JP3870558B2 - Operation method of garbage processing machine - Google Patents

Operation method of garbage processing machine Download PDF

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Publication number
JP3870558B2
JP3870558B2 JP19444098A JP19444098A JP3870558B2 JP 3870558 B2 JP3870558 B2 JP 3870558B2 JP 19444098 A JP19444098 A JP 19444098A JP 19444098 A JP19444098 A JP 19444098A JP 3870558 B2 JP3870558 B2 JP 3870558B2
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Prior art keywords
garbage
stirring
ventilation
flooring
stop
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JP2000024626A (en
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哲朗 渡邊
道夫 金井塚
良和 青江
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Mitsubishi Materials Corp
Diatech Co Ltd
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Mitsubishi Materials Corp
Diatech Co Ltd
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    • 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
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    • Y02W30/78Recycling of wood or furniture waste

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Description

【0001】
【発明の属する技術分野】
本発明は生ゴミ処理機の運転方法に係り、特に、微生物の作用によって生ゴミを分解・消滅させる生ゴミ処理機を良好な状態で長期に亘り安定に運転する方法に関する。
【0002】
【従来の技術】
従来、微生物を利用して生ゴミを分解・消滅させる生ゴミ処理機では、分解槽にオガクズなどの床材を適量入れ、そこに微生物を棲息させて、槽内に投入した生ゴミを二酸化炭素、水、アンモニアなどの低分子物質にまで分解して消滅させる。このような消滅型の生ゴミ処理機においては、床材中に棲息している微生物に対して酸素の供給が必要であり、そのために分解槽に空気を供給したり、床材を撹拌機で撹拌することが行われる。
【0003】
図1に、この生ゴミ処理機の構成を示す。この生ゴミ処理機では、吸引ブロア1によって分解槽(醗酵槽)2内の空気を吸引することによって、分解槽2の上部側壁に設けられた入気口3から空気を取り入れると共に、撹拌機で床材(図示せず)を撹拌することによって床材中の微生物に酸素を供給する。この床材への酸素供給を効率的に行うために、撹拌には槽内に水平に配置された撹拌軸4に丸棒形状の撹拌羽根4を螺旋状に突設した撹拌機を用い、この撹拌機を、正転→停止→逆転→停止のサイクルで回転させ、床材を左右に移動させて、槽内内容物を十分に均一に混合する。なお、図1において、6は生ゴミの投入口、7は撹拌機のモータ、8は分解槽2内を分解に適当な温度に保つためのパネルヒータ、9はフィルタ、10は排気管、11は風量調整コック、12は断熱材、13は排出口、14は制御盤である。
【0004】
【発明が解決しようとする課題】
このような生ゴミ処理機において、生ゴミを分解槽の大きさに対して適正量となるよう投入した場合、一般に、運転開始から1〜2週間は生ゴミは二酸化炭素、水、アンモニアにまで効率的に分解されるが、次第に分解が進まなくなり、槽内に酸が生成し激烈な悪臭を発生するようになる。この原因としては、投入される生ゴミが多くの場合酸性で、生ゴミの投入を継続するに従って、床材のpHが次第に低下し、これにより微生物の活性が低下すること;撹拌によってオガクズなどの床材が粉砕されてしまい、微生物が棲息しにくくなること;このように粉状に粉砕された床材が撹拌によりこねられることによって団子状に固まり、この結果、微生物に酸素供給がされにくくなること;休日などで生ゴミが投入されないにもかかわらず、生ゴミの定期的な投入を前提として水分調整が適切に行われるようにブロアによる通気量や撹拌時間が設定されているために、床材が過剰に乾燥し、微生物の不活性化や担体の微粉化を促進してしまうこと;が考えられる。
【0005】
本発明は上記従来の問題点を解決し、微生物の作用によって生ゴミを分解・消滅させる生ゴミ処理機を良好な状態で長期に亘り安定に運転することができる生ゴミ処理機の運転方法を提供することを目的とする。
【0006】
【課題を解決するための手段】
本発明の生ゴミ処理機の運転方法は、内部に床材を収容する生ゴミ分解槽と、該分解槽内に設けられた撹拌軸及び該撹拌軸に螺旋状に突設された複数の棒状の撹拌羽根よりなる撹拌機と、該分解槽内への通気手段とを備える生ゴミ処理機に、生ゴミを投入し、前記撹拌機により槽内内容物を間欠的に撹拌すると共に前記通気手段により槽内の通気を行って生ゴミを分解処理する生ゴミ処理機の運転方法において、次の▲1▼〜▲5▼の条件をすべて採用するものである。
【0007】
▲1▼ 運転開始時に、床材に対して、長期間効果が持続するpH調整材として、床材をpH8〜9程度の弱アルカリ性に長期間維持するために軽量発泡コンクリート(以下「ALC」と略記する。)を添加混合する。ALCとしては粒径が1〜10mmのものが好ましく、その初期投入量は床材に対して1/10〜1/15容量倍とするのが好ましい。
▲2▼ pH調整材の効果を更に長期間持続させるために、ALCを25〜40日に1回の頻度で分解槽に追加投入する。このALCの追加投入量は床材量に対して1/25〜1/50容量倍とするのが好ましい。
▲3▼ 水分の蒸散を損なうことなく、撹拌を穏やかにして担体の粉砕を防止するために、撹拌羽根の突設間隔を100〜200mmとする。
▲4▼ 床材として、酸素供給効率を改善するための空隙材として、また、撹拌により粉砕されにくい微生物の担体として木質チップをオガクズに混合して用いる。木質チップとしては、粒径が20〜50mmのものが好ましく、その初期投入量はオガクズに対して1/2〜1/4容量倍とするのが好ましい。
▲5▼ 休日などで生ゴミが投入されない場合の床材の過剰乾燥を防止するために、生ゴミの投入頻度に応じて、例えば、次のように間欠撹拌の間隔及び通気量を制御する。
(i) 24時間以内に生ゴミの投入がある場合: 間欠撹拌の時間間隔を撹拌:停止=1:1〜1.5とすると共に、連続的な通気を行う。
(ii) 24〜48時間内に生ゴミの投入がある場合: 間欠撹拌の時間間隔を撹拌:停止=1:2〜2.5とすると共に、連続的な通気を行う。
(iii) 48〜72時間以内に生ゴミの投入がある場合: 間欠撹拌の時間間隔を撹拌:停止=1:4〜8とすると共に、通気:通気停止=1:10〜15の時間間隔の間欠通気を行う。
(iv) 72時間以上生ゴミの投入がない場合: 間欠撹拌の時間間隔を撹拌:停止=1:50〜60とすると共に、通気:通気停止=1:50〜60の時間間隔の間欠通気を行う。
【0008】
上記▲1▼〜▲5▼の条件をすべて採用することによって、初めて、長期間生ゴミの分解・消滅を安定かつ良好に行うことが可能となる。これらの条件のうち、一つでも欠けた場合には床材のpH低下、担体の微粉化、過剰乾燥のいずれかが起こり、長期間に亘る安定運転を維持することはできなくなる。
【0009】
【発明の実施の形態】
以下に本発明の実施の形態を詳細に説明する。
【0010】
本発明においては、図1に示すような生ゴミ処理機により生ゴミを分解・消滅処理するに当り、前記▲1▼〜▲5▼の条件をすべて採用する。
【0011】
即ち、まず、生ゴミ処理機の運転開始に当って(即ち、初発において)、オガクズなどの床材に長期間効果が持続するpH調整材としてALCを混入させる。これにより床材のpHは8〜9程度の弱アルカリ性に長期間維持される。このALCの粒度は1〜10mm程度でなるべく粗目のものを使用する。粉状のALCでは反応しやすくすぐに溶解してしまうため、効果が持続しない。ALCの混入量は、容積比で床材10〜15に対してALC1程度が適当である。ALCがこの範囲よりも少ないとpH調整能力が乏しく、この範囲を超えると床材の粘性を増加させて団粒化を促進してしまう。
【0012】
また、初発のALCによるpH調整効果を更に長期間持続させるために、ALCを運転開始から25〜40日に一回の頻度で追加投入する。この追加投入の頻度が40日を超えると、床材のpHが低下してしまう恐れがあり、一度pHが低下してしまうと、ALCを投入してもpHは一時的に回復するものの、すぐに再び低下してしまい、pH調整効果が得られなくなる。追加投入の頻度が25日未満では、床材の粘性を増加させて団粒化を促進してしまう。なお、ALCの追加投入量は、床材のpHを7〜9程度に維持できる程度であれば良く、その追加投入頻度にもよるが、一般的には床材量に対して1/25〜1/50容量倍程度とするのが好ましい。
【0013】
また、担体の粉砕を防止するために撹拌を穏やかにする目的で、螺旋状に配置した丸棒型撹拌羽根の突設間隔を100〜200mmに設定する。この間隔が100mm未満では担体の粉砕を促進してしまい、200mmを超えると水分の蒸散が不足し、床材の水分調整が適切に行われなくなる。この撹拌羽根の間隔は、生ゴミ処理機の容量等によっても異なるが、分解槽容量300〜750L程度の生ゴミ処理機の場合、特に100〜120mm程度とするのが好ましい。
【0014】
また、オガクズなどの床材に、酸素供給を改善するための空隙材として、また粉砕されない微生物の担持体として木質チップを混入させる。この木質チップの粒径は20〜50mm程度が適当であり、20mm未満では短期間で粉砕されてしまい、50mmを超えるとオガクズの粉砕を促進してしまう。木質チップの混入量は容積比でオガクズ2〜4に対して木質チップ1程度が適当であり、この範囲より少ないと混入による効果が得られず、この範囲より多いと床材の水分調整が満足に行えなくなる。
【0015】
更に、休日などで生ゴミが投入されない場合に起こる床材の過剰乾燥を防止するために休日モードを設定する。投入蓋の開閉によって生ゴミの投入状態を認識し、一定時間以上開かない場合に、正転→停止→逆転→停止による間欠撹拌のインターバルを長くしていく。また、同時に通気量を制御して過剰乾燥を防止する。
【0016】
例えば、次のような制御を行う。
(i) 24時間以内に生ゴミの投入がある場合: 間欠撹拌の時間間隔を撹拌:停止=1:1〜1.5とすると共に、連続的な通気を行う。
(ii) 24〜48時間内に生ゴミの投入がある場合: 間欠撹拌の時間間隔を撹拌:停止=1:2〜2.5とすると共に、連続的な通気を行う。
(iii) 48〜72時間以内に生ゴミの投入がある場合: 間欠撹拌の時間間隔を撹拌:停止=1:4〜8とすると共に、通気:通気停止=1:10〜15の時間間隔の間欠通気を行う。
(iv) 72時間以上生ゴミの投入がない場合: 間欠撹拌の時間間隔を撹拌:停止=1:50〜60とすると共に、通気:通気停止=1:50〜60の時間間隔の間欠通気を行う。
【0017】
上記範囲より多い頻度で撹拌や通気を行った場合、床材の過剰乾燥が進行してしまい、上記範囲よりも少ないと微生物に供給する酸素が不足してしまい、微生物の活性が大きく低下してしまう。
【0018】
なお、その他の処理条件としては、次のような条件を採用するのが好ましい。
分解槽内ヒータ設定温度:30〜40℃
撹拌時の撹拌速度 :1〜3rpm
通気時の通気量 :300〜1000L/分
1回当りの生ゴミ投入量:床材量に対して1/10〜1/7容量倍
床材の水分含有率 :25〜35%
【0019】
【実施例】
以下に実施例及び比較例を挙げて本発明をより具体的に説明する。
【0020】
実施例1
図1に示す生ゴミ処理機(分解槽容量500L、床材量300L)により以下の条件を採用して、生ゴミ(野菜屑20%、残飯類80%)の分解を行った。
【0021】
なお、生ゴミは1日1回30kg投入した。ただし、10〜15日目、30〜35日目、81〜85日目には、長期休暇を想定して生ゴミの投入を行わなかった。また、撹拌機による撹拌は前半の如く、正転→停止→逆転→停止→………とした。
【0022】
[1] 初発にALC(粒径10〜20mm)をALC:床材=1:10の割合で添加混合して、初期pHを8.8とする。
[2] 床材量の1/40のALCを図2に示す如く、約30日間隔で追加投入する。
[3] 撹拌羽根の突設間隔を110mmとする。
[4] 床材として、オガクズに木質チップ(粒径20〜50mm)をチップ:オガクズ=1:3の割合で混合する。
[5] 間欠撹拌の間隔及び通気量を次の通りに制御する。
(i) 24時間以内に生ゴミの投入がある場合: 間欠撹拌の時間間隔を撹拌:停止=5分:5分とすると共に、連続的な通気を行う。
(ii) 24〜48時間内に生ゴミの投入がある場合: 間欠撹拌の時間間隔を撹拌:停止=5分:10分とすると共に、連続的な通気を行う。
(iii) 48〜72時間以内に生ゴミの投入がある場合: 間欠撹拌の時間間隔を撹拌:停止=5分:30分とすると共に、通気:通気停止=5分:55分の時間間隔の間欠通気を行う。
(iv) 72時間以上生ゴミの投入がない場合: 間欠撹拌の時間間隔を撹拌:停止=5分:55分とすると共に、通気:通気停止=1分:59分の時間間隔の間欠通気を行う。
【0023】
なお、その他の条件は以下の通りである。
分解槽内ヒータ設定温度:35℃
通気時の通気量 :400L/分
床材の初発投入量 :300L
撹拌時の撹拌速度 :3rpm
床材の初発含水率 :35%
このときの生ゴミの分解状況を床材のpHを指標として調べ、結果を図2に示した。即ち、生ゴミの分解が良好に行われた場合には、アンモニアが生成することにより床材のpHは高くなり、分解状況が悪い場合には酸が生成することにより床材のpHは低くなる。従って、床材のpHが7以上である場合には良好な分解状態、7未満では悪い分解状態であると判断することができる。
【0024】
図2より明らかなように、この実施例1では、安定な状態が長期間持続し、約4ヶ月に亘る連続運転が可能であった。これは、ALCの初期投入及び追加投入によりpHが安定し、10〜15日目、30〜35日目、81〜85日目などの生ゴミ不投入にもかかわらず床材が過剰乾燥することなく、また穏やかな撹拌によってチップの摩滅が殆ど認められなかったことから、微生物の活性が持続したことによるものと思われる。
【0025】
比較例1
実施例1において、前記[1]の条件を採用せず、即ち、初発にALCを添加せず、床材としてオガクズと木質チップを混合して用いたこと以外は同様にして処理を行い、床材のpHの経時変化を調べ、結果を図3に示した。ただし、生ゴミの投入は毎日行った。
【0026】
図3より明らかなように、この比較例1では、初発にALCを添加していないことから、pHは初発から低く、立ち上がり後、生ゴミの良好な分解に伴ってpHは上昇してくるが、安定せずにたちまち低下してしまう。pHが低下した状態でALCを投入しても、一時的なpH上昇がみられるのみで、安定な状態とはならなかった。
【0027】
比較例2
実施例1において、前記[2]の条件を採用せず、運転開始から58日間ALCの追加投入を行わなかったこと以外は同様にして処理を行い、床材のpHの経時変化を調べ、結果を図4に示した。ただし、生ゴミの不投入期間は、45〜55日目とした。
【0028】
図4より明らかなように、この比較例2では、初発にALCを添加したことにより、立ち上がりからpHの安定が認められた。45〜55日目にかけて生ゴミの投入が行われなかったが、床材の過剰乾燥は起こらず良好な状態が継続した。しかし55日目以降、急速なpH低下が起こり、その後、ALCを追加投入したが安定な状態は回復しなかった。
【0029】
比較例3
実施例1において、前記[5]の条件を採用せず、間欠撹拌の時間撹拌を撹拌:停止=5分:5分で一定とし、連続的に通気を行ったこと以外は同様にして処理を行い、床材のpHの経時変化を調べ、結果を図5に示した。ただし、生ゴミの不投入期間は60〜70日目とした。
【0030】
図5より明らかなように、この比較例3では、初発にALCを投入し、更に30日毎にALCを追加投入したことによって60日に亘って安定な状態が持続した。しかし、60〜70日目にかけて生ゴミの投入が行われなかったため、床材の過剰乾燥が起こり、微生物の活性が低下した。その後、生ゴミ投入を再開したところ、たちまちpHの低下が起こり、状態が悪化してしまった。
【0031】
比較例4
実施例1において、前記[3]の条件を採用せず、撹拌羽根の突設間隔を50mmとしたこと以外は同様にして処理を行い、床材のpHの経時変化を調べ、結果を図6に示した。ただし、生ゴミの投入は毎日行った。
【0032】
図6より明らかなように、この比較例4では、撹拌羽根の間隔が50mmで活発な撹拌が行われたため、立ち上がりから30日間は良好な状態が安定していたが、床材中のオガクズが粉砕されて微粉化し、チップもかなり摩滅して撹拌によって次第に団粒が形成されるようになり、床材への酸素供給が不足してpHが低下し、状態が悪化した。そして、ALCを追加投入しても安定な状態には回復しなかった。
【0033】
比較例5
実施例1において、前記[4]の条件を採用せず、即ち、床材として木質チップを用いず、オガクズのみを用いたこと以外は同様にして処理を行い、床材のpHの経時変化を調べ、結果を図7に示した。ただし、生ゴミの投入は毎日行った。
【0034】
図7より明らかなように、この比較例5では、撹拌羽根の間隔を110mmに設定して、穏やかな撹拌が行われるように運転したにもかかわらず、オガクズの微粉化が起こり、24日後にはpHの低下が起こった。pHは、ALCの追加投入によって一時回復したが長続きせずに、45日目には状態が悪化してしまった。
【0035】
以上の試験結果より、前記▲1▼〜▲5▼の条件のうち、一つでも欠けた場合には床材のpH低下、担体の微粉化、過剰乾燥のいずれかが起こり、良好な状態は維持されず、前記▲1▼〜▲5▼の条件をすべて組み合せた場合においてのみ、長期間に亘る安定な運転が可能になることがわかる。
【0036】
【発明の効果】
以上詳述した通り、本発明の生ゴミ処理機の運転方法によれば、微生物の作用によって生ゴミを分解・消滅させる生ゴミ処理機を良好な状態で長期に亘り安定に運転することが可能とされる。
【図面の簡単な説明】
【図1】本発明に係る生ゴミ処理機の一例を示す構成図である。
【図2】実施例1における床材のpH経時変化を示すグラフである。
【図3】比較例1における床材のpH経時変化を示すグラフである。
【図4】比較例2における床材のpH経時変化を示すグラフである。
【図5】比較例3における床材のpH経時変化を示すグラフである。
【図6】比較例4における床材のpH経時変化を示すグラフである。
【図7】比較例5における床材のpH経時変化を示すグラフである。
【符号の説明】
1 排気ブロア
2 分解槽
3 入気口
4 撹拌軸
5 撹拌羽根
6 投入口
7 撹拌モータ
8 パネルヒータ
9 フィルタ
11 風量調整コック
12 断熱材
13 排出口
14 制御盤
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for operating a garbage disposal machine, and more particularly to a method for stably operating a garbage disposal machine that decomposes and eliminates garbage by the action of microorganisms in a good state for a long period of time.
[0002]
[Prior art]
Conventionally, in a garbage processing machine that decomposes and extinguishes garbage using microorganisms, a suitable amount of flooring such as sawdust is placed in the decomposition tank, and microorganisms are placed there, and the garbage input into the tank is carbon dioxide. Decomposes into low molecular weight substances such as water and ammonia. In such an extinguishable garbage processing machine, oxygen must be supplied to the microorganisms living in the flooring. For this purpose, air is supplied to the decomposition tank or the flooring is removed with a stirrer. Stirring is performed.
[0003]
FIG. 1 shows the configuration of this garbage disposal machine. In this garbage processing machine, the air in the decomposition tank (fermentation tank) 2 is sucked by the suction blower 1 to take in air from the inlet 3 provided in the upper side wall of the decomposition tank 2, and in the stirrer Oxygen is supplied to the microorganisms in the flooring material by stirring the flooring material (not shown). In order to efficiently supply oxygen to the flooring material, a stirrer in which a round bar-shaped stirring blade 4 is spirally projected on a stirring shaft 4 disposed horizontally in a tank is used for stirring. The stirrer is rotated in a forward rotation → stop → reverse → stop cycle, and the flooring is moved left and right to mix the contents in the tank sufficiently uniformly. In FIG. 1, 6 is a garbage input, 7 is a motor of a stirrer, 8 is a panel heater for keeping the inside of the decomposition tank 2 at an appropriate temperature for decomposition, 9 is a filter, 10 is an exhaust pipe, 11 Is an air volume adjustment cock, 12 is a heat insulating material, 13 is a discharge port, and 14 is a control panel.
[0004]
[Problems to be solved by the invention]
In such a garbage processing machine, when the garbage is introduced so as to be an appropriate amount with respect to the size of the decomposition tank, generally, the garbage is reduced to carbon dioxide, water, and ammonia for one to two weeks from the start of operation. Although it is efficiently decomposed, the decomposition gradually stops, acid is generated in the tank, and a severe odor is generated. This can be attributed to the fact that most of the raw garbage is acidic and the pH of the flooring gradually decreases as the input of the raw garbage is continued, thereby reducing the activity of microorganisms; The floor material is pulverized, and microorganisms are less likely to live; the floor material pulverized in this way is kneaded by stirring to become a dumpling, and as a result, oxygen is hardly supplied to the microorganism. Even though no garbage is thrown in on holidays, etc., the air flow rate and agitation time by the blower are set so that moisture adjustment is performed properly on the premise that the garbage is periodically thrown in. It is conceivable that the material dries excessively and promotes inactivation of microorganisms and pulverization of the carrier.
[0005]
The present invention solves the above-mentioned conventional problems, and provides a method for operating a garbage disposal machine that can stably operate a garbage disposal machine that decomposes and extinguishes garbage by the action of microorganisms in a good state for a long period of time. The purpose is to provide.
[0006]
[Means for Solving the Problems]
The operation method of the garbage processing machine according to the present invention includes a garbage decomposition tank that contains a flooring material therein, a stirring shaft provided in the decomposition tank, and a plurality of rod-shaped protrusions that spirally protrude from the stirring shaft. A garbage processing machine equipped with a stirrer composed of a stirring blade and a venting means into the decomposition tank is charged with garbage, and the contents in the tank are intermittently stirred by the stirrer and the aeration means In the operation method of the garbage processing machine for decomposing the garbage by ventilating the inside of the tank, all of the following conditions (1) to (5) are adopted.
[0007]
(1) At the start of operation, a lightweight foamed concrete (hereinafter referred to as “ALC”) is used as a pH adjusting material that maintains a long-term effect on the flooring material in order to maintain the flooring material at a weakly alkaline pH of about 8 to 9 for a long time. Abbreviated) is added and mixed. ALC having a particle diameter of 1 to 10 mm is preferable, and the initial charge is preferably 1/10 to 1/15 times the volume of the flooring.
(2) In order to maintain the effect of the pH adjusting material for a longer period of time, ALC is additionally charged into the decomposition tank once every 25 to 40 days. This additional amount of ALC is preferably 1/25 to 1/50 times the volume of the flooring.
{Circle around (3)} In order to prevent the pulverization of the carrier by gentle stirring without impairing the transpiration of moisture, the protruding interval between the stirring blades is set to 100 to 200 mm.
(4) Wood chips mixed with sawdust are used as a flooring material, as a void material for improving oxygen supply efficiency, and as a carrier for microorganisms that are not easily pulverized by stirring. The wood chip preferably has a particle size of 20 to 50 mm, and the initial input amount is preferably 1/2 to 1/4 capacity times the sawdust.
{Circle around (5)} In order to prevent excessive drying of the flooring when no garbage is thrown in on a holiday or the like, the interval of intermittent stirring and the air flow rate are controlled, for example, as follows according to the throwing frequency of the garbage.
(i) When garbage is input within 24 hours: The time interval of intermittent stirring is set to stirring: stop = 1: 1 to 1.5, and continuous ventilation is performed.
(ii) When garbage is input within 24 to 48 hours: The time interval of intermittent stirring is set to stirring: stop = 1: 2-2.5, and continuous ventilation is performed.
(iii) When garbage is introduced within 48 to 72 hours: The time interval of intermittent stirring is set to stirring: stop = 1: 4-8, and the time interval of ventilation: airflow stop = 1: 10-15 Perform intermittent ventilation.
(iv) When no garbage is thrown in for 72 hours or more: The time interval of intermittent stirring is set to stirring: stop = 1: 50 to 60, and intermittent ventilation is performed at a time interval of ventilation: ventilation stop = 1: 50-60. Do.
[0008]
By adopting all the above conditions (1) to (5), it is possible for the first time to stably and satisfactorily decompose and eliminate garbage for a long time. If any one of these conditions is missing, any one of the lowering of the pH of the flooring, the pulverization of the carrier, and the excessive drying will occur, and stable operation over a long period of time cannot be maintained.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described in detail.
[0010]
In the present invention, all of the above conditions (1) to (5) are employed when the garbage is decomposed and eliminated by the garbage processing machine as shown in FIG.
[0011]
That is, first, at the start of operation of the garbage processing machine (that is, at the first time), ALC is mixed as a pH adjusting material that maintains a long-term effect in floor materials such as sawdust. Thereby, the pH of the flooring is maintained at a weak alkalinity of about 8 to 9 for a long time. The ALC has a grain size of about 1 to 10 mm and uses a coarse one as much as possible. Powdered ALC is easy to react and dissolves quickly, so the effect does not last. The mixing amount of ALC is appropriately about ALC1 with respect to the flooring materials 10 to 15 by volume ratio. If the ALC is less than this range, the ability to adjust the pH is poor, and if it exceeds this range, the viscosity of the flooring is increased and aggregation is promoted.
[0012]
In addition, in order to maintain the pH adjustment effect by the first ALC for a longer period of time, ALC is additionally introduced once every 25 to 40 days from the start of operation. If the frequency of this additional charging exceeds 40 days, the pH of the flooring may be lowered. Once the pH is lowered, the pH is temporarily recovered even if ALC is charged, but immediately Again, the pH adjustment effect cannot be obtained. If the frequency of additional charging is less than 25 days, the viscosity of the flooring is increased and aggregation is promoted. In addition, the additional input amount of ALC should just be a grade which can maintain the pH of a flooring to about 7-9, and although it depends on the additional charging frequency, generally it is 1/25 with respect to the amount of flooring. It is preferably about 1/50 times the capacity.
[0013]
In addition, for the purpose of gentle stirring to prevent pulverization of the carrier, the projecting interval of the round bar type stirring blades arranged in a spiral shape is set to 100 to 200 mm. If the distance is less than 100 mm, the carrier is pulverized. If the distance exceeds 200 mm, moisture transpiration is insufficient, and moisture adjustment of the flooring is not performed properly. The interval between the stirring blades varies depending on the capacity of the garbage processing machine, but in the case of a garbage processing machine having a decomposition tank capacity of about 300 to 750 L, it is particularly preferably about 100 to 120 mm.
[0014]
Further, a wood chip is mixed into a flooring material such as sawdust as a void material for improving oxygen supply and as a carrier for microorganisms that are not crushed. The particle size of the wood chip is suitably about 20 to 50 mm. If it is less than 20 mm, it will be pulverized in a short period of time, and if it exceeds 50 mm, crushing of sawdust will be promoted. The amount of wood chips mixed is appropriate for wood chips 2 to 4 in terms of volume ratio, and if it is less than this range, the effect of mixing cannot be obtained, and if it exceeds this range, the moisture adjustment of the flooring is satisfactory It becomes impossible to do.
[0015]
Furthermore, a holiday mode is set in order to prevent excessive drying of the floor material that occurs when garbage is not thrown in on a holiday or the like. When the input state of the garbage is recognized by opening and closing the input lid, and when it does not open for a certain period of time, the interval of intermittent stirring by forward rotation → stop → reverse rotation → stop is lengthened. At the same time, the air flow is controlled to prevent excessive drying.
[0016]
For example, the following control is performed.
(i) When garbage is input within 24 hours: The time interval of intermittent stirring is set to stirring: stop = 1: 1 to 1.5, and continuous ventilation is performed.
(ii) When garbage is input within 24 to 48 hours: The time interval of intermittent stirring is set to stirring: stop = 1: 2-2.5, and continuous ventilation is performed.
(iii) When garbage is introduced within 48 to 72 hours: The time interval of intermittent stirring is set to stirring: stop = 1: 4-8, and the time interval of ventilation: airflow stop = 1: 10-15 Perform intermittent ventilation.
(iv) When no garbage is thrown in for 72 hours or more: The time interval of intermittent stirring is set to stirring: stop = 1: 50 to 60, and intermittent ventilation is performed at a time interval of ventilation: ventilation stop = 1: 50-60. Do.
[0017]
When stirring or aeration is performed more frequently than the above range, excessive drying of the flooring proceeds, and if it is less than the above range, oxygen supplied to the microorganism is insufficient, and the activity of the microorganism is greatly reduced. End up.
[0018]
As other processing conditions, the following conditions are preferably employed.
Heater set temperature in decomposition tank: 30-40 ° C
Stirring speed during stirring: 1 to 3 rpm
Aeration rate at the time of ventilation: 300 to 1000 L / min. Input amount of raw garbage per time: 1/10 to 1/7 capacity times the moisture content of the floor material: 25 to 35% of the floor material amount
[0019]
【Example】
Hereinafter, the present invention will be described more specifically with reference to Examples and Comparative Examples.
[0020]
Example 1
The following conditions were adopted by the garbage processing machine (decomposition tank capacity 500L, flooring amount 300L) shown in FIG. 1 to decompose the garbage (vegetable waste 20%, leftovers 80%).
[0021]
In addition, 30 kg of garbage was introduced once a day. However, on the 10th to 15th days, the 30th to 35th days, and the 81st to 85th days, no garbage was thrown in assuming a long vacation. In addition, the stirring by the stirrer was performed as follows: forward rotation → stop → reverse rotation → stop →.
[0022]
[1] First, ALC (particle size: 10 to 20 mm) is added and mixed at a ratio of ALC: flooring material = 1: 10, and the initial pH is set to 8.8.
[2] As shown in Fig. 2, add ALC, which is 1/40 of the amount of flooring, at an interval of about 30 days.
[3] Set the spacing between the stirring blades to 110 mm.
[4] As a flooring material, wood chips (particle size: 20 to 50 mm) are mixed with sawdust in a ratio of chips: sawdust = 1: 3.
[5] Control intermittent agitation interval and air flow as follows.
(i) When garbage is input within 24 hours: The time interval of intermittent stirring is set to stirring: stop = 5 minutes: 5 minutes, and continuous ventilation is performed.
(ii) When garbage is input within 24 to 48 hours: The time interval of intermittent stirring is set to stirring: stop = 5 minutes: 10 minutes, and continuous ventilation is performed.
(iii) When garbage is input within 48 to 72 hours: The time interval of intermittent stirring is set to stirring: stop = 5 minutes: 30 minutes, and ventilation: aeration stop = 5 minutes: time interval of 55 minutes Perform intermittent ventilation.
(iv) When no garbage is thrown in for 72 hours or longer: The time interval of intermittent stirring is set to Stirring: Stop = 5 minutes: 55 minutes, and Aeration: Stop ventilation = 1 minute: Intermittent ventilation at a time interval of 59 minutes Do.
[0023]
Other conditions are as follows.
Heater set temperature in decomposition tank: 35 ° C
Aeration volume at the time of ventilation: 400L / Amount of initial input of floor material: 300L
Stirring speed during stirring: 3 rpm
Initial moisture content of flooring: 35%
The decomposition state of the garbage at this time was examined using the pH of the flooring as an index, and the result is shown in FIG. That is, when the garbage is decomposed well, the pH of the flooring becomes high due to the generation of ammonia, and when the decomposition condition is bad, the pH of the flooring becomes low due to the generation of acid. . Therefore, it can be judged that the floor material has a good decomposition state when the pH is 7 or more, and a pH under 7 is a bad decomposition state.
[0024]
As is clear from FIG. 2, in Example 1, a stable state was maintained for a long period of time, and continuous operation over about 4 months was possible. This is because the pH is stabilized by the initial charging and additional charging of ALC, and the flooring is excessively dried despite the absence of garbage such as the 10th to 15th day, the 30th to 35th day, and the 81st to 85th day. This was probably due to the persistence of the activity of the microorganisms because the chip was hardly worn by gentle stirring.
[0025]
Comparative Example 1
In Example 1, the conditions of [1] above were not adopted, that is, ALC was not added to the first start, and treatment was performed in the same manner except that sawdust and wood chips were mixed and used as a flooring. Changes in pH of the material over time were examined, and the results are shown in FIG. However, garbage was thrown in every day.
[0026]
As is clear from FIG. 3, in this comparative example 1, since ALC was not added to the first time, the pH was low from the first time, and after rising, the pH increased with good decomposition of garbage. , It will fall quickly without being stable. Even when ALC was added in a state where the pH was lowered, only a temporary increase in pH was observed, and a stable state was not achieved.
[0027]
Comparative Example 2
In Example 1, the conditions of [2] above were not adopted, the same treatment was performed except that ALC was not additionally added for 58 days from the start of operation, and the change over time in the pH of the flooring was examined. Is shown in FIG. However, the period of non-feeding of garbage was 45 to 55 days.
[0028]
As is clear from FIG. 4, in Comparative Example 2, the stability of pH was recognized from the start-up by adding ALC at the beginning. Although garbage was not thrown in on the 45th-55th day, the floor material did not excessively dry and the good state continued. However, from the 55th day onward, a rapid pH drop occurred. Thereafter, ALC was additionally added, but the stable state did not recover.
[0029]
Comparative Example 3
In Example 1, the above-mentioned condition [5] was not adopted, and stirring was performed for the same time except that the stirring was intermittently stirred for a period of time: Stirring: Stop = 5 minutes: 5 minutes, and continuously vented. The results were shown in FIG. 5. However, the period when the garbage was not thrown in was 60 to 70 days.
[0030]
As is clear from FIG. 5, in Comparative Example 3, ALC was first introduced, and ALC was additionally introduced every 30 days, so that a stable state was maintained for 60 days. However, since garbage was not thrown in on the 60th to 70th day, the floor material was excessively dried, and the activity of microorganisms was reduced. After that, when the input of garbage was resumed, the pH immediately dropped and the condition deteriorated.
[0031]
Comparative Example 4
In Example 1, the conditions of [3] above were not adopted, and the treatment was performed in the same manner except that the projecting interval of the stirring blades was set to 50 mm. The change over time in the pH of the flooring was examined, and the results are shown in FIG. It was shown to. However, garbage was thrown in every day.
[0032]
As is clear from FIG. 6, in Comparative Example 4, since the active stirring was performed with the interval between the stirring blades being 50 mm, the good state was stable for 30 days from the rise, but the sawdust in the flooring was The powder was pulverized and pulverized, the chips were considerably worn out, and aggregates were gradually formed by stirring. The oxygen supply to the flooring was insufficient, the pH was lowered, and the state deteriorated. And even if additional ALC was added, it did not recover to a stable state.
[0033]
Comparative Example 5
In Example 1, the condition [4] was not adopted, that is, the wood chip was not used as the flooring material, and the treatment was performed in the same manner except that only sawdust was used, and the change in pH of the flooring material over time was performed. The results are shown in FIG. However, garbage was thrown in every day.
[0034]
As is clear from FIG. 7, in Comparative Example 5, the sawdust was pulverized after 24 days, even though the stirring blade interval was set to 110 mm and the operation was performed so that gentle stirring was performed. A drop in pH occurred. The pH recovered temporarily by the addition of ALC, but did not last long, and the condition deteriorated on the 45th day.
[0035]
From the above test results, if any one of the above conditions (1) to (5) is missing, any one of the lowering of the pH of the flooring, the pulverization of the carrier, and the excessive drying occurs, and the good condition is It can be seen that stable operation over a long period of time is possible only when all of the conditions (1) to (5) are combined without being maintained.
[0036]
【The invention's effect】
As described above in detail, according to the operation method of the garbage disposal machine of the present invention, it is possible to stably operate the garbage disposal machine that decomposes and extinguishes garbage by the action of microorganisms in a good state for a long period of time. It is said.
[Brief description of the drawings]
FIG. 1 is a configuration diagram showing an example of a garbage disposal machine according to the present invention.
2 is a graph showing changes in pH of a flooring over time in Example 1. FIG.
FIG. 3 is a graph showing a change with time in pH of a flooring material in Comparative Example 1;
4 is a graph showing changes with time in pH of a flooring material in Comparative Example 2. FIG.
5 is a graph showing changes in pH of a flooring over time in Comparative Example 3. FIG.
6 is a graph showing changes with time in pH of a flooring material in Comparative Example 4. FIG.
7 is a graph showing changes with time in pH of a flooring material in Comparative Example 5. FIG.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Exhaust blower 2 Decomposition tank 3 Inlet 4 Stirring shaft 5 Stirring blade 6 Inlet 7 Stirring motor 8 Panel heater 9 Filter 11 Air flow adjustment cock 12 Heat insulating material 13 Outlet 14 Control panel

Claims (5)

内部に床材を収容する生ゴミ分解槽と、該分解槽内に設けられた撹拌軸及び該撹拌軸に螺旋状に突設された複数の棒状の撹拌羽根よりなる撹拌機と、該分解槽内への通気手段とを備える生ゴミ処理機に、生ゴミを投入し、前記撹拌機により槽内内容物を間欠的に撹拌すると共に前記通気手段により槽内の通気を行って生ゴミを分解処理する生ゴミ処理機の運転方法において、
運転開始時に、前記床材に対して軽量発泡コンクリートを添加混合すると共に、軽量発泡コンクリートを25〜40日に1回の頻度で該分解槽に追加投入し、
前記撹拌羽根の突設間隔を100〜200mmとし、
前記床材としてオカクズと木質チップとを混合したものを用い、
かつ、生ゴミの投入頻度に応じて前記間欠撹拌の間隔及び通気量を制御することを特徴とする生ゴミ処理機の運転方法。
A garbage decomposing tank that contains flooring inside, a stirring shaft provided in the decomposing tank, a stirrer comprising a plurality of rod-shaped stirring blades spirally provided on the stirring shaft, and the decomposing tank Garbage is thrown into a garbage processing machine equipped with a ventilation means for the inside, the contents in the tank are intermittently stirred by the stirrer and the tank is ventilated by the ventilation means to decompose the garbage. In the operation method of the garbage processing machine to process,
At the start of operation, lightweight foamed concrete is added to and mixed with the floor material, and lightweight foamed concrete is additionally added to the decomposition tank once every 25 to 40 days,
The protruding interval between the stirring blades is 100 to 200 mm,
As the flooring material, a mixture of geeks and wood chips is used,
And the operating method of the garbage processing machine characterized by controlling the space | interval and ventilation | gas_flowing amount of the said intermittent stirring according to the input frequency of garbage.
請求項1において、
24時間以内に生ゴミの投入がある場合には、前記間欠撹拌の時間間隔を撹拌:停止=1:1〜1.5とすると共に、連続的な通気を行い、
24〜48時間以内に生ゴミの投入がある場合には、前記間欠撹拌の時間間隔を撹拌:停止=1:2〜2.5とすると共に、連続的な通気を行い、
48〜72時間以内に生ゴミの投入がある場合には、前記間欠撹拌の時間間隔を撹拌:停止=1:4〜8とすると共に、通気:通気停止=1:10〜15の時間間隔の間欠通気を行い、
72時間以上生ゴミの投入がない場合には、前記間欠撹拌の時間間隔を撹拌:停止=1:50〜60とすると共に、通気:通気停止=1:50〜60の時間間隔の間欠通気を行うことを特徴とする生ゴミ処理機の運転方法。
In claim 1,
When there is input of garbage within 24 hours, the time interval of the intermittent stirring is set to stirring: stop = 1: 1 to 1.5, and continuous ventilation is performed.
When there is input of garbage within 24 to 48 hours, the time interval of the intermittent stirring is set to stirring: stop = 1: 2-2.5 and continuous ventilation is performed.
When garbage is input within 48 to 72 hours, the time interval of the intermittent stirring is set to stirring: stop = 1: 4 to 8 and the time interval of ventilation: aeration stop = 1: 10 to 15 is set. Intermittent ventilation,
When there is no input of garbage for 72 hours or more, the time interval of the intermittent stirring is set to stirring: stop = 1: 50 to 60, and intermittent ventilation is performed at a time interval of ventilation: ventilation stop = 1: 50-60. The operation method of the garbage disposal machine characterized by performing.
請求項1又は2において、前記軽量発泡コンクリートの粒径が1〜10mmであり、その初期投入量が床材に対して1/10〜1/15容量倍であることを特徴とする生ゴミ処理機の運転方法。In Claim 1 or 2, The particle size of the said lightweight foamed concrete is 1-10 mm, The initial input amount is 1/10-1/15 times the volume with respect to a flooring, The garbage processing characterized by the above-mentioned. How to operate the machine. 請求項1ないし3のいずれか1項において、前記木質チップの粒径が20〜50mmであり、その投入量がオガクズに対して1/2〜1/4容量倍であることを特徴とする生ゴミ処理機の運転方法。4. The raw material according to claim 1, wherein the particle size of the wood chip is 20 to 50 mm, and the input amount is 1/2 to 1/4 times the capacity of sawdust. Operation method of garbage disposal machine. 請求項1ないし4のいずれか1項において、前記軽量発泡コンクリートの初発投入量が床材に対して1/10〜1/15容量倍、25〜40日に1回の頻度における追加投入量が床材量に対して1/25〜1/50容量倍であることを特徴とする生ゴミ処理機の運転方法。In any 1 item | term of the Claims 1 thru | or 4, the initial input amount of the said lightweight foamed concrete is 1/10-1/15 times capacity | capacitance with respect to a flooring, and the additional input amount in the frequency of once every 25-40 days The operation method of the garbage processing machine characterized by being 1 / 25-1 / 50 capacity times with respect to the amount of flooring.
JP19444098A 1998-07-09 1998-07-09 Operation method of garbage processing machine Expired - Fee Related JP3870558B2 (en)

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