (1)
手段(20)及び遠赤外線加熱手段(30)を備え且つ
熱風が室内に導入されるようにした乾燥処理室(10)
と、攪拌手段(50)、遠赤外線加熱手段(30)及び
醗酵処理物の排出口(62)を備え、予め添加された醗
酵菌により上記処理室(10)からの乾燥処理物を醗酵
促進する醗酵室(60)とより成る有機性廃棄物の醗酵
化装置。 2、上記乾燥処理室(10)と醗酵室(60)との間に
乾燥処理物を移送させる為の移送手段(40)が設けら
れている請求項1記載の醗酵化装置。 3、上記攪拌手段(20)が、左右一対の平行回動軸(
22)(22)と、該回動軸(22)(22)の周体に
固設された複数のパドル(21…)とを備え、該回動軸
(22)(22)及びパドル(21…)には軸端のロー
タリジョイント(23)を介し熱風発生手段(70)よ
り供給される熱風を乾燥処理室(10)内に噴出させる
為の通路(22a)(21a)及び吐出孔(22b)(
21b)が形成されている請求項1記載の醗酵化装置。 4、上記遠赤外線加熱手段(30)は、乾燥処理室(1
0)及び醗酵室(60)の天井部に設けられている請求
項1記載の醗酵化装置。 5、上記乾燥処理室(10)及び醗酵室(60)には排
気管(71)が連結され、該排気管(71)からの多湿
ガスは凝縮器(73)により凝縮・脱水された後上記熱
風発生手段(70)に導入されるようにした請求項1又
は3記載の醗酵化装置。 6、上記乾燥処理室(10)及び醗酵室(60)の周囲
に加熱用ジャケット(75)(76)が設けられている
請求項1記載の醗酵化装置。 7、上記移送手段(40)がパイプスクリューコンベア
である請求項2記載の醗酵化装置。[Claims] 1. A dryer equipped with an organic waste inlet (12), a means for stirring the input waste (20), and a far-infrared heating means (30), and in which hot air is introduced into the room. Processing room (10)
, a stirring means (50), a far-infrared heating means (30), and a discharge port (62) for the fermented product, which promotes fermentation of the dried product from the processing chamber (10) using fermentation bacteria added in advance. An organic waste fermentation device comprising a fermentation chamber (60). 2. The fermentation apparatus according to claim 1, further comprising a transfer means (40) for transferring the dried product between the drying chamber (10) and the fermentation chamber (60). 3. The stirring means (20) has a pair of left and right parallel rotation shafts (
22) (22) and a plurality of paddles (21...) fixed to the circumferential body of the rotation shaft (22) (22), the rotation shaft (22) (22) and the paddle (21...). ) have passages (22a) (21a) and discharge holes (22b) for blowing hot air supplied from the hot air generation means (70) into the drying chamber (10) via the rotary joint (23) at the end of the shaft. )(
21. The fermentation apparatus according to claim 1, wherein 21b) is formed. 4. The far infrared heating means (30) is installed in the drying chamber (1
2. The fermentation apparatus according to claim 1, wherein the fermentation apparatus is provided on the ceiling of the fermentation chamber (60) and the fermentation chamber (60). 5. An exhaust pipe (71) is connected to the drying chamber (10) and the fermentation chamber (60), and the humid gas from the exhaust pipe (71) is condensed and dehydrated by the condenser (73), and then the above-mentioned The fermentation apparatus according to claim 1 or 3, wherein the fermentation device is introduced into the hot air generating means (70). 6. The fermentation apparatus according to claim 1, wherein heating jackets (75) and (76) are provided around the drying chamber (10) and the fermentation chamber (60). 7. The fermentation apparatus according to claim 2, wherein the transfer means (40) is a pipe screw conveyor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1049453A JPH02229587A (en) | 1989-03-01 | 1989-03-01 | Fermenting device for organic waste |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1049453A JPH02229587A (en) | 1989-03-01 | 1989-03-01 | Fermenting device for organic waste |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02229587A true JPH02229587A (en) | 1990-09-12 |
| JPH0451235B2 JPH0451235B2 (en) | 1992-08-18 |
Family
ID=12831559
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1049453A Granted JPH02229587A (en) | 1989-03-01 | 1989-03-01 | Fermenting device for organic waste |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02229587A (en) |
Cited By (31)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0470180U (en) * | 1990-10-30 | 1992-06-22 | ||
| JPH04240176A (en) * | 1991-01-16 | 1992-08-27 | Akira Ito | Organic waste fermentation tank |
| JPH04338187A (en) * | 1991-05-10 | 1992-11-25 | Akira Ito | Organic waste disposer |
| JPH04349987A (en) * | 1991-05-28 | 1992-12-04 | Kinpachi Fujimura | Garbage disposal and its device |
| JPH05105567A (en) * | 1991-10-22 | 1993-04-27 | Akira Ito | Organic waste treatment equipment |
| JPH05220463A (en) * | 1991-12-18 | 1993-08-31 | Sosuukai:Kk | Raw refuse treating oven |
| JPH06172072A (en) * | 1992-12-08 | 1994-06-21 | Toomen Constr Kk | Organic matter fermentation system |
| JPH06247785A (en) * | 1993-02-22 | 1994-09-06 | Toyo Dainamu Kk | Device for fermentation and drying |
| JPH0664799U (en) * | 1992-04-14 | 1994-09-13 | 株式会社石川鉄工所 | High temperature treatment tank |
| JPH06256616A (en) * | 1993-03-09 | 1994-09-13 | Shin Etsu Chem Co Ltd | Polyvinyl alcohol hydrogel excellent in stability and its preparation |
| JPH06257731A (en) * | 1993-03-09 | 1994-09-16 | Ngk Insulators Ltd | Sludge incinerating method |
| JPH06262161A (en) * | 1993-03-15 | 1994-09-20 | Hideki Fujimoto | Treatment of crude refuse and device therefor |
| JPH06277644A (en) * | 1991-02-07 | 1994-10-04 | Shibuya Kogyo Co Ltd | Method and apparatus for treating garbage |
| JPH06276849A (en) * | 1993-03-30 | 1994-10-04 | Kubota Corp | Grain storage part of combine harvester |
| JPH06312168A (en) * | 1993-04-27 | 1994-11-08 | Shibuya Kogyo Co Ltd | Garbage processing method and apparatus therefor |
| JPH0710668A (en) * | 1993-06-25 | 1995-01-13 | Toyo Dynam Kk | Fermentation drying equipment |
| JPH078999A (en) * | 1993-06-29 | 1995-01-13 | Hokuetsu Kogyo Co Ltd | Sludge dryer |
| JPH077791U (en) * | 1993-07-06 | 1995-02-03 | 株式会社福原鋳物製作所 | Kitchen waste processing equipment |
| JPH0739851A (en) * | 1993-07-26 | 1995-02-10 | Toshikuni Komatsu | High-speed organic matter fermentation treatment method and apparatus thereof |
| JPH0739978U (en) * | 1993-12-27 | 1995-07-18 | 三友工業株式会社 | Fermenter |
| JPH07214037A (en) * | 1994-02-10 | 1995-08-15 | Akira Ito | Organic waste treatment equipment |
| JPH0810742A (en) * | 1994-06-28 | 1996-01-16 | Ito Seikan Kogyo Kk | Fermentation treatment method of organic waste and its equipment |
| WO1997037783A1 (en) * | 1996-04-04 | 1997-10-16 | Tomoyasu Tokuyama | Raw refuse disposer |
| JP2005231912A (en) * | 2004-02-17 | 2005-09-02 | Koichi Kobayashi | Apparatus and method of composting organic waste using hot air oven |
| JP2006263636A (en) * | 2005-03-25 | 2006-10-05 | Peace Sangyo Kk | Garbage disposal equipment |
| JP2007125472A (en) * | 2005-11-01 | 2007-05-24 | Shin Meiwa Ind Co Ltd | Garbage dryer and garbage drying system |
| JP2010264447A (en) * | 1996-09-11 | 2010-11-25 | Herhof Verwaltungs Gmbh | Biological heat treatment method of waste |
| JP2012096219A (en) * | 2010-11-01 | 2012-05-24 | Jiao Xuezhen | Technique and equipment for substance circulation in organism waste |
| JP2013046882A (en) * | 2011-08-27 | 2013-03-07 | Vioce Co Ltd | Drying device of sludge or the like |
| CN110862277A (en) * | 2019-12-10 | 2020-03-06 | 山东王工环保科技有限公司 | Organic waste biological drying treatment fermentation box |
| JP2021032442A (en) * | 2019-08-21 | 2021-03-01 | 新東工業株式会社 | Agitation dryer |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6246988A (en) * | 1985-08-23 | 1987-02-28 | 株式会社 ジヤパン・ニユ−・エネルギ−・センタ− | Organic matter quick fermentation solidification equipment |
-
1989
- 1989-03-01 JP JP1049453A patent/JPH02229587A/en active Granted
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6246988A (en) * | 1985-08-23 | 1987-02-28 | 株式会社 ジヤパン・ニユ−・エネルギ−・センタ− | Organic matter quick fermentation solidification equipment |
Cited By (31)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0470180U (en) * | 1990-10-30 | 1992-06-22 | ||
| JPH04240176A (en) * | 1991-01-16 | 1992-08-27 | Akira Ito | Organic waste fermentation tank |
| JPH06277644A (en) * | 1991-02-07 | 1994-10-04 | Shibuya Kogyo Co Ltd | Method and apparatus for treating garbage |
| JPH04338187A (en) * | 1991-05-10 | 1992-11-25 | Akira Ito | Organic waste disposer |
| JPH04349987A (en) * | 1991-05-28 | 1992-12-04 | Kinpachi Fujimura | Garbage disposal and its device |
| JPH05105567A (en) * | 1991-10-22 | 1993-04-27 | Akira Ito | Organic waste treatment equipment |
| JPH05220463A (en) * | 1991-12-18 | 1993-08-31 | Sosuukai:Kk | Raw refuse treating oven |
| JPH0664799U (en) * | 1992-04-14 | 1994-09-13 | 株式会社石川鉄工所 | High temperature treatment tank |
| JPH06172072A (en) * | 1992-12-08 | 1994-06-21 | Toomen Constr Kk | Organic matter fermentation system |
| JPH06247785A (en) * | 1993-02-22 | 1994-09-06 | Toyo Dainamu Kk | Device for fermentation and drying |
| JPH06256616A (en) * | 1993-03-09 | 1994-09-13 | Shin Etsu Chem Co Ltd | Polyvinyl alcohol hydrogel excellent in stability and its preparation |
| JPH06257731A (en) * | 1993-03-09 | 1994-09-16 | Ngk Insulators Ltd | Sludge incinerating method |
| JPH06262161A (en) * | 1993-03-15 | 1994-09-20 | Hideki Fujimoto | Treatment of crude refuse and device therefor |
| JPH06276849A (en) * | 1993-03-30 | 1994-10-04 | Kubota Corp | Grain storage part of combine harvester |
| JPH06312168A (en) * | 1993-04-27 | 1994-11-08 | Shibuya Kogyo Co Ltd | Garbage processing method and apparatus therefor |
| JPH0710668A (en) * | 1993-06-25 | 1995-01-13 | Toyo Dynam Kk | Fermentation drying equipment |
| JPH078999A (en) * | 1993-06-29 | 1995-01-13 | Hokuetsu Kogyo Co Ltd | Sludge dryer |
| JPH077791U (en) * | 1993-07-06 | 1995-02-03 | 株式会社福原鋳物製作所 | Kitchen waste processing equipment |
| JPH0739851A (en) * | 1993-07-26 | 1995-02-10 | Toshikuni Komatsu | High-speed organic matter fermentation treatment method and apparatus thereof |
| JPH0739978U (en) * | 1993-12-27 | 1995-07-18 | 三友工業株式会社 | Fermenter |
| JPH07214037A (en) * | 1994-02-10 | 1995-08-15 | Akira Ito | Organic waste treatment equipment |
| JPH0810742A (en) * | 1994-06-28 | 1996-01-16 | Ito Seikan Kogyo Kk | Fermentation treatment method of organic waste and its equipment |
| WO1997037783A1 (en) * | 1996-04-04 | 1997-10-16 | Tomoyasu Tokuyama | Raw refuse disposer |
| JP2010264447A (en) * | 1996-09-11 | 2010-11-25 | Herhof Verwaltungs Gmbh | Biological heat treatment method of waste |
| JP2005231912A (en) * | 2004-02-17 | 2005-09-02 | Koichi Kobayashi | Apparatus and method of composting organic waste using hot air oven |
| JP2006263636A (en) * | 2005-03-25 | 2006-10-05 | Peace Sangyo Kk | Garbage disposal equipment |
| JP2007125472A (en) * | 2005-11-01 | 2007-05-24 | Shin Meiwa Ind Co Ltd | Garbage dryer and garbage drying system |
| JP2012096219A (en) * | 2010-11-01 | 2012-05-24 | Jiao Xuezhen | Technique and equipment for substance circulation in organism waste |
| JP2013046882A (en) * | 2011-08-27 | 2013-03-07 | Vioce Co Ltd | Drying device of sludge or the like |
| JP2021032442A (en) * | 2019-08-21 | 2021-03-01 | 新東工業株式会社 | Agitation dryer |
| CN110862277A (en) * | 2019-12-10 | 2020-03-06 | 山东王工环保科技有限公司 | Organic waste biological drying treatment fermentation box |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0451235B2 (en) | 1992-08-18 |
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