JP2000015227A - Refuse treatment apparatus - Google Patents

Refuse treatment apparatus

Info

Publication number
JP2000015227A
JP2000015227A JP18875198A JP18875198A JP2000015227A JP 2000015227 A JP2000015227 A JP 2000015227A JP 18875198 A JP18875198 A JP 18875198A JP 18875198 A JP18875198 A JP 18875198A JP 2000015227 A JP2000015227 A JP 2000015227A
Authority
JP
Japan
Prior art keywords
tank
refuse
aeration
fermentation
fermentation tank
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
JP18875198A
Other languages
Japanese (ja)
Other versions
JP2915903B1 (en
Inventor
Tsutomu Ando
勗 安藤
Keiko Oba
敬子 大羽
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.)
ANDOU KK
Ando Co Ltd
Original Assignee
ANDOU KK
Ando Co Ltd
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 ANDOU KK, Ando Co Ltd filed Critical ANDOU KK
Priority to JP18875198A priority Critical patent/JP2915903B1/en
Application granted granted Critical
Publication of JP2915903B1 publication Critical patent/JP2915903B1/en
Publication of JP2000015227A publication Critical patent/JP2000015227A/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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/20Sludge processing

Abstract

PROBLEM TO BE SOLVED: To provide a refuse treatment apparatus which reduces the volume of various kinds of refuse containing garbage and others as main components inexpensively and hygienically in a short time and can deodorize the refuse. SOLUTION: In a refuse treatment apparatus 1 equipped with a fermentation tank 11, an aeration tank 12, a return route 13, an exhaust passage 14, and an air supply passage 15, the fermentation tank 11 has rotary blades 25 which mix refuse which contains a biostructure as a main component and is charged into the tank with aerobic microorganisms while crushing the refuse and transfer the mixture, the refuse from the fermentation tank 11 is mixed with water and air for aeration in the aeration tank 12, aerated sludge is transferred again to the fermentation tank 11 through the return route 13, gas generated in the fermentation tank 11 is discharged outside the tank through the exhaust passage 14, and air is supplied to the aeration tank 12 through the air supply passage 15.

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】本発明は、生物組織を主成分
とするゴミの処理装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for treating refuse mainly composed of biological tissue.

【0002】[0002]

【従来の技術】近年、各家庭、店舗、工場等からの廃棄
物は増大する一方で、公害発生防止の観点からその処理
に対する規制が厳しくなっている。このため、各自治体
を始めとして、各企業にとっても廃棄物を如何に処理す
るかが大きな問題となりつつある。生ゴミ等の生物組織
を主成分とするゴミの処理についても同様で、放置すれ
ば悪臭源となるだけでなく、衛生上も好ましくなく、廃
棄場所を探すのも容易ではなく、適切な処理が求められ
ている。そして、従来、この種のゴミについては、一般
的に土中に埋めて分解させるか、焼却する処理方法が採
られていた。
2. Description of the Related Art In recent years, while the amount of waste from homes, stores, factories, and the like has increased, regulations on the treatment of the waste have become strict from the viewpoint of preventing pollution. Therefore, how to treat waste is becoming a big problem for each local government and each company. The same applies to the treatment of garbage mainly composed of biological tissue such as garbage. If left untreated, it will not only be a source of foul odors, it is also unfavorable in terms of hygiene, and it is not easy to find a disposal place. It has been demanded. Heretofore, this type of refuse has generally been treated by burying it in the soil for decomposition or incineration.

【0003】[0003]

【発明が解決しようとする課題】上述したゴミの処理方
法のうち、焼却による場合、ばい煙による大気汚染等の
問題を生じる。一方、ゴミを土中に埋めて分解させる場
合、生物組織を生態系に還元させるという環境的には優
れた面もある一方で、ゴミ処理のための場所選びの難し
さ、ゴミを埋めるために大変な労力を要し、埋めたゴミ
が分解するのに長期間要する等の問題がある。
Among the above-mentioned methods for treating garbage, incineration causes problems such as air pollution due to soot and smoke. On the other hand, when garbage is buried in the soil and decomposed, there is an environmentally superior aspect of returning biological tissues to the ecosystem, but it is difficult to select a place for garbage disposal, There is a problem that it takes a lot of labor and it takes a long time for the buried garbage to decompose.

【0004】かかる状況に鑑み、本発明者は、古紙や生
ゴミなどの生物組織を主成分とするゴミの処理装置につ
き鋭意研究を重ねた結果、微生物による醗酵作用および
曝気処理を利用してゴミの容積を有効に減少させ、無臭
化し得ることを見出した。本発明は、かかる従来の問題
点をなくすことを課題として、かつ上述した経緯に基づ
きなされたもので、安価かつ短時間に、しかも衛生的に
生ゴミ等の生物組織を主成分とする種々のゴミの容積を
縮小し、かつ無臭化することを可能とするゴミ処理装置
を提供しようとするものである。
[0004] In view of such circumstances, the present inventor has conducted intensive studies on an apparatus for treating garbage mainly composed of biological tissue such as waste paper and garbage, and as a result, the garbage has been utilized by utilizing the fermentation action of microorganisms and aeration treatment. Has been found to be able to effectively reduce the volume and deodorize. The present invention has been made based on the above-described background, with the object of eliminating the conventional problems, and is inexpensive, short-time, and sanitary for various types of biological tissues such as garbage. It is an object of the present invention to provide a refuse treatment apparatus capable of reducing the volume of refuse and eliminating odor.

【0005】[0005]

【課題を解決するための手段】上記課題を解決するため
に、本発明は、少なくとも醗酵槽と曝気槽と帰還路と排
気流路と給気流路とを備え、上記醗酵槽が、槽内に投入
された生物組織を主成分とするゴミを粉砕しつつ、好気
性微生物と混合して移送する回転羽根車を有し、上記曝
気槽が、上記醗酵槽からのゴミを水および空気と混合し
て曝気処理に付し、上記帰還路が、曝気処理に付された
汚泥を再度上記醗酵槽に移送し、上記排気流路が、上記
醗酵槽から発生した気体を槽外に排出し、上記給気流路
が、上記曝気槽に空気を供給する構成とした。
In order to solve the above-mentioned problems, the present invention comprises at least a fermentation tank, an aeration tank, a return path, an exhaust passage, and an air supply passage, and the fermentation tank is provided in the tank. While crushing the garbage containing the input biological tissue as a main component, it has a rotary impeller for mixing and transferring the garbage with aerobic microorganisms, and the aeration tank mixes the garbage from the fermentation tank with water and air. The return path transfers the sludge subjected to the aeration treatment to the fermentation tank again, and the exhaust passage discharges gas generated from the fermentation tank to the outside of the fermentation tank. The air flow path was configured to supply air to the aeration tank.

【0006】[0006]

【発明の実施の形態】つぎに、本発明の一実施形態を図
面にしたがって説明する。図1は、本発明の第1実施形
態に係るゴミ処理装置1を示し、このゴミ処理装置1
は、醗酵槽11と曝気槽12と帰還路13と排気流路1
4と給気流路15とを備えている。
Next, an embodiment of the present invention will be described with reference to the drawings. FIG. 1 shows a dust processing apparatus 1 according to a first embodiment of the present invention.
Is a fermentation tank 11, an aeration tank 12, a return path 13, and an exhaust path 1.
4 and an air supply channel 15.

【0007】醗酵槽11は、両端部が閉じられ水平に配
置された筒状体で、一方の端部の上面にゴミを投入する
ためのゴミ投入口21を有するとともに、他方の端部に
醗酵ゴミ排出口22を有している。醗酵槽11の内部に
は、上記筒状体と同軸上、水平に配置された回転軸23
上に適宜間隔をあけて取りつけた複数の羽根部材24か
らなる回転羽根車25が設けられている。回転軸23
は、醗酵槽11の一方の端面を貫いて延びた当該回転軸
23の端部にて、スプロケット26、27およびチェー
ン28を介してモータ29により駆動されるようになっ
ている。この回転軸23とともに回転する羽根部材24
は、一定方向に回転することによりゴミを粉砕しつつい
ずれか1の方向に移送できる形状のものであればいずれ
の形状を有するものでもよいが、例えば、図2および図
3に示すような形状、配置で設けることができる。図2
においては回転軸23上に一定の間隔を空けて2枚の羽
根部材24が同じ向きに180°の角度を有して設けら
れており、また、図3においては羽根部材24Aが反対
の向きに0°の角度を有して設けられているが、回転軸
上に複数の羽根部材を適宜の間隔、角度、向きで設ける
ことができる。この羽根部材24により、ゴミ投入口2
1より投入されたゴミは、均一に粉砕されつつ好気性微
生物と均一に混合されることにより醗酵処理され、順
次、醗酵ゴミ排出口22から曝気槽12に向けて移送さ
れる。
The fermenter 11 is a tubular body having both ends closed and arranged horizontally. The fermenter 11 has a dust insertion port 21 at one end for introducing dust, and a fermentation fermenter at the other end. It has a dust discharge port 22. Inside the fermenter 11, a rotating shaft 23 horizontally arranged coaxially with the cylindrical body.
A rotating impeller 25 composed of a plurality of blade members 24 attached at appropriate intervals is provided above. Rotating shaft 23
Is driven by a motor 29 via sprockets 26 and 27 and a chain 28 at an end of the rotating shaft 23 extending through one end face of the fermenter 11. The blade member 24 that rotates together with the rotation shaft 23
May have any shape as long as the dust can be transferred in any one direction while being crushed by rotating in a certain direction. For example, the shape shown in FIGS. 2 and 3 may be used. , Arrangement. FIG.
In FIG. 3, two blade members 24 are provided at a fixed interval on the rotating shaft 23 at the same direction at an angle of 180 °, and in FIG. 3, the blade members 24A are oriented in the opposite direction. Although provided at an angle of 0 °, a plurality of blade members can be provided at appropriate intervals, angles, and directions on the rotating shaft. This blade member 24 allows the dust input port 2
The refuse introduced from 1 is fermented by being uniformly crushed and uniformly mixed with aerobic microorganisms, and is sequentially transferred from the fermentation refuse outlet 22 to the aeration tank 12.

【0008】このゴミの醗酵によって発生した水蒸気を
含む気体は醗酵槽11の上面に設けた排気流路14から
大気中に放出されるが、所望により、該気体中に含まれ
る水蒸気を、該排気流路14から分岐する水蒸気流路1
4aを介して曝気槽12に送給してもよい。この曝気槽
12に流れる水蒸気は、該水蒸気流路14aの途中また
は曝気槽12内で凝結し、液体へと変化する。なお、醗
酵槽11内で発生した気体の全てを槽外に排出し、曝気
槽12にはこの気体を送らず、専用の給水流路により曝
気槽12内に水を供給するようにしてもよい。
The gas containing water vapor generated by the fermentation of the garbage is released into the atmosphere from an exhaust passage 14 provided on the upper surface of the fermenter 11. If desired, the water vapor contained in the gas is removed by the exhaust gas. Steam flow path 1 branched from flow path 14
It may be supplied to the aeration tank 12 via 4a. The steam flowing through the aeration tank 12 condenses in the middle of the steam flow path 14a or in the aeration tank 12, and changes into a liquid. In addition, all the gas generated in the fermentation tank 11 may be discharged to the outside of the tank, and the gas may not be sent to the aeration tank 12, but water may be supplied to the aeration tank 12 through a dedicated water supply channel. .

【0009】さらに、醗酵槽11内には、その内壁面に
曝気槽12に向うゴミの移送方向に対して垂直方向に立
設された堰31が設けてあり、この堰31により醗酵槽
11内は二つのブロックに区画される。醗酵槽11内で
は、ゴミが醗酵ゴミ排出口22に近づくにつれて醗酵が
進み、温度が上昇してゆく一方、ゴミ自身の温度が上昇
することにより醗酵が促進されるため、隣接するより高
温のブロックとより低温のブロック間で、すなわちより
高温のブロックからより低温のブロックへと熱が伝導し
易いように、堰31は熱伝導性の良好な材質のものであ
るのが望ましい。なお、堰31は、醗酵槽11の高さの
約1/2の高さとするのが好ましく、適宜間隔をあけて
複数設けることもできる。
Further, in the fermentation tank 11, a weir 31 is provided on the inner wall surface of the fermentation tank 11 in a direction perpendicular to the direction in which the garbage is transferred toward the aeration tank 12. Is divided into two blocks. In the fermenter 11, the fermentation proceeds as the garbage approaches the fermentation garbage discharge port 22, and the temperature rises. On the other hand, the temperature of the garbage itself increases to promote fermentation. It is desirable that the weir 31 be made of a material having good thermal conductivity so that heat can be easily conducted between the lower temperature block and the lower temperature block, that is, from the higher temperature block to the lower temperature block. The height of the weir 31 is preferably about half the height of the fermentation tank 11, and a plurality of weirs 31 may be provided at appropriate intervals.

【0010】醗酵槽11のゴミ排出口22から曝気槽1
2に移送された醗酵ゴミは、水と、給気ポンプ32によ
り給気流路15を経て、曝気槽12内に配置された多数
のノズルを有する散気管33を介して供給される空気と
混合されて曝気処理に付され汚泥となる。すなわち、上
記好気性微生物の作用によってゴミ中の有機物が酸化分
解される。この際の醗酵ゴミと水との混合比は、例えば
容積比で20:80〜30:70である。また、図1お
よび図4に示す実施形態では、曝気槽12の底部に散気
管33を設けて曝気処理を促進するようにしてあるが、
この配置に限定されるものでなく、醗酵ゴミと空気とが
均一に混合されて上記微生物の作用によって汚泥の酸化
分解が促進されるものであればいずれの配置であっても
よい。なお、本明細書においては、この好気性微生物を
含む汚泥を通気混合させる処理を曝気処理という。
[0010] From the garbage discharge port 22 of the fermentation tank 11, the aeration tank 1
The fermentation waste transferred to 2 is mixed with water and air supplied through a diffuser 33 having a number of nozzles arranged in the aeration tank 12 via an air supply passage 15 by an air supply pump 32. And subjected to aeration treatment to become sludge. That is, the organic substances in the refuse are oxidatively decomposed by the action of the aerobic microorganisms. The mixing ratio between the fermentation waste and water at this time is, for example, 20:80 to 30:70 in volume ratio. Further, in the embodiment shown in FIGS. 1 and 4, a diffuser 33 is provided at the bottom of the aeration tank 12 to promote the aeration process.
The arrangement is not limited to this arrangement, and any arrangement may be used as long as the fermentation garbage and air are uniformly mixed to promote the oxidative decomposition of sludge by the action of the microorganism. In the present specification, the process of aerating and mixing the sludge containing aerobic microorganisms is referred to as aeration.

【0011】ついで、曝気槽12内で曝気処理された汚
泥は、帰還ポンプ34によって帰還路13を介して再度
醗酵槽11により移送され、新たなゴミとともにゴミ投
入口21から醗酵槽11内に投入され、上記同様の処理
が適宜回数繰り返される。この繰り返し処理されるゴミ
は、適宜回数の醗酵工程の段階において未分解の有機質
成分を含んでいるが、これを醗酵槽11外に取り出し、
堆肥として利用することもできる。なお、上記汚泥は必
ずしもゴミ投入口21から醗酵槽11内に投入する必要
はなく、ゴミ投入口21の近傍の醗酵槽11の壁部に別
途汚泥投入口を設けて、投入することもできる。
Then, the sludge aerated in the aeration tank 12 is transported again by the fermenter 11 through the return path 13 by the return pump 34, and is fed into the fermenter 11 through the refuse inlet 21 together with new refuse. Then, the same processing as described above is repeated an appropriate number of times. The garbage that is repeatedly processed contains undecomposed organic components in the fermentation process at an appropriate number of times.
It can also be used as compost. The sludge does not necessarily need to be introduced into the fermentation tank 11 from the refuse input port 21, but may be provided by providing a separate sludge input port on the wall of the fermentation tank 11 near the refuse input port 21.

【0012】図4は、本発明の第2実施形態に係るゴミ
処理装置2を示し、上述したゴミ処理装置1とは、醗酵
槽11に代えて醗酵槽11Aを設けた点を除き実質的に
同一であり、共通部分については説明を省略する。この
ゴミ処理装置2の醗酵槽11Aは、両端面が閉じられた
筒状の外処理槽41と、この外処理槽41に包囲され、
かつこの外処理槽41に対して同軸上にて相対回転可能
に設けられ、両端面が閉じられ、端部にて外処理槽41
と連通する開口部42を有する筒状の内処理槽43とか
らなっている。そして、外処理槽41および内処理槽4
3の内部には、上記同様曝気槽12に向うゴミの移送方
向に対して垂直方向に立設された堰31I、31Oがそ
れぞれ複数設けてあり、この堰31I、31Oにより醗
酵槽11A内はそれぞれ軸方向に沿って隣り合う複数の
ブロックに区画されている。
FIG. 4 shows a refuse treatment apparatus 2 according to a second embodiment of the present invention. The refuse treatment apparatus 1 is substantially the same as the refuse treatment apparatus 1 except that a fermentation tank 11A is provided instead of the fermentation tank 11. They are the same, and the description of the common parts is omitted. The fermentation tank 11A of the refuse treatment apparatus 2 has a cylindrical outer processing tank 41 with both end faces closed, and is surrounded by the outer processing tank 41.
The outer processing tank 41 is provided coaxially with the outer processing tank 41 so as to be rotatable relative to the outer processing tank 41.
And a cylindrical inner processing tank 43 having an opening 42 communicating with the inner processing tank 43. And the outer processing tank 41 and the inner processing tank 4
A plurality of weirs 31I and 31O are provided in the inside of the fermenter 11A in the vertical direction with respect to the transfer direction of the garbage toward the aeration tank 12 as described above. It is partitioned into a plurality of blocks that are adjacent along the axial direction.

【0013】内処理槽43の内部には、図1に示す装置
と同様、回転羽根車25が設けられ、さらに内処理槽4
3の外周部にも複数の羽根部材24が設けられ、内処理
槽43とともに回転羽根車25同様の羽根車が形成され
ている。この内処理槽43は、適宜歯車列、あるいはチ
ェーン、スプロケットの組合わせを利用して回転羽根車
25用のモータ29により駆動するようにしてもよく、
別個のモータにより駆動するようにしてもよい。
A rotary impeller 25 is provided inside the inner processing tank 43 similarly to the apparatus shown in FIG.
A plurality of impeller members 24 are also provided on the outer peripheral portion of 3, and an impeller similar to the rotary impeller 25 is formed together with the inner processing tank 43. The inner processing tank 43 may be driven by the motor 29 for the rotary impeller 25 using a combination of a gear train, a chain, and a sprocket as appropriate.
It may be driven by a separate motor.

【0014】なお、外処理槽41の内部に設けられた堰
31Oは外処理槽41と内処理槽43との間の空隙部の
径方向の寸法の約1/2の高さを有するのが好ましく、
内処理槽43の内部に設けた堰31Iは内処理槽43の
内径の約1/2の高さを有するのが好ましい。ところ
で、醗酵槽11内の温度は、その大きさ、堰31、31
I、31Oの数、槽内の位置等により変動し得るが、微
生物の醗酵により常温〜60℃となる。かくして、醗酵
槽11は、通常、加温手段などを要せずゴミ処理にかか
るコストを低減し得るが、槽内に加温手段を設けてより
一層醗酵を促進するようにしてもよい。
The weir 310 provided inside the outer processing tank 41 has a height approximately half the radial dimension of the gap between the outer processing tank 41 and the inner processing tank 43. Preferably
The weir 31I provided inside the inner processing tank 43 preferably has a height of about 約 of the inner diameter of the inner processing tank 43. By the way, the temperature in the fermenter 11 depends on its size, weirs 31, 31.
The temperature may vary from room temperature to 60 ° C. due to the fermentation of microorganisms, although it may vary depending on the number of I and 31O, the position in the tank, and the like. Thus, the fermenter 11 usually does not require a heating means or the like, and can reduce the cost for refuse treatment. However, a heating means may be provided in the tank to further promote fermentation.

【0015】また、上述したゴミ処理装置1または2に
よって処理されるゴミは、生物組織自体または生物組織
由来の、生物組織を主成分とするゴミであれば特に限定
されるものではないが、例えば、古紙、動物の肉、野
菜、果物、残飯、天ぷら、コーヒーや茶の粕、糞尿、草
花、卵殻、稲や麦の藁、落ち葉などの一般家庭で廃棄さ
れるゴミのほか、食品加工工場、レストラン、調理場な
どから出る排液やゴミなどの産業的に廃棄されるゴミが
挙げられる。
The refuse to be treated by the above-mentioned refuse treatment apparatus 1 or 2 is not particularly limited as long as it is biological tissue itself or refuse derived from the biological tissue and mainly composed of biological tissue. , Waste paper, animal meat, vegetables, fruits, garbage, tempura, coffee and tea lees, manure, flowers, eggshell, rice and wheat straw, fallen leaves and other general waste, Garbage that is industrially discarded, such as effluents and garbage from restaurants and kitchens, may be mentioned.

【0016】さらに、ゴミと混合して醗酵させる好気性
微生物は、生物組織などの有機物の分解によって生じる
硫化水素、アンモニア、低沸点硫化物などの臭気成分を
酸化分解し得る微生物であればいずれの細菌、真菌、原
生動物であってもよいが、好ましくは一般に自然界に生
息する土壌菌や、腐敗菌と称される細菌が挙げられる。
これらの好気性微生物は単独または2種以上を組合わせ
て使用することができ、通常の微生物の固定化方法を用
いて固相に固定化し、その微生物床を醗酵槽11および
曝気槽12内に設けることもできる。
Furthermore, the aerobic microorganisms to be fermented by mixing with garbage are any microorganisms capable of oxidatively decomposing odorous components such as hydrogen sulfide, ammonia, and low-boiling sulfide generated by the decomposition of organic substances such as biological tissues. It may be a bacterium, a fungus, or a protozoa, but preferably includes a soil bacterium generally inhabiting in nature and a bacterium called a spoilage bacterium.
These aerobic microorganisms can be used alone or in combination of two or more. The microorganisms are immobilized on a solid phase using a usual microorganism immobilization method, and the microorganism bed is placed in the fermentation tank 11 and the aeration tank 12. It can also be provided.

【0017】上記の醗酵槽、曝気槽、および帰還路中の
ゴミは、好気性微生物による醗酵作用を促進するため
に、通常pH5以上に保たれる。ゴミのpHの調整は、
ゴミ投入時または工程途中に投入し得るpH調整剤によ
って行い、このpH調整剤としては通常のpH調整剤を
用いることができるが、例えば、曝気処理した汚泥など
が挙げられる。
The refuse in the fermentation tank, aeration tank, and return path is usually maintained at pH 5 or higher to promote fermentation by aerobic microorganisms. Adjustment of garbage pH
It is carried out with a pH adjuster that can be put in at the time of charging dust or in the middle of the process. As the pH adjuster, a normal pH adjuster can be used, for example, sludge that has been subjected to aeration treatment.

【0018】また、繊維質のような、容易に粉砕でき
ず、処理に長時間を要するゴミを投入する場合には、粉
砕助剤をゴミとともに醗酵槽に投入することができる。
粉砕助剤は、ゴミと共に攪拌、混合されるとその間の摩
擦によってゴミの粉砕を補助し得るものであれば特に限
定されるものではないが、多孔質材料が好ましく、例え
ば加圧発泡加工した黒曜石などが挙げられる。
In addition, when refuse such as fibrous material which cannot be easily crushed and requires a long time for processing is introduced, a grinding aid can be introduced into the fermentation tank together with the refuse.
The grinding aid is not particularly limited as long as it can assist the grinding of the dust by friction during stirring and mixing with the dust, but a porous material is preferable, for example, obsidian processed by pressure foaming And the like.

【0019】また、所望により、上記曝気槽中の汚泥に
無臭化酵素を添加して、さらに効率的にゴミを無臭化す
ることもできる。無臭化酵素は、英国HI−BAR社製
品でアイスランドケルプを醗酵させて得た生分解菌の活
性化剤で、例えばティーメックス株式会社からBio Cat
なる商品名で販売されている。
Further, if desired, a deodorizing enzyme can be added to the sludge in the aeration tank to more efficiently deodorize the refuse. Deodorizing enzyme is an activator of biodegradable bacteria obtained by fermenting Iceland kelp with a product of HI-BAR, UK.
Sold under the trade name

【0020】[0020]

【発明の効果】以上の説明より明らかなように、第1発
明によれば、少なくとも醗酵槽と曝気槽と帰還路と排気
流路と給気流路とを備え、上記醗酵槽が、槽内に投入さ
れた生物組織を主成分とするゴミを粉砕しつつ、好気性
微生物と混合して移送する回転羽根車を有し、上記曝気
槽が、上記醗酵槽からのゴミを槽内で水および空気と混
合して曝気処理に付し、上記帰還路が、曝気処理に付さ
れた汚泥を再度上記醗酵槽に移送し、上記排気流路が、
上記醗酵槽から発生した気体を槽外に排出し、上記給気
流路が、上記曝気槽に空気を供給する構成としてある。
このため、安価かつ短時間に、しかも衛生的に生物組織
を主成分とする種々のゴミの容積を縮小し、かつ該ゴミ
を無臭化することが可能になるという効果を奏する。
As is apparent from the above description, according to the first aspect, at least the fermentation tank, the aeration tank, the return path, the exhaust path, and the air supply path are provided, and the fermentation tank is provided in the tank. A whirlpool for mixing and transferring aerobic microorganisms while pulverizing garbage containing the input biological tissue as a main component has a rotary impeller, and the aeration tank is configured to transfer garbage from the fermentation tank with water and air in the tank. And the mixture is subjected to aeration treatment, and the return path transfers the sludge subjected to the aeration treatment to the fermentation tank again, and the exhaust passage,
Gas generated from the fermentation tank is discharged out of the tank, and the air supply channel supplies air to the aeration tank.
For this reason, there is an effect that it is possible to reduce the volume of various kinds of dust mainly composed of biological tissue inexpensively, in a short time, and in a sanitary manner, and to make the dust odorless.

【0021】また、第2発明によれば、第1発明の構成
に加えて、上記醗酵槽が、その内壁面に上記曝気槽に向
うゴミの移送方向に対して垂直方向に立設された少なく
とも1つの堰を有する構成としてある。このため、第1
発明による効果に加えて、醗酵槽内でゴミがブロック毎
に効率よく醗酵され、かつより醗酵が進行してより高い
温度を有するゴミから隣接するブロックのより低い温度
を有するゴミに熱が伝導され、そのゴミの醗酵がより促
進されるという効果を奏する。
According to a second aspect of the present invention, in addition to the configuration of the first aspect, at least the fermentation tank is provided on an inner wall surface of the fermentation tank in a direction perpendicular to the direction in which the garbage is transferred to the aeration tank. The structure has one weir. Therefore, the first
In addition to the effects of the present invention, the refuse is efficiently fermented block by block in the fermenter, and the heat is transferred from the higher temperature refuse to the lower temperature refuse of the adjacent block as the fermentation proceeds. This has the effect that fermentation of the garbage is further promoted.

【0022】さらに、第3発明によれば、第2発明の構
成に加えて、上記醗酵槽が、両端面が閉じられた筒状の
外処理槽と、この外処理槽に包囲され、かつこの外処理
槽に対して同軸上にて相対回転可能に設けられ、両端面
が閉じられ、端部にて上記外処理槽と連通する開口部を
有する筒状の内処理槽とからなる構成としてある。この
ため、第2発明による効果に加えて、ゴミ処理装置本体
をよりコンパクトな形状にすることができ、かつより醗
酵が進行してより高い温度を有する内処理槽内のゴミか
らより低い温度を有する外処理槽内のゴミに熱が伝導さ
れ、そのゴミの醗酵がより促進されるという効果を奏す
る。
According to a third aspect of the present invention, in addition to the configuration of the second aspect, the fermentation tank is surrounded by a cylindrical external processing tank having both ends closed, and is surrounded by the external processing tank. The outer processing tank is provided so as to be rotatable relative to the outer processing tank, both end faces are closed, and a cylindrical inner processing tank having an opening communicating with the outer processing tank at an end. . For this reason, in addition to the effect of the second invention, it is possible to make the refuse treatment apparatus main body more compact, and to reduce the temperature of refuse from the refuse in the inner treatment tank having a higher temperature as fermentation proceeds. Heat is conducted to the refuse in the external processing tank having the refuse, and the fermentation of the refuse is further promoted.

【0023】さらに、第4発明によれば、上記各発明の
構成に加えて、上記曝気槽でゴミと混合される上記水の
供給源が上記排気流路である構成としてある。このた
め、上記各発明による効果に加えて、別途給水流路を設
ける必要がなくなり、醗酵槽内においてゴミから一旦蒸
発した水を再利用できるという効果を奏する。
Further, according to the fourth aspect of the invention, in addition to the configuration of each of the above aspects of the invention, the supply source of the water mixed with dust in the aeration tank is the exhaust flow path. For this reason, in addition to the effects of the above inventions, there is no need to provide a separate water supply flow path, and the water once evaporated from the refuse in the fermentation tank can be reused.

【0024】さらに、第5発明によれば、上記各発明の
構成に加えて、上記ゴミがpH5以上に調整されている
構成としてある。このため、上記各発明による効果に加
えて、好気性微生物によるゴミの醗酵・曝気処理をより
促進できるという効果を奏する。
According to a fifth aspect of the present invention, in addition to the configuration of each of the above-described inventions, the dust is adjusted to have a pH of 5 or more. For this reason, in addition to the effects of the above inventions, there is an effect that fermentation and aeration of garbage by aerobic microorganisms can be further promoted.

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

【図1】 本発明の第1実施形態に係るゴミ処理装置の
全体構成を示す図である。
FIG. 1 is a diagram illustrating an entire configuration of a refuse disposal apparatus according to a first embodiment of the present invention.

【図2】 図1に示す装置におけるある種の態様の回転
羽根車を示す図である。
FIG. 2 is a diagram illustrating a rotating impeller of an embodiment of the apparatus shown in FIG. 1;

【図3】 図1に示す装置における別の態様の回転羽根
車を示す図である。
FIG. 3 is a view showing another embodiment of the rotary impeller in the apparatus shown in FIG. 1;

【図4】 本発明の第2実施形態に係るゴミ処理装置の
全体構成を示す図である。
FIG. 4 is a diagram illustrating an entire configuration of a dust processing apparatus according to a second embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1、2 ゴミ処理装置 11、11A 醗酵
槽 12 曝気槽 13 帰還路 14 排気流路 14a 水蒸気流路 15 給気流路 21 ゴミ投入口 22 醗酵ゴミ排出口 23、23A 回転
軸 24、24A 羽根部材 25、25A 回転
羽根車 26、27 スプロケット 28 チェーン 29 モータ 31、31I、31O 堰 32 給気ポンプ 33 散気管 34 帰還ポンプ 41 外処理槽 42 開口部 43 内処理槽
1, 2 refuse treatment apparatus 11, 11A fermentation tank 12 aeration tank 13 return path 14 exhaust path 14a steam path 15 supply air path 21 refuse inlet 22 fermentation refuse outlet 23, 23A rotating shaft 24, 24A blade member 25, 25A Rotating impeller 26, 27 Sprocket 28 Chain 29 Motor 31, 31I, 31O Weir 32 Air supply pump 33 Air diffuser 34 Return pump 41 Outer processing tank 42 Opening 43 Inner processing tank

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 少なくとも醗酵槽と曝気槽と帰還路と排
気流路と給気流路とを備え、 上記醗酵槽が、槽内に投入された生物組織を主成分とす
るゴミを粉砕しつつ、当該醗酵槽内の好気性微生物と混
合して移送する回転羽根車を有し、 上記曝気槽が、上記醗酵槽からのゴミを水および空気と
混合して曝気処理に付し、 上記帰還路が、曝気処理に付された汚泥を再度上記醗酵
槽に移送し、 上記排気流路が、上記醗酵槽から発生した気体を槽外に
排出し、 上記給気流路が、上記曝気槽に空気を供給することを特
徴とするゴミ処理装置。
1. A fermentation tank having at least a fermentation tank, an aeration tank, a return path, an exhaust flow path, and an air supply flow path, wherein the fermentation tank pulverizes garbage mainly containing biological tissue put into the tank. A rotating impeller that mixes and transports with the aerobic microorganisms in the fermentation tank; the aeration tank mixes garbage from the fermentation tank with water and air to perform aeration treatment; Transferring the sludge subjected to the aeration treatment to the fermentation tank again, the exhaust passage discharging the gas generated from the fermentation tank out of the tank, and the air supply passage supplying air to the aeration tank. A garbage disposal apparatus characterized in that:
【請求項2】 上記醗酵槽が、その内壁面に上記曝気槽
に向うゴミの移送方向に対して垂直方向に立設された少
なくとも1つの堰を有することを特徴とする請求項1記
載のゴミ処理装置。
2. The refuse according to claim 1, wherein said fermentation tank has at least one weir standing on an inner wall surface thereof in a direction perpendicular to a transfer direction of the refuse toward the aeration tank. Processing equipment.
【請求項3】 上記醗酵槽が、両端面が閉じられた筒状
の外処理槽と、この外処理槽に包囲され、かつこの外処
理槽に対して同軸上にて相対回転可能に設けられ、両端
面が閉じられ、端部にて上記外処理槽と連通する開口部
を有する筒状の内処理槽とからなることを特徴とする請
求項1または2いずれか1項記載のゴミ処理装置。
3. The fermenter is provided with a cylindrical outer processing tank having both end faces closed, and is provided so as to be surrounded by the outer processing tank and rotatable coaxially with the outer processing tank. 3. A refuse treatment apparatus according to claim 1, further comprising a cylindrical inner treatment tank having both ends closed and an opening communicating with the outer treatment tank at an end. .
【請求項4】 上記曝気槽でゴミと混合される上記水の
供給源が上記排気流路であることを特徴とする請求項1
〜3いずれか1項記載のゴミ処理装置。
4. The exhaust flow path according to claim 1, wherein a supply source of the water mixed with dust in the aeration tank is the exhaust passage.
The refuse treatment apparatus according to any one of claims 1 to 3.
【請求項5】 上記ゴミがpH5以上に調整されている
ことを特徴とする1〜4いずれか1項記載のゴミ処理装
置。
5. The refuse treatment apparatus according to claim 1, wherein the refuse is adjusted to have a pH of 5 or more.
JP18875198A 1998-07-03 1998-07-03 Garbage disposal device Expired - Fee Related JP2915903B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18875198A JP2915903B1 (en) 1998-07-03 1998-07-03 Garbage disposal device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18875198A JP2915903B1 (en) 1998-07-03 1998-07-03 Garbage disposal device

Publications (2)

Publication Number Publication Date
JP2915903B1 JP2915903B1 (en) 1999-07-05
JP2000015227A true JP2000015227A (en) 2000-01-18

Family

ID=16229143

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18875198A Expired - Fee Related JP2915903B1 (en) 1998-07-03 1998-07-03 Garbage disposal device

Country Status (1)

Country Link
JP (1) JP2915903B1 (en)

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