JP2001039787A - Composting device and method for composting organic waste - Google Patents

Composting device and method for composting organic waste

Info

Publication number
JP2001039787A
JP2001039787A JP2000174286A JP2000174286A JP2001039787A JP 2001039787 A JP2001039787 A JP 2001039787A JP 2000174286 A JP2000174286 A JP 2000174286A JP 2000174286 A JP2000174286 A JP 2000174286A JP 2001039787 A JP2001039787 A JP 2001039787A
Authority
JP
Japan
Prior art keywords
composting
tank
stirring
stirring tank
organic waste
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
JP2000174286A
Other languages
Japanese (ja)
Inventor
Shinichi Shimose
眞一 下瀬
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.)
CHUO KIKO KK
KOGA KIKAI SEISAKUSHO KK
Asahi Koki Co Ltd
Original Assignee
CHUO KIKO KK
KOGA KIKAI SEISAKUSHO KK
Asahi Koki 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 CHUO KIKO KK, KOGA KIKAI SEISAKUSHO KK, Asahi Koki Co Ltd filed Critical CHUO KIKO KK
Priority to JP2000174286A priority Critical patent/JP2001039787A/en
Publication of JP2001039787A publication Critical patent/JP2001039787A/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
    • 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
    • Y02W30/00Technologies for solid waste management
    • Y02W30/40Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

Landscapes

  • Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)
  • Accessories For Mixers (AREA)
  • Fertilizers (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain compost at a low cost by utilizing indigenous microorganisms by providing the subject device with an agitating device provided with an agitating tank and agitating vanes and a pressure reduction device for reducing the pressure in the agitating tank. SOLUTION: Garbage is fed from through-pipes 11, 12 and 13 into the agitating tank 10 and is properly inoculated with the indigenous microorganisms. The privately made microorganisms formed by culturing the microorganisms living on the soil of fields, or the like, are usable. The inside of the agitating tank 10 is heated by the steam passing a steam passage 20. The garbage is stirred by driving a motor, thereby rotating stirring vanes 17. As a result, the garbage and the indigenous microorganisms are mixed and the heat generation of the garbage is initiated. At this time, the pressure in the agitating tank 10 is reduced by a vacuum pump. The pressure reduction is so executed that the boiling point of the water existing in the agitating tank 10 attains about 60 deg.C. The fermentation of the garbage progresses and the temperature is raised by the heat of fermentation until about 60 deg.C is attained but the temperature in the agitating tank 10 does not rise any more while the water exists therein. The inside of the agitating tank is thus maintained at which the microorganism can act.

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】本発明は堆肥化装置及び有機
廃棄物の堆肥化方法に関するものである。更に詳しく
は、微生物の発酵熱が装置内部に蓄積しても高温になら
ないようにすることにより、入手に特に費用がかからな
い土着微生物を利用できるようにして堆肥を安価に製造
でき、装置も安価に製造できて耐久性も向上させること
ができる堆肥化装置及び有機廃棄物の堆肥化方法に関す
る。
The present invention relates to a composting apparatus and a method for composting organic waste. More specifically, by preventing fermentation heat of microorganisms from accumulating inside the device, the temperature does not become high, so that indigenous microorganisms that are not particularly expensive to obtain can be used, and compost can be manufactured inexpensively. The present invention relates to a composting apparatus which can be manufactured and can improve durability, and a method for composting organic waste.

【0002】[0002]

【従来技術】微生物を使用した有機廃棄物の堆肥化装置
は従来から数多く提案されている。従来のこのような堆
肥化装置は、タンク内に焼酎の搾りかすや生ゴミ等の有
機廃棄物を投入し、微生物を適量接種した後、撹拌装置
によってこれを撹拌し、発酵熱により蒸散する水分をタ
ンク外部に排出しながら堆肥化させる構造のものであ
る。この堆肥化装置には、放線菌や高温菌等の市販の微
生物が使用されており、発酵時の装置内部の温度は微生
物の発酵熱が蓄積されることによって数百℃に達するこ
とがある。
2. Description of the Related Art Many organic waste composting apparatuses using microorganisms have been proposed. Such a conventional composting device is configured to put organic waste such as shochu pomace and garbage into a tank, inoculate an appropriate amount of microorganisms, stir the mixture with a stirrer, and evaporate water by fermentation heat. Is discharged to the outside of the tank while composting. Commercially available microorganisms such as actinomycetes and thermophiles are used in this composting device, and the temperature inside the device during fermentation may reach several hundred degrees centigrade due to accumulation of fermentation heat of the microorganism.

【0003】[0003]

【発明が解決しようとする課題】しかし、上記したよう
な微生物を使用した堆肥化装置には、次のような課題が
あった。すなわち、堆肥化装置は微生物による発酵熱に
よって装置内部の温度が数百℃にもなるために耐熱性を
高めてあるが、そのために装置が高価になってしまう。
また、耐熱性が高めてあるとはいっても、長期にわたり
使用すれば傷みがひどくなり、耐久性に課題があるのは
否めない。
However, a composting apparatus using the above-mentioned microorganism has the following problems. That is, the composting device has increased heat resistance because the temperature inside the device reaches several hundred degrees centigrade due to heat of fermentation by microorganisms, but the device becomes expensive.
Further, even if the heat resistance is enhanced, it is undeniable that there is a problem in durability due to severe damage when used for a long time.

【0004】また、従来の堆肥化装置に使用される微生
物は比較的高価であり、継続的に購入していくには経済
的負担も大きい。ところで、一般の土壌に棲息する土着
微生物といわれる微生物も自然界において生物の死骸、
植物等、有機物の分解、堆肥化を行っている。この土着
微生物を堆肥化装置に利用できれば、微生物を別に購入
する必要がないので、堆肥を安価に製造することができ
る。しかし、この土着微生物は、60℃程度までは活発
に活動するけれども、温度がそれ以上になると休眠状態
となり、100℃程度になると死んでしまう。このた
め、例えばこの土着微生物を従来の堆肥化装置に使用し
た場合、発酵熱により装置内部の温度が高温になると死
んでしまい、発酵、堆肥化ができなくなる。
[0004] In addition, microorganisms used in conventional composting devices are relatively expensive, and the economic burden is large if they are purchased continuously. By the way, microorganisms called indigenous microorganisms that inhabit general soil are also dead bodies of organisms in nature,
It decomposes organic matter such as plants and composts. If the indigenous microorganisms can be used in a composting device, it is not necessary to purchase the microorganisms separately, so that compost can be produced at low cost. However, although the indigenous microorganisms are active up to about 60 ° C., they become dormant when the temperature becomes higher than that, and die at about 100 ° C. Therefore, for example, when this indigenous microorganism is used in a conventional composting device, if the temperature inside the device becomes high due to the heat of fermentation, it will die and fermentation and composting will not be possible.

【0005】本発明は上記課題を解消するもので、微生
物の発酵熱が装置内部に蓄積しても高温にならないよう
にして、入手に特に費用がかからない土着微生物を利用
できるようにし、堆肥を安価に製造できる堆肥化装置及
び有機廃棄物の堆肥化方法を提供することを目的とす
る。また、装置が高温にならないようにすることによっ
て、従来の装置のような高温に耐える高価な材料を使用
する必要がないようにして、装置を安価に製造できるよ
うにし、耐久性も向上させることができる堆肥化装置及
び有機廃棄物の堆肥化方法を提供することを目的とす
る。
[0005] The present invention solves the above-mentioned problems, so that even if the heat of fermentation of microorganisms accumulates inside the apparatus, the temperature does not become high, so that indigenous microorganisms, which are not particularly expensive to obtain, can be used. It is an object of the present invention to provide a composting apparatus and a method for composting organic waste, which can be manufactured at low cost. Also, by preventing the device from becoming hot, it is not necessary to use expensive materials that can withstand high temperatures as in conventional devices, so that the device can be manufactured at low cost and durability can be improved. It is an object of the present invention to provide a composting apparatus and a method for composting organic waste.

【0006】[0006]

【課題を解決するための手段】上記目的を達成するため
に講じた本発明の手段は次のとおりである。第1の発明
にあっては、有機廃棄物を堆肥化する堆肥化装置であっ
て、撹拌槽と撹拌羽根を備えた撹拌装置と、上記撹拌槽
の内部を減圧する減圧装置と、を備えていることを特徴
とする、堆肥化装置である。
Means of the present invention taken to achieve the above object are as follows. According to the first invention, there is provided a composting device for composting organic waste, comprising: a stirring device having a stirring tank and stirring blades; and a decompression device for decompressing the inside of the stirring tank. A composting device characterized in that:

【0007】第2の発明にあって、有機廃棄物を堆肥化
する堆肥化装置であって、撹拌槽と撹拌羽根を備えた撹
拌装置と、上記撹拌槽の内部を加温する加温装置と、上
記撹拌槽の内部を減圧する減圧装置と、上記減圧装置に
よって吸引される槽内空気に含まれる蒸気を液化する液
化装置と、を備えていることを特徴とする、堆肥化装置
である。
According to a second aspect of the present invention, there is provided a composting device for composting organic waste, comprising: a stirring device having a stirring tank and stirring blades; and a heating device for heating the inside of the stirring tank. And a liquefaction device for liquefying vapor contained in the air in the tank sucked by the decompression device.

【0008】第3の発明にあっては、上記撹拌装置の撹
拌羽根に加温手段を備えていることを特徴とする、第2
の発明に係る堆肥化装置である。
[0008] In a third aspect of the present invention, the stirring blade of the stirring device is provided with a heating means.
The present invention relates to a composting device according to the invention.

【0009】第4の発明にあっては、有機廃棄物の堆肥
化方法であって、撹拌槽の内部を減圧して沸点を下げる
ことにより土着微生物が活動可能な温度を維持し、上記
撹拌槽の内部で土着微生物によって有機廃棄物を発酵さ
せて堆肥化することを特徴とする、有機廃棄物の堆肥化
方法である。
[0009] In a fourth aspect of the present invention, there is provided a method for composting organic waste, wherein the temperature in which indigenous microorganisms can be activated is maintained by reducing the boiling point by reducing the pressure inside the stirring tank. A method for composting organic waste, comprising fermenting organic waste by indigenous microorganisms inside the plant and composting the same.

【0010】(作用)本発明の堆肥化装置では、まず、
撹拌槽の内部に生ゴミ等の有機廃棄物が適量投入され、
これに土着微生物が適量接種される。撹拌槽の内部の温
度は加温装置により、土着微生物が活動可能な温度(一
般的には、70℃が上限)に設定される。
(Operation) In the composting apparatus of the present invention, first,
An appropriate amount of organic waste such as garbage is put into the stirring tank,
This is inoculated with an appropriate amount of indigenous microorganisms. The temperature inside the stirring tank is set by a heating device to a temperature at which indigenous microorganisms can be activated (generally, 70 ° C. is an upper limit).

【0011】撹拌槽の内部の有機廃棄物と土着微生物の
混合物は槽内で撹拌羽根によって撹拌され、土着微生物
の活動によって有機廃棄物の発酵が始まる。また、撹拌
槽の内部は減圧装置によって減圧される。なお、この減
圧は槽内にある有機廃棄物に含まれている水の沸点が6
0℃程度になるように行われる。
The mixture of the organic waste and the indigenous microorganisms in the stirring tank is stirred by the stirring blade in the tank, and the fermentation of the organic waste is started by the activity of the indigenous microorganisms. The pressure inside the stirring tank is reduced by a pressure reducing device. Note that this pressure reduction is such that the boiling point of water contained in the organic waste in the tank is 6 ° C.
It is performed so that the temperature becomes about 0 ° C.

【0012】撹拌槽内の有機廃棄物の発酵が進み、その
発酵熱によって温度が上昇し、沸点である60℃に達す
ると沸騰し、蒸発を始める。また、発酵熱は、沸点にお
いて順次気化熱に変わり、撹拌槽内に水があるうちはほ
とんど蓄積されないので、撹拌槽内部の温度は沸点であ
る60℃以上には上昇しない。従って、撹拌槽内の温度
は、土着微生物が活動可能な温度で維持される。そし
て、発酵中の有機廃棄物に含まれる水分は蒸気となり、
この蒸気は減圧装置による槽内空気の吸引によって直接
槽外へ排出されるか、液化装置によって液化されて空気
と共に排出される。水分が排出されることにより有機廃
棄物の発酵が促進され、短時間で堆肥化する。
The fermentation of the organic waste in the stirring tank progresses, and the temperature rises due to the heat of the fermentation. When the temperature reaches a boiling point of 60 ° C., the substance boils and starts to evaporate. In addition, the heat of fermentation is sequentially changed to heat of vaporization at the boiling point, and is hardly accumulated while water is present in the stirring tank. Therefore, the temperature inside the stirring tank does not rise to 60 ° C. or higher, which is the boiling point. Therefore, the temperature in the stirring tank is maintained at a temperature at which indigenous microorganisms can be activated. And the water contained in the organic waste during fermentation becomes steam,
This vapor is discharged directly to the outside of the tank by suction of the air in the tank by the decompression device, or liquefied by the liquefaction device and discharged together with the air. The drainage of water promotes the fermentation of organic waste, and composts in a short time.

【0013】このように、撹拌槽の内部を減圧すること
により、内部の水分の沸点を下げることができ、蓄積さ
れる発酵熱は60℃程度の温度で気化熱に変わるので、
槽内の温度は土着微生物が活動可能な60℃程度の温度
で維持される。従って、比較的低い温度で活動し、高温
では死んでしまう土着微生物を堆肥化装置に使用するこ
とが可能となり、入手するのに費用がかからない土着微
生物を使用することにより堆肥を安価に製造することが
できる。
As described above, by reducing the pressure inside the stirring tank, the boiling point of the water inside can be lowered, and the accumulated fermentation heat is converted to heat of vaporization at a temperature of about 60 ° C.
The temperature in the tank is maintained at a temperature of about 60 ° C. at which indigenous microorganisms can act. Therefore, it is possible to use indigenous microorganisms that operate at a relatively low temperature and die at a high temperature in a composting device, and to produce inexpensive compost by using indigenous microorganisms that are inexpensive to obtain. Can be.

【0014】また、撹拌槽の温度が高温にならないの
で、撹拌槽等、各部において熱による劣化が起こりにく
く、耐久性が向上する。更に、高価な耐熱性材料を使用
する必要がないので、装置の製造コストも安価に抑える
ことができる。
In addition, since the temperature of the stirring tank does not become high, deterioration of each part such as the stirring tank due to heat hardly occurs, and the durability is improved. Further, since it is not necessary to use an expensive heat-resistant material, the manufacturing cost of the apparatus can be reduced.

【0015】撹拌装置の撹拌羽根に加温手段を備えてい
るものは、撹拌槽の内部を加温する際により効果的で迅
速な加温が可能である。
When the stirring blade of the stirring device is provided with a heating means, more effective and quick heating is possible when heating the inside of the stirring tank.

【0016】[0016]

【発明の実施の形態】本発明の実施の形態を図面に基づ
き更に詳細に説明する。図1は本発明に係る堆肥化装置
の実施の形態を示す正面図、図2は図1に示す堆肥化装
置の平面図、図3は図1に示す堆肥化装置の右側面図、
図4は撹拌槽及び撹拌羽根の構造を示す一部を断面した
要部説明図、図5は撹拌羽根の送り面の傾斜の組合せを
示す説明図、図6は取出し口に設けてある密閉装置の構
造を示し、(a)は側面図、(b)は平面図である。
Embodiments of the present invention will be described in more detail with reference to the drawings. 1 is a front view showing an embodiment of the composting device according to the present invention, FIG. 2 is a plan view of the composting device shown in FIG. 1, FIG. 3 is a right side view of the composting device shown in FIG.
4 is an explanatory view of a main part in which a part of the structure of a stirring tank and a stirring blade is shown, FIG. 5 is an explanatory view showing a combination of inclinations of feed surfaces of the stirring blade, and FIG. 6 is a sealing device provided at an outlet. (A) is a side view and (b) is a plan view.

【0017】符号Mは堆肥化装置で、H綱で形成された
台座9の上に取り付けてある。堆肥化装置Mは、撹拌装
置1と、加温装置2と、減圧装置である真空ポンプ3
と、液化装置4を備えている。撹拌装置1は、両端部が
塞がれた円筒形状の撹拌槽10を備えている。撹拌槽1
0は横置きに固定されている。撹拌槽10の外周部に
は、加温装置2を構成する蒸気通路20(図4参照)が
形成されている。蒸気通路20は、撹拌槽10の外周部
を螺旋状に周回するようにして設けてあり、撹拌槽10
の上部にあたる蒸気通路20の前後端部には、導入接続
管21と排出接続管22が設けてある。なお、蒸気通路
20の撹拌槽10の底部側には、四箇所にドレン23が
設けてある。
Reference numeral M denotes a composting device, which is mounted on a pedestal 9 formed of an H class. The composting device M includes a stirring device 1, a heating device 2, and a vacuum pump 3 as a decompression device.
And a liquefaction device 4. The stirring device 1 includes a cylindrical stirring tank 10 whose both ends are closed. Stirring tank 1
0 is fixed horizontally. A steam passage 20 (see FIG. 4) constituting the heating device 2 is formed on an outer peripheral portion of the stirring tank 10. The steam passage 20 is provided so as to spiral around the outer periphery of the stirring tank 10.
An inlet connection pipe 21 and a discharge connection pipe 22 are provided at the front and rear ends of the steam passage 20 corresponding to the upper part of the pipe. In addition, drains 23 are provided at four places on the bottom side of the stirring tank 10 in the steam passage 20.

【0018】撹拌槽10の上部には、蒸気通路20を貫
通して撹拌槽10の内部に通じる通管11、12、13
が三箇所に並設してある。図1における左側の通管は後
述するように液化装置4に接続する連結部となる。ま
た、右側の通管13はホッパー機能を有する蓋130を
設けて有機廃棄物の投入部となる。中央部の通管12は
設計変更時に対応するための予備で、通常は蓋120で
塞がれている。
In the upper part of the stirring tank 10, there are provided pipes 11, 12, 13 penetrating through the steam passage 20 and communicating with the inside of the stirring tank 10.
Are juxtaposed in three places. The passage on the left side in FIG. 1 serves as a connecting portion connected to the liquefaction apparatus 4 as described later. In addition, the right communication pipe 13 is provided with a lid 130 having a hopper function, and serves as an input section for organic waste. The central pipe 12 is a spare for coping with a design change, and is usually closed by a lid 120.

【0019】撹拌槽10の両端部には、上記したように
円形の端板14、15が設けられている。端板14、1
5の中心部分には、軸受装置140、150が設けてあ
る。軸受装置140、150には、端板14、15を貫
通して管状の回転軸16が軸支してある。回転軸16の
両側端部には、導入接続管160と排出接続管161が
設けてある。なお、回転軸16の図1において左側の導
入接続管160側には従動スプロケット162が設けて
ある。
At both ends of the stirring tank 10, the circular end plates 14, 15 are provided as described above. End plates 14, 1
5 are provided with bearing devices 140 and 150 in the center. Each of the bearing devices 140 and 150 has a tubular rotary shaft 16 that extends through the end plates 14 and 15. An inlet connection pipe 160 and a discharge connection pipe 161 are provided at both ends of the rotating shaft 16. A driven sprocket 162 is provided on the left side of the rotary shaft 16 in FIG.

【0020】回転軸16には、長さ方向に等間隔をもっ
て五箇所に撹拌羽根17が設けてある。撹拌羽根17
は、撹拌槽10の内径よりやや短い通気管170を備え
ている。通気管170はそれぞれ回転軸16を貫通して
取り付けてあり、その一端部には中空体である羽根体1
71を備えている。通気管170の内部は回転軸16内
部と通気可能に連通させてあり、羽根体171の内部は
同様に通気管170の内部と通気可能に連通させてあ
る。
The rotating shaft 16 is provided with stirring blades 17 at five locations at equal intervals in the longitudinal direction. Stirring blade 17
Is provided with a vent pipe 170 slightly shorter than the inner diameter of the stirring tank 10. Each of the ventilation pipes 170 is attached so as to penetrate through the rotary shaft 16, and has a hollow body 1 at one end thereof.
71 are provided. The inside of the ventilation pipe 170 is communicated with the inside of the rotating shaft 16 so as to be able to ventilate, and the inside of the blade body 171 is similarly communicated with the inside of the ventilation pipe 170 so as to be able to ventilate.

【0021】図5を参照する(なお、図5では説明の便
宜上、実際には周方向に異なった位置にある羽根体17
1を同一直線上に表している)。羽根体171は、断面
形状が三角形のものと平行四辺形のものがあり、一端側
の平行四辺形状の羽根体171を除いてそれらが交互に
配置されている。すなわち、図5における上部側の送り
面172は平行になり、下部側の送り面173はジグザ
グになる。そして、回転軸16がA方側へ回転するとき
には、有機廃棄物はa方向へ送られ、回転軸16がB方
向へ回転するときは、有機廃棄物は決まった方向へ移動
することがない。これにより、回転軸16をA方向へ回
転させて有機廃棄物を排出側へ送り、回転軸16をB方
向に回転させて有機廃棄物を撹拌する等、回転方向によ
って有機廃棄物の動きを制御することができる。
Referring to FIG. 5, (in FIG. 5, for convenience of explanation, the blades 17 which are actually located at different positions in the circumferential direction are referred to.
1 is on the same straight line). The blades 171 have a triangular cross-section and a parallelogram, and are alternately arranged except for the parallelogram-shaped blades 171 at one end. That is, the upper feed surface 172 in FIG. 5 is parallel, and the lower feed surface 173 is zigzag. When the rotating shaft 16 rotates in the direction A, the organic waste is sent in the direction a. When the rotating shaft 16 rotates in the direction B, the organic waste does not move in a fixed direction. Accordingly, the rotation of the rotating shaft 16 in the direction A sends the organic waste to the discharge side, and the rotating shaft 16 is rotated in the direction B to stir the organic waste. can do.

【0022】図6(a)、(b)を参照する。撹拌槽1
0の図1における右側の端板14の下部には、槽内でつ
くられた堆肥を取り出すための円形の取出し口18が設
けてある。取出し口18の外部側には、密閉装置19が
設けてある。密閉装置19は取出し口18の口縁部に対
応してこれを密閉する密閉蓋190を備えている。密閉
蓋190はガイド191に沿って進退する移行体192
に取り付けてある。移行体192はハンドル193を備
えたネジロッド194を回して進退させるようになって
いる。密閉蓋190は、有機廃棄物を発酵させるために
撹拌槽10の内部を減圧するときに塞がれ、できた堆肥
を排出するときには開けられる。
Referring to FIGS. 6A and 6B. Stirring tank 1
In the lower part of the right end plate 14 in FIG. 1 of FIG. 0, there is provided a circular take-out port 18 for taking out the compost made in the tank. A sealing device 19 is provided outside the outlet 18. The sealing device 19 is provided with a sealing lid 190 corresponding to the edge of the outlet 18 for sealing the outlet. The sealing lid 190 is provided with a transition body 192 that advances and retreats along a guide 191.
It is attached to. The transition body 192 is adapted to turn a screw rod 194 provided with a handle 193 to advance and retreat. The hermetic lid 190 is closed when the inside of the stirring tank 10 is depressurized in order to ferment the organic waste, and is opened when discharging the produced compost.

【0023】撹拌槽10の上部には、液化装置4が排出
側(図1において右側)がやや低くなるように傾斜させ
て固定されている。液化装置4は両端を封鎖した円筒体
内部に多数のパイプを平行に配置し、それらの隙間部分
に冷却水を流通させる公知構造を有しており、パイプに
蒸気を通してこれを冷却し、液化するものである。撹拌
槽10の通管11から導出された連結管110は液化装
置4の一端寄りに連結してあり、内部のパイプに通じて
いる。液化装置4に接続してある排出管41は、台座9
に撹拌槽10と並設してある真空ポンプ3の吸引側に接
続されている。
A liquefaction device 4 is fixed to the upper part of the stirring tank 10 so as to be inclined such that the discharge side (right side in FIG. 1) is slightly lower. The liquefaction apparatus 4 has a known structure in which a large number of pipes are arranged in parallel inside a cylindrical body whose both ends are closed, and cooling water is circulated through gaps between the pipes. Things. A connecting pipe 110 led out from the communicating pipe 11 of the stirring tank 10 is connected near one end of the liquefaction apparatus 4 and communicates with an internal pipe. The discharge pipe 41 connected to the liquefaction apparatus 4 is
Is connected to the suction side of the vacuum pump 3 provided in parallel with the stirring tank 10.

【0024】撹拌槽10の上部には、加温装置2を構成
する蒸気発生装置24(図2参照)が配置されている。
蒸気発生装置24と上記導入接続管21は接続管25に
よって接続されている。また、排出接続管22と上記回
転軸16の導入接続管160は接続管26で接続されて
いる。更に、排出接続管161には排出管27が接続し
てあり、排出管27は撹拌槽10の下方へ延長されて上
記各ドレン23が合流接続してある。
A steam generator 24 (see FIG. 2) constituting the heating device 2 is disposed above the stirring tank 10.
The steam generator 24 and the introduction connection pipe 21 are connected by a connection pipe 25. Further, the discharge connection pipe 22 and the introduction connection pipe 160 of the rotary shaft 16 are connected by a connection pipe 26. Further, a discharge pipe 27 is connected to the discharge connection pipe 161, and the discharge pipe 27 is extended below the stirring tank 10 so that the drains 23 are connected together.

【0025】台座9には、減速装置を備えた駆動モータ
ー7が撹拌槽10と並んで設けられている。駆動モータ
ー7の回転軸には駆動スプロケット70が取り付けてあ
る。駆動スプロケット70と、上記回転軸16に設けて
ある従動スプロケット162の間にはチェーン71が巻
掛けてある。
The pedestal 9 is provided with a drive motor 7 equipped with a speed reducer, alongside the stirring tank 10. A drive sprocket 70 is attached to the rotation shaft of the drive motor 7. A chain 71 is wound between the driving sprocket 70 and a driven sprocket 162 provided on the rotary shaft 16.

【0026】(作 用)図1ないし図6を参照して本発
明の堆肥化装置Mの作用を説明する。撹拌槽10の内部
に通管13から有機廃棄物である生ゴミが適量投入され
る。そして、この有機廃棄物に土着微生物が適量接種さ
れる。この土着部生物は、畑等の土壌に棲息するものを
培養した自家製のものが使用でき、入手に費用がかから
ない。蒸気発生装置24から接続管25を通り蒸気が送
られ、導入接続管21から蒸気通路20内に導入され
る。撹拌槽10の内部は、蒸気通路20内を通る蒸気に
よって加温される。
(Operation) The operation of the composting apparatus M of the present invention will be described with reference to FIGS. An appropriate amount of garbage, which is an organic waste, is charged into the stirring tank 10 through the conduit 13. Then, the organic waste is inoculated with an appropriate amount of indigenous microorganisms. As the indigenous organisms, home-grown organisms obtained by culturing those that inhabit the soil such as fields can be used, and there is no cost to obtain them. Steam is sent from the steam generator 24 through the connection pipe 25, and is introduced into the steam passage 20 from the introduction connection pipe 21. The inside of the stirring tank 10 is heated by steam passing through the steam passage 20.

【0027】排出接続管22から排出された蒸気は接続
管26を通り、導入接続管160から回転軸16の内部
に導入される。回転軸16内の蒸気は撹拌羽根17の内
部にも行きわたり、撹拌槽10の内部を加温する。排出
接続管161から排出された蒸気は排出管27を通り、
ドレン23から落ちる水滴と共に排出される。
The steam discharged from the discharge connecting pipe 22 passes through the connecting pipe 26 and is introduced into the rotary shaft 16 from the introducing connecting pipe 160. The steam in the rotating shaft 16 also reaches the inside of the stirring blade 17 and heats the inside of the stirring tank 10. The steam discharged from the discharge connection pipe 161 passes through the discharge pipe 27,
The water is discharged together with the water drops falling from the drain 23.

【0028】一方、駆動モーター7の作動により回転軸
16は回転し、撹拌羽根17により生ゴミは撹拌され
る。これによって、撹拌槽10の内部の生ゴミと土着微
生物は混合され、土着微生物の活動によって生ゴミの発
酵が始まる。また、撹拌槽10の内部は真空ポンプ3に
よって減圧される。この減圧は撹拌槽10内にある水の
沸点が60℃程度になるように行われる(実際上はほぼ
真空に近い状態まで減圧される)。なお、真空ポンプ3
により吸引される槽内空気は、連結管110から液化装
置4を通る。槽内空気には、後述する発酵熱により発生
する蒸気が含まれ、この蒸気は液化装置4で液化されて
気液分離が行われ、水は気体と共に真空ポンプ3により
吸引されて排出される。
On the other hand, the rotation shaft 16 is rotated by the operation of the drive motor 7, and the garbage is stirred by the stirring blade 17. Thereby, the garbage and the indigenous microorganisms inside the stirring tank 10 are mixed, and the fermentation of the garbage starts by the activity of the indigenous microorganisms. The pressure inside the stirring tank 10 is reduced by the vacuum pump 3. This depressurization is performed so that the boiling point of water in the stirring tank 10 becomes about 60 ° C. (in practice, the pressure is reduced to a state close to almost vacuum). The vacuum pump 3
The air in the tank sucked by is passed from the connecting pipe 110 to the liquefaction apparatus 4. The air in the tank contains steam generated by fermentation heat, which will be described later. This steam is liquefied by the liquefaction device 4 to perform gas-liquid separation, and the water is sucked and discharged by the vacuum pump 3 together with the gas.

【0029】撹拌槽10内の生ゴミの発酵が進み、その
発酵熱によって温度が上昇し、沸点である60℃に達す
ると沸騰し、蒸発を始める。また、発酵熱は、沸点にお
いて順次気化熱に変わり、撹拌槽10内に水があるうち
はほとんど蓄積されないので、撹拌槽10内部の温度は
沸点である60℃以上には上昇しない。従って、撹拌槽
10内の温度は、土着微生物が活動可能な温度で維持さ
れる。このようにして、発酵中の生ゴミに含まれる水分
が真空ポンプ3によって槽外へ排出される。これによ
り、生ゴミの発酵が促進され、短時間で堆肥化する。更
には、真空ポンプ3から排出される水(槽内空気に含ま
れる蒸気が液化したもの)を回収し、クーリングタワー
等の蒸発散装置により気化させ、残さ物を撹拌槽10の
内部へ戻し堆肥化する操作も可能である。
The fermentation of the garbage in the stirring tank 10 proceeds, and the temperature rises due to the heat of the fermentation. When the garbage reaches the boiling point of 60 ° C., it boils and starts to evaporate. Further, the fermentation heat is sequentially changed to heat of vaporization at the boiling point, and is hardly accumulated while water is present in the stirring tank 10, so that the temperature inside the stirring tank 10 does not rise to 60 ° C. or more, which is the boiling point. Therefore, the temperature in the stirring tank 10 is maintained at a temperature at which indigenous microorganisms can be activated. Thus, the moisture contained in the garbage being fermented is discharged out of the tank by the vacuum pump 3. Thereby, fermentation of garbage is promoted, and composting is performed in a short time. Further, the water discharged from the vacuum pump 3 (the liquefied vapor contained in the air in the tank) is collected and vaporized by an evaporator such as a cooling tower, and the residue is returned to the inside of the stirring tank 10 for composting. Operation is also possible.

【0030】なお、本明細書で使用している用語と表現
はあくまで説明上のものであって、限定的なものではな
く、上記用語、表現と等価の用語、表現を除外するもの
ではない。また、本発明は図示の実施の形態に限定され
るものではなく、技術思想の範囲内において種々の変形
が可能である。
The terms and expressions used in the present specification are merely illustrative, not restrictive, and do not exclude the terms and expressions equivalent to the above-mentioned terms and expressions. Further, the present invention is not limited to the illustrated embodiment, and various modifications are possible within the scope of the technical idea.

【0031】[0031]

【発明の効果】本発明は上記構成を備え、次の効果を有
する。 (a)本発明の堆肥化装置は、撹拌槽の内部を減圧する
ことにより、内部の水分の沸点を下げることができ、蓄
積される発酵熱は60℃程度の温度で気化熱に変わり、
槽内の温度は土着微生物が活動可能な温度で維持され
る。従って、比較的低い温度で活動し、高温では死んで
しまう土着微生物を堆肥化装置に使用することが可能と
なり、入手するのに費用がかからない土着微生物を使用
することにより堆肥を安価に製造することができる。
The present invention has the above configuration and has the following effects. (A) The composting device of the present invention can lower the boiling point of the water inside by reducing the pressure inside the stirring tank, and the accumulated fermentation heat changes to heat of vaporization at a temperature of about 60 ° C.,
The temperature in the tank is maintained at a temperature at which indigenous microorganisms can operate. Therefore, it is possible to use indigenous microorganisms that operate at a relatively low temperature and die at a high temperature in a composting device, and to produce inexpensive compost by using indigenous microorganisms that are inexpensive to obtain. Can be.

【0032】(b)撹拌槽の温度が高温にならないの
で、撹拌槽等、各部において熱による劣化が起こりにく
く、耐久性が向上する。更に、高価な耐熱性材料を使用
する必要がないので、装置の製造コストも安価に抑える
ことができる。
(B) Since the temperature of the stirring tank does not become high, deterioration of each part such as the stirring tank due to heat hardly occurs, and the durability is improved. Further, since it is not necessary to use an expensive heat-resistant material, the manufacturing cost of the apparatus can be reduced.

【0033】(c)撹拌装置の撹拌羽根に加温手段を備
えているものは、撹拌槽の内部を加温する際により効果
的で迅速な加温が可能である。
(C) A stirring device provided with a heating means in the stirring blade of the stirring device enables more effective and quick heating when heating the inside of the stirring tank.

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

【図1】本発明に係る堆肥化装置の実施の形態を示す正
面図。
FIG. 1 is a front view showing an embodiment of a composting device according to the present invention.

【図2】図1に示す堆肥化装置の平面図。FIG. 2 is a plan view of the composting apparatus shown in FIG.

【図3】図1に示す堆肥化装置の右側面図。FIG. 3 is a right side view of the composting apparatus shown in FIG.

【図4】撹拌槽及び撹拌羽根の構造を示す一部を断面し
た要部説明図。
FIG. 4 is an explanatory view of a main part in which a part of a structure of a stirring tank and a stirring blade is shown in section.

【図5】撹拌羽根の送り面の傾斜の組合せを示す説明
図。
FIG. 5 is an explanatory view showing a combination of inclinations of a feed surface of a stirring blade.

【図6】取出し口に設けてある密閉装置の構造を示し、
(a)は側面図、(b)は平面図。
FIG. 6 shows the structure of a sealing device provided at an outlet,
(A) is a side view, (b) is a plan view.

【符号の説明】[Explanation of symbols]

M 堆肥化装置 1 撹拌装置 10 撹拌槽 11、12、13 通管 110 連結管 120、130 蓋 14、15 端板 140、150 軸受装置 16 回転軸 160 回転軸 161 排出接続管 162 従動スプロケット 17 撹拌羽根 170 通気管 171 羽根体 172、173 送り面 18 取出し口 19 密閉装置 190 密閉蓋 191 ガイド 192 移行体 193 ハンドル 194 ネジロッド 2 加温装置 20 蒸気通路 21 導入接続管 22 排出接続管 23 ドレン 24 蒸気発生装置 25 接続管 26 接続管 27 排出管 3 真空ポンプ 4 液化装置 41 排出管 7 駆動モーター 70 スプロケット 71 チェーン 9 台座 M Composting device 1 Stirring device 10 Stirring tank 11, 12, 13 Through pipe 110 Connecting pipe 120, 130 Cover 14, 15 End plate 140, 150 Bearing device 16 Rotating shaft 160 Rotating shaft 161 Discharge connecting pipe 162 Driven sprocket 17 Stirring blade 170 Ventilation pipe 171 Blade body 172, 173 Sending surface 18 Outlet 19 Sealing device 190 Sealing lid 191 Guide 192 Transition body 193 Handle 194 Screw rod 2 Heating device 20 Steam passage 21 Inlet connection tube 22 Discharge connection tube 23 Drain 24 Steam generation device Reference Signs List 25 connection pipe 26 connection pipe 27 discharge pipe 3 vacuum pump 4 liquefier 41 discharge pipe 7 drive motor 70 sprocket 71 chain 9 pedestal

フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C05F 17/00 C05F 5/00 // C05F 5/00 9/00 9/00 B09B 3/00 ZABD (72)発明者 下瀬 眞一 山口県厚狭郡山陽町大字津布田1223番地の 4Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat II (reference) C05F 17/00 C05F 5/00 // C05F 5/00 9/00 9/00 B09B 3/00 ZABD (72) Inventor Shinichi Shimose 4 of 1223 Tsufuda, Sanyo-cho, Asa-gun, Yamaguchi

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 有機廃棄物を堆肥化する堆肥化装置であ
って、 撹拌槽(10)と撹拌羽根(17)を備えた撹拌装置(1) と、 上記撹拌槽(10)の内部を減圧する減圧装置と、を備えて
いることを特徴とする、 堆肥化装置。
A composting device for composting organic waste, comprising: a stirring device (1) having a stirring tank (10) and a stirring blade (17); And a pressure reducing device.
【請求項2】 有機廃棄物を堆肥化する堆肥化装置であ
って、 撹拌槽(10)と撹拌羽根(17)を備えた撹拌装置(1) と、 上記撹拌槽(10)の内部を加温する加温装置(2) と、 上記撹拌槽(10)の内部を減圧する減圧装置と、 上記減圧装置によって吸引される槽内空気に含まれる蒸
気を液化する液化装置(4) と、を備えていることを特徴
とする、堆肥化装置。
2. A composting device for composting organic waste, comprising: a stirring device (1) having a stirring tank (10) and a stirring blade (17); and an interior of the stirring tank (10). A heating device (2) for heating, a decompression device for decompressing the inside of the stirring tank (10), and a liquefaction device (4) for liquefying vapor contained in the air in the tank sucked by the decompression device. A composting device, comprising:
【請求項3】 上記撹拌装置(1) の撹拌羽根(17)に加温
手段を備えていることを特徴とする、 請求項2記載の堆肥化装置。
3. The composting device according to claim 2, wherein a heating means is provided on the stirring blade (17) of the stirring device (1).
【請求項4】 有機廃棄物の堆肥化方法であって、 撹拌槽(10)の内部を減圧して沸点を下げることにより土
着微生物が活動可能な温度を維持し、上記撹拌槽(10)の
内部で土着微生物によって有機廃棄物を発酵させて堆肥
化することを特徴とする、 有機廃棄物の堆肥化方法。
4. A method for composting organic waste, comprising reducing the boiling point by reducing the pressure inside the stirring tank (10) to maintain a temperature at which indigenous microorganisms can be activated. A method for composting organic waste, comprising fermenting organic waste internally with indigenous microorganisms to form a compost.
JP2000174286A 1997-09-30 2000-06-09 Composting device and method for composting organic waste Pending JP2001039787A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000174286A JP2001039787A (en) 1997-09-30 2000-06-09 Composting device and method for composting organic waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000174286A JP2001039787A (en) 1997-09-30 2000-06-09 Composting device and method for composting organic waste

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP28466097A Division JP3099269B2 (en) 1997-09-30 1997-09-30 Composting device and method of stirring organic waste in composting device

Publications (1)

Publication Number Publication Date
JP2001039787A true JP2001039787A (en) 2001-02-13

Family

ID=18676358

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000174286A Pending JP2001039787A (en) 1997-09-30 2000-06-09 Composting device and method for composting organic waste

Country Status (1)

Country Link
JP (1) JP2001039787A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1273561A4 (en) * 2000-03-15 2005-01-26 Japan Noble Systems Inc Method and apparatus for producing organic fertilizer
US7497392B2 (en) 2006-07-17 2009-03-03 Alliance Technology Group, Inc. Process and apparatus for transforming waste materials into fuel
WO2019087931A1 (en) * 2017-10-30 2019-05-09 株式会社下瀬微生物研究所 Shell treatment device and shell treatment method
US11458414B2 (en) 2013-10-13 2022-10-04 Synergy Burcell Technologies, Llc Methods and apparatus utilizing vacuum for breaking organic cell walls

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1273561A4 (en) * 2000-03-15 2005-01-26 Japan Noble Systems Inc Method and apparatus for producing organic fertilizer
US7497392B2 (en) 2006-07-17 2009-03-03 Alliance Technology Group, Inc. Process and apparatus for transforming waste materials into fuel
US8034132B2 (en) 2006-07-17 2011-10-11 Visiam, Llc Process and apparatus for transforming waste materials into fuel
US11458414B2 (en) 2013-10-13 2022-10-04 Synergy Burcell Technologies, Llc Methods and apparatus utilizing vacuum for breaking organic cell walls
WO2019087931A1 (en) * 2017-10-30 2019-05-09 株式会社下瀬微生物研究所 Shell treatment device and shell treatment method

Similar Documents

Publication Publication Date Title
CN1062254C (en) Stereoscopic multi-layer multi-purpose fermentation device
CN111659711B (en) Household garbage pretreatment device and pretreatment method thereof
CN108191474A (en) A kind of animal wastes harmless resource recycles intelligent processing system and method
CN105503311A (en) Integrated high-temperature aerobiotic organic waste processor
JP3370306B2 (en) Organic waste treatment method and apparatus
JPH0947747A (en) Method for vacuum drying and fermenting organic waste at high speed and device therefor
CN210419798U (en) Organic fertilizer fermentation device convenient to operate
JP2001039787A (en) Composting device and method for composting organic waste
CN110551626A (en) Controllable horizontal solid state fermentation jar of humiture
JPH11106277A (en) Composting apparatus and composting of organic waste
JPH10258265A (en) High speed vacuum drying and fermentation method for organic waste
CN214528762U (en) Agaricus bisporus residue compost fermentation equipment
JP2004130181A (en) Agitator in organic waste treatment apparatus
CN114213168A (en) Organic waste low-emission micro-oxygen fermentation equipment
CN106431543A (en) Bio-fertilizer continuous production equipment
CN113149384A (en) Sludge aerobic fermentation device
CN213680431U (en) Sophora alopecuroide retting fertilizer fermentation device
JP2004169957A (en) Dry treatment method for waste with high moisture content
CN219656523U (en) Copanlisib production drying equipment
JP3782316B2 (en) Garbage disposal equipment
CN217809259U (en) Biochar preparation device
CN220597346U (en) Fertilizer degradation equipment
CN211005158U (en) High-efficient agricultural fertilizer fermentation equipment
CN217732922U (en) Be used for beasts and birds excrement and urine aerobic fermentation equipment
JP3075312U (en) Organic waste drying equipment

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20040929

A711 Notification of change in applicant

Free format text: JAPANESE INTERMEDIATE CODE: A711

Effective date: 20041105

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A821

Effective date: 20041105

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20060815

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20061205

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20070403