JPH11156332A - Garbage fermentation treatment equipment - Google Patents

Garbage fermentation treatment equipment

Info

Publication number
JPH11156332A
JPH11156332A JP9344054A JP34405497A JPH11156332A JP H11156332 A JPH11156332 A JP H11156332A JP 9344054 A JP9344054 A JP 9344054A JP 34405497 A JP34405497 A JP 34405497A JP H11156332 A JPH11156332 A JP H11156332A
Authority
JP
Japan
Prior art keywords
tank
refuse
fermentable
fermenter
heater
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
JP9344054A
Other languages
Japanese (ja)
Inventor
Kazuo Nibu
一夫 丹生
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.)
NITechno Co Ltd
Original Assignee
NITechno 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 NITechno Co Ltd filed Critical NITechno Co Ltd
Priority to JP9344054A priority Critical patent/JPH11156332A/en
Publication of JPH11156332A publication Critical patent/JPH11156332A/en
Pending legal-status Critical Current

Links

Classifications

    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
    • Y02P60/87—Re-use of by-products of food processing for fodder production

Landscapes

  • Fodder In General (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

(57)【要約】 【課題】 ごみ発酵処理装置に於て、発酵性ごみと包装
食品、トレイ、ビニル、セロハン、割り箸等の非発酵性
ごみが混在したまま投入・発酵処理できるようにし、か
つ、処理後に完熟粉体と非発酵物とに自動的に分離でき
るようにする。 【解決手段】 発酵槽2と発酵槽2の下流側の完熟槽4
と、発酵槽2の槽壁外面に付設される第1ヒータ5と、
完熟槽4の槽壁外面に付設される第2ヒータと、発酵槽
2内の発酵性ごみと非発酵性ごみを破砕しつつ攪拌する
第1回転羽根9と、完熟槽4内の発酵性ごみと非発酵性
ごみを攪拌する第2回転羽根10と、発酵処理済品を完熟
粉体11と非発酵物12とに分離する篩い機13と、を備え
る。
(57) [Summary] PROBLEM TO BE SOLVED: In a refuse fermentation treatment apparatus, fermentable refuse and non-fermentable refuse such as packaged food, tray, vinyl, cellophane, disposable chopsticks, etc. are mixed and fermented, After the treatment, it can be automatically separated into a mature powder and a non-fermented product. SOLUTION: The fermenter 2 and a mature tank 4 downstream of the fermenter 2 are provided.
A first heater 5 attached to the outer surface of the tank wall of the fermenter 2,
A second heater attached to the outer surface of the tank wall of the ripe tub 4, a first rotary blade 9 for stirring and crushing the fermentable refuse and the non-fermentable refuse in the fermentation tub 2, and the fermentable refuse in the ripe tub 4 And a second rotating blade 10 for stirring the non-fermentable refuse, and a sieving machine 13 for separating the fermented product into a mature powder 11 and a non-fermented product 12.

Description

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

【0001】[0001]

【発明の属する技術分野】この発明はごみ発酵処理装置
に関する。
TECHNICAL FIELD The present invention relates to a refuse fermentation treatment apparatus.

【0002】[0002]

【従来の技術】従来、畜産施設から排出する畜糞、魚市
場や魚屋等から排出する魚屑、市場やレストラン等から
排出する野菜屑、家庭、ホテル、スーパー等から排出す
る生ごみ、及び、その他のごみを、短期間で発酵処理す
る装置として、発酵槽内にブロワー、温風ヒータ等によ
り温風吹き込みを行い、温風量を変えることにより温度
制御して、投入直後のごみを加熱させて発酵させるもの
が知られている。また、発酵熱により温められた排気ガ
スを熱交換して給気ガスを予熱する装置をさらに付設し
たもの等が公知であった。
2. Description of the Related Art Conventionally, animal waste discharged from livestock facilities, fish waste discharged from fish markets and fish stores, vegetable waste discharged from markets and restaurants, garbage discharged from households, hotels, supermarkets, and others. As a device for fermenting garbage in a short period of time, blow air into the fermenter with a blower, hot air heater, etc., control the temperature by changing the amount of hot air, and heat the garbage immediately after throwing in the fermentation. What causes them to be known. Further, there has been known a device further provided with a device for preheating the supply gas by exchanging heat with the exhaust gas heated by fermentation heat.

【0003】[0003]

【発明が解決しようとする課題】しかし、上述のような
従来のごみ発酵処理装置では、セロハン、ビニール、ト
レイ等、あるいは、それらにて包装された食品、さらに
は、瓶詰め飲料の栓等を分離処理することができず、非
発酵性ごみを人の手で取り除いてから発酵性ごみのみを
発酵槽内に投入しなければならなかったので、不便であ
った。また、温風を直接発酵槽内に送り込むものでは、
微生物に必要な空気量、水分蒸発に必要な空気量に対し
て10倍以上の加熱用空気量が必要となり、排気ガスの脱
臭設備の規模が大きくなってしまうという問題があっ
た。さらに、熱電導効果を高めるために、発酵槽の下方
に温風吹き出し口が設けられていたが、温度制御のため
に温風量を変化させることにより吹き出し口の目詰まり
が発生し、長期間の安定稼働ができなかった。
However, in the above-mentioned conventional garbage fermentation treatment apparatus, cellophane, vinyl, trays, etc., or food packaged therewith, and further, bottled beverage stoppers, etc. are separated. It was inconvenient because it could not be treated and only the fermentable waste had to be thrown into the fermenter after removing the non-fermentable waste by hand. In the case of sending hot air directly into the fermenter,
The amount of air required for heating microorganisms and the amount of air for heating that is 10 times or more the amount of air required for evaporating moisture are required, and there is a problem that the scale of the deodorizing equipment for exhaust gas becomes large. Furthermore, in order to enhance the heat conduction effect, a hot air outlet was provided below the fermenter, but the outlet was clogged by changing the amount of hot air for temperature control, resulting in a long-term discharge. Stable operation was not possible.

【0004】[0004]

【課題を解決するための手段】本発明は上述の問題を解
決するため、発酵性ごみと非発酵性ごみが投入される開
閉可能な投入口を有する密閉状の発酵槽と、該発酵槽の
下流側に配設されると共にごみ排出口を有する密閉状の
完熟槽と、上記発酵槽の槽壁外面に付設されて該槽壁を
介して発酵槽内を加温する第1ヒータと、上記完熟槽の
槽壁外面に付設されて該槽壁を介して完熟槽内を加温す
る第2ヒータと、上記発酵槽内の発酵性ごみと非発酵性
ごみを破砕しつつ攪拌する第1回転羽根と、上記完熟槽
内の発酵性ごみと非発酵性ごみを攪拌する第2回転羽根
と、を備える。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention provides a hermetically sealed fermenter having an openable / closable inlet into which fermentable refuse and non-fermentable refuse are charged; A hermetically-sealed ripe tank provided downstream and having a waste discharge port, a first heater attached to an outer surface of a tank wall of the fermenter and heating the inside of the fermenter via the tank wall; A second heater attached to the outer surface of the tank wall of the ripe tank and heating the inside of the ripe tank via the tank wall; and a first rotation for crushing and stirring the fermentable and non-fermentable waste in the fermentation tank. A blade, and a second rotating blade that stirs the fermentable refuse and the non-fermentable refuse in the mature tank.

【0005】また、完熟槽から排出される発酵処理済品
を完熟粉体と非発酵物とに分離する篩い機を備え、該篩
い機に完熟粉体を所定重量に袋詰めする袋詰め機を連結
する。
A sieving machine for separating the fermented product discharged from the ripening tank into a ripened powder and a non-fermented material is provided, and the sieving machine is provided with a bagging machine for bagging the ripened powder to a predetermined weight. Link.

【0006】また、発酵槽と完熟槽が隣接して設けら
れ、該発酵槽と完熟槽の間に、オーバーフロー口を有す
る区画壁が設けられている。また、発酵槽の容積が完熟
槽の容積よりも大きく設定され、かつ、第1ヒータの発
熱量が第2ヒータの発熱量よりも大きく設定されてい
る。
[0006] Further, a fermentation tank and a ripe tank are provided adjacent to each other, and a partition wall having an overflow port is provided between the fermentation tank and the ripe tank. Further, the volume of the fermenter is set larger than the volume of the mature tank, and the heat value of the first heater is set larger than the heat value of the second heater.

【0007】また、第1回転羽根が、発酵槽と完熟槽に
貫通状に設けられると共に共通駆動源に連結されて水平
軸心廻りに回転駆動される軸部の発酵槽側に、複数形成
され、かつ、第2回転羽根が、上記軸部の完熟槽側に複
数形成されている。また、発酵槽内を発酵最適温度に維
持する温度制御手段と、発酵槽・完熟槽の槽壁外面に夫
々付設された第1ヒータ・第2ヒータを外側から包囲す
る保温材とを備える。
A plurality of first rotating blades are formed on the fermenter tank side of a shaft portion which is provided in a penetrating manner in the fermenter tank and the ripe tank and is connected to a common drive source and driven to rotate about a horizontal axis. Further, a plurality of second rotating blades are formed on the side of the mature portion of the shaft portion. The fermenter includes temperature control means for maintaining the inside of the fermenter at an optimum fermentation temperature, and a heat insulating material surrounding the first heater and the second heater respectively provided on the outer surfaces of the tank walls of the fermenter and the ripe tank.

【0008】[0008]

【発明の実施の形態】以下、図面に基づいて本発明を詳
しく説明する。図1と図2と図3は本発明に係るごみ発
酵処理装置の実施の一形態を示し、この装置は、発酵性
ごみと非発酵性ごみが投入される開閉可能な投入口1を
有する密閉状の発酵槽2と、その発酵槽2の下流側に配
設されると共に自動開閉蓋付きのごみ排出口3を有する
密閉状の完熟槽4と、発酵槽2の槽壁外面に付設されて
その槽壁を介して発酵槽2内を加温する第1ヒータ5
と、完熟槽4の槽壁外面に付設されてその槽壁を介して
完熟槽4内を加温する第2ヒータ6と、発酵槽2内の発
酵性ごみ7と非発酵性ごみ8を破砕しつつ攪拌する第1
回転羽根9と、完熟槽4内の発酵性ごみ7と非発酵性ご
み8を攪拌する第2回転羽根10と、完熟槽4から排出さ
れる発酵処理済品を完熟粉体11と非発酵物12とに分離す
る篩い機13と、を備えている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in detail with reference to the drawings. 1, 2 and 3 show an embodiment of a waste fermentation treatment apparatus according to the present invention, which has a closed and openable inlet 1 into which fermentable waste and non-fermentable waste are introduced. Fermentation tank 2, a hermetically sealed ripe tank 4 which is disposed downstream of the fermentation tank 2 and has a refuse discharge port 3 with an automatic opening / closing lid, and which is attached to the outer surface of the tank wall of the fermentation tank 2. A first heater 5 for heating the inside of the fermenter 2 via the tank wall
And a second heater 6 attached to the outer surface of the tank wall of the ripe tank 4 and heating the inside of the ripe tank 4 through the tank wall, and crushing the fermentable waste 7 and the non-fermentable waste 8 in the fermentation tank 2. The first to stir while stirring
The rotating blades 9, the second rotating blades 10 for stirring the fermentable refuse 7 and the non-fermentable refuse 8 in the ripening tank 4, and the fermented product discharged from the ripening tank 4 into the ripe powder 11 And a sieving machine 13 that separates the sifter 12 from the sifter 12.

【0009】発酵槽2と完熟槽4は、断面形状U字状の
弯曲壁部14とその弯曲壁部14の左右両端部に配設される
鉛直壁部15, 15と弯曲壁部14と鉛直壁部15, 15の上端縁
に形成される外鍔部16とから成る上方開口状の外槽壁17
の内部を、上部にオーバーフロー口20, 20を有する区画
壁18にて2区画に分けて、さらに、外槽壁17の上方開口
部を上蓋体19にて施蓋して、形成される。
The fermentation tank 2 and the ripe tank 4 are formed by a curved wall portion 14 having a U-shaped cross section, and vertical wall portions 15 and 15 disposed on both left and right ends of the curved wall portion 14, and a vertical wall portion formed by the curved wall portion 14. An outer tank wall 17 having an upper opening shape and comprising an outer flange portion 16 formed at the upper edge of the wall portions 15 and 15
Is divided into two sections by a partition wall 18 having overflow ports 20, 20 at the upper part, and the upper opening of the outer tank wall 17 is covered with an upper lid 19.

【0010】つまり、発酵槽2と完熟槽4は隣接して設
けられ、発酵槽2と完熟槽4の間に、オーバーフロー口
20, 20を切欠形成した区画壁18が設けられている。さら
に、発酵槽2の容積が完熟槽4の容積よりも大きく設定
される。例えば、発酵槽2の容積を完熟槽4の容積の4
〜6倍程度に設定する。また、外槽壁17の内、発酵槽2
を成す部分の上部に吸気口21が設けられる。吸気口21の
近傍には、吸気用温風ヒータ49が設けられる。さらに、
外層壁17に排気口47が設けられる。
That is, the fermenter 2 and the ripe tank 4 are provided adjacent to each other, and an overflow port is provided between the fermenter 2 and the ripe tank 4.
A partition wall 18 having notches 20 and 20 is provided. Further, the volume of the fermenter 2 is set to be larger than the volume of the mature tank 4. For example, the volume of the fermenter 2 is set to 4 times the volume of the
Set to about 6 times. In the outer tank wall 17, the fermenter 2
An intake port 21 is provided above the portion that forms In the vicinity of the intake port 21, an intake hot air heater 49 is provided. further,
An exhaust port 47 is provided in the outer layer wall 17.

【0011】また、このごみ発酵処理装置は、発酵槽2
・完熟槽4の槽壁外面に夫々付設された第1ヒータ5・
第2ヒータ6を外側から包囲する保温材23を有してい
る。図例では、1枚の保温材23にて第1ヒータ5と第2
ヒータ6の両方を包囲しているが、第1ヒータ5と第2
ヒータ6を別々の保温材23にて包囲してもよい。また、
投入口1近傍に開閉を検知するセンサー48を設け、その
センサー48を、所定時間(例えば48時間)投入口1の開
閉がない場合は、攪拌用のモータ、通気用のブロワー、
及び、第1ヒータ5と第2ヒータ6の電源を自動的にO
FFとするタイマー手段に、電気的に接続する。なお、
電源が自動的にOFFされた後でも、投入口1の開閉に
よりタイマー手段がリセットされて通常運転を開始す
る。
[0011] The refuse fermentation treatment apparatus comprises a fermenter 2
First heaters 5 attached to the outer surface of the tank wall of the ripe tank 4
It has a heat insulating material 23 surrounding the second heater 6 from the outside. In the illustrated example, the first heater 5 and the second heater
It surrounds both heaters 6, but the first heater 5 and the second
The heater 6 may be surrounded by a separate heat insulating material 23. Also,
A sensor 48 for detecting opening / closing is provided in the vicinity of the inlet 1, and the sensor 48 is provided with a motor for stirring, a blower for ventilation, when there is no opening / closing of the inlet 1 for a predetermined time (for example, 48 hours).
Also, the power of the first heater 5 and the second heater 6 is automatically turned on.
The FF is electrically connected to timer means. In addition,
Even after the power is automatically turned off, the opening and closing of the inlet 1 resets the timer means and starts the normal operation.

【0012】さらに、図2に示すように、発酵槽2内を
発酵最適温度に維持する温度制御手段24を設ける。温度
制御手段24は、第1温度検出器27と第2温度検出器28
と、第1温度設定器29と第2温度設定器30と、ヒータ運
転操作器31と、を備える。第1温度検出器27は発酵槽2
内のごみ26(発酵性ごみ7)の温度を検出し、温度信号
を第1温度設定器29に送る。また、第2温度検出器28
は、第1ヒータ5によって加熱される槽壁の内面(又は
外面)に取付けられ、槽壁内面の温度を検出し、温度信
号を第2温度設定器30に送る。第1温度設定器29と第2
温度設定器30は、各々、上限温度設定値、下限温度設定
値を持ち、第1ヒータ5の作動と停止を行うヒータ運転
操作器31を制御する。
Further, as shown in FIG. 2, a temperature control means 24 for maintaining the inside of the fermenter 2 at an optimum fermentation temperature is provided. The temperature control means 24 includes a first temperature detector 27 and a second temperature detector 28.
, A first temperature setter 29, a second temperature setter 30, and a heater operation controller 31. The first temperature detector 27 is the fermenter 2
The temperature of the refuse 26 (fermentable refuse 7) is detected, and a temperature signal is sent to the first temperature setting device 29. In addition, the second temperature detector 28
Is attached to the inner surface (or outer surface) of the tank wall heated by the first heater 5, detects the temperature of the inner surface of the tank wall, and sends a temperature signal to the second temperature setting device 30. 1st temperature setter 29 and 2nd
The temperature setter 30 has an upper limit temperature set value and a lower limit temperature set value, respectively, and controls a heater operation controller 31 for operating and stopping the first heater 5.

【0013】制御方法は、槽壁(鉄皮)温度が第1温度
設定器29の上限温度設定値になるまでは、第1ヒータ5
を運転して槽壁内面温度が第2温度設定器30の上限温度
設定値に達すると運転を停止し、第2温度設定器30の下
限温度設定値まで低下すると再び運転する。そして、槽
壁温度が第1温度設定器29の上限温度設定値以上に上昇
した時には、槽壁温度が第1温度設定器29の下限温度設
定値になるまで、第2温度設定器30からの信号に関係な
く第1ヒータ5の運転を停止し、その下限温度設定値に
まで低下すると、運転を再開する。
The control method is as follows: until the temperature of the tank wall (steel shell) reaches the upper limit temperature set value of the first temperature setter 29, the first heater 5
The operation is stopped when the inner wall surface temperature of the bath wall reaches the upper limit temperature set value of the second temperature setter 30, and the operation is resumed when the temperature falls to the lower limit temperature set value of the second temperature setter 30. Then, when the bath wall temperature rises above the upper limit temperature set value of the first temperature setter 29, the second temperature setter 30 is operated until the bath wall temperature reaches the lower limit temperature set value of the first temperature setter 29. The operation of the first heater 5 is stopped irrespective of the signal, and when the temperature drops to the lower limit temperature set value, the operation is restarted.

【0014】ここで、各温度設定器29,30の上限、下限
温度設定値を、処理物を発酵最適温度に維持する値とす
る。例えば、処理物温度、即ち、第1温度設定器29の上
限設定値は、菌を死滅させない90℃以下、下限設定値
は、発酵菌の最も活動する40℃以上、及び、槽壁の内面
温度、即ち、第2温度設定器30の上限設定値は 100℃以
下、下限設定値は40℃以上とすることが望ましい。
Here, the upper and lower limit temperature set values of the temperature setting devices 29 and 30 are set to values at which the processed material is maintained at the optimum fermentation temperature. For example, the temperature of the processed material, that is, the upper limit set value of the first temperature setting device 29 is 90 ° C. or less that does not kill bacteria, the lower limit set value is 40 ° C. or more where fermentation bacteria are most active, and the inner surface temperature of the tank wall. That is, it is desirable that the upper limit set value of the second temperature setter 30 be 100 ° C. or less and the lower limit set value be 40 ° C. or more.

【0015】また、図3に示すように、完熟槽4内の温
度を制御する温度制御手段25を設ける。その温度制御手
段25は、発酵槽2の温度制御手段24と同様の構造とさ
れ、第1温度検出器32と第2温度検出器33と、第1温度
設定器34と第2温度設定器35と、ヒータ運転操作器36
と、を備える。そして、第2ヒータ6は、第1ヒータ5
と同様の制御がなされる。また、第1ヒータ5の発熱量
を第2ヒータ6の発熱量よりも大きく設定する。具体的
には、第1ヒータ5の発熱量を第2ヒータ6の発熱量に
対して2〜5倍大きく設定するのが好ましい。例えば、
第1ヒータ5として1.3kwのヒータを9個使用し、第
2ヒータ6として0.3 kwのヒータを9個使用する。な
お、図3に示した温度制御手段25を省略して、図2に示
した温度制御手段24のみにて、第1ヒータ5と第2ヒー
タ6の作動を制御して、発酵槽2内の温度制御と完熟槽
4内の温度制御を行うように構成しても良い。なお、面
状ヒータ、シースヒータ又は温水、蒸気の使用に依り均
一加熱方式としても良い。
Further, as shown in FIG. 3, a temperature control means 25 for controlling the temperature in the ripe bath 4 is provided. The temperature control means 25 has the same structure as the temperature control means 24 of the fermenter 2, and includes a first temperature detector 32, a second temperature detector 33, a first temperature setter 34 and a second temperature setter 35. And the heater operation controller 36
And. The second heater 6 is connected to the first heater 5
The same control as described above is performed. Further, the heat value of the first heater 5 is set to be larger than the heat value of the second heater 6. Specifically, it is preferable to set the heat generation amount of the first heater 5 to 2 to 5 times larger than the heat generation amount of the second heater 6. For example,
Nine 1.3 kW heaters are used as the first heater 5, and nine 0.3 kW heaters are used as the second heater 6. Note that the temperature control means 25 shown in FIG. 3 is omitted, and the operation of the first heater 5 and the second heater 6 is controlled only by the temperature control means 24 shown in FIG. The temperature control and the temperature control in the ripe bath 4 may be performed. It is to be noted that a uniform heating method may be used depending on the use of a planar heater, a sheath heater or hot water or steam.

【0016】次に、図1と図2と図3に示すように、第
1回転羽根9が、発酵槽2と完熟槽4に貫通状に設けら
れると共に共通駆動源に連結されて水平軸心50廻りに回
転駆動される軸部37の発酵槽2側に、複数形成され、か
つ、第2回転羽根10が、軸部37の完熟槽4側に複数形成
されている。
Next, as shown in FIG. 1, FIG. 2 and FIG. 3, the first rotating blades 9 are provided in the fermentation tank 2 and the ripe tank 4 in a penetrating manner and are connected to a common driving source so as to be horizontal axis center. A plurality of shafts 37 that are driven to rotate around 50 are formed on the fermenter 2 side, and a plurality of second rotary blades 10 are formed on the shaft 37 on the side of the mature tank 4.

【0017】軸部37の一端部には、図示省略のスプロケ
ットが固着され、そのスプロケットと、共通駆動源とし
てのモーターの出力軸に固着された小径のスプロケット
にチェーンを懸架して、軸部37を回転駆動可能とする。
A sprocket (not shown) is fixed to one end of the shaft 37, and a chain is suspended between the sprocket and a small-diameter sprocket fixed to an output shaft of a motor as a common drive source. Can be driven to rotate.

【0018】第1回転羽根9と第2回転羽根10は、野
菜、ハム、チーズ、ソーセージ等の包装食品、あるい
は、セロハン、ビニール、トレイ、割り箸、ビール栓等
から成る非発酵性ごみ8や、野菜、肉類、加工食品等の
生ごみからなる発酵性ごみ7の固まりを破砕できるよう
な形状(例えば帯板状、又は棒状)に形成される。な
お、軸部37に複数本の細棒状の攪拌用パドルを形成し、
その攪拌用パドルの先端部にリボン状の攪拌羽根を橋絡
状に取付けて第1回転羽根9と第2回転羽根10を構成し
てもよい。
The first rotating blade 9 and the second rotating blade 10 are used for packaging food such as vegetables, ham, cheese, sausage, or non-fermentable garbage 8 composed of cellophane, vinyl, tray, split chopsticks, beer stopper, etc. It is formed into a shape (for example, a strip or a bar) that can break up the lump of the fermentable garbage 7 made of garbage such as vegetables, meats and processed foods. In addition, a plurality of thin rod-shaped stirring paddles are formed on the shaft portion 37,
The first rotating blade 9 and the second rotating blade 10 may be configured by attaching a ribbon-shaped stirring blade to the tip of the stirring paddle in a bridging manner.

【0019】また、図1に示すように、完熟槽4のごみ
排出口3の外側に排出シュート39が設けられ、その排出
シュート39の先端開口部の下方に上方開口状の篩い機13
が配設される。その篩い機13に、完熟粉体11を計量して
所定重量に袋詰めする袋詰機40を連結する。袋詰機40
は、篩い機13の下方に設けられると共にビニール袋等の
完熟粉体収納袋41が収納される袋詰部42と、袋詰部42の
下方に配設される計量器43と、を備える。また、篩い機
13の近傍に、非発酵性ごみ収納箱44を配置する。
As shown in FIG. 1, a discharge chute 39 is provided outside the waste discharge port 3 of the ripe tub 4, and an upper opening sieving machine 13 is provided below the opening of the tip of the discharge chute 39.
Is arranged. To the sieving machine 13, a bagging machine 40 for weighing the mature powder 11 and bagging it to a predetermined weight is connected. Bagging machine 40
Is provided with a bag filling section 42 provided below the sieving machine 13 and for accommodating a ripe powder storage bag 41 such as a plastic bag, and a measuring device 43 provided below the bag filling section 42. Also sieving machine
A non-fermentable refuse storage box 44 is arranged near 13.

【0020】また、このごみ発酵処理装置は、図4のブ
ロック図に示すように、発酵槽2にごみを自動的に投入
する自動投入手段45を備える。
Further, as shown in the block diagram of FIG. 4, the refuse fermentation treatment apparatus includes an automatic input means 45 for automatically inputting refuse to the fermenter 2.

【0021】次に、このごみ発酵処理装置の作動を、図
5のフローチャート図を参照しつつ説明する。まず、図
4に示した自動投入手段45にて、発酵槽2に発酵性ごみ
7と非発酵性ごみ8が混在したごみを投入する。このと
き、発酵・熟成に関与する微生物を混入させる。そのよ
うな微生物としては、糖分分解菌、蛋白質分解菌、セル
ロース分解菌及びリグニン分解菌等があげられる。ま
た、無機系塩基性物質、天然有機物、及び、薬剤の全て
の組合せを発酵性材とし、ごみに混入させるのも好まし
い。さらには、脱臭作用を有する微生物を混入させるの
が望ましい。
Next, the operation of the refuse fermentation treatment apparatus will be described with reference to the flowchart of FIG. First, garbage in which fermentable garbage 7 and non-fermentable garbage 8 are mixed is fed into the fermenter 2 by the automatic charging means 45 shown in FIG. At this time, microorganisms involved in fermentation / ripening are mixed. Examples of such microorganisms include sugar-degrading bacteria, protein-degrading bacteria, cellulose-degrading bacteria, and lignin-degrading bacteria. It is also preferable that all combinations of inorganic basic substances, natural organic substances, and drugs are used as fermentable materials and mixed with garbage. Further, it is desirable to mix microorganisms having a deodorizing effect.

【0022】そして、図1と図2に示すように、発酵槽
2内の第1回転羽根9を回転させ、ごみを破砕しつつ攪
拌する。即ち、野菜、ハム、チーズ、ソーセージ等の包
装食品や、セロハン、ビニール、トレイ、箸、ビール栓
等の非発酵性ごみ8、さらには、発酵性ごみ7の固まり
を、第1回転羽根9が破砕しつつ攪拌する。この際、第
1回転羽根9は、3〜30分間の正回転と、同時間の逆回
転を、回転方向変更時に数秒〜数十秒間の停止時間をと
りながら繰り返す。また、ごみ投入と同時に第1ヒータ
5と温度制御手段24により、発酵槽2内が発酵最適温度
に維持され、発酵性ごみ7の発酵を促進する。具体的に
は、発酵性ごみ7の種類に応じて、槽内壁面温度で40℃
以上 100℃以下の値に維持される。
Then, as shown in FIG. 1 and FIG. 2, the first rotating blade 9 in the fermenter 2 is rotated to agitate while crushing refuse. That is, the first rotating blades 9 pack the packaged foods such as vegetables, ham, cheese, sausage, etc., the non-fermentable refuse 8 such as cellophane, vinyl, tray, chopsticks, and beer stoppers, and the fermentable refuse 7. Stir while crushing. At this time, the first rotating blade 9 repeats the forward rotation for 3 to 30 minutes and the simultaneous reverse rotation while taking a stop time of several seconds to several tens seconds when changing the rotation direction. In addition, the fermenter 2 is maintained at the optimum fermentation temperature by the first heater 5 and the temperature control means 24 at the same time as the refuse is supplied, and the fermentation of the fermentable refuse 7 is promoted. Specifically, according to the type of fermentable garbage 7, the inner wall temperature of the tank is 40 ° C.
It is maintained at a value of 100 ° C or higher.

【0023】また、発酵槽2から溢れた発酵処理物(ご
み)は、図1と図3に示すように、オーバーフロー口20
を通って完熟槽4に入る。その処理物は、完熟槽4内の
第2回転羽根10にて攪拌され、かつ、第2ヒータ6と温
度制御手段25にて発酵最適温度に維持されつつ完熟す
る。そして、処理済のごみが完熟槽4からごみ排出口3
を通って排出シュート39へと溢れ出て、篩い機13に入
る。なお、排出口3は処理物投入時から2〜4時間は開
状態とされ、その間、オーバーフローにより完熟槽4か
ら篩い機13へと処理物が出る。発酵処理済品は、篩い機
13にて、完熟粉体11と非発酵物12とに分離され、完熟粉
体11は袋詰機40の完熟粉体収納袋41に収納され、非発酵
物12は非発酵性ごみ収納箱44に収納される。
The fermentation product (garbage) overflowing from the fermentation tank 2 is filled with an overflow port 20 as shown in FIGS.
And enters the maturation tank 4. The treated product is agitated by the second rotating blades 10 in the maturation tank 4 and matures while being maintained at the optimum fermentation temperature by the second heater 6 and the temperature control means 25. Then, the processed waste is discharged from the mature tank 4 to the waste outlet 3
Through the discharge chute 39 and into the sieving machine 13. The discharge port 3 is kept open for 2 to 4 hours from the input of the processed material. During this time, the processed material flows out of the mature tank 4 to the sieving machine 13 due to overflow. Fermented products are sieving machines
At 13, the mature powder 11 is separated into the non-fermented product 12 and the mature powder 11 is stored in the mature powder storage bag 41 of the bagging machine 40, and the non-fermented product 12 is stored in the non-fermentable garbage storage box 44. Is stored in.

【0024】なお、排出口3が開状態の間は篩い機13が
作動し、排出口3が閉状態のときは篩い機13が停止す
る。その後、袋41が所定重量(例えば25kg〜30kg)に達
すると計量器43が警告音又は警告灯を作動させると共に
ごみ排出口3を自動的に閉じる。そして、作業者が袋41
を取り出す。その後、空の袋41を袋詰機40にセットし、
さらにその後、排出口3を開く。こうして、2〜4時間
の時間が経過するか、処理物の排出が無くなるかの何れ
かにより、処理物の取り出しが完了する。
The sieving machine 13 operates while the discharge port 3 is open, and stops when the discharge port 3 is closed. Thereafter, when the bag 41 reaches a predetermined weight (for example, 25 kg to 30 kg), the weighing device 43 activates a warning sound or a warning light and automatically closes the dust discharge port 3. Then, the worker enters the bag 41
Take out. After that, set the empty bag 41 in the bagging machine 40,
Thereafter, the outlet 3 is opened. In this way, the removal of the processed material is completed when either the time of 2 to 4 hours elapses or the discharge of the processed material stops.

【0025】なお、処理物の破砕、攪拌と保温は、発酵
槽2と完熟槽4にて、夫々、24〜48時間程度行うのが好
ましい。また、第1回転羽根9と第2回転羽根10の回転
方向変更における停止時間は、発酵性ごみ7の種類に応
じて30分〜3時間程度の範囲内で調整する。
It is preferable that the crushing, stirring, and keeping of the temperature of the treated material are performed in the fermenter 2 and the ripe tank 4 for about 24 to 48 hours, respectively. The stop time in changing the rotation direction of the first rotating blade 9 and the second rotating blade 10 is adjusted within a range of about 30 minutes to 3 hours depending on the type of the fermentable waste 7.

【0026】また、連続攪拌モードに切換えて長時間
(48時間以上)連続的に攪拌することもできる。このと
き、吸気口21近傍の吸気用温風ヒータ49を作動させる。
これにより、ウィークエンド等の処理量の多い場合で
も、通常の2倍近い処理能力のアップが得られる。ま
た、寒冷地に於ける冬季発酵処理時の結露防止と、発酵
促進効果(発酵の長時間化の防止効果)が得られる。
Further, by switching to the continuous stirring mode, the stirring can be continuously performed for a long time (48 hours or more). At this time, the hot air heater 49 for intake near the intake port 21 is operated.
As a result, even when the processing amount is large, such as during a weekend, the processing capacity can be almost doubled. In addition, dew condensation can be prevented during the winter fermentation treatment in a cold region, and a fermentation accelerating effect (an effect of preventing a prolonged fermentation) can be obtained.

【0027】次に、図6は、本発明に係るごみ発酵処理
装置の他の実施の形態におけるブロック図を示し、発酵
槽2に連通連結される脱臭手段22と、完熟粉体が収納さ
れた袋を密封する袋密封器46を、備える。他の構成は図
1〜図5に記載したものと同様である。脱臭手段22は、
脱臭部と排気ファンを有し、排気ファンを駆動させるこ
とによって、外気が吸気口から発酵槽2と完熟槽4に入
り、蒸発水分と臭気を含む気体が排気口から出て脱臭手
段22を通り、ほぼ脱臭された気体が大気に出る。袋密封
器46は、例えば、ビニール圧着器又はミシン機から成
る。即ち、完熟体収納袋としてビニール製の袋又は紙袋
を使用し、完熟体収納後に開口部を圧着又はミシン止め
して密封する。
FIG. 6 is a block diagram showing another embodiment of the refuse fermentation treatment apparatus according to the present invention, in which a deodorizing means 22 communicatively connected to the fermenter 2 and a mature powder are stored. A bag sealer 46 for sealing the bag is provided. Other configurations are the same as those described in FIGS. 1 to 5. The deodorizing means 22 is
It has a deodorizing section and an exhaust fan, and by driving the exhaust fan, outside air enters the fermentation tank 2 and the mature tank 4 from the intake port, and gas containing evaporated moisture and odor passes through the exhaust port and passes through the deodorizing means 22. , Almost deodorized gas goes to the atmosphere. The bag sealer 46 is composed of, for example, a vinyl crimping machine or a sewing machine. That is, a vinyl bag or a paper bag is used as the fully matured body storage bag, and after the fully matured body is stored, the opening is pressed or machined and sealed.

【0028】なお、図7に示すように、回転羽根70(第
1回転羽根9、第2回転羽根10)の横断面形状を、鋭利
な角部71、71を有する形状(図例では横断面ひし形)と
しても良い。つまり、発酵性ごみ7と、この発酵性ごみ
7を包装する非発酵性ごみ8とを同時に投入して、これ
を破砕して発酵させる横断面が鋭利な角部71、71を有す
る回転羽根70を備えた発酵槽2、及び完熟槽4を具備す
る。これにより、樹脂シートや紙等で包装された包装食
品をそのまま投入しても確実に破砕でき、内容有機物
(発酵性ごみ7)の完熟処理が可能となる。
As shown in FIG. 7, the cross-sectional shape of the rotary blade 70 (the first rotary blade 9 and the second rotary blade 10) is changed to a shape having sharp corners 71, 71 (in the illustrated example, a cross-sectional shape). (Rhombus). In other words, the fermentable refuse 7 and the non-fermentable refuse 8 for packaging the fermentable refuse 7 are simultaneously charged, and the crushed and fermented refuse 8 is rotated by a rotating blade 70 having sharp corners 71, 71. And a fermentation tank 4 provided with a fermentation tank. Thereby, even if the packaged food packaged with a resin sheet, paper, or the like is input as it is, it can be reliably crushed, and the content organic matter (fermentable waste 7) can be fully matured.

【0029】なお、本発明は上述の実施の形態以外にも
設計変更可能であり、例えば、ごみ(発酵性ごみ7)の
ペーハーが発酵適正範囲を外れた場合にペーハー調整剤
を投入するペーハー調整剤投入器を、付設してもよい。
また、自動投入手段45を省略して、人の手にてごみを投
入するように構成してもよい。また、脱臭手段22、計量
器43、袋密封器46、篩い機13を省略してもよい場合があ
る。
The present invention can be modified in design other than the above-mentioned embodiment. For example, when the pH of the garbage (fermentable garbage 7) is out of the proper range for fermentation, the pH adjustment is performed by adding a pH adjusting agent. An agent dispenser may be provided.
Further, the automatic input means 45 may be omitted, and the refuse may be input manually. In some cases, the deodorizing means 22, the measuring device 43, the bag sealer 46, and the sieving machine 13 may be omitted.

【0030】[0030]

【発明の効果】本発明は、上述の構成により次に示すよ
うな著大な効果を奏する。
The present invention has the following remarkable effects by the above-mentioned structure.

【0031】(請求項1によれば、)装置全体の構造が
簡単になると共に規模を比較的小さくすることができ
る。かつ、長期間安定して使用でき、メンテナンスが楽
である。さらに、野菜、肉類、加工食品等からなる発酵
性ごみ7と、包装食品、セロハン、ビニール、トレイ、
箸、ビール栓等の非発酵性ごみ8が混在したごみをその
まま投入することができる。しかも、短い時間で効率良
く、これらのごみ7を発酵処理できる。即ち、投入した
ごみを投入から24〜48時間という短期間で、堆肥あるい
は飼料(完熟粉体11)として取り出すことができる。
According to the first aspect, the structure of the entire apparatus can be simplified and the scale can be relatively small. In addition, it can be used stably for a long time, and maintenance is easy. Furthermore, fermentable garbage 7 consisting of vegetables, meat, processed food, etc., packaged food, cellophane, vinyl, tray,
Garbage in which non-fermentable garbage 8 such as chopsticks and beer stoppers are mixed can be introduced as it is. In addition, the waste 7 can be fermented efficiently in a short time. That is, the introduced refuse can be taken out as compost or feed (ripe powder 11) within a short period of 24 to 48 hours after the introduction.

【0032】(請求項2によれば、)投入したごみを、
発酵した完熟粉体11と非発酵物12との2種類に、自動的
に分離することができる。従って、その後の処理が容易
となる。 (請求項3によれば、)発酵槽2から完熟槽4へと順次
発酵が進むので、ごみの投入を連続して行うことができ
る。
(According to claim 2), the input waste is
The fermented ripe powder 11 and the non-fermented material 12 can be automatically separated into two types. Therefore, subsequent processing becomes easy. (According to claim 3) Since the fermentation proceeds sequentially from the fermenter 2 to the fully matured tank 4, refuse can be continuously supplied.

【0033】(請求項4によれば、)発酵に重点が置か
れて、連続的な流れとしてのバランスが良く、全体とし
て能率的にごみを処理できる。 (請求項5によれば、)発酵に最適の温度に常時維持可
能となり、一層ごみ処理の能率が向上する。 (請求項6によれば、)加温のためのエネルギー消費量
を節約できる。 (請求項7によれば、)発酵性ごみ7と、非発酵性ごみ
8が混在したごみを、そのまま投入し、粉砕できる。か
つ、駆動源が1台で済み、全体の簡素化を図りうる。
The emphasis is on fermentation (according to claim 4), the balance as a continuous stream is good, and the waste can be efficiently treated as a whole. (According to claim 5), it is possible to always maintain the optimum temperature for fermentation, and the efficiency of waste treatment is further improved. (According to claim 6) Energy consumption for heating can be saved. (According to claim 7) Garbage in which fermentable garbage 7 and non-fermentable garbage 8 are mixed can be directly introduced and pulverized. In addition, only one drive source is required, and the entire system can be simplified.

【0034】(請求項8によれば、)処理済物(完熟粉
体11)を自動的に袋詰めすることができる。かつ、一定
重量なので、その後の処理及び取扱いが容易となる。 (請求項9によれば、)樹脂シートや紙等で包装された
包装食品をそのまま投入しても確実に破砕でき、内容有
機物(発酵性ごみ7)の完熟処理が可能となる。
(According to claim 8), the processed product (the mature powder 11) can be automatically bagged. In addition, since the weight is constant, subsequent processing and handling are easy. (According to claim 9) Even if a packaged food packaged with a resin sheet, paper, or the like is supplied as it is, it can be reliably crushed, and the content organic matter (fermentable waste 7) can be fully matured.

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

【図1】本発明の実施の一形態を示す一部破断した斜視
図である。
FIG. 1 is a partially broken perspective view showing one embodiment of the present invention.

【図2】発酵槽の断面図である。FIG. 2 is a sectional view of a fermenter.

【図3】完熟槽の断面図である。FIG. 3 is a sectional view of a ripe bath.

【図4】装置全体の構成を示すブロック図である。FIG. 4 is a block diagram illustrating a configuration of the entire apparatus.

【図5】処理方法のフローチャート図である。FIG. 5 is a flowchart of a processing method.

【図6】他の実施の形態に於ける全体構成を示すブロッ
ク図である。
FIG. 6 is a block diagram showing an overall configuration according to another embodiment.

【図7】回転羽根の拡大断面図である。FIG. 7 is an enlarged sectional view of a rotary blade.

【符号の説明】[Explanation of symbols]

1 投入口 2 発酵槽 3 ごみ排出口 4 完熟槽 5 第1ヒータ 6 第2ヒータ 7 発酵性ごみ 8 非発酵性ごみ 9 第1回転羽根 10 第2回転羽根 11 完熟粉体 12 非発酵物 13 篩い機 18 区画壁 20 オーバーフロー口 23 保温材 24 温度制御手段 37 軸部 40 袋詰機 50 水平軸心 70 回転羽根 71 角部 DESCRIPTION OF SYMBOLS 1 Input port 2 Fermenter 3 Garbage discharge 4 Ripe tank 5 First heater 6 Second heater 7 Fermentable waste 8 Non-fermentable waste 9 First rotating blade 10 Second rotating blade 11 Ripe powder 12 Non-fermented material 13 Sieve Machine 18 Partition wall 20 Overflow port 23 Insulation material 24 Temperature control means 37 Shaft 40 Bagging machine 50 Horizontal axis 70 Rotating blade 71 Corner

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】 発酵性ごみ7と非発酵性ごみ8が投入さ
れる開閉可能な投入口1を有する密閉状の発酵槽2と、
該発酵槽2の下流側に配設されると共にごみ排出口3を
有する密閉状の完熟槽4と、上記発酵槽2の槽壁外面に
付設されて該槽壁を介して発酵槽2内を加温する第1ヒ
ータ5と、上記完熟槽4の槽壁外面に付設されて該槽壁
を介して完熟槽4内を加温する第2ヒータ6と、上記発
酵槽2内の発酵性ごみ7と非発酵性ごみ8を破砕しつつ
攪拌する第1回転羽根9と、上記完熟槽4内の発酵性ご
み7と非発酵性ごみ8を攪拌する第2回転羽根10と、を
備えたことを特徴とするごみ発酵処理装置。
1. A closed fermenter 2 having an openable / closable inlet 1 into which fermentable refuse 7 and non-fermentable refuse 8 are charged;
A hermetically sealed ripe tank 4 which is disposed downstream of the fermenter 2 and has a refuse discharge port 3, and which is attached to the outer surface of the tank wall of the fermenter 2 and passes through the fermenter 2 through the tank wall. A first heater 5 for heating, a second heater 6 attached to the outer surface of the tank wall of the mature tank 4 for heating the inside of the mature tank 4 through the tank wall, and fermentable waste in the fermenter tank 2 7 and a first rotating blade 9 for crushing and stirring the non-fermentable refuse 8, and a second rotating blade 10 for stirring the fermentable refuse 7 and the non-fermentable refuse 8 in the maturation tank 4. A garbage fermentation treatment apparatus characterized by the above-mentioned.
【請求項2】 完熟槽4から排出される発酵処理済品を
完熟粉体11と非発酵物12とに分離する篩い機13を、備え
ている請求項1記載のごみ発酵処理装置。
2. The garbage fermentation treatment apparatus according to claim 1, further comprising a sieving machine for separating the fermented product discharged from the ripening tank into a ripened powder and a non-fermented product.
【請求項3】 発酵槽2と完熟槽4が隣接して設けら
れ、該発酵槽2と完熟槽4の間に、オーバーフロー口20
を有する区画壁18が設けられている請求項1記載のごみ
発酵処理装置。
3. A fermenter 2 and a ripe tank 4 are provided adjacent to each other, and an overflow port 20 is provided between the fermenter 2 and the ripe tank 4.
The refuse fermentation treatment apparatus according to claim 1, further comprising a partition wall (18) having:
【請求項4】 発酵槽2の容積が完熟槽4の容積よりも
大きく設定され、かつ、第1ヒータ5の発熱量が第2ヒ
ータ6の発熱量よりも大きく設定されている請求項1記
載のごみ発酵処理装置。
4. The capacity of the fermenter tank 2 is set to be larger than the capacity of the ripe tank 4 and the calorific value of the first heater 5 is set to be larger than the calorific value of the second heater 6. Garbage fermentation treatment equipment.
【請求項5】 発酵槽2内を発酵最適温度に維持する温
度制御手段24が設けられている請求項4記載のごみ発酵
処理装置。
5. The garbage fermentation treatment apparatus according to claim 4, further comprising temperature control means for maintaining the inside of the fermenter 2 at an optimum fermentation temperature.
【請求項6】 発酵槽2・完熟槽4の槽壁外面に夫々付
設された第1ヒータ5・第2ヒータ6を外側から包囲す
る保温材23を有している請求項1記載のごみ発酵処理装
置 。
6. The refuse fermentation according to claim 1, further comprising a heat insulating material surrounding the first heater and the second heater from the outside, which are respectively provided on the outer surfaces of the tank walls of the fermentation tank and the ripe tank. Processing equipment.
【請求項7】 第1回転羽根9が、発酵槽2と完熟槽4
に貫通状に設けられると共に共通駆動源に連結されて水
平軸心50廻りに回転駆動される軸部37の発酵槽2側に、
複数形成され、かつ、第2回転羽根10が、上記軸部37の
完熟槽4側に複数形成されている請求項1記載のごみ発
酵処理装置。
7. The first rotating blade 9 comprises a fermentation tank 2 and a ripe tank 4
The shaft 37 which is provided in a penetrating shape and is connected to a common driving source and is rotated around the horizontal axis 50 is provided on the fermenter 2 side.
2. The refuse fermentation treatment apparatus according to claim 1, wherein a plurality of the plurality of second rotating blades are formed on the side of the mature tank 4 of the shaft portion 37. 3.
【請求項8】 完熟槽4から排出される処理済品を完熟
粉体11と非発酵物12とに分離する篩い機13を、備え、該
篩い機13に、完熟粉体11を計量して所定重量に袋詰めす
る袋詰機40が連結されている請求項1記載のごみ発酵処
理装置。
8. A sieving machine 13 for separating the treated product discharged from the ripening tank 4 into a ripened powder 11 and a non-fermented product 12, and the sifter 13 weighs the ripened powder 11 2. The garbage fermentation treatment apparatus according to claim 1, wherein a bag filling machine 40 for packing bags to a predetermined weight is connected.
【請求項9】 発酵性ごみ7と、この発酵性ごみ7を包
装する非発酵性ごみ8とを同時投入して、これを破砕し
て発酵させる横断面が鋭利な角部71、71を有する回転羽
根70を備えた発酵槽2、及び完熟槽4、を具備すること
を特徴とするごみ発酵処理装置。
9. A fermentable refuse 7 and a non-fermentable refuse 8 for packaging the fermentable refuse 7 are simultaneously supplied, and the crushed and fermented refuse 8 has sharp corner portions 71, 71 for crushing and fermenting. A refuse fermentation treatment apparatus comprising: a fermentation tank 2 having a rotary blade 70;
JP9344054A 1997-11-27 1997-11-27 Garbage fermentation treatment equipment Pending JPH11156332A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9344054A JPH11156332A (en) 1997-11-27 1997-11-27 Garbage fermentation treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9344054A JPH11156332A (en) 1997-11-27 1997-11-27 Garbage fermentation treatment equipment

Publications (1)

Publication Number Publication Date
JPH11156332A true JPH11156332A (en) 1999-06-15

Family

ID=18366304

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9344054A Pending JPH11156332A (en) 1997-11-27 1997-11-27 Garbage fermentation treatment equipment

Country Status (1)

Country Link
JP (1) JPH11156332A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100678382B1 (en) 2005-10-13 2007-02-02 순천대학교 산학협력단 Sound insulation
CN105834193A (en) * 2016-04-01 2016-08-10 浙江华庆元生物科技有限公司 Organic garbage microorganism treatment device
CN107671105A (en) * 2017-09-25 2018-02-09 常州波纳斯风力发电设备科技有限公司 Intelligent kitchen garbage treater and application method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100678382B1 (en) 2005-10-13 2007-02-02 순천대학교 산학협력단 Sound insulation
CN105834193A (en) * 2016-04-01 2016-08-10 浙江华庆元生物科技有限公司 Organic garbage microorganism treatment device
CN107671105A (en) * 2017-09-25 2018-02-09 常州波纳斯风力发电设备科技有限公司 Intelligent kitchen garbage treater and application method

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