JPH05310490A - Fermentation dryer - Google Patents

Fermentation dryer

Info

Publication number
JPH05310490A
JPH05310490A JP4143200A JP14320092A JPH05310490A JP H05310490 A JPH05310490 A JP H05310490A JP 4143200 A JP4143200 A JP 4143200A JP 14320092 A JP14320092 A JP 14320092A JP H05310490 A JPH05310490 A JP H05310490A
Authority
JP
Japan
Prior art keywords
fermentation
drying drum
fermentation drying
drum
axis
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
JP4143200A
Other languages
Japanese (ja)
Other versions
JPH0774113B2 (en
Inventor
Koichi Miyata
耕一 宮田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
MIYATA TECHNICAL KK
Original Assignee
MIYATA TECHNICAL KK
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 MIYATA TECHNICAL KK filed Critical MIYATA TECHNICAL KK
Priority to JP4143200A priority Critical patent/JPH0774113B2/en
Publication of JPH05310490A publication Critical patent/JPH05310490A/en
Publication of JPH0774113B2 publication Critical patent/JPH0774113B2/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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Fertilizers (AREA)

Abstract

PURPOSE:To enable the good practice of pulverizing, stirring and mixing of an organic waste, the treatment in a short time and simplification of an apparatus in fermentation drying treatment. CONSTITUTION:The objective fermentation dryer is equipped with a transversely installed fermentation drying drum 2, a gear motor 6 for rotating and driving the fermentation drying drum 2 around the shaft center, a driving shaft 44, inserted into the fermentation drying drum 2 parallel to the shaft center and rotated and driven, pulverizing pawls 45, attached to the driving shaft 44 and located in the fermentation drying drum 2, a burner 9 for feeding hot air into the fermentation drying drum 2 and a gas discharge duct 10 for discharging a gas from the fermentation drying drum 2. In the fermentation drying treatment, an organic waste subjected to moisture conditioning and soil bacteria are introduced into the fermentation drying drum 2 to rotate and drive the fermentation drying drum 2 and the driving shaft 44. Thereby, lumps of the waste and the soil bacteria are pulverized to simultaneously stir and mix the waste with the soil bacteria. Furthermore, the hot air is fed into the fermentation drying drum 2 to carry out the fermentation and drying of the waste.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、生ゴミ等の有機性廃棄
物の高速発酵及び乾燥処理を行って肥料化又は飼料化す
る発酵乾燥装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fermenting / drying apparatus for performing high-speed fermentation and drying treatment of organic waste such as raw garbage to produce fertilizer or feed.

【0002】[0002]

【従来の技術】従来、生ゴミ等の有機性廃棄物の高速発
酵及び乾燥処理を行う装置では、例えば加熱装置及び攪
拌装置を備えた槽が少なくとも2層以上直列に配置され
ており、各槽に有機性廃棄物が順次移送されて、発酵乾
燥処理が行なわれ、処理物が排出されていた(このよう
な装置の一例が特開平1−145388号公報に開示さ
れている。)。
2. Description of the Related Art Conventionally, in an apparatus for high-speed fermentation and drying treatment of organic waste such as garbage, for example, at least two tanks equipped with a heating device and a stirring device are arranged in series, and each tank is The organic waste was sequentially transferred to the soil, the fermentation drying process was performed, and the processed product was discharged (an example of such a device is disclosed in JP-A-1-145388).

【0003】[0003]

【発明が解決しようとする課題】しかし、上記従来の装
置では、発酵処理槽が2層以上必要となって装置が複雑
になると共に、有機性廃棄物の処理時間が、2〜3日を
要するという問題があった。本発明の目的は、簡易な構
造であって、極めて短時間で発酵乾燥処理を行うことが
できる発酵乾燥装置を提供することである。
However, the above-mentioned conventional apparatus requires two or more fermentation treatment tanks, which complicates the apparatus and requires a processing time of 2-3 days for organic waste. There was a problem. An object of the present invention is to provide a fermentation / drying device having a simple structure and capable of performing fermentation / drying treatment in an extremely short time.

【0004】[0004]

【課題を解決するための手段】上記目的を達成するため
に、本発明の特徴とするところは、横設され、有機性廃
棄物及び土壌菌が投入されて、軸心回りに回転駆動され
ると共に、給気口及び排気口を備える発酵乾燥ドラム
と、発酵乾燥ドラムの軸心と平行な軸心を有し、軸心回
りに回転駆動されて、醗酵乾燥ドラム内の有機性廃棄物
及び土壌菌の塊を粉砕して、攪拌混合する粉砕装置と、
給気口から発酵乾燥ドラム内へ熱風を供給する熱風供給
装置とを有する点にある。尚、発酵乾燥ドラムの軸心方
向両側部に給気口及び排気口が備えられると共に、発酵
乾燥ドラムの軸心方向両側部が、軸心方向外側方に向か
うテーパー状のテーパー部とされることもある。又、給
気口及び排気口が、醗酵乾燥ドラムの軸心よりも上位と
されると共に、上記軸心から鉛直方向上方にのびる鉛直
面よりも、発酵乾燥ドラムの回転方向前方に配置される
こともある。更に、粉砕装置が、発酵乾燥ドラムに横設
された駆動軸と、駆動軸に備えられ且つ発酵乾燥ドラム
内に位置する粉砕爪を有することもある。又、有機性廃
棄物及び土壌菌が醗酵乾燥ドラム内の軸心方向中央部に
寄るように、粉砕爪が駆動軸に備えられることもある。
更に、粉砕装置の軸心が、醗酵乾燥ドラムの軸心よりも
下位とされると共に、発酵乾燥ドラムの軸心から鉛直方
向下方にのびる鉛直面よりも、発酵乾燥ドラムの回転方
向前方に配置されることもある。
In order to achieve the above object, a feature of the present invention is that it is installed laterally, and organic waste and soil fungus are charged therein and driven to rotate about its axis. Along with the fermentation drying drum having an air supply port and an exhaust port, and having an axis parallel to the axis of the fermentation drying drum, the organic waste and soil in the fermentation drying drum are driven to rotate around the axis. A crushing device for crushing a lump of bacteria and mixing with stirring,
It has a hot air supply device for supplying hot air from the air supply port into the fermentation and drying drum. In addition, both sides of the fermentation and drying drum in the axial direction are provided with air supply ports and exhaust ports, and both sides of the fermentation and drying drum in the axial direction are tapered portions that extend outward in the axial direction. There is also. Further, the air supply port and the exhaust port are arranged higher than the shaft center of the fermentation drying drum, and are arranged in front of the rotation direction of the fermentation drying drum with respect to the vertical plane extending vertically upward from the shaft center. There is also. Further, the crushing device may have a drive shaft laterally provided on the fermentation drying drum and a crushing claw provided on the drive shaft and located inside the fermentation drying drum. In addition, a crushing claw may be provided on the drive shaft so that the organic waste and the soil fungus are closer to the central portion in the axial direction in the fermentation drying drum.
Further, the axis of the crushing device is lower than the axis of the fermentation drying drum, and is arranged in the front in the rotation direction of the fermentation drying drum, rather than the vertical plane extending vertically downward from the axis of the fermentation drying drum. Sometimes

【0005】[0005]

【作用】発酵乾燥処理を行う場合には、発酵乾燥ドラム
内に、水分調節された処理物と土壌菌を投入する。この
状態で、発酵乾燥ドラム及び粉砕装置を回転駆動すると
共に、熱風供給装置から熱風を発酵乾燥ドラム内に供給
する。これにより、発酵乾燥ドラム内に投入された処理
物及び土壌菌は、発酵乾燥ドラムの回転により、発酵乾
燥ドラムの内面と連れ回って、全体的に反転させられな
がら、攪拌混合されると共に、粉砕装置が、発酵乾燥ド
ラム内の処理物及び土壌菌の塊を粉砕して、攪拌混合す
る。
[Function] When the fermentation and drying process is performed, the water-controlled product and soil fungus are put into the fermentation and drying drum. In this state, the fermentation drying drum and the crushing device are rotationally driven, and hot air is supplied from the hot air supply device into the fermentation drying drum. As a result, the processed material and soil fungus put in the fermentation drying drum are rotated and mixed together with the inner surface of the fermentation drying drum, while being stirred and mixed while being inverted, as a whole. An apparatus grinds the processed material and soil fungus mass in the fermentation drying drum, and mixes them by stirring.

【0006】又、熱風供給装置から供給される熱風によ
り、発酵乾燥ドラム内の温度は急速に上昇し、これによ
り、処理物が加熱されると共に、処理物が乾燥され、こ
れによって、発酵処理が進行し、処理物は準完熟状態と
なる。この準完熟処理された中間処理物は、更に、熱風
供給装置からの熱風により、乾燥処理が行われ、乾燥す
ると、黒褐色、細粉状の完成処理物、即ち腐食土化した
肥料又は飼料となる。上記のように乾燥すると、熱風供
給装置による発酵乾燥ドラム内への熱風の供給が停止さ
れて、発酵乾燥ドラム内の温度が低下し、乾燥した完成
処理物は、放冷される。
Further, the hot air supplied from the hot air supply device rapidly raises the temperature in the fermentation and drying drum, whereby the processed product is heated and the processed product is dried, whereby the fermentation process is carried out. As it progresses, the processed product becomes semi-ripe. This semi-ripened intermediate processed product is further dried by hot air from a hot air supply device, and when dried, becomes a black brown, fine powdery completed processed product, that is, a fertilizer or feed that has been converted to corrosive soil. .. When dried as described above, the supply of hot air into the fermentation drying drum by the hot air supply device is stopped, the temperature inside the fermentation drying drum is lowered, and the dried finished processed product is allowed to cool.

【0007】[0007]

【実施例】以下、本発明の一実施例を図面に基づき説明
する。図1及び図2等に示すように、発酵乾燥装置は、
架台1と、発酵乾燥ドラム2と、左右一対の支持装置3
と、蓋体4,5と、ギアモータ6と、粉砕装置7と、検
出スイッチ8と、バーナ9と、排気ダクト10と、台車
11等から成る。架台1は、左右方向に横設された本体
フレーム13と、各本体フレーム13の左右両端部から
下設された4本の脚部14を有する。図3乃至図5に示
すように、発酵乾燥ドラム2は、架台1の上方で左右方
向に横設されて、軸心回りに回転駆動されるもので、本
体16と、着脱蓋17から成る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. As shown in FIG. 1 and FIG.
Frame 1, fermentation / drying drum 2, and a pair of left and right supporting devices 3
It includes a lid 4, 5, a gear motor 6, a crushing device 7, a detection switch 8, a burner 9, an exhaust duct 10, a carriage 11 and the like. The gantry 1 has a body frame 13 that is provided laterally in the left-right direction, and four leg portions 14 that are provided below both left and right ends of each body frame 13. As shown in FIGS. 3 to 5, the fermentation and drying drum 2 is horizontally installed above the gantry 1 and is driven to rotate about its axis, and includes a main body 16 and a removable lid 17.

【0008】本体16は、その軸心方向中央部を構成し
且つ軸心方向に関して一定径とされた円筒状の円筒部1
9と、本体16の軸心方向両側部を構成し且つ軸心方向
外側方に向かってテーパー状とされたテーパー部20,
21と、各テーパー部20,21の外側端部に付設され
たリング部22,23とから構成されている。円筒部1
9の軸心方向中央部には、開口部24が形成されて、こ
の開口部24が着脱蓋17により着脱自在に施蓋されて
いる。各リング部22,23の内側端部には、他の部分
より大径とされた大径部25,26が形成されると共
に、右側リング部22の外側端部には、従動スプロケッ
ト27が外嵌固定されている。
The main body 16 constitutes a central portion in the axial direction and has a cylindrical shape having a constant diameter in the axial direction.
9, and a tapered portion 20 that constitutes both axial side portions of the main body 16 and is tapered outward in the axial direction,
21 and ring portions 22 and 23 attached to the outer ends of the tapered portions 20 and 21, respectively. Cylindrical part 1
An opening 24 is formed in the central portion of the shaft 9 in the axial direction, and the opening 24 is detachably covered by a removable lid 17. Large-diameter portions 25 and 26 having a larger diameter than the other portions are formed at the inner end portions of the ring portions 22 and 23, and a driven sprocket 27 is attached to the outer end portion of the right ring portion 22. It is fitted and fixed.

【0009】図6に示すように、各支持装置3は、発酵
乾燥ドラム2を回転自在に支持するもので、本体フレー
ム13に固定されるブラケット31と、ブラケット31
の前後両端部に左右方向の支軸32により回転自在に支
持される前後一対の鍔付きローラ33とから成り、各ロ
ーラ33が発酵乾燥ドラム2の各大径部25,26を転
動自在に支持している。各蓋体4,5は、円盤状とされ
ると共に、外周縁部が軸心方向内側方に突出しており、
発酵乾燥ドラム2の各リング部22,23に外嵌され
て、発酵乾燥ドラム2の両端開口を施蓋している。各蓋
体5は本体フレーム13にブラケット35,36を介し
て支持されている。右側蓋体5には、扇型状の排気口3
7が形成されている。
As shown in FIG. 6, each supporting device 3 rotatably supports the fermentation and drying drum 2, and a bracket 31 fixed to the main body frame 13 and a bracket 31.
And a pair of front and rear flanged rollers 33 that are rotatably supported by left and right support shafts 32 at the front and rear ends of the fermenting and drying drum 2. I support you. Each of the lids 4 and 5 has a disk shape, and the outer peripheral edge portion thereof protrudes inward in the axial direction,
The fermenting / drying drum 2 is fitted onto the respective ring portions 22 and 23 so as to cover both ends of the fermenting / drying drum 2. Each lid 5 is supported by the body frame 13 via brackets 35 and 36. The right lid 5 has a fan-shaped exhaust port 3
7 are formed.

【0010】ギアモータ6は、発酵乾燥ドラム2を回転
駆動するもので、本体フレーム13の右側部の後部にモ
ータサドル39を介して備えられている。ギアモータ6
からは、内側方に出力軸40が突設されて、この出力軸
40に駆動スプロケット41が固設され、このスプロケ
ット41が従動スプロケット27とチェーン42を介し
て連動連結されている。粉砕装置7は、発酵乾燥ドラム
2の軸心と平行な軸心を有し、軸心回りに回転駆動され
て、醗酵乾燥ドラム2内の有機性廃棄物及び土壌菌の塊
を粉砕して、攪拌混合するもので、駆動軸44と、粉砕
爪45と、ギアモータ46等を有する。
The gear motor 6 drives the fermentation and drying drum 2 to rotate, and is provided at the rear of the right side of the main body frame 13 via a motor saddle 39. Gear motor 6
From the above, an output shaft 40 is provided so as to project inward, a drive sprocket 41 is fixedly mounted on the output shaft 40, and the sprocket 41 is interlocked with a driven sprocket 27 via a chain 42. The crushing device 7 has an axis parallel to the axis of the fermentation drying drum 2 and is driven to rotate about the axis to crush the organic waste and the lump of soil bacteria in the fermentation drying drum 2, It is agitated and mixed, and has a drive shaft 44, a crushing claw 45, a gear motor 46, and the like.

【0011】駆動軸44は、発酵乾燥ドラム2に左右方
向に横設されて、各蓋体4,5及び/又はブラケット3
5,36に回転自在に支持されるもので、その軸心が醗
酵乾燥ドラム2の軸心よりも下位とされると共に、発酵
乾燥ドラム2の軸心から鉛直方向下方にのびる鉛直面4
8よりも回転方向前方に配置されている。尚、実施例で
は、駆動軸44の軸心は、上記鉛直面48と、発酵乾燥
ドラム2の軸心からのび且つ上記鉛直面48よりも90
度だけ発酵乾燥ドラム2の回転方向前方に位置する水平
面49との間の周方向中央位置乃至略中央位置とされて
いる。尚、Aが発酵乾燥ドラム2の回転方向を示し、B
が駆動軸44及び粉砕爪45の回転方向を示すが、実施
例では、両回転方向A,Bは同一とされている。駆動軸
44の右端部には、従動スプロケット50が固設される
と共に、駆動軸44には、発酵乾燥ドラム2内に位置す
る取付フランジ51が、軸心方向に関して、所定間隔置
きに数枚並設されている。
The drive shaft 44 is provided laterally on the fermentation and drying drum 2 in the left-right direction, and each of the lids 4 and 5 and / or the bracket 3 is provided.
5, 36 is rotatably supported, and its axis is lower than the axis of the fermentation and drying drum 2, and the vertical plane 4 extends vertically downward from the axis of the fermentation and drying drum 2.
It is arranged in front of 8 in the rotation direction. In the embodiment, the axis of the drive shaft 44 extends from the vertical plane 48, extends from the axis of the fermentation and drying drum 2 and is 90 degrees larger than the vertical plane 48.
It is set at a central position or a substantially central position in the circumferential direction between the fermenting and drying drum 2 and the horizontal plane 49 located forward of the rotating direction. In addition, A indicates the rotation direction of the fermentation drying drum 2, and B
Indicates the rotation direction of the drive shaft 44 and the crushing claw 45, but in the embodiment, both rotation directions A and B are the same. A driven sprocket 50 is fixed to the right end of the drive shaft 44, and a plurality of mounting flanges 51 located in the fermentation and drying drum 2 are arranged on the drive shaft 44 at predetermined intervals in the axial direction. It is set up.

【0012】粉砕爪45は、各取付フランジ51に、一
個宛着脱自在に取付けられるもので、粉砕爪45として
は、例えば、耕耘爪等が使用される。隣接する粉砕爪4
5は、周方向に関して、180度ずれると共に、左右の
粉砕爪45の先端部は、左右方向に関して、反対側を指
向するように曲げられて、粉砕装置7の駆動時には、粉
砕爪45により、有機性廃棄物及び土壌菌が醗酵乾燥ド
ラム2内の軸心方向中央部に寄るようにされている。ギ
アモータ46は、本体フレーム13の右側部の前部に備
えられている。ギアモータ46からは、内側方に出力軸
53が突設されて、この出力軸53に駆動スプロケット
54が固設され、このスプロケット54が、チェーン5
5を介して、従動スプロケット50と連動連結されてい
る。
The crushing claw 45 is detachably attached to each of the mounting flanges 51 one by one. As the crushing claw 45, for example, a plowing claw or the like is used. Adjacent grinding claw 4
5 is displaced by 180 degrees with respect to the circumferential direction, and the tip portions of the left and right crushing claws 45 are bent so as to be directed to the opposite side with respect to the left and right direction. Waste and soil fungi are arranged in the fermentation drying drum 2 at the central portion in the axial direction. The gear motor 46 is provided at the front part on the right side of the main body frame 13. An output shaft 53 is projected inward from the gear motor 46, and a drive sprocket 54 is fixedly mounted on the output shaft 53.
The driven sprocket 50 is interlocked and coupled via the connector 5.

【0013】検出スイッチ8は、発酵乾燥ドラム2の回
転位置を検出し、ギアモータ6を制御して、発酵乾燥ド
ラム2の開口部24を周方向に関して任意の位置で停止
させるもので、近接タイプとされており、図7に示すよ
うに、右側蓋体5の外周部の外側面にブラケット57を
介して着脱自在に取付けられており、従動スプロケット
27に取付けられたボルト58を検出する。バーナ9
は、発酵乾燥ドラム2内に熱風を供給する熱風供給装置
として例示されるもので、右側蓋体5等に装着されると
共に、その熱風吹出筒60が右側蓋体5に挿通されて、
先端の給気口61が軸心方向内側方に開口している。給
気口61及び排気口37は、醗酵乾燥ドラム2の軸心よ
りも上位とされると共に、上記軸心から鉛直方向上方に
のびる鉛直面62よりも回転方向前方に配置されてい
る。尚、実施例では、給気口61は、上記鉛直面62
と、発酵乾燥ドラム2の軸心からのび且つ上記鉛直面6
2よりも90度だけ発酵乾燥ドラム2の回転方向前方に
位置する水平面63との間の周方向中央位置とされてお
り、又、排気口37は周方向に関して、上記鉛直面62
と水平面63との間の略全長にわたって形成されてお
り、給気口61及び排気口37は、駆動軸44と径方向
略対称箇所に位置する。
The detection switch 8 detects the rotational position of the fermentation and drying drum 2 and controls the gear motor 6 to stop the opening 24 of the fermentation and drying drum 2 at an arbitrary position in the circumferential direction. As shown in FIG. 7, the bolt 58, which is detachably attached to the outer surface of the outer peripheral portion of the right lid 5 via a bracket 57, is attached to the driven sprocket 27. Burner 9
Is exemplified as a hot air supply device for supplying hot air into the fermentation drying drum 2, and is attached to the right side lid body 5 or the like, and the hot air blowing tube 60 is inserted into the right side lid body 5,
The air supply port 61 at the tip is opened inward in the axial direction. The air supply port 61 and the exhaust port 37 are positioned higher than the axis of the fermentation drying drum 2 and are arranged in front of the vertical plane 62 extending vertically upward from the axis in the rotational direction. In the embodiment, the air supply port 61 has the vertical surface 62.
And extending from the axis of the fermentation and drying drum 2 and the vertical plane 6
It is located at a center position in the circumferential direction between the horizontal plane 63 and the horizontal plane 63 located forward of the fermentation drying drum 2 by 90 degrees, and the exhaust port 37 has the vertical plane 62 in the circumferential direction.
Is formed over substantially the entire length between the horizontal plane 63 and the horizontal plane 63, and the air supply port 61 and the exhaust port 37 are located substantially symmetrically with the drive shaft 44 in the radial direction.

【0014】排気ダクト10は、発酵乾燥ドラム2内か
ら排気するためのもので、立設状の簡易集塵式とされ
て、右側蓋体5に取付けられている。排気ダクト10の
内側部には、排気口37と連通する排気用開口65が形
成されている。台車11は、上方及び右側方に開口する
もので、架台1の本体フレーム13の下方に配置され
て、発酵乾燥ドラム2の下方に位置する。
The exhaust duct 10 is for exhausting air from the inside of the fermentation and drying drum 2, and is a standing dust collection type and is attached to the right lid 5. An exhaust opening 65 communicating with the exhaust port 37 is formed inside the exhaust duct 10. The dolly 11 is open to the upper side and the right side, is arranged below the main body frame 13 of the gantry 1, and is located below the fermentation and drying drum 2.

【0015】次に、上記のように構成された発酵乾燥装
置の運転動作を説明する。発酵乾燥処理を行う有機物と
しては、例えば、頭、骨付魚のアラや残飯等を使用し、
これらの含水率は65〜75%程度である。このような
有機物に含水率10%程度の乾燥おから又はおがくずを
水分調整材として加え、水分率40〜60%の範囲に調
整して処理物を形成する。又、併用される土壌菌は、好
適活動範囲が温度60〜75℃、水分率50%前後のも
のが選定され、例えば、市販のMU菌(長野県松本市大
字入山辺8961内城農法研究所製)が好適である。
Next, the operation of the fermentation / drying apparatus configured as described above will be described. As the organic matter to be fermented and dried, for example, head, boned fish ara or leftover rice etc. are used,
Their water content is about 65 to 75%. Dried okara or sawdust having a water content of about 10% is added as a water content adjusting agent to such an organic material to adjust the water content to a range of 40 to 60% to form a treated product. The soil bacteria to be used together have a suitable activity range of 60 to 75 ° C and a moisture content of about 50%. For example, commercially available MU bacteria (8961 Iriyamabe, Nagano Prefecture Matsumoto City, Uchijo Agricultural Research Institute) Manufactured) is preferable.

【0016】発酵乾燥装置により処理を行う場合には、
まず、発酵乾燥ドラム2を開口部24を上側とした状態
で停止させると共に、着脱蓋17を取り外しておき、水
分調節された処理物と土壌菌を、重量比で、1対1/1
0000の割合で配合して、発酵乾燥ドラム2内にその
開口部24から投入する。この場合において、給気口6
1及び排気口37が、発酵乾燥ドラム2の回転中心であ
る軸心よりも上位とされているので、発酵乾燥ドラム2
内に、処理物を、良好な攪拌混合が可能な軸心位置の近
傍まで投入でき、作業能率を向上できる。次に、両ギア
モータ6,46を駆動して、発酵乾燥ドラム2及び粉砕
装置7の駆動軸44を回転駆動すると共に、バーナ9か
ら熱風を発酵乾燥ドラム2内に供給する。
When the treatment is carried out by a fermentation dryer,
First, the fermentation drying drum 2 is stopped with the opening 24 on the upper side, and the attachment / detachment lid 17 is removed, so that the treated matter and the soil fungus are adjusted to a weight ratio of 1: 1/1.
It is blended at a ratio of 0000 and put into the fermentation drying drum 2 through the opening 24. In this case, the air supply port 6
1 and the exhaust port 37 are positioned higher than the shaft center which is the rotation center of the fermentation drying drum 2, the fermentation drying drum 2
The processed product can be charged into the vicinity of the axial center position where good stirring and mixing can be performed, and the work efficiency can be improved. Next, both gear motors 6 and 46 are driven to rotationally drive the fermentation drying drum 2 and the drive shaft 44 of the crushing device 7, and hot air is supplied from the burner 9 into the fermentation drying drum 2.

【0017】これにより、発酵乾燥ドラム2内に投入さ
れた処理物及び土壌菌は、発酵乾燥ドラム2の回転によ
り、発酵乾燥ドラム2の内面と連れ回って、全体的に反
転させられながら、攪拌混合されると共に、粉砕装置7
の粉砕爪45が、発酵乾燥ドラム2内の処理物及び土壌
菌の塊を粉砕して、攪拌混合する。又、バーナ9から供
給される250〜350℃の熱風により、発酵乾燥ドラ
ム2内の温度は急速に上昇し、これにより、ドラム2内
の上層部は300〜350℃に達する。これにより、処
理物の温度は、運転開始後、約20分で約60℃に加熱
され、又、処理物の水分率は投入時より2〜3%低下す
る。
As a result, the treated material and soil fungi put into the fermentation and drying drum 2 are stirred by the rotation of the fermentation and drying drum 2 while being rotated with the inner surface of the fermentation and drying drum 2 and being totally inverted. While being mixed, the crushing device 7
The crushing claw 45 of crushes the lump of the processed material and soil fungus in the fermentation and drying drum 2 and stirs and mixes them. Further, the temperature in the fermentation and drying drum 2 rapidly rises due to the hot air of 250 to 350 ° C. supplied from the burner 9, whereby the upper layer portion in the drum 2 reaches 300 to 350 ° C. As a result, the temperature of the treated product is heated to about 60 ° C. in about 20 minutes after the start of operation, and the moisture content of the treated product is reduced by 2 to 3% from the time of the addition.

【0018】ところで、上記のような発酵乾燥ドラム2
の回転駆動と、バーナ9からの発酵乾燥ドラム2内への
熱風の供給により、発酵処理が進行し、処理物は連続し
て熱風を受けて更に加熱されると共に、発酵処理速度が
高進する。この状態で約30分間経過すると、処理物の
温度は約75℃となり、水分率は投入時より5〜7%低
下し、ここで処理物は準完熟状態となる。この準完熟処
理された中間処理物は、更にバーナ9からの熱風によ
り、乾燥処理が行われる。この乾燥処理を約30分行う
と、処理物の温度は約85℃に上昇し、水分率は10%
以下に低下して、黒褐色、細粉状の完成処理物、即ち腐
食土化した肥料又は飼料となる。
By the way, the fermentation and drying drum 2 as described above is used.
By the rotation drive of No. 1 and the supply of hot air from the burner 9 into the fermentation drying drum 2, the fermentation process proceeds, the processed product is continuously heated by further receiving hot air, and the fermentation process speed increases. .. After about 30 minutes have passed in this state, the temperature of the processed product becomes about 75 ° C., and the moisture content is lowered by 5 to 7% from the time of the introduction, and the processed product is in a semi-ripe state. The semi-ripened intermediate processed product is further dried by hot air from the burner 9. When this drying treatment is performed for about 30 minutes, the temperature of the treated product rises to about 85 ° C and the water content is 10%.
It decreases to below, and it becomes a blackish brown, finely powdered finished product, that is, a fertilizer or feed that has been converted to corrosive soil.

【0019】上記のようにして、有機性廃棄物等から成
る処理物は、発酵乾燥ドラム2内で土壌菌の作用と熱風
とにより発酵及び乾燥が促進され、投入から約1時間半
で黒褐色、細粉状の完成処理物、即ち腐食土化した肥料
又は飼料とされる。即ち、高温の熱風を発酵乾燥ドラム
2内に供給することにより、土壌菌の最適活動温度域に
極めて短時間に加熱できると共に、有機性廃棄物等から
成る処理物の高温処理が行えるので、発酵処理時間を著
しく短縮することができ、しかも、1個の発酵乾燥ドラ
ム2で発酵処理に連続して乾燥処理が行え、構造が簡易
である。そして、上記のように乾燥すると、バーナ9に
よる発酵乾燥ドラム2内への熱風の供給が停止されて、
発酵乾燥ドラム2内の温度が低下し、乾燥した完成処理
物は、放冷される。
As described above, the treated product consisting of the organic waste or the like is fermented and dried in the fermentation and drying drum 2 by the action of the soil bacteria and the hot air to accelerate the fermentation and drying. It is used as a finely processed finished product, that is, as a fertilizer or feed that has been converted to corrosive soil. That is, by supplying high-temperature hot air into the fermentation drying drum 2, it is possible to heat the soil bacteria to the optimum activity temperature range in an extremely short period of time and to perform high-temperature treatment of the treated matter including organic waste. The processing time can be remarkably shortened, and further, the drying process can be performed continuously with the fermentation process with one fermentation drying drum 2, and the structure is simple. Then, when dried as described above, the supply of hot air into the fermentation drying drum 2 by the burner 9 is stopped,
The temperature in the fermentation and drying drum 2 decreases, and the dried processed product is allowed to cool.

【0020】上記のように、有機性廃棄物の処理時に
は、発酵乾燥ドラム2全体が回転駆動されるので、発酵
乾燥ドラム2内に投入された処理物及び土壌菌は、発酵
乾燥ドラム2の回転により、発酵乾燥ドラム2の内面と
連れ回って、全体的に反転させられながら、攪拌混合さ
れると共に、発酵乾燥ドラム2全体が高温となって、こ
の発酵乾燥ドラム2内面と処理物が連れ回るので、処理
物の乾燥が良好に行われる。これを、発酵乾燥槽内に、
回転駆動される攪拌混合用スクリューが備えられている
一例と比較した場合に、上記一例では、本願発明とは異
なり、攪拌混合が部分的にとどまると共に、処理物が、
本願発明のように、高温となった発酵乾燥ドラム2内面
と連れ回らないので、処理物の乾燥を本願発明程には良
好に行えない。
As described above, during the processing of the organic waste, the entire fermentation and drying drum 2 is rotationally driven, so that the processed products and soil fungi put in the fermentation and drying drum 2 rotate in the fermentation and drying drum 2. As a result, the inner surface of the fermentation and drying drum 2 is rotated, and while being totally inverted, the mixture is stirred and mixed, and the temperature of the entire fermentation and drying drum 2 becomes high, and the inner surface of the fermentation and drying drum 2 and the processed product are rotated together. Therefore, the processed product is dried well. In the fermentation and drying tank,
When compared with an example in which a screw for stirring and rotating is provided, in the above example, unlike the invention of the present application, while stirring and mixing is partially retained, the processed product is
Unlike the invention of the present application, since it does not follow the inner surface of the fermentation and drying drum 2 that has reached a high temperature, the processed product cannot be dried as well as the invention of the present application.

【0021】又、本発明では、更に、粉砕装置7が回転
駆動されて、その粉砕爪45が、発酵乾燥ドラム2内の
処理物及び土壌菌の塊を粉砕するので、発酵乾燥ドラム
2内に大きな処理物を投入した場合でも、処理物を容易
に粉砕できると共に、処理物が乾燥する過程において、
発酵乾燥ドラム2内の処理物の表面上には、ダマと呼ば
れる処理物及び土壌菌の塊ができ易いが、このダマを粉
砕爪45により容易に粉砕できる。更に、上記粉砕時
に、例え、粉砕爪45と発酵乾燥ドラム2内面間に処理
物が噛み込んでも、粉砕装置7の駆動軸44が、発酵乾
燥ドラム2の軸心とずれていると共に、発酵乾燥ドラム
2の回転方向Aと粉砕装置7の回転方向Bが同一である
ので、上記噛み込み状態が解除され易い。
Further, in the present invention, the crushing device 7 is further driven to rotate, and the crushing claw 45 crushes the mass of the processed material and soil fungus in the fermentation drying drum 2, so that the fermentation drying drum 2 is crushed. Even when a large processed product is charged, the processed product can be easily crushed, and in the process of drying the processed product,
On the surface of the processed product in the fermentation and drying drum 2, a processed product called lump and a lump of soil bacteria are easily formed, and this lump can be easily crushed by the crushing claw 45. Further, even when the processed material is caught between the crushing claw 45 and the inner surface of the fermentation / drying drum 2 during the crushing, the drive shaft 44 of the crushing device 7 is displaced from the axis of the fermentation / drying drum 2, and the fermentation / drying is performed. Since the rotation direction A of the drum 2 and the rotation direction B of the crushing device 7 are the same, the above-mentioned bite state is easily released.

【0022】又、粉砕爪45も、発酵乾燥ドラム2の回
転と協働して、発酵乾燥ドラム2内の処理物及び土壌菌
を攪拌混合するので、発酵乾燥ドラム2内の処理物及び
土壌菌を、より一層良好に攪拌混合できる。特に、処理
時には、発酵乾燥ドラム2の回転により、処理物及び土
壌菌は、周方向に関して、発酵乾燥ドラム2の回転方向
Aに押されて、図5の仮想線で示すように、この回転方
向Aにずれた位置となるが、実施例では、駆動軸44の
軸心が、鉛直面48と、発酵乾燥ドラム2の軸心からの
び且つ上記鉛直面48よりも90度だけ発酵乾燥ドラム
2の回転方向前方に位置する水平面49との間の周方向
中央位置乃至略中央位置とされているので、粉砕爪45
の回転領域67の大半が、発酵乾燥ドラム2内の処理物
及び土壌菌の存在領域68と重なり合い、それ故、粉砕
爪45による上記粉砕及び攪拌混合をより一層効果的に
行える。
Further, since the crushing claw 45 also cooperates with the rotation of the fermentation and drying drum 2 to stir and mix the treated material and soil bacteria in the fermentation and drying drum 2, the treated material and soil bacteria in the fermentation and drying drum 2 are agitated and mixed. Can be mixed with stirring even better. In particular, at the time of processing, the fermented and dried drum 2 is rotated so that the treated material and soil fungus are pushed in the rotational direction A of the fermented and dried drum 2 with respect to the circumferential direction, and as shown by the phantom line in FIG. Although the position is shifted to A, in the embodiment, the axis of the drive shaft 44 extends from the vertical plane 48 and the axis of the fermentation and drying drum 2 and is 90 degrees from the vertical plane 48 of the fermentation and drying drum 2. The crushing claw 45 is located at the center position or the substantially center position in the circumferential direction with respect to the horizontal plane 49 located forward in the rotation direction.
Most of the rotating area 67 of the above overlaps with the existing area 68 of the processed material and soil fungus in the fermentation and drying drum 2, so that the crushing and stirring and mixing by the crushing claw 45 can be performed more effectively.

【0023】又、上記の場合において、発酵乾燥ドラム
2の軸心方向両端部が、軸心方向中央部に向かうテーパ
ー状のテーパー部20,21とされているので、テーパ
ー部20,21上の処理物は発酵乾燥ドラム2の回転に
伴い、軸心方向中央部側に送られることとなると共に、
粉砕装置7の左右各側の粉砕爪45の先端部は、左右方
向に関して、反対側を指向するように曲げられて、有機
性廃棄物及び土壌菌が醗酵乾燥ドラム内の軸心方向中央
部に寄るようにされているので、発酵乾燥ドラム2内の
処理物は、より一層発酵乾燥ドラム2の軸心方向中央部
に寄り易く、処理物の攪拌混合がより一層良好に行われ
ると共に、処理物が給気口61及び排気口37に行きに
くく、処理物により給気口61及び排気口37が閉塞さ
れにくい。
Further, in the above case, since both ends in the axial direction of the fermentation and drying drum 2 are tapered parts 20 and 21 which are tapered toward the central part in the axial direction, the above-mentioned tapered parts 20 and 21 are formed. The processed product will be sent to the central portion side in the axial direction as the fermentation and drying drum 2 rotates, and
The tips of the crushing claws 45 on the left and right sides of the crushing device 7 are bent so as to be directed to the opposite sides in the left-right direction, so that the organic waste and soil fungus are at the central portion in the axial center of the fermentation drying drum. Since the processed products in the fermentation and drying drum 2 are closer to the central portion of the fermentation and drying drum 2 in the axial direction, the processed products can be stirred and mixed more favorably, and Does not easily reach the air supply port 61 and the air exhaust port 37, and the air supply port 61 and the air exhaust port 37 are less likely to be blocked by the processed material.

【0024】特に、処理時には、上記のように、発酵乾
燥ドラム2の回転により、処理物及び土壌菌の存在領域
68は、周方向に関して、発酵乾燥ドラム2の回転方向
Aに押されて、図5の仮想線で示すように、この回転方
向Aにずれた位置となるが、給気口61及び排気口37
は、発酵乾燥ドラム2の軸心より上位とされると共に、
発酵乾燥ドラム2の軸心から鉛直方向上方にのびる鉛直
面62よりも発酵乾燥ドラム2の回転方向前方に位置す
るので、給気口61及び排気口37が、発酵乾燥ドラム
2内の処理物及び土壌菌の存在領域68と、発酵乾燥ド
ラム2の径方向に関して対向する状態となり、従って、
給気口61及び排気口37に処理物及び土壌菌が行きに
くく、給気口61及び排気口37が詰まりにくい。
In particular, at the time of processing, as described above, by the rotation of the fermentation drying drum 2, the area 68 in which the treated material and the soil fungus are present is pushed in the rotational direction A of the fermentation drying drum 2 with respect to the circumferential direction. As shown by the phantom line in FIG. 5, the position is deviated in the rotation direction A, but the air supply port 61 and the exhaust port 37.
Is higher than the axis of the fermentation and drying drum 2,
Since the fermentation drying drum 2 is located in front of the vertical plane 62 extending vertically upward from the axis of the fermentation drying drum 2 in the rotation direction of the fermentation drying drum 2, the air supply port 61 and the exhaust port 37 are disposed in the fermentation drying drum 2. The soil bacteria existing region 68 and the fermentation drying drum 2 are in a state of facing each other in the radial direction.
The treated material and soil fungus do not easily reach the air supply port 61 and the air exhaust port 37, and the air supply port 61 and the air exhaust port 37 are less likely to be clogged.

【0025】而して、上記のようにして、完成処理物の
温度が低下すれば、一旦、ギアモータ6,46の駆動を
停止して、着脱蓋17を取外し、開口部24を開放す
る。この状態で、発酵乾燥ドラム2の下方に台車11を
配置して、ギアモータ6により、発酵乾燥ドラム2を回
転駆動する。これにより、発酵乾燥ドラム2の回転に伴
い、その内部の完成処理物は開口部24から順次台車1
1内に落下する。尚、上記の間において、発酵乾燥ドラ
ム2内の蒸発水分及び、乾燥して醗酵乾燥ドラム2内に
浮遊する粉塵は排気口37、排気用開口65を介して排
気ダクト10内に入る。そして、粉塵は排気ダクト10
の下方に溜まり、ガス成分は外部に排出される。
As described above, when the temperature of the finished processed product is lowered, the driving of the gear motors 6 and 46 is once stopped, the attachment / detachment lid 17 is removed, and the opening 24 is opened. In this state, the carriage 11 is arranged below the fermentation / drying drum 2, and the gear / motor 6 drives the fermentation / drying drum 2 to rotate. As a result, as the fermentation and drying drum 2 rotates, the finished products inside the fermentation and drying drum 2 are sequentially transferred from the opening 24 to the carriage 1.
It falls into 1. During the above period, evaporated water in the fermentation drying drum 2 and dust that has dried and floated in the fermentation drying drum 2 enter the exhaust duct 10 through the exhaust port 37 and the exhaust opening 65. And dust is exhaust duct 10
The gas component is accumulated below the gas and is discharged to the outside.

【0026】又、排気ダクト10の下部に溜まった粉塵
は、図示省略したキャップを取り外すことにより、排気
ダクト10から容易に取出すことができる。尚、発酵乾
燥ドラム2のリング部22,23と蓋体4,5間には、
隙間があるが、この隙間には、完成処理物が詰まって、
シールされるので、2回目の処理からは、上記隙間から
有機性廃棄物が漏れ出たりすることはない。尚、上記実
施例の粉砕装置では、駆動軸に粉砕爪を備えたが、駆動
軸にロータリカッターを備えてもよく、或いは、駆動軸
と粉砕爪の代わりに、オーガスクリューを備えてもよ
い。
The dust collected in the lower portion of the exhaust duct 10 can be easily taken out from the exhaust duct 10 by removing a cap (not shown). In addition, between the ring portions 22 and 23 of the fermentation drying drum 2 and the lids 4 and 5,
There is a gap, but this gap is filled with finished products,
Since it is sealed, the organic waste does not leak from the above-mentioned gap from the second treatment. In addition, in the crushing device of the above embodiment, the drive shaft is provided with the crushing pawl, but the drive shaft may be provided with the rotary cutter, or, instead of the drive shaft and the crushing pawl, an auger screw may be provided.

【0027】[0027]

【発明の効果】以上説明したように、本発明によれば、
高温の熱風を発酵乾燥ドラム内に供給することにより、
土壌菌の最適活動温度域に極めて短時間で加熱できると
共に、有機性廃棄物の高温処理が行えるので、発酵乾燥
処理時間を著しく短縮することができ、しかも、1個の
発酵乾燥ドラムで発酵処理に連続して乾燥処理が行え、
構造が簡易である。特に、発酵乾燥ドラム自体を回転す
ることにより、発酵乾燥ドラム内の廃棄物を攪拌混合す
るようにしているので、発酵乾燥ドラム内に投入された
廃棄物及び土壌菌は、発酵乾燥ドラムの回転により、発
酵乾燥ドラムの内面と連れ回って、全体的に反転させら
れながら、攪拌混合されることとなると共に、発酵乾燥
ドラム2全体が高温となって、この発酵乾燥ドラム2内
面と廃棄物が連れ回るので、廃棄物の乾燥が良好に行わ
れる。
As described above, according to the present invention,
By supplying hot hot air into the fermentation and drying drum,
Since it can be heated to the optimum activity temperature range of soil bacteria in an extremely short time and high-temperature treatment of organic waste can be performed, the fermentation drying treatment time can be significantly shortened, and furthermore, the fermentation treatment can be performed with one fermentation drying drum. Can be continuously dried.
The structure is simple. In particular, since the waste in the fermentation drying drum is agitated and mixed by rotating the fermentation drying drum itself, the waste and soil bacteria put in the fermentation drying drum are not mixed by the rotation of the fermentation drying drum. While being mixed with the inner surface of the fermentation and drying drum while being totally inverted, the mixture is agitated and mixed, and the entire temperature of the fermentation and drying drum 2 becomes high, and the inner surface of the fermentation and drying drum 2 and the waste material are mixed. Since it rotates, the waste is dried well.

【0028】これを、発酵乾燥槽内に、回転駆動される
攪拌混合用スクリューが備えられている一例と比較した
場合に、上記一例では、本願発明とは異なり、攪拌混合
が部分的にとどまると共に、廃棄物が、本願発明のよう
に、高温となった発酵乾燥ドラム内面と連れ回らないの
で、廃棄物の乾燥を本願発明程には良好に行えない。
又、本発明では、横軸回りに回転駆動されて、醗酵乾燥
ドラム内の有機性廃棄物及び土壌菌の塊を粉砕して、攪
拌混合する粉砕装置が備えられているので、発酵乾燥ド
ラム内に大きな廃棄物を投入した場合でも、廃棄物を容
易に粉砕できると共に、醗酵処理時や乾燥処理時に、廃
棄物及び土壌菌の塊ができても、容易に粉砕できて、醗
酵乾燥処理を良好に行え、しかも、発酵乾燥ドラムの回
転による廃棄物及び土壌菌の攪拌混合だけではなく、粉
砕装置によっても廃棄物及び土壌菌の攪拌混合を行える
ので、廃棄物及び土壌菌の攪拌混合をより一層良好に行
える。
When this is compared with an example in which a stirring and mixing screw that is driven to rotate is provided in the fermentation drying tank, in the above example, unlike the present invention, the stirring and mixing is partially stopped and Unlike the present invention, the waste does not circulate along with the inner surface of the fermentation and drying drum that has reached a high temperature, so that the waste cannot be dried as well as the present invention.
Further, in the present invention, by being driven to rotate about the horizontal axis, the organic waste and the soil fungus in the fermentation drying drum are crushed, and a crushing device for stirring and mixing is provided. Even if a large amount of waste is added to the waste, the waste can be easily crushed, and even if waste or soil fungus clumps are formed during fermentation or drying, it can be easily crushed and the fermentation drying process is good. Moreover, since not only stirring and mixing of waste and soil fungi by rotating the fermentation drying drum, but also stirring and mixing of waste and soil fungi can be performed by a pulverizer, the stirring and mixing of waste and soil fungi can be further improved. You can do well.

【0029】更に、請求項2のように、発酵乾燥ドラム
の軸心方向両側部に給気口及び排気口が備えられると共
に、発酵乾燥ドラムの軸心方向両側部が、軸心方向外側
方に向かうテーパー状のテーパー部とされれば、発酵乾
燥ドラムのテーパー部上の廃棄物及び土壌菌は発酵乾燥
ドラムの回転に伴い、発酵乾燥ドラムの軸心方向中央部
側に送られることとなり、廃棄物及び土壌菌の攪拌混合
がより一層良好に行われると共に、廃棄物及び土壌菌が
給気口及び排気口に行きにくく、廃棄物及び土壌菌によ
り給気口及び排気口が閉塞されにくい。又、請求項3の
ように、給気口及び排気口が、醗酵乾燥ドラムの軸心よ
りも上位とされると共に、上記軸心から鉛直方向上方に
のびる鉛直面よりも回転方向前方に配置されれば、更
に、給気口及び排気口が詰まりにくいと共に、上記のよ
うに、給気口及び排気口が、醗酵乾燥ドラムの軸心より
も上位とされれば、発酵乾燥ドラム内に、廃棄物及び土
壌菌を、良好な攪拌混合が可能な軸心位置の近傍まで投
入でき、作業能率を向上できる。
Further, as described in claim 2, the fermentation and drying drum is provided with air supply ports and exhaust ports on both sides in the axial direction, and both sides in the axial direction of the fermentation and drying drum are located outward in the axial direction. If it is a tapered taper section toward the end, waste and soil fungus on the tapered section of the fermentation and drying drum will be sent to the central portion in the axial direction of the fermentation and drying drum as the fermentation and drying drum rotates. Stirring and mixing of the substance and the soil bacterium are more favorably performed, and the waste and the soil bacterium are less likely to reach the air supply port and the exhaust port, and the air supply port and the air outlet are less likely to be blocked by the waste and the soil bacterium. Further, as in claim 3, the air supply port and the exhaust port are arranged above the axis of the fermentation drying drum, and are arranged in the rotational direction forward of the vertical plane extending vertically upward from the axis. Then, further, the air supply port and the exhaust port are less likely to be clogged, and as described above, if the air supply port and the exhaust port are positioned higher than the axis of the fermentation drying drum, they are discarded in the fermentation drying drum. Material and soil fungi can be added up to the vicinity of the axial center position where good stirring and mixing can be performed, and work efficiency can be improved.

【0030】更に、請求項5のように、有機性廃棄物及
び土壌菌が醗酵乾燥ドラム内の軸心方向中央部に寄るよ
うに、粉砕爪が駆動軸に備えられれば、発酵乾燥ドラム
内の廃棄物及び土壌菌を、その軸心方向中央部に寄せる
ことができて、廃棄物及び土壌菌の攪拌混合をより一層
良好に行えると共に、発酵乾燥ドラムの軸心方向両側部
に給気口及び排気口を備えておけば、廃棄物及び土壌菌
が給気口及び排気口に行きにくく、廃棄物及び土壌菌に
より給気口及び排気口が閉塞されにくい。又、請求項6
のように、粉砕装置の軸心が、醗酵乾燥ドラムの軸心よ
りも下位とされると共に、上記軸心から鉛直方向下方に
のびる鉛直面よりも回転方向前方に配置されれば、粉砕
装置により、より一層良好に、発酵乾燥ドラム内の廃棄
物及び土壌菌の塊を粉砕できると共に、廃棄物及び土壌
菌を攪拌混合できる。
Further, when the driving shaft is provided with the crushing claw so that the organic waste and the soil fungus are near the central portion in the axial center of the fermentation drying drum as in claim 5, the inside of the fermentation drying drum is The waste and soil fungi can be brought closer to the central portion in the axial direction, and the waste and soil fungi can be mixed and mixed more satisfactorily. If the exhaust port is provided, it is difficult for waste and soil bacteria to reach the air supply port and exhaust port, and it is difficult for the waste product and soil bacteria to block the air supply port and exhaust port. Also, claim 6
As described above, the axis of the crusher is lower than the axis of the fermentation drying drum, and if it is arranged in the rotation direction forward of the vertical plane extending vertically downward from the axis, the In addition, the waste and soil fungus in the fermentation and drying drum can be pulverized, and the waste and soil fungus can be mixed with stirring.

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

【図1】本発明の一実施例を示す全体正面図である。FIG. 1 is an overall front view showing an embodiment of the present invention.

【図2】同全体側面図である。FIG. 2 is a side view of the same.

【図3】同正面断面図である。FIG. 3 is a front sectional view of the same.

【図4】図1のA−A線矢視断面図である。4 is a cross-sectional view taken along the line AA of FIG.

【図5】図3のB−B線矢視断面図である。5 is a sectional view taken along the line BB of FIG.

【図6】図4のC−C線矢視断面図である。6 is a cross-sectional view taken along the line CC of FIG.

【図7】図4のD−D線矢視図である。FIG. 7 is a view taken along the line DD of FIG.

【符号の説明】[Explanation of symbols]

1…架台、2…発酵乾燥ドラム、6…ギアモータ、7…
粉砕装置、9…バーナ(熱風供給装置)、10…排気ダ
クト、20,21…テーパー部、37…排気口、44…
駆動軸、45…粉砕爪、46…ギアモータ、48,62
…鉛直面、60…熱風吹出筒、61…給気口。
1 ... Stand, 2 ... Fermentation / drying drum, 6 ... Gear motor, 7 ...
Crushing device, 9 ... Burner (hot air supply device), 10 ... Exhaust duct, 20, 21 ... Tapered portion, 37 ... Exhaust port, 44 ...
Drive shaft, 45 ... Grinding claw, 46 ... Gear motor, 48, 62
… Vertical surface, 60… Hot air outlet, 61… Air inlet.

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】横設され、有機性廃棄物及び土壌菌が投入
されて、軸心回りに回転駆動されると共に、給気口及び
排気口を備える発酵乾燥ドラムと、 発酵乾燥ドラムの軸心と平行な軸心を有し、軸心回りに
回転駆動されて、醗酵乾燥ドラム内の有機性廃棄物及び
土壌菌の塊を粉砕して、攪拌混合する粉砕装置と、 給気口から発酵乾燥ドラム内へ熱風を供給する熱風供給
装置とを有することを特徴とする発酵乾燥装置。
1. A fermentation drying drum, which is installed horizontally, is charged with organic waste and soil fungi, and is driven to rotate about its axis, and has an air supply port and an exhaust port, and the axis of the fermentation drying drum. It has an axis parallel to the axis, and is driven to rotate around the axis to crush the organic waste and soil fungus mass in the fermentation drying drum, and a crushing device to stir and mix, and fermentation drying from the air inlet. A fermenting / drying apparatus comprising: a hot air supply device that supplies hot air into the drum.
【請求項2】発酵乾燥ドラムの軸心方向両側部に給気口
及び排気口が備えられると共に、発酵乾燥ドラムの軸心
方向両側部が、軸心方向外側方に向かうテーパー状のテ
ーパー部とされた請求項1記載の発酵乾燥装置。
2. A fermenting / drying drum is provided with an air supply port and an exhaust port on both sides in the axial direction, and both sides in the axial direction of the fermentation / drying drum are tapered parts that extend outward in the axial direction. The fermentation drying apparatus according to claim 1, wherein
【請求項3】給気口及び排気口が、醗酵乾燥ドラムの軸
心よりも上位とされると共に、上記軸心から鉛直方向上
方にのびる鉛直面よりも、発酵乾燥ドラムの回転方向前
方に配置された請求項1又は2記載の発酵乾燥装置。
3. An air supply port and an exhaust port are arranged above the shaft center of the fermentation drying drum, and are arranged forward of the vertical plane extending vertically upward from the shaft center in the rotational direction of the fermentation drying drum. The fermentation drying apparatus according to claim 1 or 2.
【請求項4】粉砕装置が、発酵乾燥ドラムに横設された
駆動軸と、駆動軸に備えられ且つ発酵乾燥ドラム内に位
置する粉砕爪を有する請求項1乃至3の何れかに記載の
発酵乾燥装置。
4. The fermentation according to claim 1, wherein the crushing device has a drive shaft laterally provided on the fermentation drying drum and a crushing claw provided on the drive shaft and located inside the fermentation drying drum. Drying device.
【請求項5】有機性廃棄物及び土壌菌が醗酵乾燥ドラム
内の軸心方向中央部に寄るように、粉砕爪が駆動軸に備
えられた請求項4記載の醗酵乾燥装置。
5. The fermentation drying apparatus according to claim 4, wherein the driving shaft is provided with a crushing claw so that the organic waste and the soil fungus are near the center of the fermentation drying drum in the axial direction.
【請求項6】粉砕装置の軸心が、醗酵乾燥ドラムの軸心
よりも下位とされると共に、発酵乾燥ドラムの軸心から
鉛直方向下方にのびる鉛直面よりも、発酵乾燥ドラムの
回転方向前方に配置された請求項1乃至5の何れかに記
載の発酵乾燥装置。
6. The axis of the crushing device is lower than the axis of the fermentation drying drum, and is forward in the rotation direction of the fermentation drying drum, rather than the vertical plane extending vertically downward from the axis of the fermentation drying drum. The fermentation and drying apparatus according to any one of claims 1 to 5, which is arranged in.
JP4143200A 1992-05-07 1992-05-07 Organic waste treatment equipment Expired - Fee Related JPH0774113B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4143200A JPH0774113B2 (en) 1992-05-07 1992-05-07 Organic waste treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4143200A JPH0774113B2 (en) 1992-05-07 1992-05-07 Organic waste treatment equipment

Publications (2)

Publication Number Publication Date
JPH05310490A true JPH05310490A (en) 1993-11-22
JPH0774113B2 JPH0774113B2 (en) 1995-08-09

Family

ID=15333206

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4143200A Expired - Fee Related JPH0774113B2 (en) 1992-05-07 1992-05-07 Organic waste treatment equipment

Country Status (1)

Country Link
JP (1) JPH0774113B2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08117582A (en) * 1994-10-18 1996-05-14 Jinichiro Negishi Mixer
JP2003038628A (en) * 2001-07-26 2003-02-12 Takahito Nakamura Foamed deodorizing material and metal mold for foamed deodorizing material and method for manufacturing foamed deodorizing material using this metal mold
KR20040016045A (en) * 2002-08-14 2004-02-21 주식회사 엔바이로피아 Aerotropic organic wastes stabilizing system for reclaiming pre-process
EP2011616A1 (en) 2007-07-06 2009-01-07 Iconorm GmbH Insulation body for a thermally insulated concrete wall and thermally insulated concrete wall and method for its manufacture
JP2016131948A (en) * 2015-01-21 2016-07-25 株式会社大平製作所 Agitator
CN114988929A (en) * 2022-06-16 2022-09-02 河南通达重工科技有限公司 Organic fertilizer production and processing system and application method

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5411391A (en) * 1977-06-24 1979-01-27 Isamu Tadokoro Card clothing for rasing fabric with fine yarn number count
JPS5438345A (en) * 1977-08-31 1979-03-22 Matsushita Electric Works Ltd Vinyl chloride resin compostion
JPS55168045U (en) * 1979-05-23 1980-12-03

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5411391A (en) * 1977-06-24 1979-01-27 Isamu Tadokoro Card clothing for rasing fabric with fine yarn number count
JPS5438345A (en) * 1977-08-31 1979-03-22 Matsushita Electric Works Ltd Vinyl chloride resin compostion
JPS55168045U (en) * 1979-05-23 1980-12-03

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08117582A (en) * 1994-10-18 1996-05-14 Jinichiro Negishi Mixer
JP2003038628A (en) * 2001-07-26 2003-02-12 Takahito Nakamura Foamed deodorizing material and metal mold for foamed deodorizing material and method for manufacturing foamed deodorizing material using this metal mold
KR20040016045A (en) * 2002-08-14 2004-02-21 주식회사 엔바이로피아 Aerotropic organic wastes stabilizing system for reclaiming pre-process
EP2011616A1 (en) 2007-07-06 2009-01-07 Iconorm GmbH Insulation body for a thermally insulated concrete wall and thermally insulated concrete wall and method for its manufacture
JP2016131948A (en) * 2015-01-21 2016-07-25 株式会社大平製作所 Agitator
CN114988929A (en) * 2022-06-16 2022-09-02 河南通达重工科技有限公司 Organic fertilizer production and processing system and application method
CN114988929B (en) * 2022-06-16 2023-11-24 河南通达重工科技有限公司 Organic fertilizer production and processing system and application method

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Publication number Publication date
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