JP3035290B1 - Organic waste water conditioning equipment - Google Patents

Organic waste water conditioning equipment

Info

Publication number
JP3035290B1
JP3035290B1 JP11077594A JP7759499A JP3035290B1 JP 3035290 B1 JP3035290 B1 JP 3035290B1 JP 11077594 A JP11077594 A JP 11077594A JP 7759499 A JP7759499 A JP 7759499A JP 3035290 B1 JP3035290 B1 JP 3035290B1
Authority
JP
Japan
Prior art keywords
drum
organic waste
adjusting
raw material
moisture
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP11077594A
Other languages
Japanese (ja)
Other versions
JP2000263100A (en
Inventor
隆久 島田
Original Assignee
株式会社第一コンサルタント
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 株式会社第一コンサルタント filed Critical 株式会社第一コンサルタント
Priority to JP11077594A priority Critical patent/JP3035290B1/en
Application granted granted Critical
Publication of JP3035290B1 publication Critical patent/JP3035290B1/en
Publication of JP2000263100A publication Critical patent/JP2000263100A/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

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

Abstract

【要約】 【課題】 比較的効率よく有機肥料を製造せしめること
ができる処理物を製造する有機廃棄物の水分調整装置を
提供することを課題としている。 【解決手段】 水分を含む有機廃棄物からなる処理物を
収容して回転させるドラム1の内部にドラム1の回転に
伴って反転落下する処理物を接衝せしめる調整部7を設
け、この調整部7を落下接衝した処理物をさらに下方に
通過させて落下させるようにすのこ状,格子状又は網状
に形成した。
An object of the present invention is to provide a device for adjusting the water content of an organic waste, which produces a treated product capable of relatively efficiently producing an organic fertilizer. SOLUTION: An adjusting unit 7 is provided inside a drum 1 for holding and rotating a processed material made of organic waste containing water, and for bringing a processed material falling down with the rotation of the drum 1 into contact with the rotating object. 7 was formed in the shape of a grid, a grid, or a net so that the treated material which had dropped and contacted it was passed further downward and dropped.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】この発明は牛糞等の畜糞や下
水汚泥等の有機廃棄物から有機肥料を製造せしめるため
の原料を製造する有機廃棄物の水分調整装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for controlling the water content of an organic waste for producing a raw material for producing an organic fertilizer from an organic waste such as cattle dung or sewage sludge.

【0002】[0002]

【従来の技術】従来中空のドラム内に畜糞や下水汚泥等
の水分を含んだ有機廃棄物からなる処理物と乾燥材とを
投入し、上記ドラムを回転させ、有機廃棄物と乾燥材と
を撹拌混合することで上記有機廃棄物と乾燥材との混合
物(材料混合物)を、該材料混合物の水分率が概ね60
〜65%となるように調整して製造する有機廃棄物の水
分調整装置が知られている。そして前記水分率が約60
〜65%の材料混合物を好気性の一次発酵させ、さらに
一次発酵せしめられた材料混合物を嫌気性の二次発酵さ
せて有機肥料が製造される。
2. Description of the Related Art Conventionally, a processed material consisting of organic waste containing moisture such as animal waste or sewage sludge and a drying material are charged into a hollow drum, and the drum is rotated to separate the organic waste and the drying material. By stirring and mixing, the mixture (material mixture) of the organic waste and the desiccant is converted to a water content of about 60%.
A device for adjusting the water content of an organic waste, which is manufactured by adjusting the water content to 65% or less, is known. And the moisture content is about 60
An organic fertilizer is produced by subjecting ~ 65% of the material mixture to aerobic primary fermentation and further anaerobic secondary fermentation of the primary fermented material mixture.

【0003】つまり上記水分調整装置は一次発酵をさせ
るための水分率が約60〜65%の材料混合物(有機肥
料の原料塊)を製造する装置であり、一次発酵を専用の
装置等で行う場合は上記原料塊を専用の一次発酵装置に
移動させ、また一次発酵を水分調整装置内で行う場合は
原料塊を水分調整装置にいれたまま一次発酵させる。
[0003] In other words, the above-mentioned water adjusting device is a device for producing a material mixture (raw material mass of organic fertilizer) having a water content of about 60 to 65% for the primary fermentation. Moves the raw material mass to a dedicated primary fermentation device, and when the primary fermentation is carried out in the moisture adjusting device, the primary fermentation is performed while the raw material mass remains in the moisture adjusting device.

【0004】そして上記水分調整装置によると、ドラム
の回転により有機廃棄物と乾燥材とが攪拌混合されて原
料塊となるが、原料塊の製造工程として回転中に材料混
合物がドラムの上方に運ばれると、前記材料混合物がド
ラムの底面(材料混合物が上方に運ばれているときに底
側になっている面)側に落下(反転落下)し、徐々に水
分率が調整され原料塊が製造される。
According to the above-mentioned water adjusting device, the organic waste and the desiccant are stirred and mixed into a raw material mass by the rotation of the drum, and the material mixture is transported above the drum during the rotation as a production process of the raw material mass. When the material mixture is dropped, the material mixture falls (reversed falls) to the bottom surface of the drum (the bottom surface when the material mixture is carried upward), and the moisture content is gradually adjusted to produce a raw material mass. Is done.

【0005】[0005]

【発明が解決しようとする課題】しかし上記水分調整装
置による原料塊の製造においては、材料混合物のドラム
底面側への反転落下時に材料混合物内に内包される空気
が逃げるため、製造される原料塊は材料の密度が比較的
高くなる。これにより一次発酵が好気性の発酵であるた
め、上記のように原料塊の材料の密度が高い(空気の含
有率が低い)場合は、一次発酵が比較的困難となり、発
酵の促進が遅く、その結果有機肥料の製造効率が低くな
るという欠点があった。
However, in the production of a raw material mass by the above-mentioned moisture adjusting device, the air contained in the material mixture escapes when the material mixture is inverted and dropped onto the bottom surface of the drum. Has a relatively high material density. Thereby, since the primary fermentation is aerobic fermentation, when the density of the raw material mass is high (the content of air is low) as described above, the primary fermentation becomes relatively difficult, and the promotion of fermentation is slow, As a result, there is a disadvantage that the production efficiency of the organic fertilizer is reduced.

【0006】[0006]

【課題を解決するための手段】上記課題を解決するため
の本発明の有機廃棄物の水分調整装置は、水分を含む有
機廃棄物からなる処理物を収容して回転させる中空のド
ラム1を回転自在に横方向に支持し、ドラム1の内部に
はドラム1の回転に伴ってドラム1内で反転落下する処
理物を接衝せしめる調整部7を設けた装置において、上
記調整部7を落下接衝した処理物をさらに下方に通過さ
せて落下させるようにすのこ状,格子状又は網状に形成
してなることを第1の特徴としている。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, an apparatus for adjusting the water content of an organic waste according to the present invention rotates a hollow drum 1 which accommodates and rotates a processed material composed of organic waste containing water. In an apparatus provided with an adjusting portion 7 which is freely supported in a lateral direction and which makes the inside of the drum 1 come into contact with a processing object which falls inside the drum 1 with the rotation of the drum 1, the adjusting portion 7 is dropped. A first feature is that the processed material is formed in a saw-like shape, a lattice shape, or a net shape so that the impacted processed material is passed downward and dropped.

【0007】第2にドラム1の周壁内には、該周壁内面
との間に所定の排水又は通気用の空間を介して設置さ
れ、通水又は通風可能な多数の小孔8aを穿設した内壁
8を設けてなることを特徴としている。
Secondly, a number of small holes 8a are provided in the peripheral wall of the drum 1 between the inner surface of the drum 1 and the inner surface of the drum 1 through a predetermined space for drainage or ventilation, through which water can flow or air can flow. It is characterized in that an inner wall 8 is provided.

【0008】第3にドラム1の一端側に排出口18を設
けてなることを特徴としている。
Third, a discharge port 18 is provided at one end of the drum 1.

【0009】第4に投入された処理物をドラム1の回転
に伴ってドラム1内において排出側に順じ移動せしめる
ようにドラム1の軸心を排出側が下降するように傾斜せ
しめてなることを特徴としている。
Fourthly, the axial center of the drum 1 is inclined such that the discharge side is lowered so that the processed material supplied is moved in the drum 1 to the discharge side as the drum 1 rotates. Features.

【0010】第5に投入された処理物をドラム1の回転
に伴ってドラム1内において排出側に順じ移動せしめる
ように調整部7をドラム1の軸心に対して傾斜させて設
けたことを特徴としている。
Fifthly, the adjusting section 7 is provided to be inclined with respect to the axis of the drum 1 so as to move the loaded workpiece in the drum 1 to the discharge side as the drum 1 rotates. It is characterized by.

【0011】第6にドラム1の排出側に、排出移送され
た処理物を受け取り、再度水分調整する補助ドラム31
を接続してなることを特徴としている。
Sixth, an auxiliary drum 31 for receiving the processed material discharged and transferred and adjusting the moisture again on the discharge side of the drum 1.
Are connected.

【0012】[0012]

【発明の実施の形態】図1,図2は本発明の有機廃棄物
の水分調整装置の正面概略図及び左側面概略図であり、
該水分調整装置は略円筒形をなすドラム1が支持部2に
支持された構造となっており、牛糞等の畜糞,下水汚
泥,生ごみ等の水分を含む有機廃棄物からなる処理物か
ら有機肥料を生成せしめる原料の塊(原料塊)を製造す
る従来公知の機能を有する装置となっている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIGS. 1 and 2 are a schematic front view and a schematic left side view, respectively, of an apparatus for adjusting the water content of an organic waste according to the present invention.
The moisture adjusting device has a structure in which a drum 1 having a substantially cylindrical shape is supported by a support portion 2, and can be used to convert organic waste containing water such as cattle dung and sewage sludge and garbage into organic waste. The apparatus has a conventionally known function for producing a lump of raw material (raw material lump) for producing fertilizer.

【0013】すなわちドラム1内に上記有機廃棄物及び
後述する乾燥材を投入し、ドラム1を回転させ、有機廃
棄物と乾燥材とを撹拌混合せしめて有機廃棄物と乾燥材
が混合された材料混合物を、該材料混合物の水分調整を
行いながら原料塊として製造する従来公知の機能を有す
る装置となっている。そして製造せしめられた原料塊は
従来公知の一次発酵装置(図示しない)に送られて好気
性の一次発酵せしめられ、その後二次発酵装置(図示し
ない)に送られ嫌気性の二次発酵せしめられて有機肥料
として生成される。
That is, the above-mentioned organic waste and a desiccant described later are put into the drum 1, the drum 1 is rotated, and the organic waste and the desiccant are stirred and mixed. The apparatus has a conventionally known function of producing a mixture as a raw material mass while adjusting the water content of the material mixture. The raw material mass thus produced is sent to a conventionally known primary fermentation device (not shown) to be subjected to aerobic primary fermentation, and then sent to a secondary fermentation device (not shown) to be subjected to anaerobic secondary fermentation. Produced as organic fertilizer.

【0014】なお一般的に上記有機廃棄物の水分率は約
90%程度、また乾燥材の水分率は30%程度となって
いるが、本実施形態においては有機廃棄物:乾燥材=
1:1(重量比)と設定されており、水分調整開始時には
不均一な水分率である材料混合物の水分率を約60〜6
5%程度に均一化する(水分率を約60〜65%程度に
なるまで水分調整する)構造となっている。つまり製造
される原料塊は水分率が60〜65%の材料混合物であ
る。
In general, the moisture content of the organic waste is about 90%, and the moisture content of the desiccant is about 30%. In the present embodiment, the organic waste: desiccant =
It is set to 1: 1 (weight ratio), and at the start of the moisture adjustment, the moisture ratio of the material mixture, which is a non-uniform moisture ratio, is about 60 to 6%.
The structure is such that the water content is made uniform to about 5% (the water content is adjusted until the water content becomes about 60 to 65%). In other words, the raw material mass to be manufactured is a material mixture having a water content of 60 to 65%.

【0015】一方前述のように上記ドラム1は略円筒形
をなし、該ドラム1の外周にはリングRが外嵌せしめら
れている。そして該リングRの周面には、1つのリング
Rに対して左右両側に支持輪2が回転自在に周接してお
り、つまりドラム1はリングRを介して支持輪2に横方
向に回転自在に支持されている。このとき上記支持輪2
における少なくとも1つにはスプロケット6が取り付け
られているとともに、該スプロケット6がモータ9によ
り駆動されており、これによりドラム1はモータ9によ
り回転駆動せしめられる。
On the other hand, as described above, the drum 1 has a substantially cylindrical shape, and a ring R is fitted around the outer periphery of the drum 1. On the peripheral surface of the ring R, the support wheel 2 is rotatably and circumferentially in contact with one ring R on both left and right sides, that is, the drum 1 is freely rotatable laterally on the support wheel 2 via the ring R. It is supported by. At this time, the support wheel 2
Is mounted with a sprocket 6 and the sprocket 6 is driven by a motor 9, whereby the drum 1 is driven to rotate by the motor 9.

【0016】なお支持輪にはフランジ2aが設けられて
おり、該フランジ2aによりドラム1の軸心方向の位置
決めが行われている。またドラム1の両端面からはドラ
ム1の中心線(軸線)と同心で中空の軸3,4が突設さ
れており、さらにドラム1の内部には軸心方向に長尺な
調整部である撹拌スクリーン7(図3参照)が、両端面
に固定されて径方向に複数(本実施形態の場合は120
度間隔で3つ)固着されている。
A flange 2a is provided on the support wheel, and the positioning of the drum 1 in the axial direction is performed by the flange 2a. Hollow shafts 3 and 4 protruding from both end surfaces of the drum 1 and concentric with the center line (axis) of the drum 1 are provided. Inside the drum 1 is an adjusting portion which is elongated in the axial direction. A plurality of agitating screens 7 (see FIG. 3) are fixed to both end faces and are radially plural (120 in the case of the present embodiment).
3) at fixed intervals.

【0017】つまり上記攪拌スクリーン7はドラム1の
回転に伴ってドラム1内で反転落下する材料混合物と接
衝するものであり、図3,図4に示されるように略長方
形形状の外形の網状をなし、所定間隔で網(格子)を形
成せしめるように複数の縦横の杆状の部材7a,7bに
よって形成せしめられている。なお上記攪拌スクリーン
7を所定ピッチの格子状又はすのこ状に形成せしめても
良い。
That is, the stirring screen 7 comes into contact with the material mixture which is turned upside down in the drum 1 with the rotation of the drum 1, and as shown in FIGS. And a plurality of vertical and horizontal rod-shaped members 7a and 7b so as to form a net (grid) at predetermined intervals. In addition, the stirring screen 7 may be formed in a grid shape or a grid shape with a predetermined pitch.

【0018】さらに上記ドラム1の周壁には、周壁内面
(内周面)に沿って内周面に対して所定間隔で通風又は
通水が可能な多数の小孔8a(図5参照)が形成せしめ
られたパンチングメタル板等の孔空き板8が内壁として
ドラム1の両端面に固定されて設けられている。
Further, a large number of small holes 8a (see FIG. 5) are formed in the peripheral wall of the drum 1 along the inner surface (inner surface) of the drum at predetermined intervals with respect to the inner surface. A perforated plate 8 such as a punched metal plate or the like is fixed to both end surfaces of the drum 1 as inner walls.

【0019】一方図3に示されるように上記ドラム1に
おける一方の端面1aにはスライド式のシャッター11
等により開閉自在に開口する投入口12が設けられてい
るが、該投入口12はホッパ13の排出部14と連結可
能な構造となっており、該ホッパ13を介してドラム1
内に有機廃棄物及び乾燥材を投入することができる構造
となっている。
On the other hand, as shown in FIG. 3, a sliding shutter 11 is provided on one end face 1a of the drum 1.
The opening 12 is provided so as to be openable and closable by, for example, the opening 12. The inlet 12 is configured to be connectable to the discharge section 14 of the hopper 13, and the drum 1 is
It has a structure in which organic waste and desiccant can be charged.

【0020】なお上記ホッパ13は有機廃棄物を投入せ
しめる投入部15と、該投入部15から投入された有機
廃棄物を搬送せしめる搬送らせん17と、該搬送らせん
17により搬送された有機廃棄物を排出せしめる前述の
排出部14とから構成された従来公知のものであり、詳
細な説明は割愛する。
The hopper 13 has a charging section 15 for charging the organic waste, a transport spiral 17 for transporting the organic waste input from the charging section 15, and an organic waste transported by the transport spiral 17. This is a conventionally known device including the above-described discharging unit 14 for discharging, and a detailed description is omitted.

【0021】またドラム1の他方の端面1bにもスライ
ド式のシャッター16等により開閉自在に開口する排出
口18が形成せしめられており、該排出口18を介して
(排出口18を開き)製造せしめられた原料塊を外部に
取り出すことができる。なお搬送用の搬送らせんを備え
た排出装置(図示せず)を排出口18に取り付け、該排
出装置を介して原料塊を排出せしめる構造としてもよ
い。このときシャッター16は端面1bの外面側に円周
方向にスライド自在に支持された構造となっている。
The other end face 1b of the drum 1 is also provided with a discharge port 18 which can be opened and closed by a slide type shutter 16 or the like, through which the discharge port 18 is opened (the discharge port 18 is opened). The crushed raw material mass can be taken out. In addition, a discharge device (not shown) provided with a transfer spiral for transfer may be attached to the discharge port 18 to discharge the raw material lump through the discharge device. At this time, the shutter 16 has a structure supported on the outer surface side of the end face 1b so as to be slidable in the circumferential direction.

【0022】さらに上記ドラム1の端面1a側には、ド
ラム1内に温風を送風する加温装置19が設けられてお
り、該加温装置19によりドラム1内の温度を、原料塊
の温度が発酵装置に送る以前に原料塊がある程度発酵を
開始し、一次発酵の助長を促す温度となるように調節す
ることができるように構成されている。
Further, a heating device 19 for blowing hot air into the drum 1 is provided on the end surface 1a side of the drum 1, and the temperature inside the drum 1 is reduced by the heating device 19 to the temperature of the raw material mass. The fermentation apparatus is configured such that the raw material mass starts fermentation to some extent before being sent to the fermentation apparatus, and can be adjusted to a temperature that promotes primary fermentation.

【0023】このとき上記加温装置19は図3に示され
るように送風ダクト21の上手側にヒータ22が、該ヒ
ータ22の上手側にファン23がそれぞれ配置された構
造となっており、ヒータ22を加温し、該ヒータ22の
上手側からファン23を駆動させると、送風ダクト21
(送風ダクト21の下手側)から温風が排風される構造
となっている。なお加温装置19は図1,図2に示され
るように接地支持されているとともに、一方の軸3内に
送風ダクト21が挿入されてドラム1内に約60℃〜7
0℃の温風を送風する構成となっている。
At this time, as shown in FIG. 3, the heating device 19 has a structure in which a heater 22 is arranged on the upper side of the air duct 21 and a fan 23 is arranged on the upper side of the heater 22. When the fan 22 is heated from the upper side of the heater 22 and the fan
(The lower side of the ventilation duct 21) has a structure in which warm air is exhausted. The heating device 19 is supported on the ground as shown in FIGS. 1 and 2, and a ventilation duct 21 is inserted into one shaft 3 so that the heating device 19 has a temperature of about 60 ° C.
It is configured to blow hot air of 0 ° C.

【0024】そして送風ダクト21の先端(下手側端
部)には分岐部材24を介して管状の配管部材26が接
続されており、前述の温風はこの配管部材26内を送ら
れるが、該配管部材26は上記分岐部材24により所定
の本数(本実施形態においては2本)に分岐せしめられ
ている。そして各配管部材26には図5に示されるよう
にエア(温風)の吹出口27が複数穿設されており、前
述の孔空き板8とドラム1の内周面との間の間隙(空
間)に、回転中心に対して対向して配管されている。
A tubular pipe member 26 is connected to the tip (lower end) of the blower duct 21 via a branch member 24, and the above-described warm air is sent through the pipe member 26. The pipe member 26 is branched into a predetermined number (two in this embodiment) by the branch member 24. As shown in FIG. 5, a plurality of air (warm air) outlets 27 are formed in each pipe member 26, and a gap between the perforated plate 8 and the inner peripheral surface of the drum 1 is formed. Space), the pipe is provided so as to face the center of rotation.

【0025】これにより加温装置19からの温風はドラ
ム1内の配管部材26内に送られ、配管部材26の吹出
口27から孔空き板8を介してドラム1内に噴射され、
ドラム1内の温度が調節される。なお他方の軸4は前述
のように中空となっているため、ドラム1内の排気が行
われ、以上の空気循環によりドラム1内の温度が設定調
節される。
As a result, the warm air from the heating device 19 is sent into the pipe member 26 in the drum 1 and is injected into the drum 1 from the outlet 27 of the pipe member 26 through the perforated plate 8.
The temperature in the drum 1 is adjusted. Since the other shaft 4 is hollow as described above, the inside of the drum 1 is evacuated, and the temperature inside the drum 1 is set and adjusted by the above air circulation.

【0026】以上に示される構造により、有機肥料の原
料塊を製造せしめるべく従来同様投入ホッパ13を介し
てドラム1内に蓄糞,下水汚泥,生ごみ等の水分率約9
0%の有機廃棄物と、既に完成している有機肥料やおが
くず,ぬか等の水分率約30%の乾燥材とを投入し、加
温装置19から温風を送風し、ドラム1内の温度を調節
しながらモータ9によりドラム1を回転させることで、
有機廃棄物と乾燥材とを攪拌混合せしめて、前述のよう
に材料混合物の水分率の調整を行いながら原料塊の製造
を行う。
With the above-described structure, in order to produce a raw material lump of organic fertilizer, the water content of feces, sewage sludge, garbage and the like is reduced to about 9 in the drum 1 through the input hopper 13 as in the conventional case.
0% of organic waste and already completed organic fertilizer, sawdust, bran and other drying materials having a moisture content of about 30% are charged, warm air is blown from the heating device 19, and the temperature in the drum 1 is increased. By rotating the drum 1 by the motor 9 while adjusting the
The organic waste and the drying material are mixed with stirring, and the raw material mass is produced while adjusting the moisture content of the material mixture as described above.

【0027】そして原料塊の完成時には、該原料塊を他
の一次発酵装置において一次発酵させる場合は、原料塊
を水分調整装置(ドラム1)から取出して一次発酵装置
に移動させ、また原料塊をドラム1内において一次発酵
させる場合は、原料塊をドラム1に入れたままでそれぞ
れ一次発酵させるが、一次発酵前あるいは後の原料塊の
ドラム1からの排出は、シャッター16を開き排出口1
8を開放せしめることで、上記排出口18を介して行う
ことができる。
When the raw material mass is completed, if the raw material mass is subjected to primary fermentation in another primary fermentation device, the raw material mass is taken out of the moisture adjusting device (drum 1), moved to the primary fermentation device, and the raw material mass is removed. When primary fermentation is performed in the drum 1, the primary fermentation is performed while the raw material lump remains in the drum 1, but the raw material lump before or after the primary fermentation is discharged from the drum 1 by opening the shutter 16 and opening the discharge port 1.
The opening 8 can be performed through the outlet 18 by opening the opening 8.

【0028】この際シャッター16がドラム1の端面1
bの外面側でスライドして排出口18を開閉せしめるた
め、シャッター16の開閉がドラム1の回転の妨げにな
ることが無く、ドラム1を回転させながらシャッター1
6をスライドさせて原料塊(一次発酵前あるいは後)を
排出せしめることができる。
At this time, the shutter 16 is connected to the end face 1 of the drum 1.
b, slides on the outer surface side to open and close the discharge port 18. Therefore, opening and closing of the shutter 16 does not hinder rotation of the drum 1, and the shutter 1 is rotated while rotating the drum 1.
6 can be slid to discharge the raw material mass (before or after the primary fermentation).

【0029】一方ドラム1内においては、ドラム1の回
転により上方に運ばれた材料混合物が下方に反転落下す
るが、ドラム1内の攪拌スクリーン7が材料混合物を一
旦接衝せしめて、さらに下方に通過させて底面(材料混
合物が上方に運ばれているときに底側になっている面)
に落下させるため、材料混合物は網状又はすのこ状又は
格子状の撹拌スクリーン7により粉砕され粒状化されな
がら、水分調整(乾燥又は水分率の均一化)せしめられ
原料塊となる。このとき水分調整中に上記のように材料
混合物が粒状化されるため、原料塊には空気が十分に含
まれる。
On the other hand, in the drum 1, the material mixture conveyed upward by the rotation of the drum 1 reversely falls downward, but the stirring screen 7 in the drum 1 once abuts the material mixture, and further moves downward. Through the bottom (the bottom side when the material mixture is being carried upwards)
The material mixture is pulverized and granulated by a mesh-like, saw-like or lattice-like stirring screen 7 while being adjusted in water content (drying or equalization of water content) to be a raw material mass. At this time, since the material mixture is granulated as described above during the moisture adjustment, the raw material mass sufficiently contains air.

【0030】そしてこの空気により上記原料塊は好気性
の発酵が容易に進む性状を有し、これにより原料塊の一
次発酵及び二次発酵が円滑に進み、比較的効率よく有機
肥料が製造される。このとき攪拌スクリーン7は攪拌混
合中に粒状化されるように材料混合物と当接すればよい
ため、本実施形態においては格子(網)状或いはすのこ
状に形成されているが、他に格子状とすのこ状の両方が
混ざったような形状等でも良く、また原料塊の空気の含
有率の格子又はすのこのピッチに対する依存は少ない。
The air has the property that the aerobic fermentation of the raw material mass proceeds easily, whereby primary fermentation and secondary fermentation of the raw material mass smoothly proceed, and an organic fertilizer is produced relatively efficiently. . At this time, the stirring screen 7 may be brought into contact with the material mixture so as to be granulated during the stirring and mixing. Therefore, in this embodiment, the stirring screen 7 is formed in a grid (net) shape or a grid shape. It may be a shape in which both of the shape of a grid are mixed, and the dependence of the air content of the raw material mass on the grid or the pitch of the glove is small.

【0031】また材料混合物から排出される水分は孔空
き板8(小孔8a)から孔空き板8とドラム1の周壁内
面(内周面)との間の空間に排出せしめられ、孔空き板
8の内部側に位置する材料混合物側に戻らないように構
成されている。つまり孔空き板8とドラム1の周壁内面
との間の空間は排水又は通気用の空間であり、ドラム1
の周壁に小孔(図示せず)を形成せしめることで、容易
に外部に排水せしめることができる。
The water discharged from the material mixture is discharged from the perforated plate 8 (small holes 8a) into the space between the perforated plate 8 and the inner surface (inner peripheral surface) of the peripheral wall of the drum 1, and the perforated plate 8 8 so as not to return to the material mixture side located inside. That is, the space between the perforated plate 8 and the inner surface of the peripheral wall of the drum 1 is a space for drainage or ventilation,
By forming a small hole (not shown) in the peripheral wall of, the water can be easily drained to the outside.

【0032】また本実施形態の場合加温装置19により
前述のようにドラム1内の温度が調節されるため、ドラ
ム内の温度が外気温等に大きく影響されること無く安定
せしめられ、季節等による外気温の変化の影響を大きく
受けること無く安定して原料塊を製造することができ
る。
In the present embodiment, since the temperature inside the drum 1 is adjusted by the heating device 19 as described above, the temperature inside the drum is stabilized without being greatly affected by the outside air temperature or the like. Thus, the raw material lump can be stably manufactured without being greatly affected by the change in the outside air temperature.

【0033】なおドラムの回転は比較的遅く、2〜3r
pm程度となっている。また有機廃棄物に生ごみを使用
する場合、攪拌スクリーン7に刃(図示せず)を設け、
該刃により有機廃棄物の切断を行いながら攪拌混合する
ように構成してもよい。またドラム1側に温度センサ等
を取り付け、ドラム1内の温度を管理し、このデータに
基づいて加温装置19をアクティブに制御してドラム1
内の温度管理をより詳細に行うように構成しても良い。
The rotation of the drum is relatively slow,
pm. In addition, when using garbage for organic waste, the stirring screen 7 is provided with a blade (not shown),
The blade may be configured to stir and mix while cutting the organic waste. Also, a temperature sensor or the like is attached to the drum 1 side to manage the temperature inside the drum 1, and based on this data, the heating device 19 is actively controlled to
It may be configured to perform the temperature management in the inside in more detail.

【0034】また前述のようにドラム1が円筒形状をな
すため装置(ドラム1)の大型化が容易であり、必要以
上に大きなスペースを取ることなく大規模に有機肥料製
造処理を行うことができるが、特に図6に示すようにド
ラム1の一端(排出側)に他のドラム(補助ドラム)3
1の一端側を接続用のリング30等を介して接続し、上
手側(有機廃棄物の投入側)のドラム1で製造された原
料塊等を順次下手側のドラム31側に移動させること
で、各ドラム1,31内で原料塊の一次発酵終了まで、
あるいは2次発酵終了までの製造過程をこなすことがで
き、大規模で、大量の材料を容易に処理することができ
る。
Since the drum 1 has a cylindrical shape as described above, the size of the apparatus (drum 1) can be easily increased, and the organic fertilizer production processing can be performed on a large scale without taking an unnecessarily large space. However, as shown in FIG. 6, another drum (auxiliary drum) 3 is attached to one end (discharge side) of the drum 1.
1 is connected via a connecting ring 30 or the like, and the raw material mass or the like manufactured by the drum 1 on the upper side (organic waste input side) is sequentially moved to the lower drum 31 side. , Until the end of the primary fermentation of the raw material mass in each drum 1, 31
Alternatively, the production process up to the completion of the secondary fermentation can be performed, and a large-scale, large-volume material can be easily processed.

【0035】すなわち上手側のドラム1の排出口を開放
(開口)し、材料混合物が所定の状態、例えば水分率の
均一化が80%程度終了した時点や、原料塊となった時
点で、次の(下手側の)補助ドラム31に自動的に移動
する等のように、材料混合物を状態に応じてドラム移動
させるように構成することで有機廃棄物の水分調整処理
等を連続して且つ大規模に行うことができる。
That is, when the discharge port of the drum 1 on the upper side is opened (opened), the material mixture is set in a predetermined state, for example, when the homogenization of the water content is completed at about 80%, or when the material mixture becomes a raw material mass, By moving the material mixture in accordance with the state of the drum, such as automatically moving to the (lower side) auxiliary drum 31, the moisture adjustment processing of organic waste can be continuously and greatly performed. Can be done on a scale.

【0036】特に図6に示されるように投入された材料
混合物がドラム1,31の回転に伴ってドラム1,31
内において排出口側に順次移動せしめるように両ドラム
1,31を、ドラム1,31の軸心の排出側が下降する
ように傾斜せしめて支持することで、ドラム1からドラ
ム31に材料混合物又は原料塊を排出装置なしに容易に
移動させることができ、ドラム31から原料塊等を容易
に取り出すことができる。
In particular, as shown in FIG.
The drums 1 and 31 are tilted and supported such that the discharge side of the axis of the drums 1 and 31 is lowered so as to be sequentially moved to the discharge port side, so that the material mixture or the raw material is transferred from the drum 1 to the drum 31. The lump can be easily moved without a discharge device, and the raw material lump and the like can be easily taken out from the drum 31.

【0037】なおドラムが1つの場合(図1〜図4の
例)においてもドラム1を、軸心の排出側が下がるよう
に傾斜せしめて支持することで、材料混合物又は原料塊
を容易に排出させることができるが、さらに攪拌スクリ
ーン7を投入された材料混合物がドラム1,31の回転
に伴ってドラム1,31内において排出口側に順次移動
せしめられるようにドラム1,31の軸心に対して傾斜
させて設けても同様の効果が得られる。
Even in the case of one drum (the example in FIGS. 1 to 4), the material mixture or the raw material mass can be easily discharged by supporting the drum 1 by inclining so that the discharge side of the shaft is lowered. However, the material mixture charged with the stirring screen 7 is further moved to the discharge port side in the drums 1 and 31 with the rotation of the drums 1 and 31 with respect to the axis of the drums 1 and 31. The same effect can be obtained even if the inclination is provided.

【0038】また上手側のドラム1の排出側の端部(端
面)と補助ドラム31の投入(入力)側の端部を共に開
放せしめることで、材料混合物の移動を容易に行うこと
ができるが、図6(b)に示すように、上手側のドラム
1の排出側と下手側のドラム31の入力側との間に前述
と同様の排出口32とシャッター33とを介設し、前述
のような材料混合物の所定状態で、シャッター33が自
動的に開き材料混合物がドラム1からドラム31に移動
するように構成しても良い。なお上記シャッターの自動
開閉はドラムが1つの場合の排出側に採用しても良い。
The material mixture can be easily moved by opening both the discharge-side end (end face) of the better drum 1 and the input (input) end of the auxiliary drum 31. As shown in FIG. 6B, a discharge port 32 and a shutter 33 similar to those described above are interposed between the discharge side of the upper drum 1 and the input side of the lower drum 31, and In such a predetermined state of the material mixture, the shutter 33 may be automatically opened to move the material mixture from the drum 1 to the drum 31. The automatic opening and closing of the shutter may be adopted on the discharge side when there is one drum.

【0039】[0039]

【発明の効果】以上のように構成される本発明の構造に
よると、ドラム内に調整部が設けられているため、処理
物を撹拌混合せしめるべくドラムを回転させると、転動
する処理物がドラムの回転により上方に運ばれ下方に反
転落下する際に、処理物は一旦調整部に接衝してから、
さらに下方に通過せしめられて底面に衝突するため、調
整部により粒状化されながら、水分調整され一塊の有機
肥料の原料(原料塊)となる。
According to the structure of the present invention constructed as described above, since the adjusting portion is provided in the drum, when the drum is rotated to stir and mix the processed material, the processed material to be rolled is reduced. When it is carried upward by the rotation of the drum and falls downward and falls, the processed material once contacts the adjustment unit,
Since it is further passed down and collides with the bottom surface, the water is adjusted while being granulated by the adjusting unit, and the raw material (raw material mass) of the organic fertilizer is obtained.

【0040】このためできあがった原料塊には空気が十
分に含まれ、この空気により上記原料塊は好気性の一次
発酵が容易に進む性状を有し、原料塊の一次発酵が円滑
に進み、比較的効率よく有機肥料が製造されるという利
点がある。特に調整部が網状又はすのこ状又は格子状で
ある場合は、粒状化が効率よく行われ、原料塊に含まれ
る空気の量が増える。
For this reason, the completed raw material mass contains air sufficiently, and the air has a property that the aerobic primary fermentation easily proceeds by this air, and the primary fermentation of the raw material mass smoothly proceeds. There is an advantage that an organic fertilizer is produced efficiently and efficiently. In particular, in the case where the adjusting section is in a net shape, in a grid shape, or in a grid shape, granulation is efficiently performed, and the amount of air contained in the raw material mass increases.

【0041】またドラムの周面内に、複数の小孔が穿設
された内壁を、上記周壁内面との間に所定の排水又は通
気用の空間を介して設置することにより、水分調整中に
発生(材料から排出される)する水分が上記空間内に溜
り、内壁内に位置する処理物に水分が戻らず、水分調整
が円滑に行われ、また空気循環も上記空間を介して円滑
に行うことができるという利点もある。
Further, an inner wall provided with a plurality of small holes is provided in the peripheral surface of the drum through a predetermined space for drainage or ventilation between the inner wall of the drum and the inner surface of the drum. Moisture generated (discharged from the material) accumulates in the space, and the water does not return to the processing object located in the inner wall, so that the moisture adjustment is smoothly performed, and the air circulation is also smoothly performed through the space. There is also the advantage that it can be done.

【0042】そしてドラムの一方の端部に、ドラム内の
処理物を排出せしめる排出口を形成せしめることで、処
理物の取出し等が容易となるが、ドラムの軸心を排出側
が下降するように傾斜せしめてドラムを支持する、ある
いは調整部を軸心に対して傾斜して支持することによ
り、排出用の装置等を設けること無く、排出口側から処
理物をに取出すことができる。
By forming a discharge port at one end of the drum for discharging the processed material in the drum, it is easy to take out the processed material. However, it is possible to lower the axis of the drum so that the discharging side is lowered. By inclining the drum and supporting the adjusting portion with respect to the axis, the processed material can be taken out from the discharge port side without providing a discharge device or the like.

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

【図1】水分調整装置の正面概略図である。FIG. 1 is a schematic front view of a moisture adjusting device.

【図2】水分調整装置の側面概略図である。FIG. 2 is a schematic side view of a moisture adjusting device.

【図3】(a),(b),(c)は水分調整装置の正面
断面図及び左右側面図である。
FIGS. 3 (a), (b) and (c) are a front sectional view and a left and right side view of a moisture adjusting device.

【図4】(a),(b)は攪拌スクリーンの正面図及び
側面図である。
FIGS. 4A and 4B are a front view and a side view of a stirring screen.

【図5】(a),(b)は配管部材部分の断面図及び側
面図である。
FIGS. 5A and 5B are a cross-sectional view and a side view of a piping member.

【図6】(a),(b)は、ドラムを連続して接続した
状態のドラムの側断面図及びシャッターを採用した場合
のドラム端面の断面図である。
FIGS. 6A and 6B are a side sectional view of the drum in a state where the drums are continuously connected and a sectional view of the drum end face when a shutter is employed.

【符号の説明】[Explanation of symbols]

1 ドラム 7 攪拌スクリーン(調整部) 8 孔空き板(内壁) 18 排出口 31 補助ドラム DESCRIPTION OF SYMBOLS 1 Drum 7 Stirring screen (adjustment part) 8 Perforated plate (inner wall) 18 Discharge port 31 Auxiliary drum

フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C02F 11/00 - 11/20 B09B 3/00 C05F 1/00 - 17/02 B01F 9/00 - 13/10 Continuation of the front page (58) Field surveyed (Int. Cl. 7 , DB name) C02F 11/00-11/20 B09B 3/00 C05F 1/00-17/02 B01F 9/00-13/10

Claims (6)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 水分を含む有機廃棄物からなる処理物を
収容して回転させる中空のドラム(1)を回転自在に横
方向に支持し、ドラム(1)の内部にはドラム(1)の
回転に伴ってドラム(1)内で反転落下する処理物を接
衝せしめる調整部(7)を設けた装置において、上記調
整部(7)を落下接衝した処理物をさらに下方に通過さ
せて落下させるようにすのこ状,格子状又は網状に形成
してなる有機廃棄物の水分調整装置。
1. A hollow drum (1) rotatably supporting a hollow drum (1) for containing and rotating a processed material composed of organic waste containing water, and a drum (1) having a hollow inside the drum (1). In an apparatus provided with an adjusting section (7) for abutting a processed object which is inverted and dropped in the drum (1) with rotation, the processed object dropped and abutted on the adjusting section (7) is passed further downward. A device for adjusting the water content of organic waste, which is formed in the shape of a grid, a grid or a net so that it can be dropped.
【請求項2】 ドラム(1)の周壁内には、該周壁内面
との間に所定の排水又は通気用の空間を介して設置さ
れ、通水又は通風可能な多数の小孔(8a)を穿設した
内壁(8)を設けてなる請求項1の有機廃棄物の水分調
整装置。
2. In the peripheral wall of the drum (1), a number of small holes (8a) are provided between the inner surface of the drum and the inner surface of the drum via a predetermined space for drainage or ventilation, and through which water can flow or ventilate. 2. The organic waste moisture control device according to claim 1, further comprising a perforated inner wall.
【請求項3】 ドラム(1)の一端側に排出口(18)
を設けてなる請求項1又は2の有機廃棄物の水分調整装
置。
3. A discharge port (18) at one end of the drum (1).
The organic waste moisture adjusting device according to claim 1 or 2, further comprising:
【請求項4】 投入された処理物をドラム(1)の回転
に伴ってドラム(1)内において排出側に順じ移動せし
めるようにドラム(1)の軸心を排出側が下降するよう
に傾斜せしめてなる請求項1又は2又は3の有機廃棄物
の水分調整装置。
4. An axis of the drum (1) is inclined such that the discharge side is lowered so that the input processed material is moved to the discharge side in the drum (1) as the drum (1) rotates. 4. The apparatus for adjusting the water content of an organic waste according to claim 1, 2 or 3 at least.
【請求項5】 投入された処理物をドラム(1)の回転
に伴ってドラム(1)内において排出側に順じ移動せし
めるように調整部(7)をドラム(1)の軸心に対して
傾斜させて設けた請求項1又は2又は3又は4の有機廃
棄物の水分調整装置。
5. An adjusting unit (7) is provided with respect to the axis of the drum (1) so that the input processed material is moved to the discharge side in the drum (1) in accordance with the rotation of the drum (1). The apparatus for adjusting the moisture content of organic waste according to claim 1, 2, 3, or 4, which is provided at an angle.
【請求項6】 ドラム(1)の排出側に、排出移送され
た処理物を受け取り、再度水分調整する補助ドラム(3
1)を接続してなる請求項3又は4又は5の有機廃棄物
の水分調整装置。
6. An auxiliary drum (3) for receiving the processed material discharged and transferred and adjusting the moisture again on the discharge side of the drum (1).
6. The organic waste moisture control apparatus according to claim 3, wherein 1) is connected.
JP11077594A 1999-03-23 1999-03-23 Organic waste water conditioning equipment Expired - Fee Related JP3035290B1 (en)

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JP2000263100A JP2000263100A (en) 2000-09-26

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