JPH07299441A - Crude refuse treating device and treatment thereof - Google Patents

Crude refuse treating device and treatment thereof

Info

Publication number
JPH07299441A
JPH07299441A JP6120815A JP12081594A JPH07299441A JP H07299441 A JPH07299441 A JP H07299441A JP 6120815 A JP6120815 A JP 6120815A JP 12081594 A JP12081594 A JP 12081594A JP H07299441 A JPH07299441 A JP H07299441A
Authority
JP
Japan
Prior art keywords
garbage
crushing
water
stirring
discharging
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.)
Pending
Application number
JP6120815A
Other languages
Japanese (ja)
Inventor
Sanai Fujita
佐内 藤田
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP6120815A priority Critical patent/JPH07299441A/en
Publication of JPH07299441A publication Critical patent/JPH07299441A/en
Pending 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)
  • Treatment Of Sludge (AREA)
  • Fertilizers (AREA)

Abstract

PURPOSE:To provide a crude refuse treating device and treating method capable of easily treating crude refuse, separating water from this crude refuse and recovering the treated matter subjected to dehydration as a fertilizer, etc. CONSTITUTION:This crude refuse treating device is provided with a crushing and agitating means 1 which crushes the crude refuse and agitates and mixes the crushed crude refuse as well as a flocculating agent, reacting agent and alkaline chlorine dioxide soln. and a treated matter discharging means 2 which discharges the treated matter subjected to the crushing, agitating and mixing treatments by this crushing and agitating means 1 by a centrifugal sepn. The device is further provided with a dehydrating means 3 which dehydrates and filters the water content from the treated matter discharged from the discharging means 2, a water content discharging means 4 which discharges the water content removed by this dehydrating means 3, a removing means 5 which removes the treated matter sticking to the dehydrating means 3 and a housing means 6 which houses the treated matter removed by the removing means 5.

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、生ゴミが主に家庭、食
堂等から排出される野菜、魚、肉等を含む各種の生ゴミ
の処理装置及び処理方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus and method for treating various kinds of raw garbage, including vegetables, fish, meat, etc., which are mainly discharged from homes, restaurants and the like.

【0002】[0002]

【従来の技術】家庭や食堂等から排出される生ゴミは、
水分を含み、腐敗、悪臭の発生等の理由により、その処
理に困っており、有効な処理手段がなく、公害問題を起
こしているのが現状である。
2. Description of the Related Art Raw garbage discharged from homes, cafeterias, etc.
Due to the fact that it contains water, it rots, develops an offensive odor, etc., it is difficult to treat it, and there is no effective treatment means, which causes pollution problems.

【0003】これらの生ゴミには水分が多く含まれ腐
敗、悪臭の発生原因となっている。そこで、これら生ゴ
ミの有効な処理装置、方法が求められている。
A large amount of water is contained in these food wastes, which causes decomposition and odor. Therefore, there is a demand for an effective processing device and method for these raw garbage.

【0004】[0004]

【発明が解決しようとする課題】本発明は上記事情に鑑
みなされたものであり、生ゴミに含まれる水分と、水分
が除去された処理物とに分離処理し、水分は放流し、処
理物は肥料、飼料等に再利用することができる生ゴミ処
理装置及び処理方法を提供することを目的とする。
SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and separates the water contained in raw garbage from the processed product from which the water has been removed, releases the water, and then the processed product. Aims to provide an apparatus and a method for treating food waste that can be reused as fertilizer, feed and the like.

【0005】[0005]

【課題を解決するための手段】本発明は上記課題を解決
したものである。すなわち本発明は、生ゴミを破砕し、
破砕した水を含む生ゴミと凝集剤、反応剤、アルカリ性
二酸化塩素溶液を攪拌混合する破砕攪拌手段1と、前記
破砕攪拌手段1により破砕攪拌混合処理した処理物を遠
心分離により排出する処理物排出手段2と、前記排出手
段2により排出された処理物から水分を脱水濾過する脱
水手段3と、前記脱水手段3により脱水した水分を排出
する水分排出手段4と、前記脱水手段3に付着する処理
物を除去する除去手段5と、前記除去手段5により除去
された処理物を収容する収容手段6とを具備することを
特徴とする。
The present invention has solved the above problems. That is, the present invention crushes raw garbage,
Crushing and stirring means 1 for stirring and mixing raw garbage containing crushed water, a flocculant, a reaction agent, and an alkaline chlorine dioxide solution, and discharging the treated material crushed and stirred and mixed by the crushing and stirring means 1 by centrifugation. Means 2, dewatering means 3 for dehydrating and filtering water from the processed material discharged by the discharging means 2, water discharging means 4 for discharging water dehydrated by the dehydrating means 3, and processing for adhering to the dehydrating means 3. It is characterized by comprising a removing means 5 for removing the substance, and an accommodating means 6 for accommodating the treated substance removed by the removing means 5.

【0006】また本発明は、生ゴミを破砕し、破砕した
水を含む生ゴミと凝集剤、反応剤、アルカリ性二酸化塩
素溶液を攪拌混合し、破砕攪拌混合処理した処理物を遠
心分離装置の孔から排出し、排出した処理物から水分を
脱水し、脱水した処理物を収容することを特徴とする生
ゴミの処理方法である。
Further, according to the present invention, raw garbage is crushed, and raw garbage containing crushed water, an aggregating agent, a reaction agent, and an alkaline chlorine dioxide solution are stirred and mixed, and the processed product subjected to the crushing stirring and mixing treatment is subjected to a hole in a centrifugal separator. The method of treating raw garbage is characterized in that the raw material is discharged from the container, the water is dehydrated from the discharged processed product, and the dehydrated processed product is stored.

【0007】前記破砕攪拌手段1は、水を含む生ゴミを
供給する供給口7、凝集剤供給口8、反応剤供給口9、
アルカリ性二酸化塩素溶液供給口10を備え、生ゴミを
破砕し、破砕した生ゴミと凝集剤、反応剤、アルカリ性
二酸化塩素溶液を攪拌混合する破砕攪拌翼11と、破砕
攪拌処理した処理物を前記処理物排出手段2へ供給する
供給口12とを有することを特徴とする。
The crushing and stirring means 1 has a supply port 7 for supplying raw garbage containing water, a coagulant supply port 8, a reactant supply port 9,
The alkaline chlorine dioxide solution supply port 10 is provided, and crushed raw garbage is crushed, and the crushed stirring blade 11 for stirring and mixing the crushed raw garbage with a flocculant, a reactant, and an alkaline chlorine dioxide solution, and the processed product subjected to the crushed stirring treatment It has the supply port 12 which supplies to the thing discharge means 2.

【0008】前記破砕攪拌翼11は、破砕攪拌槽の下部
に設けられ、円筒状の槽の中心から半径方向に周壁付近
まで達するように構成され、前記破砕攪拌翼11の回転
軸が破砕攪拌槽の下のモータと接続され、高速回転する
ことを特徴とする。
The crushing and stirring blade 11 is provided at the lower part of the crushing and stirring tank so as to reach from the center of the cylindrical tank to the vicinity of the peripheral wall in the radial direction, and the rotation axis of the crushing and stirring blade 11 is the crushing and stirring tank. It is connected to the motor below and rotates at high speed.

【0009】前記処理物排出手段2は、前記破砕攪拌手
段1の下方に配設し、円錐状で、底部周囲に該処理物を
排出する複数の孔13を形成し、モータにより回転し、
該底部周囲に形成される孔13の径が約10mm〜20
mmであり、該孔は処理物排出装置2の底部の円周方向
に約1cm〜5cm間隔に形成されてなることを特徴と
する。
The treated material discharging means 2 is arranged below the crushing and stirring means 1, has a plurality of conical holes 13 for discharging the treated material around the bottom, and is rotated by a motor.
The diameter of the hole 13 formed around the bottom is about 10 mm to 20 mm.
mm, and the holes are formed at intervals of about 1 cm to 5 cm in the circumferential direction of the bottom of the processed material discharge device 2.

【0010】前記脱水手段3は、前記処理物排出手段2
の外側に配設し、円筒状であり、多孔質の周壁14と、
該周壁14の外側に配設された濾布又は濾紙15と、該
濾布又は濾紙15の更に外側には、水分を排出する多孔
質の周壁16を備え、モータにより回転することを特徴
とする。
The dehydrating means 3 is the processed material discharging means 2
Disposed on the outer side of, and having a cylindrical and porous peripheral wall 14,
A filter cloth or filter paper 15 disposed outside the peripheral wall 14 and a porous peripheral wall 16 for discharging water are further provided outside the filter cloth or filter paper 15, and are rotated by a motor. .

【0011】前記脱水手段3の内側の多孔質の周壁14
は、内側に向け多数の突起部を形成し、該各突起部の先
端部に孔を形成し、外側の多孔質の周壁16は外側に向
け多数の突起部を形成し、該各突起部の先端部に孔を形
成することを特徴とする。
A porous peripheral wall 14 inside the dehydrating means 3
Forms a large number of protrusions toward the inside, forms a hole at the tip of each protrusion, and the porous outer peripheral wall 16 forms a large number of protrusions toward the outside. It is characterized in that a hole is formed at the tip.

【0012】前記処理物排出装置2及び前記脱水装置3
の回転軸が同一であり、モータと接続されてなり、該回
転軸が高速回転することを特徴とする。
The treated product discharging device 2 and the dehydrating device 3
The rotary shafts are the same, are connected to a motor, and the rotary shafts rotate at high speed.

【0013】前記水分排出手段4は、前記脱水装置3の
外側に配設し、開閉自在な水分排出口17を有する。ま
た該水分排出口17には水分と汚泥を分離する汚泥凝沈
装置21が連結されることを特徴とする。
The water discharging means 4 is provided outside the dehydrating device 3 and has a water discharging port 17 which can be opened and closed. A sludge settling device 21 for separating moisture and sludge is connected to the moisture outlet 17.

【0014】前記除去手段5は、一部にブラシ18を形
成し、前記脱水装置3の内側に配設され、該ブラシ18
が多孔質の周壁14と付着、離脱するように構成され、
該多孔質の周壁14に付着する固形物を除去する。
The removing means 5 has a brush 18 formed in a part thereof, and is disposed inside the dehydrating device 3, and the brush 18 is provided.
Is configured to attach to and detach from the porous peripheral wall 14,
The solid matter attached to the porous peripheral wall 14 is removed.

【0015】前記固形物を収容する収容手段6は、前記
処理物排出手段2の下方に配設し、開閉自在な固形物排
出口を有することを特徴とする。
The accommodating means 6 for accommodating the solid matter is arranged below the treated material discharge means 2 and has an openable and closable solid matter discharge port.

【0016】本発明に使用されるアルカリ性二酸化塩素
溶液は、500ppm〜1500ppmであり、凝集剤
は動物骨粉を主成分とする粉状の凝集剤であり、反応剤
は、PH10〜PH12の水酸化ナトリウムであること
を特徴とする。
The alkaline chlorine dioxide solution used in the present invention has a concentration of 500 ppm to 1500 ppm, the aggregating agent is a powdery aggregating agent containing animal bone powder as a main component, and the reaction agent is sodium hydroxide of PH10 to PH12. Is characterized in that.

【0017】本発明に使用される生ゴミと凝集剤、反応
剤、アルカリ性二酸化塩素溶液との混合比が、生ゴミ1
000kgに対して、凝集剤250cc〜450cc、
反応剤100cc〜300cc、アルカリ性二酸化塩素
溶液200cc〜400ccであり、本発明で処理され
る生ゴミが、食品生ゴミであることを特徴とする。
The mixing ratio of the raw garbage used in the present invention to the coagulant, the reaction agent and the alkaline chlorine dioxide solution is 1
With respect to 000 kg, flocculating agent 250 cc to 450 cc,
The reactants are 100 cc to 300 cc, the alkaline chlorine dioxide solution is 200 cc to 400 cc, and the garbage treated in the present invention is food garbage.

【0018】[0018]

【作用】本発明によれば、生ゴミに含まれる野菜、魚等
は破砕機1により破砕され、破砕された生ゴミは水を含
む泥状になる。泥状になった生ゴミと凝集剤、反応剤、
アルカリ性二酸化塩素溶液を攪拌混合する。
According to the present invention, vegetables, fish and the like contained in raw garbage are crushed by the crusher 1, and the crushed raw garbage becomes a mud containing water. Mud-like garbage and flocculant, reactive agent,
Stir mix the alkaline chlorine dioxide solution.

【0019】該破砕攪拌混合処理した処理物は、回転す
る処理物排出装置2に供給され、該装置に形成される複
数の孔13から、遠心分離作用により該脱水装置3に形
成される多孔質の周壁14に強い衝撃で叩き付けられ
る。
The processed product subjected to the crushing, stirring and mixing process is supplied to the rotating processed product discharging device 2 and is porous from the plurality of holes 13 formed in the device to the dehydrating device 3 by centrifugal separation. It is struck with a strong impact on the peripheral wall 14 of the.

【0020】該多孔質の周壁14に叩き付けられた処理
物に含まれる水分は、回転する脱水装置3に形成される
多数の孔と濾布又は濾紙15を通して、遠心分離作用に
より水分排出装置4へと飛ばされる。このようにして処
理物から水分が抜かれる。
Moisture contained in the treated material struck on the porous peripheral wall 14 passes through a large number of holes formed in the rotating dehydrating device 3 and the filter cloth or filter paper 15 to the moisture discharging device 4 by centrifugal action. Is skipped. In this way, water is removed from the processed material.

【0021】一方、水分を抜かれた処理物は、収容容器
6に収容されることとなるが、該多孔質の周壁14に付
着した処理物は処理物除去装置5によりかき落とされ収
容容器6に収容される。
On the other hand, the processed product from which the moisture has been removed is stored in the storage container 6, but the processed product attached to the porous peripheral wall 14 is scraped off by the processed product removing device 5 and stored in the storage container 6. Be accommodated.

【0022】また、該多孔質の周壁14に付着した処理
物を除去することにより、水分排出装置4への水分の排
出が円滑に行われることとなる。
Further, by removing the processed material adhering to the porous peripheral wall 14, the moisture can be smoothly discharged to the moisture discharging device 4.

【0023】このような構成の本発明によれば、水を含
む生ゴミを水分と脱水された処理物とを有効かつ正確に
分離処理することが可能となる。排出された水分はその
まま放流しても公害問題となることはない。
According to the present invention having such a structure, it becomes possible to effectively and accurately separate the raw garbage containing water from the water and the dehydrated treated material. The discharged water does not pose a pollution problem even if it is discharged as it is.

【0024】また、水分排出口17から排出された水分
は、混入されている凝集剤、反応剤の作用により、凝沈
槽21において水と残存する汚泥とが分離され、該凝沈
槽21の底に沈殿する汚泥は再度本発明に係る処理装置
で処理することにより、更に水分と生ゴミの分離が確実
に行われる。
The water discharged from the water discharge port 17 is separated into water and residual sludge in the coagulation tank 21 by the action of the coagulant and the reaction agent mixed therein, and the sludge in the coagulation tank 21 is separated. By again treating the sludge settling on the bottom with the treatment apparatus according to the present invention, the water and the garbage can be more reliably separated.

【0025】また、混入されるアルカリ性二酸化塩素溶
液の作用により処理された水に含まれる細菌等が殺菌、
脱臭されることとなる。
Further, bacteria and the like contained in the water treated by the action of the mixed alkaline chlorine dioxide solution are sterilized,
It will be deodorized.

【0026】脱水された処理物は、二重の遠心分離作用
により殆ど水分が抜かれており、又殺菌防臭処理もなさ
れているので、そのまま廃棄してもよいが、肥料等とし
て利用することができる。
The dehydrated treated product has almost no water content due to the double centrifugal separation action and has been subjected to sterilization and deodorization treatment, so that it can be discarded as it is, but it can be used as a fertilizer or the like. .

【0027】[0027]

【実施例】本発明に係る生ゴミの処理装置を添付図を参
照しつつ詳細に説明する。図1は本発明に係る生ゴミの
処理装置の概略構成を示す断面図であり、図2は図1の
A−A線概略断面図である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A garbage disposal device according to the present invention will be described in detail with reference to the accompanying drawings. FIG. 1 is a cross-sectional view showing a schematic configuration of an apparatus for treating garbage according to the present invention, and FIG. 2 is a schematic cross-sectional view taken along the line AA of FIG.

【0028】図において、1は破砕攪拌装置であり、7
は生ゴミ供給用の供給口、8は凝集剤供給用の供給口、
9は反応剤供給用の供給口、10はアルカリ性二酸化塩
素溶液供給用の供給口である。
In the figure, 1 is a crushing stirring device, and 7
Is a supply port for supplying garbage, 8 is a supply port for supplying coagulant,
Reference numeral 9 is a supply port for supplying a reactant, and 10 is a supply port for supplying an alkaline chlorine dioxide solution.

【0029】11は生ゴミを破砕かつ攪拌、混合する破
砕攪拌翼であり、12は破砕、攪拌混合処理した処理物
を処理物排出装置2へ供給する供給口である。
Reference numeral 11 is a crushing and stirring blade for crushing, stirring and mixing raw garbage, and 12 is a supply port for supplying the processed material that has been crushed, stirred and mixed to the processed material discharging device 2.

【0030】前記破砕攪拌翼11は、破砕攪拌槽の下部
に設けられ、円筒状の槽の中心から半径方向に周壁付近
まで達するように形成され、前記破砕攪拌翼11の回転
軸は破砕攪拌槽の下方に配設されるモータと接続されて
いる。
The crushing and stirring blade 11 is provided in the lower part of the crushing and stirring tank, and is formed so as to reach from the center of the cylindrical tank to the vicinity of the peripheral wall in the radial direction. The rotating shaft of the crushing and stirring blade 11 is the crushing and stirring tank. Is connected to a motor arranged below.

【0031】なお、本実施例では、モータを破砕攪拌槽
の下方に配設したが、モータの設置箇所は本装置の外側
であってもよい。
In this embodiment, the motor is arranged below the crushing and stirring tank, but the motor may be installed outside the device.

【0032】水、野菜等を含む生ゴミは供給口7から供
給され、破砕攪拌翼11により野菜等の固形物は破砕さ
れ、破砕された生ゴミは泥状となる。
Raw garbage containing water, vegetables and the like is supplied from the supply port 7, solid matters such as vegetables are crushed by the crushing and stirring blade 11, and the crushed raw garbage becomes muddy.

【0033】該泥状物と、供給口8からの凝集剤、供給
口9からの反応剤、供給口10からのアルカリ性二酸化
塩素溶液とが破砕攪拌翼11により攪拌混合処理され、
攪拌混合処理された処理物は、供給口12から処理物排
出装置2へ供給される。
The mud, the coagulant from the supply port 8, the reactant from the supply port 9, and the alkaline chlorine dioxide solution from the supply port 10 are agitated and mixed by a crushing and stirring blade 11.
The processed product subjected to the stirring and mixing process is supplied from the supply port 12 to the processed product discharge device 2.

【0034】凝集剤を混入するのは、水と汚泥とを分離
させるためであり、反応剤は該凝集剤の凝集、分離作用
を増強するためである。アルカリ性二酸化塩素溶液を混
入するのは、生ゴミに含まれる肉、魚等の腐敗により発
生する細菌や悪臭を殺菌・脱臭するためである。
The coagulant is mixed in to separate water and sludge, and the reaction agent enhances the coagulating and separating action of the coagulant. The reason why the alkaline chlorine dioxide solution is mixed is to sterilize and deodorize bacteria and bad odors generated by the decay of meat, fish and the like contained in raw garbage.

【0035】従って、本装置により排出される水や脱水
された処理物に含まれる細菌や悪臭は除去され、公害問
題を引き起こすことはなく、また排出される水に残存す
る汚泥は凝沈槽21で更に水と分離されるので、再度本
装置で処理することができる。
Therefore, the bacteria and malodor contained in the water discharged by this apparatus and the dehydrated treated material are removed, and no pollution problem is caused, and the sludge remaining in the discharged water is the coagulation tank 21. Since it is further separated from water in the above step, it can be treated again by this apparatus.

【0036】前記分離、凝集、殺菌等の反応は、混合物
の濃度をPH6.5〜8.5にするのが好適であり、濃
度が高い場合には水で希釈することが必要である。また
破砕攪拌混合処理時間は、処理する生ゴミの種類、量に
対応して調整弁により調整される。
In the reactions such as separation, coagulation and sterilization, it is preferable to adjust the concentration of the mixture to PH 6.5 to 8.5, and when the concentration is high, it is necessary to dilute with water. Further, the crushing stirring and mixing treatment time is adjusted by the adjusting valve in accordance with the type and amount of raw garbage to be treated.

【0037】二酸化塩素は、通常、塩素酸ナトリウム又
は塩素酸カルシウムに酸を作用させることによって製造
されるが、このようにして得られた二酸化塩素は、はげ
しい爆発性を有し極めて危険性の高いので、その取り扱
いには十分注意をしなければならない。
Chlorine dioxide is usually produced by reacting sodium chlorate or calcium chlorate with an acid. The chlorine dioxide thus obtained has a very explosive property and is extremely dangerous. Therefore, be careful when handling it.

【0038】そこで、このような二酸化塩素をアルカリ
性の水溶液中で安定化し、安定化された状態の二酸化塩
素(以下、安定化二酸化塩素という)としたものが開発
されている。本発明に係る生ゴミ処理装置ではこの安定
化二酸化塩素溶液が使用される。
Therefore, such chlorine dioxide is stabilized in an alkaline aqueous solution, and chlorine dioxide in a stabilized state (hereinafter referred to as stabilized chlorine dioxide) has been developed. This stabilized chlorine dioxide solution is used in the garbage disposal according to the present invention.

【0039】アルカリ性の二酸化塩素溶液のPHは8〜
10が好ましく、アルカリ性の二酸化塩素溶液の温度は
通常50〜90°C、好ましく60〜80°Cである。
温度が90°Cを越えると二酸化塩素が不安定になる。
The pH of the alkaline chlorine dioxide solution is 8 to
10 is preferable, and the temperature of the alkaline chlorine dioxide solution is usually 50 to 90 ° C, preferably 60 to 80 ° C.
When the temperature exceeds 90 ° C, chlorine dioxide becomes unstable.

【0040】このようなアルカリ性二酸化塩素溶液が殺
菌、脱臭効果を有することは既に周知である。(特開昭
60−66752号等)
It is already well known that such an alkaline chlorine dioxide solution has a sterilizing and deodorizing effect. (JP-A-60-66752, etc.)

【0041】また、本発明に係る生ゴミ処理装置で使用
される凝集剤は、動物骨粉を主成分とするものであり、
凝集機能、さらに凝集速度を考慮すれば動物骨粉の割合
の多いものが好ましく、例えば、動物骨粉が50〜80
重量%のものがあげられる。この動物骨粉はアルカリ性
溶液の吸収能の高い他のアルカリ性の吸着材で代替する
こともできる。
The coagulant used in the garbage disposal according to the present invention is mainly composed of animal bone powder,
Considering the aggregating function and the aggregating rate, it is preferable that the proportion of animal bone meal is large, for example, animal bone meal is 50-80.
Weight% can be mentioned. This animal bone meal can be replaced with another alkaline adsorbent having a high absorption capacity for alkaline solutions.

【0042】前記の動物骨粉は、従来畜産場等でほとん
ど廃棄されていた骨、特に牛、馬、羊等の硬骨が主体の
動物の骨であり、生骨を例えば次のように処理して得ら
れる。
The above-mentioned animal bone powder is bone that has been mostly discarded in conventional livestock farms, especially animal bones mainly composed of hard bones such as cows, horses and sheep. Raw bones are treated as follows, for example. can get.

【0043】生骨を焼成しやすい大きさに切断し、煮
沸、900〜1100°℃前後で焼成して得られるもの
である。骨に骨成分以外のゼラチン、脂肪、淡白質、に
かわ等の有機物が残存すると酸化腐敗の原因となるの
で、これを確実に除去しておくことが必要である。
It is obtained by cutting raw bone into a size that can be easily baked, boiling it, and baking it at about 900 to 1100 ° C. It is necessary to remove the gelatin, fat, white matter, glue, and other organic substances other than bone components that remain in the bone, because they cause oxidative rot.

【0044】上記煮沸工程によって、外側のみならず気
孔内に付着している有機物を骨から大方分離除去するこ
とができる。その上で上記焼成工程を通すことによっ
て、残存する有機物を完全に除去することができ、同時
に骨中の湿度 (水分) を数%以下、好ましくはほぼ0%
にまで低下させることができる。
By the above-mentioned boiling step, most of the organic substances attached not only to the outside but also to the inside of the pores can be separated and removed from the bone. The remaining organic substances can be completely removed by passing through the above-mentioned baking step, and at the same time, the humidity (moisture) in the bone is less than a few percent, preferably about 0%.
Can be reduced to

【0045】上記焼成条件によれば、骨は白骨化して無
数の気孔を有した原形組織状態を維持する。上記焼成冷
却後、この骨を破砕しパウダー機にかけて150〜25
0メッシュ前後、特に好ましくは180〜220メッシ
ュの粉状の骨粉とする。
According to the above-mentioned firing conditions, the bone becomes white and maintains the original tissue state having numerous pores. After baking and cooling, the bone is crushed and powdered for 150 to 25
Bone powder in the form of powder of about 0 mesh, particularly preferably 180 to 220 mesh is used.

【0046】上記骨粉は、生骨の場合、原料の生骨に比
して重量比約40%の収量が得られる。粒子は、カルシウ
ム(約33重量%)を主成分とし、リン(約16.7重量%)
、バリウム (約1.03重量%) 、ナトリウム (約0.76重
量%) 、イオウ (約0.64重量%) 、他にマグネシウム、
カリウム、塩素、アミン、鉄等からなっており、粒子の
内外にわたって無数微小気孔が連通存在しており、アル
カリ性である。
In the case of raw bone, the above-mentioned bone meal gives a yield of about 40% by weight compared to the raw bone. The particles are mainly composed of calcium (about 33% by weight) and phosphorus (about 16.7% by weight).
Barium (about 1.03% by weight), sodium (about 0.76% by weight), sulfur (about 0.64% by weight), other magnesium,
It is composed of potassium, chlorine, amine, iron, etc., and has numerous micropores that communicate with the inside and outside of the particles, and is alkaline.

【0047】バインダーとしては、例えばベントナイ
ト、酸性白土、活性白土、カオリン粘土、セリサイト、
パイオフィライト、耐火粘土、モンモリロナイト、等が
あげられる。
Examples of the binder include bentonite, acid clay, activated clay, kaolin clay, sericite,
Examples include piophyllite, refractory clay, montmorillonite, and the like.

【0048】本発明に使用される反応剤は、水酸化ナト
リウムであり、濃度がPH9〜12、更に好ましくはP
H10〜11である。
The reaction agent used in the present invention is sodium hydroxide, and the concentration thereof is PH 9 to 12, more preferably P.
H10-11.

【0049】2は処理物排出装置であり、13は処理物
を排出する複数の孔である。該処理物排出装置2は、前
記破砕攪拌装置1の下方に配設され、底面に向け広がる
円錐状の筒体であり、底部付近周囲には複数の孔13を
形成し、モータにより回転するようになっている。
Reference numeral 2 is a treated material discharging device, and 13 is a plurality of holes for discharging the treated material. The treated material discharging device 2 is a conical cylindrical body which is disposed below the crushing and stirring device 1 and spreads toward the bottom surface. It has become.

【0050】該底部周囲に形成される孔13の径及び孔
の間隔は、本発明に係る装置で処理する生ゴミの種類に
より異なるが、通常は孔の径が約10mm〜20mmが
好ましく、円周方向に約1cm〜5cm間隔に形成する
のが好ましい。
The diameter of the holes 13 formed around the bottom and the distance between the holes vary depending on the type of raw garbage treated by the apparatus according to the present invention, but normally the diameter of the holes is preferably about 10 mm to 20 mm, It is preferable to form them at intervals of about 1 cm to 5 cm in the circumferential direction.

【0051】該処理物排出装置2は、前記破砕攪拌装置
1により破砕攪拌混合処理された処理物を複数の孔13
から、遠心分離作用により強い勢いで脱水装置3に配設
される多孔質の周壁14に叩き付ける。
The processed product discharge device 2 has a plurality of holes 13 for processing the processed product which is crushed and stirred and mixed by the crushing and stirring device 1.
Then, it is slammed against the porous peripheral wall 14 arranged in the dehydrator 3 with a strong force by the centrifugal separation action.

【0052】3は脱水装置であり、14は内側の多孔質
の周壁、15は濾布又は濾紙、16は外側の多孔質の周
壁である。
3 is a dehydrator, 14 is an inner porous peripheral wall, 15 is a filter cloth or filter paper, and 16 is an outer porous peripheral wall.

【0053】該脱水装置3は、前記処理物排出装置2の
外側に配設され、前記処理物排出装置2のモータ回転軸
と同一回転軸により回転する。脱水装置3は円筒状であ
り、上部が開放され、底部は図2に示すように該モータ
回転軸と連動する4本の軸棒20が形成される。
The dehydrating device 3 is arranged outside the processed product discharging device 2 and rotates by the same rotary shaft as the motor rotating shaft of the processed product discharging device 2. The dehydrating device 3 has a cylindrical shape, the upper part of which is open, and the bottom part of which is formed with four shaft rods 20 interlocking with the motor rotating shaft, as shown in FIG.

【0054】該底部に形成される軸棒20の断面は、上
方細りの略台形状である。該脱水された処理物が収容容
器に落ち易いからである。
The cross section of the shaft rod 20 formed at the bottom is a substantially trapezoidal shape that is tapered upward. This is because the dehydrated processed product easily falls into the storage container.

【0055】本実施例では、モータ回転軸と連動する軸
棒20を4本形成する場合を説明したが、軸棒の数はこ
れに限られるものではなく、生ゴミの種類、量等により
軸棒の数は何本にしてもよい。
In the present embodiment, the case where four shaft rods 20 interlocking with the motor rotating shaft are formed has been described, but the number of shaft rods is not limited to this, and the shaft may be changed depending on the type and amount of raw dust. Any number of bars can be used.

【0056】また、前記処理物排出装置2と脱水装置3
の回転駆動源であるモータは、本実施例では、前記処理
物排出装置2の下方に設置したが、モータの設置箇所は
本装置の外側であってもよいことは勿論である。
Further, the treated product discharging device 2 and the dehydrating device 3
In the present embodiment, the motor that is the rotational drive source is installed below the treated material discharge device 2. However, it goes without saying that the motor may be installed outside the device.

【0057】脱水装置3には濾布又は濾紙15を挟ん
で、内側と外側には多孔質の周壁14、16が形成され
る。濾布又は濾紙15は前記処理物から水分のみを排出
するものであり、不織布が好適である。
A filter cloth or filter paper 15 is sandwiched in the dehydrator 3 and porous peripheral walls 14 and 16 are formed on the inside and outside. The filter cloth or filter paper 15 discharges only water from the treated material, and a non-woven fabric is preferable.

【0058】図3は脱水装置3を説明するための拡大図
である。図に示すように、濾布又は濾紙15の両側に多
孔質の周壁14、16が配設されており、内側の多孔質
の周壁14は、内側に向け多数の突起部を形成し、該各
突起部の先端部に孔を形成する。一方外側の多孔質の周
壁16は外側に向け多数の突起部を形成し、該各突起部
の先端部に孔を形成する。
FIG. 3 is an enlarged view for explaining the dehydrator 3. As shown in the figure, porous peripheral walls 14 and 16 are arranged on both sides of a filter cloth or filter paper 15, and the inner porous peripheral wall 14 forms a large number of protrusions toward the inside. A hole is formed at the tip of the protrusion. On the other hand, the outer peripheral wall 16 is formed with a number of protrusions toward the outside, and holes are formed at the tips of the protrusions.

【0059】このような構成によれば、内側の多孔質の
周壁14の周辺に付着する前記脱水された処理物を容易
に除去でき、外側の多孔質の周壁16は水分を円滑に吐
き出すことができる。
According to this structure, the dehydrated processed material adhering to the periphery of the inner porous peripheral wall 14 can be easily removed, and the outer porous peripheral wall 16 can smoothly expel water. it can.

【0060】前記処理物排出装置2の複数の孔13から
排出される処理物は、内側の多孔質の周壁14に強く叩
き付けられ、遠心分離作用により水分は該多数の孔、濾
布又は濾紙15、外側の周壁16に形成される多数の孔
を経て、水分排出装置4に導かれる。
The processed product discharged from the plurality of holes 13 of the processed product discharging device 2 is strongly struck against the inner peripheral wall 14 of the porous body, and the water content is removed by the centrifugal action, and the plurality of holes, filter cloth or filter paper 15 are removed. , Is guided to the water discharge device 4 through a large number of holes formed in the outer peripheral wall 16.

【0061】4は水分排出装置であり、前記脱水装置3
と外枠部材19の間に配設され、円筒状であり、開閉自
在な水分排出口17を有する。該水分排出口17から排
出される水は、泥状物は含まれず殺菌、脱臭されている
のでそのまま放流してもよいが、微粒子の汚泥が含まれ
ているので、これらを取り除くのが好ましい。
Reference numeral 4 denotes a water discharging device, which is the dehydrating device 3
It is arranged between the outer frame member 19 and the outer frame member 19, has a cylindrical shape, and has a water discharge port 17 that can be opened and closed. The water discharged from the water discharge port 17 does not contain mud and is sterilized and deodorized and may be discharged as it is, but since it contains fine particle sludge, it is preferable to remove it.

【0062】図4は水分排出口17に連結される凝沈装
置21の概略構成を示す断面図である。図において、2
2は水分排出口17と連通する水管、23は水排出口、
24は汚泥排出口である。
FIG. 4 is a sectional view showing a schematic structure of the coagulation / sedimentation device 21 connected to the water outlet 17. In the figure, 2
2 is a water pipe communicating with the water outlet 17, 23 is a water outlet,
24 is a sludge discharge port.

【0063】図に示すように、水分排出口17から排出
される水は、これと連通する水管22を通り、水管22
の先端から溢れ出る。溢れ出た水は凝沈槽21を下降
し、この際に混入されている凝集剤の作用により水に含
まれる汚泥は水と分離し、凝沈槽21の底部に沈殿す
る。
As shown in the figure, the water discharged from the water outlet 17 passes through the water pipe 22 communicating with the water outlet 22.
Overflows from the tip of. The overflowed water descends in the coagulation tank 21, and the sludge contained in the water is separated from the water by the action of the coagulant mixed in the coagulation tank 21, and settles on the bottom of the coagulation tank 21.

【0064】汚泥が除去された水は水排出口23から排
出され、凝沈槽21の底部に沈殿した汚泥は汚泥排出口
24から排出される。汚泥排出口24から排出される汚
泥は汚泥排出口24に設置されるタイマ、電磁弁により
自動的に生ゴミ供給口7に供給することができる。
The water from which the sludge has been removed is discharged from the water discharge port 23, and the sludge settled on the bottom of the coagulation tank 21 is discharged from the sludge discharge port 24. The sludge discharged from the sludge discharge port 24 can be automatically supplied to the raw garbage supply port 7 by a timer or a solenoid valve installed in the sludge discharge port 24.

【0065】上記凝沈装置21により処理された水はそ
のまま放流してもよいが、更に例えば、この水を汚水槽
で曝気処理し、反応槽へ送り凝集剤を添加し、攪拌して
汚泥を凝集沈殿させ、汚泥と水を分離することもでき
る。
The water treated by the coagulating / precipitating device 21 may be discharged as it is. Further, for example, this water is subjected to aeration treatment in a waste water tank, fed to a reaction tank, a coagulant is added, and stirred to remove sludge. It is also possible to coagulate and settle and separate sludge and water.

【0066】5は処理物除去装置であり、18はブラシ
である。該除去装置5は前記脱水装置3の内側に配設さ
れ、該ブラシ18が該多孔質の周壁14と付着、離脱す
るように配設され、脱水装置3の回転に連動して回転す
るようになっている。
Reference numeral 5 is a treated material removing device, and 18 is a brush. The removing device 5 is disposed inside the dehydrating device 3, the brush 18 is disposed so as to be attached to and detached from the porous peripheral wall 14, and is rotated in association with the rotation of the dehydrating device 3. Has become.

【0067】処理物除去装置5に形成されるブラシ18
により、内側の多孔質の周壁14の周辺に付着する脱水
された処理物は除去され、収容容器6に落とされると共
に、水を排出する内側の周壁14に形成される多数の孔
が塞がれるのを防止する。
The brush 18 formed on the treated material removing device 5
As a result, the dehydrated processed material adhering to the periphery of the inner porous peripheral wall 14 is removed and dropped into the storage container 6, and a large number of holes formed in the inner peripheral wall 14 for discharging water are closed. Prevent.

【0068】6は前記脱水された処理物を収容する収容
容器であり、前記処理物排出装置2の下方に配設され、
開閉自在な処理物排出口を有する。
Reference numeral 6 denotes a container for containing the dehydrated processed product, which is arranged below the processed product discharging device 2.
It has a processed product outlet that can be opened and closed.

【0069】収容容器6は前記脱水装置3により脱水さ
れ自動的に落ちてくる処理物や、内側の多孔質の周壁1
4の周辺に付着し前記除去装置5により除去され落ちて
くる処理物を収容するものである。
The storage container 6 is a processed product which is dehydrated by the dehydrating device 3 and automatically falls, and a porous peripheral wall 1 inside.
The object to be processed is attached to the periphery of 4 and is removed by the removing device 5 and falls.

【0070】収容された処理物は、前記したように二重
の遠心分離作用により殆ど水分が含まれず、又殺菌防臭
処理もなされているので、そのまま廃棄してもよいが、
肥料等として利用することもできる。
The treated product contained therein contains almost no water due to the double centrifugal separation action as described above and is sterilized and deodorized. Therefore, it may be discarded as it is.
It can also be used as fertilizer.

【0071】[0071]

【発明の効果】本発明によれば、生ゴミを好適に簡便に
処理して、生ゴミから水分を簡易かつ確実に分離でき、
脱水された処理物は回収して肥料等として利用可能であ
る。
EFFECTS OF THE INVENTION According to the present invention, it is possible to appropriately and easily treat raw garbage, and to easily and surely separate water from raw garbage.
The dehydrated processed product can be recovered and used as fertilizer or the like.

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

【図1】本発明に係る生ゴミの処理装置の概略構成を示
す断面図である。
FIG. 1 is a cross-sectional view showing a schematic configuration of an apparatus for treating garbage according to the present invention.

【図2】図1のA−A線概略断面図である。FIG. 2 is a schematic cross-sectional view taken along the line AA of FIG.

【図3】脱水装置を説明するための拡大図である。FIG. 3 is an enlarged view for explaining a dehydrator.

【図4】汚泥凝沈装置の概略構成を示す断面図である。FIG. 4 is a sectional view showing a schematic configuration of a sludge coagulation device.

【符号の説明】[Explanation of symbols]

1 破砕攪拌手段(破砕攪拌装置) 2 処理物排出手段(処理物排出装置) 3 脱水手段(脱水装置) 4 水分排出手段(水分排出装置) 5 除去手段(除去装置) 6 収容手段(収容容器) 7 生ゴミ供給口 8 凝集剤供給口 9 反応剤供給口 10 アルカリ性二酸化塩素溶液供給口 11 破砕攪拌翼 12 混合物供給口 13 孔 14 内側の多孔質の周壁 15 濾布又は濾紙 16 外側の多孔質の周壁 17 水分排出口 18 ブラシ 19 外枠部材 20 軸棒 21 汚泥凝沈装置(汚泥凝沈槽) 22 水管 23 水排出口 24 汚泥排出口 DESCRIPTION OF SYMBOLS 1 Crushing stirring means (crushing stirring apparatus) 2 Processed substance discharge means (processed substance discharge device) 3 Dehydration means (dehydration device) 4 Moisture discharge means (moisture discharge device) 5 Removal means (removal device) 6 Storage means (storage container) 7 Raw Dust Supply Port 8 Flocculant Supply Port 9 Reactant Supply Port 10 Alkaline Chlorine Dioxide Solution Supply Port 11 Crushing and Stirring Blade 12 Mixture Supply Port 13 Pore 14 Inner Porous Perimeter Wall 15 Filter Cloth or Filter Paper 16 Outside Porous Peripheral wall 17 Moisture outlet 18 Brush 19 Outer frame member 20 Shaft 21 Sludge settling device (sludge settling tank) 22 Water pipe 23 Water outlet 24 Sludge outlet

Claims (20)

【特許請求の範囲】[Claims] 【請求項1】 生ゴミを破砕し、破砕した水を含む生ゴ
ミと凝集剤、反応剤、アルカリ性二酸化塩素溶液を攪拌
混合する破砕攪拌手段(1)と、 前記破砕攪拌手段(1)により破砕攪拌混合処理した処
理物を遠心分離により排出する処理物排出手段(2)
と、 前記処理物排出手段(2)により排出された処理物から
水分を脱水濾過する脱水手段(3)と、 前記脱水手段(3)により脱水した水分を排出する水分
排出手段(4)と、 前記脱水手段(3)に付着する脱水した処理物を除去す
る除去手段(5)と、 前記除去手段(5)により除去された処理物を収容する
収容手段(6)と、を具備することを特徴とする生ゴミ
の処理装置。
1. A crushing stirring means (1) for crushing raw garbage and stirring and mixing raw garbage containing crushed water, a flocculant, a reactant and an alkaline chlorine dioxide solution, and crushing by said crushing stirring means (1). Processed product discharge means (2) for discharging the processed product that has been subjected to stirring and mixing by centrifugation.
A dehydrating means (3) for dehydrating and filtering water from the treated material discharged by the treated material discharging means (2); and a moisture discharging means (4) for discharging moisture dehydrated by the dehydrating means (3), A removing means (5) for removing the dehydrated processed material adhering to the dehydrating means (3); and an accommodating means (6) for accommodating the processed material removed by the removing means (5). Characteristic raw garbage processing equipment.
【請求項2】 生ゴミを破砕し、破砕した水を含む生ゴ
ミと凝集剤、反応剤、アルカリ性二酸化塩素溶液を攪拌
混合し、破砕攪拌混合処理した処理物を遠心分離装置の
孔から排出し、排出した処理物から遠心分離装置により
水分を脱水し、脱水した処理物を収容することを特徴と
する生ゴミの処理方法。
2. Crushing raw garbage, stirring and mixing raw garbage containing crushed water, a flocculant, a reactant, and an alkaline chlorine dioxide solution, and crushing and stirring and mixing the treated product is discharged from the hole of the centrifugal separator. A method of treating raw garbage, which comprises dehydrating water from a discharged treated product by a centrifugal separator and storing the dehydrated treated product.
【請求項3】 前記破砕攪拌手段(1)は、水を含む生
ゴミを供給する生ゴミ供給口(7)、凝集剤供給口
(8)、反応剤供給口(9)、アルカリ性二酸化塩素溶
液供給口(10)を備え、生ゴミを破砕し、破砕した生
ゴミと凝集剤、反応剤、アルカリ性二酸化塩素溶液を攪
拌混合する破砕攪拌翼(11)と、破砕攪拌処理した処
理物を前記処理物排出手段(2)へ供給する供給口(1
2)とを有することを特徴とする請求項1に記載の生ゴ
ミの処理装置。
3. The crushing and stirring means (1) is provided with a garbage feed port (7) for feeding garbage containing water, a coagulant feed port (8), a reactant feed port (9), and an alkaline chlorine dioxide solution. A crushing stirring blade (11) equipped with a supply port (10) for crushing raw garbage and stirring and mixing the crushed raw garbage with a coagulant, a reaction agent and an alkaline chlorine dioxide solution, and the processed product subjected to the crushing stirring treatment Supply port (1) for supplying to the material discharge means (2)
2) The garbage treatment device according to claim 1, further comprising:
【請求項4】 前記破砕攪拌翼(11)が、破砕攪拌槽
の下部に設けられ、円筒状の槽の中心から半径方向に周
壁付近まで達することを特徴とする請求項1又は3に記
載の生ゴミの処理装置。
4. The crushing stirring blade (11) is provided in the lower part of the crushing stirring tank, and extends from the center of the cylindrical tank to the vicinity of the peripheral wall in the radial direction. Raw garbage processing equipment.
【請求項5】 前記破砕攪拌翼(11)の回転軸が破砕
攪拌槽の下のモータと接続されてなることを特徴とする
請求項1、3又は4に記載の生ゴミの処理装置。
5. The apparatus for treating raw garbage according to claim 1, 3 or 4, wherein a rotating shaft of the crushing stirring blade (11) is connected to a motor below the crushing stirring tank.
【請求項6】 前記処理物排出手段(2)は、前記破砕
攪拌手段(1)の下方に配設し、円錐状で、底部周囲に
該処理物を排出する複数の孔(13)を形成し、モータ
により回転することを特徴とする請求項1に記載の生ゴ
ミの処理装置。
6. The processed material discharging means (2) is arranged below the crushing and stirring means (1) and has a plurality of conical holes (13) around the bottom for discharging the processed material. The garbage processing apparatus according to claim 1, wherein the garbage disposal is rotated by a motor.
【請求項7】 前記処理物排出装置(2)の底部周囲に
形成される孔(13)の径が約10mm〜20mmであ
り、該孔は処理物排出装置(2)の底部の円周方向に約
1cm〜5cm間隔に形成されてなることを特徴とする
請求項1又は6に記載の生ゴミの処理装置。
7. The diameter of the hole (13) formed around the bottom of the treated material discharging device (2) is about 10 mm to 20 mm, and the hole is in the circumferential direction of the bottom of the treated material discharging device (2). The raw garbage processing apparatus according to claim 1 or 6, wherein the apparatus is formed at intervals of about 1 cm to 5 cm.
【請求項8】 前記脱水手段(3)は、前記処理物排出
手段(2)の外側に配設し、円筒状であり、多孔質の周
壁(14)と、該周壁(14)の外側に配設された濾布
又は濾紙(15)と、該濾布又は濾紙(15)の更に外
側に水分を排出する多孔質の周壁(16)を備え、モー
タにより回転することを特徴とする請求項1に記載の生
ゴミの処理装置。
8. The dehydration means (3) is arranged outside the treated material discharge means (2) and has a cylindrical shape. The dehydration means (3) is provided on a porous peripheral wall (14) and outside the peripheral wall (14). A filter cloth or filter paper (15) provided, and a porous peripheral wall (16) for discharging moisture to the outside of the filter cloth or filter paper (15), which are rotated by a motor. 1. The garbage treatment device according to 1.
【請求項9】 前記脱水手段(3)の内側の多孔質の周
壁(14)は、内側に向け多数の突起部を形成し、該各
突起部の先端部に孔を形成し、外側の多孔質の周壁(1
6)は外側に向け多数の突起部を形成し、該各突起部の
先端部に孔を形成することを特徴とする請求項1又は8
に記載の生ゴミの処理装置。
9. The porous peripheral wall (14) inside the dewatering means (3) has a large number of protrusions directed inward, and holes are formed at the tips of the protrusions. Quality surrounding wall (1
6. The method according to claim 6 is characterized in that a large number of projections are formed toward the outside and holes are formed at the tips of the projections.
The garbage processing device described in.
【請求項10】 前記処理物排出装置(2)及び前記脱
水装置(3)の回転軸が同一であり、モータと接続され
てなることを特徴とする請求項1、6〜8に記載の生ゴ
ミの処理装置。
10. The raw product according to claim 1, wherein the treated product discharging device (2) and the dehydrating device (3) have the same rotary shaft and are connected to a motor. Garbage disposal equipment.
【請求項11】 前記破砕攪拌翼(11)の回転軸、前
記処理物排出装置(2)及び前記脱水装置(3)の回転
軸が高速回転することを特徴とする請求項1、3〜9に
記載の生ゴミの処理装置。
11. The rotating shaft of the crushing stirring blade (11) and the rotating shafts of the treated material discharging device (2) and the dewatering device (3) rotate at high speed. The garbage processing device described in.
【請求項12】 前記水分排出手段(4)は、前記脱水
装置(3)の外側に配設し、開閉自在な水分排出口(1
7)を有することを特徴とする請求項1に記載の生ゴミ
の処理装置。
12. The water discharging means (4) is arranged outside the dehydrating device (3) and can be opened and closed freely.
7. The garbage processing apparatus according to claim 1, further comprising 7).
【請求項13】 前記水分排出手段(4)に形成される
水分排出口(17)に水分と汚泥を分離する汚泥凝沈装
置(21)が連結されることを特徴とする請求項1又は
12に記載の生ゴミの処理装置。
13. The sludge settling device (21) for separating water and sludge is connected to a water outlet (17) formed in the water discharging means (4). The garbage processing device described in.
【請求項14】 前記除去手段(5)は、一部にブラシ
(18)を形成し、前記脱水装置(3)の内側に配設さ
れ、該ブラシ(18)が多孔質の周壁(14)と付着、
離脱するように構成され、該多孔質の周壁(14)に付
着する脱水された処理物を除去することを特徴とする請
求項1に記載の生ゴミの処理装置。
14. The removing means (5) is partially provided with a brush (18) and is disposed inside the dehydrator (3), and the brush (18) has a porous peripheral wall (14). And adhere,
The apparatus for treating raw garbage according to claim 1, wherein the apparatus is configured to be detached and removes the dehydrated treated matter attached to the porous peripheral wall (14).
【請求項15】 前記脱水された処理物を収容する収容
手段(6)は、前記処理物排出手段(2)の下方に配設
し、開閉自在な処理物排出口を有することを特徴とする
請求項1に記載の生ゴミの処理装置。
15. The storage means (6) for storing the dehydrated processed product is arranged below the processed product discharging means (2) and has an openable and closable processed product outlet. The garbage processing device according to claim 1.
【請求項16】 アルカリ性二酸化塩素溶液が、500
ppm〜1500ppmであることを特徴とする請求項
1又は2に記載の生ゴミの処理装置又は処理方法。
16. The alkaline chlorine dioxide solution comprises 500
It is ppm-1500ppm, The processing apparatus or the processing method of the garbage of Claim 1 or 2 characterized by the above-mentioned.
【請求項17】 凝集剤が動物骨粉を主成分とする粉状
の凝集剤であることを特徴とする請求項1又は2に記載
の生ゴミの処理装置又は処理方法。
17. The apparatus or method for treating raw garbage according to claim 1, wherein the flocculant is a powdery flocculant containing animal bone powder as a main component.
【請求項18】 反応剤が、PH9〜PH12の水酸化
ナトリウムであることを特徴とする請求項1又は2に記
載の生ゴミの処理装置又は処理方法。
18. The garbage treating apparatus or method according to claim 1 or 2, wherein the reaction agent is sodium hydroxide having a pH of 9 to PH12.
【請求項19】 生ゴミと凝集剤、反応剤、アルカリ性
二酸化塩素溶液との混合比が、生ゴミ1000kgに対
して、凝集剤250cc〜450cc、反応剤100c
c〜300cc、アルカリ性二酸化塩素溶液200cc
〜400ccであることを特徴とする請求項1又は2に
記載の生ゴミの処理装置又は処理方法。
19. The mixing ratio of the garbage to the coagulant, the reaction agent and the alkaline chlorine dioxide solution is 250 cc to 450 cc of the coagulant and 100 c of the reaction agent to 1000 kg of garbage.
c-300 cc, alkaline chlorine dioxide solution 200 cc
To 400 cc, The raw garbage processing apparatus or processing method according to claim 1 or 2, wherein
【請求項20】 生ゴミが、食品生ゴミであることを特
徴とする請求項1又は2に記載の生ゴミの処理装置又は
処理方法。
20. The garbage processing device or method according to claim 1, wherein the garbage is food garbage.
JP6120815A 1994-05-11 1994-05-11 Crude refuse treating device and treatment thereof Pending JPH07299441A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6120815A JPH07299441A (en) 1994-05-11 1994-05-11 Crude refuse treating device and treatment thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6120815A JPH07299441A (en) 1994-05-11 1994-05-11 Crude refuse treating device and treatment thereof

Publications (1)

Publication Number Publication Date
JPH07299441A true JPH07299441A (en) 1995-11-14

Family

ID=14795663

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6120815A Pending JPH07299441A (en) 1994-05-11 1994-05-11 Crude refuse treating device and treatment thereof

Country Status (1)

Country Link
JP (1) JPH07299441A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106734054A (en) * 2016-11-24 2017-05-31 赣州科源甬致科技有限公司 A kind of refuse moisture separation equipment
CN111115863A (en) * 2020-03-09 2020-05-08 温州芬嘉科技有限公司 Sewage treatment device with garbage
CN111558605A (en) * 2020-06-04 2020-08-21 湖南自然创造生物科技有限公司 Wet garbage disposer
CN111995109A (en) * 2020-08-03 2020-11-27 张业文 Environment-friendly sewage treatment device convenient for quantitatively collecting sewage at different water levels
CN114308985A (en) * 2021-12-31 2022-04-12 重庆医药高等专科学校 Static distribution center cytotoxic drug leakage emergency recovery device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106734054A (en) * 2016-11-24 2017-05-31 赣州科源甬致科技有限公司 A kind of refuse moisture separation equipment
CN111115863A (en) * 2020-03-09 2020-05-08 温州芬嘉科技有限公司 Sewage treatment device with garbage
CN111558605A (en) * 2020-06-04 2020-08-21 湖南自然创造生物科技有限公司 Wet garbage disposer
CN111995109A (en) * 2020-08-03 2020-11-27 张业文 Environment-friendly sewage treatment device convenient for quantitatively collecting sewage at different water levels
CN114308985A (en) * 2021-12-31 2022-04-12 重庆医药高等专科学校 Static distribution center cytotoxic drug leakage emergency recovery device

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