JPS6137236B2 - - Google Patents
Info
- Publication number
- JPS6137236B2 JPS6137236B2 JP54150368A JP15036879A JPS6137236B2 JP S6137236 B2 JPS6137236 B2 JP S6137236B2 JP 54150368 A JP54150368 A JP 54150368A JP 15036879 A JP15036879 A JP 15036879A JP S6137236 B2 JPS6137236 B2 JP S6137236B2
- Authority
- JP
- Japan
- Prior art keywords
- fermenter
- radial
- outlet
- composting
- paddle
- 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
Links
- 239000000463 material Substances 0.000 claims description 46
- 238000009264 composting Methods 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 7
- 238000000855 fermentation Methods 0.000 description 10
- 230000004151 fermentation Effects 0.000 description 10
- 238000003756 stirring Methods 0.000 description 8
- 239000002994 raw material Substances 0.000 description 4
- 238000010276 construction Methods 0.000 description 3
- 238000007790 scraping Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 238000005273 aeration Methods 0.000 description 2
- 238000010564 aerobic fermentation Methods 0.000 description 2
- 238000013019 agitation Methods 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000010801 sewage sludge Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
Landscapes
- Fertilizers (AREA)
- Treatment Of Sludge (AREA)
Description
【発明の詳細な説明】
本発明は、都市ごみ、下水スラジ、蓄産廃棄物
などの有機物の堆肥化方法及びその装置に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for composting organic matter such as municipal waste, sewage sludge, and accumulated waste.
従来、この種の有機物の堆肥化操作は通常材料
(堆肥化原料)を一定期間貯蔵し、該期間中床面
から適当量の給気を行いながら適当な時間間隔で
撹拌して所謂切り返しを行うことにより、好気性
発酵を促進することによつて行われる。又、地域
の天候、環境などの条件によつては、野積み貯蔵
を行い、床面からの給気を省略する場合もある
が、何れにしても堆肥化に当つて、切り返し操作
は、材料の均質化や曝気の均一化、曝気表面積の
実質的拡大などの理由で必須な操作である。 Conventionally, this type of organic composting operation usually involves storing the materials (composting raw materials) for a certain period of time, and during this period, stirring at appropriate time intervals while supplying an appropriate amount of air from the floor surface, so-called turning back. This is done by promoting aerobic fermentation. Also, depending on local weather and environmental conditions, open storage may be performed and air supply from the floor may be omitted. This operation is essential for reasons such as homogenization of water, uniformity of aeration, and substantial expansion of the aeration surface area.
一方、堆肥化操作を連続化するためには、上記
の切り返し操作の為の撹拌と同時に材料を一定方
向に移動する機能が要求される。このため、周知
の近代的な堆肥化装置は、殆んどすべて撹拌と移
動とを同時に行い得る撹拌装置を有しているが、
堆肥化装置が比較的大型化すると材料の貯蔵量が
尨大となる為に、従来この撹拌装置は極めて大掛
りなものとなり堆肥化装置全体に占める建設費の
割合が大きく、コスト高になる欠点があつた。 On the other hand, in order to make the composting operation continuous, a function is required to move the material in a fixed direction at the same time as stirring for the above-mentioned turning operation. For this reason, almost all known modern composting devices have an agitation device that can perform both agitation and movement at the same time.
As the composting equipment becomes relatively large, the amount of material stored becomes large, so conventionally, this stirring equipment has become extremely large-scale, and the construction cost accounts for a large proportion of the entire composting equipment, resulting in high costs. It was hot.
本発明は、円筒状の発酵槽の中に、円周方向に
材料を移動する回転パドルを、半径方向及び円周
方向にジグザグに移動せしめることにより、従来
の方式における上記の欠点を除き、撹拌機構を材
料の貯蔵量と無関係に小型化かつ単純化し、また
撹拌機構を移動する機構も簡単となり、特に大型
の堆肥化装置の建設費を著しく低廉ならしめる堆
肥化方法とその装置を提供することを目的とする
ものである。 The present invention eliminates the above-mentioned drawbacks of the conventional method by moving a rotating paddle that moves the material in the circumferential direction in a radial and circumferential direction in a cylindrical fermenter. To provide a composting method and device, in which the mechanism is miniaturized and simplified regardless of the amount of material stored, the mechanism for moving the stirring mechanism is also simplified, and the construction cost of especially a large composting device is significantly reduced. The purpose is to
本発明は、底部の排出口から材料を排出するよ
うにした円筒状の発酵槽の中で、半径方向の軸を
中心に回転して材料を円周方向に移動せしめる回
転パドルを、前記発酵槽の半径方向及び円周方向
の両成分から成るジグザグ状の軌跡に沿つて移動
せしめて全材料を撹拌かつ移動せしめることを特
徴とする堆肥化方法及びその装置である。 The present invention provides a cylindrical fermentation tank configured to discharge materials from an outlet at the bottom, and a rotary paddle that rotates around a radial axis to move the material in the circumferential direction of the fermentation tank. A composting method and an apparatus therefor are characterized in that all materials are stirred and moved along a zigzag trajectory consisting of both radial and circumferential components.
本発明を実施例につき、図面を用いて説明すれ
ば、第1図、第2図、第3図において、円筒型発
酵槽1の軸心2を中心として架橋3が回転可能に
設けてある。即ち架橋3は、軸心2を中心として
回転可能なターンテーブル4と、発酵槽1の上面
5を走行する車輪6とを繋ぐ半径方向の部材によ
つて構成され、駆動装置7によつて矢印8の方向
に回転せしめられる。図示例では車輪6を駆動し
ているがターンテーブル4を駆動してもよいこと
は勿論である。 The present invention will be described with reference to the drawings. In FIGS. 1, 2, and 3, a bridge 3 is rotatably provided around an axis 2 of a cylindrical fermenter 1. That is, the bridge 3 is constituted by a radial member that connects a turntable 4 that is rotatable about the axis 2 and wheels 6 that run on the upper surface 5 of the fermenter 1. It is rotated in the direction of 8. In the illustrated example, the wheels 6 are driven, but it goes without saying that the turntable 4 may also be driven.
架橋3上には台車9を走行可能に設け、該台車
9からはアーム10を介して発酵槽1の半径方向
を軸心11として回転するパドル12が懸垂され
ている。図中13は台車9の駆動装置、14は回
転パドル12の駆動装置を夫々示す。 A trolley 9 is movably provided on the bridge 3, and a paddle 12 that rotates with an axis 11 in the radial direction of the fermenter 1 is suspended from the trolley 9 via an arm 10. In the figure, 13 indicates a drive device for the trolley 9, and 14 indicates a drive device for the rotary paddle 12.
矢印15及び16で示すような台車9の往復運
動と、矢印8で示すような架橋3の回転運動とか
らなるジグザグ状の軌跡で回転パドル12を移動
させることに依り、材料17は逐次撹拌されつつ
矢印8と反対方向に移動する。即ち、第4図に示
すようにパドル12の矢印8方向の移動によつて
材料はパドル12によつて切り込まれるが、この
際材料の堆積高さがパドル外径の1/2倍以上好ま
しくは1倍以上ある場合は、材料自体の遮閉効果
に依つて材料は点線矢印18で示すようにパドル
を飛び越えて移送される。 By moving the rotary paddle 12 in a zigzag trajectory consisting of the reciprocating motion of the cart 9 as shown by arrows 15 and 16 and the rotational motion of the bridge 3 as shown by the arrow 8, the material 17 is successively stirred. while moving in the opposite direction to arrow 8. That is, as shown in FIG. 4, the material is cut into the material by the paddle 12 as it moves in the direction of the arrow 8. At this time, it is preferable that the height of the material piled up is at least 1/2 times the outer diameter of the paddle. is more than one time, the material is transported over the paddle as indicated by the dotted arrow 18 due to the blocking effect of the material itself.
このような材料の切り込みとはね飛しとに依り
材料は細粒化されて著しく曝気表面積が増大する
と共に緩やかに堆積されるので、発酵槽下部の空
気室19から多孔床面20を介して給気される空
気の抵抗も少なく、しかも一様且つ速やかな好気
性発酵が行われる。次に材料の供給と排出との関
係について説明する。 Due to such incision and splashing of the material, the material is finely granulated and the aerated surface area is significantly increased, and the material is gradually deposited, so that it is passed from the air chamber 19 at the bottom of the fermenter through the porous floor surface 20. There is little resistance to the supplied air, and aerobic fermentation takes place uniformly and quickly. Next, the relationship between supply and discharge of materials will be explained.
第1図ないし第5図に示す如く、材料の供給装
置は、発酵槽上部に半径方向に設けられたベルト
コンベア21と、同コンベアの上面に接して且つ
コンベアの進行方向22に対して傾斜した掻板2
3及び同掻板を保持する駆動ベルト24とから成
つている。 As shown in FIGS. 1 to 5, the material supply device includes a belt conveyor 21 provided in the radial direction above the fermenter, and a belt conveyor 21 that is in contact with the top surface of the conveyor and inclined with respect to the traveling direction 22 of the conveyor. Scraping board 2
3 and a drive belt 24 that holds the scraper plate.
駆動ベルト24の回転方向を逐次切り換えて掻
板23を往復移動させることにより材料をコンベ
アの進行方向22と直角方向Rの方向に均一に落
下分散させることができる。 By sequentially switching the rotational direction of the drive belt 24 and reciprocating the scraper plate 23, the material can be uniformly dropped and dispersed in the direction R perpendicular to the direction of movement 22 of the conveyor.
材料の排出装置として、発酵槽1の床面の一部
半径方向に、材料が落下する排出口としてスリツ
ト25を設け、該スリツトの下部ピツト26内に
は排出コンベア27が設けられている。而してパ
ドル12によつて跳ね飛ばされて材料が拡散する
巾Bとスリツト25の巾Aとの割合によつて、排
出コンベア27で排出されずに床面に残留する材
料(即ち再循環される材料)の割合が決るから、
A寸法を適宜調整することによつて再環する材料
の割合が調節可能となる。このようにして発酵に
よつて脱水された材料と原料とを混合して、原料
の含水率を発酵に適する最適レベルに調整するこ
とが自動的に容易に行われる。 As a material discharge device, a slit 25 is provided in a radial direction of a portion of the floor surface of the fermenter 1 as a discharge port through which the material falls, and a discharge conveyor 27 is provided in a lower pit 26 of the slit. Accordingly, depending on the ratio of the width B where the material is scattered by the paddle 12 and the width A of the slit 25, the material that remains on the floor without being discharged by the discharge conveyor 27 (that is, the material that is not recycled) Since the ratio of the materials used) is determined,
By appropriately adjusting dimension A, the proportion of the material to be recirculated can be adjusted. In this way, the material dehydrated by fermentation and the raw material are mixed, and the moisture content of the raw material is automatically and easily adjusted to an optimal level suitable for fermentation.
尚、A寸法の調整は、ピツト26上に設けた平
板28の取付位置を適宜ずらせることに依り容易
に行える。 Incidentally, the A dimension can be easily adjusted by appropriately shifting the mounting position of the flat plate 28 provided on the pit 26.
又、材料の供給装置と排出装置との相互位置
は、落下する原料の安息角を考慮して、原料がス
リツト25に達しないような範囲で、スリツト中
心と原料落下位置との距離Cを最少寸法に設定す
るとよい。 In addition, the mutual positions of the material supply device and the material discharge device should be such that the distance C between the center of the slit and the material falling position is minimized within a range where the material does not reach the slit 25, taking into account the angle of repose of the falling material. It is best to set it to the dimensions.
なお、掻板23は、V字型として左右対称とす
ればベルトコンベア21のベルトの片寄りを防ぐ
ことができる。 Note that if the scraping plate 23 is V-shaped and symmetrical, it is possible to prevent the belt of the belt conveyor 21 from shifting.
本実施例において、撹拌機構である回転パドル
は材料の貯蔵量とは殆んど無関係に小型化かつ単
純化するとができるので、これを移動せしめる機
構も軽量小型となり、発酵槽が円筒形であり、全
面積をカバーする機構が簡単となることと相まつ
て、装置全体が簡単となり、しかも回転パドルは
キヤタピラ方式などに比べ構造が著しく簡単とな
るのみならず、周速を大とすることができ、材料
の小粒径化が可能で撹拌及び移動を効果的に同時
に行なうので、発酵が有効に行なわれる。また、
発酵槽の底部の出口スリツトの幅が調節可能とな
つているので、再循環する材料の割合を調節し、
原料の含水率を発酵に適する最適レベルに調節す
ることが容易である。 In this example, the rotating paddle, which is the stirring mechanism, can be made smaller and simpler regardless of the amount of material stored, so the mechanism for moving it can also be made lighter and smaller, and the fermenter is cylindrical. This, together with the simple mechanism that covers the entire area, simplifies the entire device.Moreover, the rotary paddle not only has a significantly simpler structure than the caterpillar method, but also allows for a higher circumferential speed. Since it is possible to reduce the particle size of the material and to perform stirring and movement effectively at the same time, fermentation is carried out effectively. Also,
The width of the exit slit at the bottom of the fermenter is adjustable, allowing you to control the proportion of material that is recycled.
It is easy to adjust the moisture content of the raw material to an optimal level suitable for fermentation.
なお、排出口としては上記の例の如きスリツト
を複数個設けてもよく、また、半径方向も区切ら
れた穴を複数個適宜半径方向に並べたり、また、
円周方向にも適宜分散し、かつ全体として何れか
の方向で半径方向をカバーするように配備するよ
うにしてもよい。 In addition, a plurality of slits as in the above example may be provided as the discharge port, or a plurality of holes separated in the radial direction may be appropriately arranged in the radial direction, or
They may also be appropriately distributed in the circumferential direction, and may be arranged so as to cover the radial direction in either direction as a whole.
本発明は、底部の排出口から材料を排出するよ
うにした円筒状の発酵槽の中で、半径方向の軸を
中心に回転して材料を円周方向に移動せしめる回
転パドルを、前記発酵槽の半径方向及び円周方向
の両成分から成るジグザグ状の軌跡に沿つて移動
せしめて全材料を撹拌かつ移動せしめることによ
り、回転パドル機構を円筒状の発酵槽に用いてそ
の機能が十分に発揮され、装置全体が著しく簡単
となり、建設費が低減され、しかも発酵工程を効
果的に進行せしめることができる堆肥化方法及び
その装置を提供することができ、実用上、廃棄物
処理上極めて大なる効果を有するものである。 The present invention provides a cylindrical fermentation tank configured to discharge materials from an outlet at the bottom, and a rotary paddle that rotates around a radial axis to move the material in the circumferential direction of the fermentation tank. The rotary paddle mechanism is used in a cylindrical fermenter to fully demonstrate its function by stirring and moving all the ingredients along a zigzag trajectory consisting of both radial and circumferential components. It is possible to provide a composting method and its device that can significantly simplify the entire device, reduce construction costs, and allow the fermentation process to proceed effectively, which is extremely important in terms of practical and waste treatment. It is effective.
図面は本発明の実施例を示し、第1図は側断面
図、第2図は第1図の視矢X平面図、第3図は要
部斜視図、第4図は第1図のY―Y断面図で材料
の供給・排出・撹拌の情況を示す図面、第5図は
発酵槽に対する材料の分散供給装置の平面図で、
第1図及び第4図の視矢Z図を夫々示す。
1…発酵槽、2…軸心、3…架橋、4…ターン
テーブル、5…上面、6…車輪、7…駆動装置、
8…矢印、9…台車、10…アーム、11…軸
心、12…パドル、13,14…駆動装置、1
5,16…矢印、17…材料、18…矢印、19
…空気室、20…多孔床面、21…ベルトコンベ
ア、22…進行方向、23…掻板、24…駆動ベ
ルト、25…スリツト、26…ピツト、27…排
出コンベア、28…平板。
The drawings show an embodiment of the present invention, and FIG. 1 is a side sectional view, FIG. 2 is a plan view taken along the arrow X in FIG. 1, FIG. 3 is a perspective view of main parts, and FIG. - Drawing showing the situation of supplying, discharging, and stirring of materials in a Y cross-sectional view, Figure 5 is a plan view of the device for dispersing and supplying materials to the fermenter,
1 and 4 are shown respectively. DESCRIPTION OF SYMBOLS 1...Fermentation tank, 2...Axis, 3...Bridge, 4...Turntable, 5...Top surface, 6...Wheel, 7...Drive device,
8...Arrow, 9...Dolly, 10...Arm, 11...Axis, 12...Paddle, 13, 14...Drive device, 1
5, 16...Arrow, 17...Material, 18...Arrow, 19
... Air chamber, 20 ... Porous floor surface, 21 ... Belt conveyor, 22 ... Traveling direction, 23 ... Scraping plate, 24 ... Drive belt, 25 ... Slit, 26 ... Pit, 27 ... Discharge conveyor, 28 ... Flat plate.
Claims (1)
円筒状の発酵槽の中で、半径方向の軸を中心に回
転して材料を円周方向に移動せしめる回転パドル
を、前記発酵槽の半径方向及び円周方向の両成分
から成るジグザグ状の軌跡に沿つて移動せしめて
全材料を撹拌かつ移動せしめることを特徴とする
堆肥化方法。 2 前記排出口の開口面積が調節可能であり、該
開口面積の調節により、再循環する材料の割合を
調節する特許請求の範囲第1項記載の方法。 3 底部に排出口が設けられた円筒状の発酵槽の
内部に、該発酵槽の中心を軸心として回転可能に
備えられた半径方向の架橋と、該架橋上を往復可
能に備えられた台車と、該台車の下部にあつて、
材料を前記発酵槽の円周方向に移動する機能を有
する回転パドルが備えられていることを特徴とす
る堆肥化装置。 4 前記排出口が、その開口面積が調節可能であ
る特許請求の範囲第3項記載の装置。[Claims] 1. A rotating paddle that rotates around a radial axis to move the material in the circumferential direction in a cylindrical fermenter that discharges the material from an outlet at the bottom. A composting method characterized in that all the materials are stirred and moved by moving along a zigzag trajectory consisting of both radial and circumferential components of the fermenter. 2. The method of claim 1, wherein the opening area of the outlet is adjustable, and adjusting the opening area adjusts the proportion of material to be recycled. 3 A radial bridge rotatably provided inside a cylindrical fermenter with an outlet at the bottom and rotatable around the center of the fermenter, and a trolley provided to be able to reciprocate on the bridge. And at the bottom of the trolley,
A composting device characterized in that it is equipped with a rotating paddle that has the function of moving the material in the circumferential direction of the fermenter. 4. The device according to claim 3, wherein the outlet has an adjustable opening area.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15036879A JPS5673688A (en) | 1979-11-20 | 1979-11-20 | Composting method and device therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15036879A JPS5673688A (en) | 1979-11-20 | 1979-11-20 | Composting method and device therefor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5673688A JPS5673688A (en) | 1981-06-18 |
| JPS6137236B2 true JPS6137236B2 (en) | 1986-08-22 |
Family
ID=15495458
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15036879A Granted JPS5673688A (en) | 1979-11-20 | 1979-11-20 | Composting method and device therefor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5673688A (en) |
-
1979
- 1979-11-20 JP JP15036879A patent/JPS5673688A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5673688A (en) | 1981-06-18 |
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