JP3563287B2 - Compost fermenter for aerobic fermentation - Google Patents

Compost fermenter for aerobic fermentation Download PDF

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JP3563287B2
JP3563287B2 JP4332699A JP4332699A JP3563287B2 JP 3563287 B2 JP3563287 B2 JP 3563287B2 JP 4332699 A JP4332699 A JP 4332699A JP 4332699 A JP4332699 A JP 4332699A JP 3563287 B2 JP3563287 B2 JP 3563287B2
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fermentation
compost
aerobic fermentation
fermenter
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JP2000239089A (en
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文隆 早田
凉一 中川
かおり 藤本
定雄 岡田
英夫 小出
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日立プラント建設株式会社
有限会社ガイア
岡田工業株式会社
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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
    • 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

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Description

【0001】
【発明の属する技術分野】
本発明は、好気発酵処理用の堆肥発酵槽に関し、特に、寒冷地においても畜産廃棄物や生ごみ、汚泥等を確実に堆肥発酵処理しうる好気発酵処理用の堆肥発酵槽に関する。
【0002】
【従来の技術】
好気発酵堆肥の製造装置には各種の方式がありそれぞれ実用化されている。例えば、平面・開放・連続送り型の一例として、両側に側壁があり、幅がほぼ5〜10m、長さが数十〜100mのコンクリート製の溝状発酵槽と、側壁に沿って移動しながら有機物を攪拌・移送する攪拌移送機を備えたものがある。溝状発酵槽の一方の端からホイールローダ等によって堆肥原料を投入し、攪拌移送機によって他端の方向へ原料を移動させつつ適度に攪拌すると、数日から数十日で有機物が分解発酵し、堆肥化する。
【0003】
有機物原料としては、生ごみ、厨芥、食品工場残渣、畜糞、下水汚泥その他があるが、これらを廃棄物として処分しようとすると2次公害の原因にもなりかねず、逆に、品質の高い堆肥として自然界に還元させることができれば環境の維持、向上にも大きな貢献になる。
【0004】
【発明が解決しようとする課題】
しかしながら、前記の有機物原料は、その成分や含水率、排出量が時期によっても場所によっても区々であり、これを高品質な堆肥にするためにはそれぞれに応じて発酵条件を整える必要がある。
例えば、有機廃棄物に含まれる多量の水分及び有機物の分解発酵過程で生じる水分が過剰に存在すると、嫌気性菌が活性化して腐敗が進み、悪臭が発生して周囲の生活環境を悪化させると共に、できた堆肥の品質も低く、施肥効果が期待できない。
堆肥原料としての好ましい含水率は、乾燥固形重量に対しておおよそ60ないし70%であり、原料の水分を調整するために多くの手段を講じている。簡便な方法は、有機原料に匹敵する量のおが屑、稲わら、籾殻、乾燥した堆肥等を混入することであり、電気や重油を熱源とした温風乾燥設備を付帯させることも行われている。
【0005】
特に、寒冷地においては、発酵温度の維持に注意するのは勿論、畜糞を原料にする場合は、凍結したものが持ち込まれて、その溶解に多くのエネルギーを使ったり、また既に一部は嫌気発酵しているものがあり、それによる悪臭の発生や好ましくない大腸菌等が周辺にばら撒かれることがある。
上記畜糞は、畜舎の排糞装置により、また運搬の仕方により、畜糞が大きな団子状に固まることがあるので、たとえ凍結していないものであっても、発酵時の攪拌では十分に破砕分散がなされず、内部が嫌気発酵した小塊のままで発酵過程を通過することがある。このような小塊を含む堆肥は、当然品質的にも低い堆肥となる。
【0006】
この発明の目的は、寒冷地に好適な堆肥の製造装置であって、原料中の水分を容易に調整でき、腐敗臭の発生を少なくした取扱性に優れた好気発酵処理用の堆肥発酵槽を提供することにある。
【0007】
【課題を解決するための手段】
上記課題を解決するために、有機物原料を投入するための投入部を一方の端に備え、成果物を取出すための搬出部を他方の端に備え、その間をロータリー式等の攪拌移送機によって攪拌移動させることによって有機物を好気発酵して堆肥化するための発酵処理部からなる好気発酵処理用の堆肥発酵槽において、前記投入部は、投入原料の滲出水分を流下しうる下り勾配の傾斜面と、この傾斜面から温風を吹き出し、または吸引減圧が可能な空圧手段と、添加投入された水分調整材とともに有機物原料を破砕混合する混合手段とを設けて構成する。
【0008】
原料の投入部を傾斜面にすることによって有機物原料から滲出する水分が分離され、かつ、空圧手段によって乾燥され、混合手段により水分調整材とともに有機物原料が破砕混合され、容易に水分調整することができ、寒冷環境でも発酵条件を整えることができる。
上記供給部は下り勾配の傾斜面となっているので、それに続く発酵処理部の床が氷結土層より低い地中に位置することになる。このように、床面を氷結土層より低く埋没させると、寒気の影響が少なくなり、夏冬を通じてほぼ一定の条件を保つことができる。
【0009】
前記傾斜面は、好気発酵用微生物が高濃度で生息しうる通水性及び通気性を有する材料で形成することにより、有機物原料から自然に分離する水分が通水性のある床面を通って床下に排出される。同時に、好気発酵用微生物が高濃度で繁殖し、この通性ないし好気性の土壌菌が、腐敗菌の繁殖を抑制する成分を含んだ代謝物を分泌したり、投入した有機物原料から滲出した汚水に含まれるBOD、COD、悪臭成分を分解除去するべく作用する。これらの作用効果は、菌体の自己消化によって細孔が目詰りすることがないので永続性が確保される。
前記混合手段は、対称動作する2つの並列配置のオーガスクリュー軸からなり、各スクリュー軸は、相互に逆方向をなすオーガを直列に形成して左右から目的物を寄せ集めつつ両軸間で破砕混合するべく構成することにより、軸が並行に並んだ複数のスクリューの上に、原料と水分調整材を供給すると、原料の塊を小片(ほぼ5cm以下の大きさ)に確実にほぐしながら調整材を均一に混合させることができて、好気発酵に適した通気性堆積物にすることができる。
【0010】
【発明の実施の形態】
上記解決手段をなす技術的思想の実施の形態について以下に図を参照して説明する。
図1は本発明の堆肥発酵槽の縦断面図である。
堆肥発酵槽1は、供給原料Aを投入するための一端側の投入部2と、ロータリー式等の攪拌移送機3を備える発酵処理部4と、他端側の搬出部5と、雨水を避けかつ保温のための建家6とから構成する。
【0011】
投入部2には、投入原料Aの滲出水分を流下しうる下り勾配の傾斜面7と、この傾斜面7から温風を吹き出し、または吸引減圧が可能な空圧手段8と、水分調整材Bを添加投入する添加口9と、添加調整材Bとともに有機物原料Aを破砕混合する混合手段10とを設ける。
【0012】
傾斜面7は、好気発酵用微生物が高濃度で生息する通水性及び通気性を有する材料で形成することにより、有機物原料から自然に分離する水分が通水性のある床面を通って床下に排出される。同時に、好気発酵用微生物が高濃度で繁殖し、この通性ないし好気性の土壌菌が、腐敗菌の繁殖を抑制する成分を含んだ代謝物を分泌したり、投入した有機物原料から滲出した汚水に含まれるBOD、COD、悪臭成分を分解除去するべく作用する。これらの作用効果は、菌体の自己消化によって細孔が目詰りすることがないので永続的に機能する。
【0013】
具体的な材料としては、多孔質コンクリート、表面を針状結晶化したコンクリートブロック、砂の代わりに土を用いたソイルセメントブロック、鉄や木格子の上に敷き詰めた軽石層や山砂層又は籾殻層など、入手しやすい材料を使用することができる。
【0014】
空圧手段8は、図示せぬ送風機と接続して送風と減圧を選択可能に、かつ、加熱部8aを介して傾斜面7に構成する。床下から空気を送気すると、堆積している有機物層から水分を蒸散させて、含水率を下げるとともに堆積物を好気性にし、好気性発酵を促進する。このとき、加熱部8aによる温風を供給することにより水分の調整及び発酵の促進に好ましい効果を与える。また、わずかに床下を減圧することにより、原料からの滲出水を効率よく抽出することができる。
【0015】
したがって、低温度の原料が投入されても、好ましい所定条件に合わせて発酵前の温度及び水分を調整することができるので、発酵処理部における発酵の早期立上げを図ることができる。
【0016】
添加口9は傾斜面の上方に備えた回転バレル等からなる。この回転バレルにより、おが屑、稲わら、籾殻、乾燥した堆肥等の水分調整材を混合しやすいように細片にほぐしつつ、下方の傾斜面上の原料に添加供給する。
【0017】
混合手段10は傾斜面の下端に位置する回転バレルからなり、原料の塊を小片にほぐしながら調整材を均一に混合させることができて、好気発酵に適した通気性堆積物にすることができる。この混合手段が水分調整材と原料とを均一に混合することにより、原料の含水率を発酵に適した65ないし70%にまで下げることができるので、上記含水率を超える原料をそのまま発酵過程に持ち込んだ場合に多く発生する腐敗菌の繁殖による悪臭を防止することができる。
【0018】
発酵処理部4は、ロータリー式等の攪拌移送機3を備えた床4aと側壁4bとからなる。ロータリー式攪拌移送機3は側壁4bの上端に支持され、投入部2から受けた目的物を発酵させるべく搬出部5の方向に攪拌移動させる。
【0019】
投入部2寄りの床4cは、必要に応じて水分調整のための空圧手段8を設ける。また、側壁4bに電気ヒーター等の遠赤外線を放射する加熱手段を設ける。この加熱手段により、寒冷期においても、側面の冷え込みによる結露の発生や発酵の不均一を緩和し、発酵処理すべき有機物が温められて水分の調整及び発酵の促進がより円滑に進行する。上記加熱手段は側壁4bに限らず、必要に応じて床面4aを含め、また、遠赤外線を発生する鉱石粉やセラミックスを塗布又は埋設することによっても同様の効果をえることができる。
【0020】
図2は図1のII−II線断面図である。
発酵処理部4の両側の側壁4bは凍結土層Cより深く埋設して構成する。この発酵処理部4は、供給部2が下り勾配の傾斜面7となっているので、それに続く発酵処理部4の床4c,4aが氷結土層より低い地中に位置することになる。このように、床面を氷結土層Cより低く埋没させると、寒気の影響が少なくなり、夏冬を通じてほぼ一定の条件を保つことができる。
【0021】
上記構成をなす堆肥発酵槽による堆肥発酵処理について説明する。
畜舎から排出される有機廃棄物Aは、主に敷き料と糞である。その他各種の原料の有機物Aを間欠的に搬入して堆肥発酵槽1の投入部2から投入し、通水性と通気性とを兼ね備えた多孔質コンクリートの傾斜面7を介して水分調整や解凍を行う。
【0022】
含水率の高い材料は水分調整材Bを混合する前に空圧手段8を作動させて、通水性の傾斜面7の床下を減圧にすることによって、滲出水が床面7に吸われ、強制的に余分な水分を排除することができる。次に加熱部8aから温風を供給して原料の乾燥と解凍又は加熱を行う。さらに水分調整はおが屑や出来上がった完熟堆肥を混合することによって行う。水分量の微調整は床下から吹き込む空圧手段8の空気配管からの風量や床下からの排気量を制御することで、適切な発酵環境を整えることができる。
【0023】
側壁4bに沿って攪拌移送機3を作動させると、堆積している有機物材料は出口方向へ少量づつ移動し、その過程で発酵が開始する。この攪拌に伴い、有機物材料は空気に触れて発酵に必要な酸素が供給される。
攪拌移送機3は前後方向に1日に1ないし2回程度の割合で稼動し、発酵物は、その都度、空気の供給を受けながら出口方向に移動される。発酵は20ないし30日で完了するが、初期の立ち上げを促進するために、床4cの空圧手段8によって加熱空気を吹き込むことで寒冷環境にあっても発酵期間を短縮することができる。
【0024】
図3は本発明の別の堆肥発酵槽の縦断面図である。前記同様の部材はその符号を付すことにより説明を省略する。
堆肥発酵槽21は、建屋6にファン付きの吸い込みダクト22を備え、これを空圧手段8と接続する。また、搬出部5側に後熟成23のスペースをとり、ベルトコンベヤ等の搬出装置24を設ける。
【0025】
吸い込みダクト22は、70℃以上に達する有機物の発酵熱によって温まった空気を建屋6の天井近傍で回収する。この温風を空圧手段8を介して傾斜面7等に供給する。この発酵熱で温められた発酵処理部4の空気を利用することにより、ヒーター25による加熱コストを抑えつつ、水分を調整して発酵を促進ることができる。
【0026】
有機質原料の中に藁等のセルロースが多く含まれている場合は、分解発酵が不十分になることがあるので、後熟成23のスペースにおいて数十日堆積して完熟堆肥を得る。完熟堆肥は搬出装置24により搬出部5から順次搬出する。
【0027】
図4は投入部の混合手段の他の構成例を示す斜視図である。
混合手段31は、傾斜面7の下部で対称動作する2つの並列配置のオーガスクリュー軸32、33からなり、各スクリュー軸は、相互に逆方向の螺旋面をなすオーガ面34、35を直列に形成して左右から目的物を寄せ集めつつ両軸間で破砕混合するべく構成する。その上方に水分調整材を添加する添加口36を形成する。
【0028】
投入された有機質原料はオーガスクリュウ34、35の回転によって左右方向Dに振り分けられる。大きな塊は転動しながら、また、両軸の対称動作によって両軸間に巻き込まれ、破砕されて小片に細分化する。凍結塊は空圧手段による温風により温められて融解する。
このように、上記混合手段31の対称動作する並行スクリューにより、原料の塊を小片(ほぼ5cm以下の大きさ)に確実にほぐしながら、上方の添加口36から落下する調整材を均一に混合させることができ、好気発酵に適した通気性堆積物にすることができる。
【0029】
【発明の効果】
本発明の好気発酵処理用の堆肥発酵槽は以下の効果を奏する。
堆肥発酵槽は投入部と搬出部を両端に備える発酵処理部からなり、投入部は傾斜面と空圧手段と混合手段とを備えることから、原料の投入部を傾斜面にすることによって有機物原料から滲出する水分が滞留することなく分離され、かつ、空圧手段によって乾燥され、混合手段により水分調整材とともに有機物原料が破砕混合され、水分調整した上で発酵処理部に送られる。
【0030】
上記投入部は下り勾配の傾斜面となっているので、それに続く発酵処理部の床が氷結土層より低い地中に位置することになる。このように、床面を氷結土層より低く埋没させると、寒気の影響が少なくなり、夏冬を通じてほぼ一定の条件を保つことができる。
【0031】
上記空圧手段によって床下から空気を送気すると、堆積している有機物層から水分が蒸散されて含水率を下げるとともに堆積物を好気性にし、好気性発酵を促進する。このとき、発酵処理部の発酵熱で温められた空気を利用することも可能であり、この温風を送気すると、水分の調整及び発酵の促進に好ましい効果を与える。また、わずかに床下を減圧することにより、原料からの滲出水を強制抽出することができる。
【0032】
したがって、低温度の原料が投入されても、好ましい所定条件に合わせて発酵前の温度及び水分を調整することができるので、発酵処理部における発酵の早期立上げを図ることができる。
【0033】
混合手段は、原料の塊を小片にほぐしながら調整材を均一に混合させることができて、好気発酵に適した通気性堆積物にすることができる。
籾殻やおが屑、完熟した堆肥などの水分調整材を原料に均一に混合することにより、原料の含水率を発酵に適した65ないし70%にまで下げることができるので、上記含水率を超える原料をそのまま発酵過程に持ち込んだ場合に多く発生する腐敗菌の繁殖による悪臭を防止することができる。
このようにして、本発明の好気発酵処理用の堆肥発酵槽は寒冷地における有機質廃棄物を容易に堆肥化することができる。
【図面の簡単な説明】
【図1】本発明の堆肥発酵槽の縦断面図
【図2】図1のII−II線断面図
【図3】本発明の別の堆肥発酵槽の縦断面図
【図4】投入部の混合手段の他の構成例を示す斜視図
【符号の説明】
1 堆肥発酵槽
2 投入部
3 攪拌移送機
4 発酵処理部
4a 床
4b 側壁
4c 床
5 搬出部
7 傾斜面
8 空圧手段
10 混合手段
21 堆肥発酵槽
31 混合手段
32、33 オーガスクリュー軸
34、35 オーガ面
A 供給原料
B 水分調整材
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a compost fermenter for aerobic fermentation, and more particularly to a compost fermenter for aerobic fermentation capable of reliably composting livestock waste, garbage, sludge, and the like even in cold regions.
[0002]
[Prior art]
There are various types of aerobic fermentation compost manufacturing apparatuses, and each of them has been put to practical use. For example, as an example of a flat / open / continuous feed type, there are side walls on both sides, a width of approximately 5 to 10 m, a length of several tens to 100 m, and a concrete grooved fermenter having a length of several tens to 100 m, while moving along the side walls. Some are equipped with a stirring and transferring machine for stirring and transferring organic substances. Compost raw materials are put in from one end of the grooved fermenter by a wheel loader, etc., and the raw materials are moved to the other end by a stirring transfer machine and agitated appropriately while decomposing and fermenting organic matter in several days to several tens of days. Composting.
[0003]
Organic raw materials include garbage, kitchen garbage, food factory residues, animal dung, sewage sludge, etc. If these are disposed of as waste, they can cause secondary pollution, and conversely, high quality compost If it can be returned to the natural world, it will greatly contribute to the maintenance and improvement of the environment.
[0004]
[Problems to be solved by the invention]
However, the above-mentioned organic raw materials have different components, water contents, and discharge amounts depending on the time and place, and it is necessary to adjust fermentation conditions according to each in order to make high-quality compost. .
For example, when a large amount of water contained in organic waste and water generated in the process of decomposition and fermentation of organic matter are present in excess, anaerobic bacteria are activated and decay proceeds, and foul odors are generated to deteriorate the surrounding living environment and However, the quality of the resulting compost is low and the fertilizing effect cannot be expected.
The preferred moisture content of the compost material is approximately 60 to 70% based on dry solids weight, and many measures have been taken to control the moisture content of the material. A simple method is to mix sawdust, rice straw, rice husk, dried compost, etc., in an amount comparable to that of organic raw materials, and it is also accompanied by hot air drying equipment using electricity or heavy oil as a heat source. .
[0005]
Especially in cold climates, care must be taken to maintain the fermentation temperature, and when using livestock manure as a raw material, frozen products are brought in and use a lot of energy to dissolve them. Some of them are fermented, resulting in generation of offensive odor and undesired Escherichia coli and the like may be scattered around.
The animal droppings may be solidified into large dumplings by the dropping device of the barn and by the way of transportation, so even if they are not frozen, they are sufficiently crushed and dispersed by stirring during fermentation. In some cases, the anaerobic fermented small mass may pass through the fermentation process. Compost containing such small lumps is naturally low in quality.
[0006]
It is an object of the present invention to provide a compost production apparatus suitable for cold districts, which can easily adjust the water content of raw materials, and has excellent handling characteristics with reduced generation of putrefaction odor for aerobic fermentation tanks. Is to provide.
[0007]
[Means for Solving the Problems]
In order to solve the above-mentioned problems, an input section for inputting an organic material is provided at one end, and an output section for taking out a product is provided at the other end, and the space therebetween is agitated by a rotary-type agitating transfer machine. In a compost fermentation tank for aerobic fermentation processing comprising a fermentation processing section for aerobically fermenting organic matter by moving and composting, the input section has a downward slope capable of flowing down the exuded water of the input raw material. Surface, pneumatic means capable of blowing out hot air from the inclined surface or reducing the pressure, and mixing means for crushing and mixing the organic material together with the added water adjusting material.
[0008]
Moisture leaching from the organic raw material is separated by making the input portion of the raw material an inclined surface, and is dried by pneumatic means, and the organic raw material is crushed and mixed together with the water adjusting material by the mixing means to easily adjust the water content. The fermentation conditions can be adjusted even in a cold environment.
Since the supply section has a downward slope, the floor of the subsequent fermentation section is located in the ground lower than the frozen soil layer. When the floor is buried below the frozen soil layer as described above, the influence of the cold is reduced and almost constant conditions can be maintained throughout the summer and winter.
[0009]
The inclined surface is formed of a material having water permeability and air permeability through which aerobic fermentation microorganisms can inhabit at a high concentration. Is discharged. At the same time, aerobic fermentation microorganisms proliferate at high concentrations, and these facultative or aerobic soil bacteria secrete metabolites containing components that inhibit the growth of spoilage bacteria, or exude from the input organic material. It works to decompose and remove BOD, COD and malodorous components contained in sewage. These effects and effects are ensured because the pores are not clogged by the autolysis of the cells.
The mixing means is composed of two auger screw shafts arranged in parallel to operate symmetrically, and each screw shaft forms an auger in a direction opposite to each other in series, and crushes between the two shafts while gathering a target object from right and left. By supplying the raw material and the moisture control material on a plurality of screws whose axes are arranged in parallel by mixing, the mass of the raw material is surely loosened into small pieces (about 5 cm or less in size), and Can be uniformly mixed to form an aerated sediment suitable for aerobic fermentation.
[0010]
BEST MODE FOR CARRYING OUT THE INVENTION
An embodiment of the technical idea that constitutes the above-described solution will be described below with reference to the drawings.
FIG. 1 is a longitudinal sectional view of the compost fermenter of the present invention.
The compost fermenter 1 has an input section 2 at one end for feeding the feed material A, a fermentation processing section 4 including a rotary type stirring transfer device 3, a discharge section 5 at the other end, and avoids rainwater. And a house 6 for keeping warm.
[0011]
The charging section 2 has a downwardly inclined surface 7 capable of flowing down the exuded water of the input raw material A, a pneumatic means 8 capable of blowing hot air from the inclined surface 7 or capable of reducing the pressure, and a water conditioning material B. And a mixing means 10 for crushing and mixing the organic raw material A with the addition adjusting material B.
[0012]
The inclined surface 7 is formed of a water-permeable and air-permeable material in which aerobic fermentation microorganisms inhabit at a high concentration, so that water that naturally separates from the organic material passes through the water-permeable floor surface and under the floor. Is discharged. At the same time, aerobic fermentation microorganisms proliferate at high concentrations, and these facultative or aerobic soil bacteria secrete metabolites containing components that inhibit the growth of spoilage bacteria, or exude from the input organic material. It works to decompose and remove BOD, COD and malodorous components contained in sewage. These functions and effects function forever because pores are not clogged by autolysis of the cells.
[0013]
Specific materials include porous concrete, concrete blocks with needle-like crystallized surfaces, soil cement blocks using soil instead of sand, pumice layers, mountain sand layers or rice hull layers spread over iron or wood lattice. For example, easily available materials can be used.
[0014]
The air pressure means 8 is connected to a blower (not shown) so that air blowing and pressure reduction can be selected, and is formed on the inclined surface 7 via a heating unit 8a. When air is blown from under the floor, water evaporates from the deposited organic matter layer, lowering the water content, making the sediment aerobic, and promoting aerobic fermentation. At this time, by supplying warm air by the heating unit 8a, a favorable effect is provided on the adjustment of moisture and the promotion of fermentation. Further, by slightly reducing the pressure under the floor, the seepage water from the raw material can be efficiently extracted.
[0015]
Therefore, even if a low-temperature raw material is supplied, the temperature and moisture before fermentation can be adjusted according to preferable predetermined conditions, so that fermentation in the fermentation processing unit can be started up early.
[0016]
The addition port 9 is composed of a rotary barrel or the like provided above the inclined surface. With this rotary barrel, the water adjusting material such as sawdust, rice straw, rice husk, and dried compost is loosened into small pieces so as to be easily mixed and added to the raw material on the lower inclined surface.
[0017]
The mixing means 10 is composed of a rotating barrel located at the lower end of the inclined surface, and can uniformly mix the adjusting material while loosening the mass of the raw material into small pieces, thereby forming a breathable sediment suitable for aerobic fermentation. it can. The mixing means uniformly lowers the water content of the raw material to 65 to 70%, which is suitable for fermentation, by uniformly mixing the water conditioning material and the raw material. It is possible to prevent a bad smell caused by propagation of putrefactive bacteria which often occurs when brought in.
[0018]
The fermentation processing unit 4 is composed of a floor 4a provided with a rotary type agitating transfer machine 3 and side walls 4b. The rotary stirring transfer machine 3 is supported by the upper end of the side wall 4b, and stirs and moves in the direction of the unloading unit 5 to ferment the target product received from the charging unit 2.
[0019]
The floor 4c near the charging section 2 is provided with pneumatic means 8 for adjusting moisture as needed. Further, a heating means such as an electric heater for radiating far infrared rays is provided on the side wall 4b. By this heating means, even in the cold season, the occurrence of dew condensation and uneven fermentation due to the cooling of the side surfaces are alleviated, and the organic matter to be fermented is warmed, whereby the adjustment of moisture and the promotion of fermentation proceed more smoothly. The above-mentioned heating means is not limited to the side wall 4b, and the same effect can be obtained by including or embedding ore powder or ceramics that generate far-infrared rays, if necessary, including the floor surface 4a.
[0020]
FIG. 2 is a sectional view taken along line II-II of FIG.
The side walls 4b on both sides of the fermentation processing unit 4 are buried deeper than the frozen soil layer C. In the fermentation processing unit 4, since the supply unit 2 has a downward slope 7, the floors 4c and 4a of the subsequent fermentation processing unit 4 are located in the ground lower than the frozen soil layer. When the floor is buried below the frozen soil layer C, the influence of the cold is reduced, and almost constant conditions can be maintained throughout the summer and winter.
[0021]
A compost fermentation process by the compost fermenter having the above configuration will be described.
The organic waste A discharged from the barn is mainly litter and dung. In addition, the organic matter A of various other raw materials is intermittently carried in and charged from the charging section 2 of the compost fermenter 1, and moisture adjustment and thawing are performed through the inclined surface 7 of porous concrete having both water permeability and air permeability. Do.
[0022]
For the material having a high moisture content, the pneumatic means 8 is operated before mixing the moisture adjusting material B to reduce the pressure under the floor of the water-permeable inclined surface 7, so that the exuded water is sucked into the floor 7 It is possible to eliminate excess moisture. Next, warm air is supplied from the heating unit 8a to dry and thaw or heat the raw material. Further, moisture adjustment is performed by mixing sawdust and completed ripe compost. The fine adjustment of the water content can be controlled by controlling the air flow from the air pipe of the pneumatic means 8 blown from under the floor and the exhaust amount from under the floor, so that an appropriate fermentation environment can be prepared.
[0023]
When the agitation transfer machine 3 is operated along the side wall 4b, the deposited organic material moves little by little toward the outlet, and fermentation starts in the process. With this agitation, the organic material comes into contact with air to supply oxygen necessary for fermentation.
The agitating transfer machine 3 operates in the front-rear direction about once or twice a day, and the fermented product is moved toward the outlet while being supplied with air each time. Fermentation is completed in 20 to 30 days, but the fermentation period can be shortened even in a cold environment by blowing heated air by the pneumatic means 8 of the floor 4c in order to promote the initial startup.
[0024]
FIG. 3 is a longitudinal sectional view of another compost fermenter of the present invention. The description of the same members as described above is omitted by giving the same reference numerals.
The compost fermenter 21 has a suction duct 22 with a fan in the building 6, and this is connected to the pneumatic means 8. In addition, a space for the post-ripening 23 is provided on the carry-out section 5 side, and a carry-out device 24 such as a belt conveyor is provided.
[0025]
The suction duct 22 collects the air heated by the fermentation heat of the organic matter reaching 70 ° C. or more near the ceiling of the building 6. This warm air is supplied to the inclined surface 7 and the like via the pneumatic means 8. By using the air of the fermentation processing unit 4 warmed by the fermentation heat, the fermentation can be promoted by adjusting the water content while suppressing the heating cost by the heater 25.
[0026]
If the organic raw material contains a large amount of cellulose such as straw, the decomposition and fermentation may be insufficient. Therefore, the organic material is accumulated in the space for post-ripening 23 for several tens of days to obtain a fully-ripened compost. The fully-ripened compost is sequentially carried out from the carrying-out section 5 by the carrying-out device 24.
[0027]
FIG. 4 is a perspective view showing another configuration example of the mixing means of the charging section.
The mixing means 31 comprises two auger screw shafts 32, 33 arranged side by side that operate symmetrically below the inclined surface 7, and each screw shaft connects auger surfaces 34, 35, which form spiral surfaces in mutually opposite directions, in series. It is formed so that it is formed and crushed and mixed between both shafts while collecting the target object from the left and right. Above this, an addition port 36 for adding a moisture adjusting material is formed.
[0028]
The charged organic raw material is distributed in the left-right direction D by the rotation of the August screws 34, 35. The large chunk rolls and is caught between the two axes by the symmetrical movement of the two axes, crushed and broken into small pieces. The frozen mass is melted by being warmed by warm air by the pneumatic means.
As described above, the adjusting material dropped from the upper addition port 36 is uniformly mixed by the symmetrically operated parallel screw of the mixing means 31 while reliably loosening the lump of the raw material into small pieces (about 5 cm or less in size). And can be made into a breathable sediment suitable for aerobic fermentation.
[0029]
【The invention's effect】
The compost fermenter for aerobic fermentation of the present invention has the following effects.
The compost fermentation tank is composed of a fermentation treatment section having an input section and an output section at both ends, and the input section is provided with an inclined surface, pneumatic means, and mixing means. The water exuding from the water is separated without stagnation, dried by pneumatic means, crushed and mixed with an organic material together with a water adjusting material by a mixing means, and then sent to a fermentation treatment section after adjusting the water content.
[0030]
Since the input section has a downward slope, the floor of the subsequent fermentation section is located in the ground lower than the frozen soil layer. When the floor is buried below the frozen soil layer as described above, the influence of the cold is reduced and almost constant conditions can be maintained throughout the summer and winter.
[0031]
When air is blown from under the floor by the pneumatic means, moisture is evaporated from the deposited organic matter layer to lower the water content and make the sediment aerobic, thereby promoting aerobic fermentation. At this time, it is also possible to use air warmed by the fermentation heat of the fermentation processing unit, and when this hot air is supplied, a favorable effect is exerted on the adjustment of moisture and the promotion of fermentation. Further, by slightly reducing the pressure under the floor, the seepage water from the raw material can be forcibly extracted.
[0032]
Therefore, even if a low-temperature raw material is supplied, the temperature and moisture before fermentation can be adjusted according to preferable predetermined conditions, so that fermentation in the fermentation processing unit can be started up early.
[0033]
The mixing means can uniformly mix the conditioning material while loosening the raw material mass into small pieces, and can form a gas-permeable sediment suitable for aerobic fermentation.
By uniformly mixing the water content adjusting material such as rice husk, sawdust, and ripe compost with the raw material, the water content of the raw material can be reduced to 65 to 70% suitable for fermentation. It is possible to prevent a bad smell caused by the propagation of putrefactive bacteria, which often occurs when the bacterium is directly brought into the fermentation process.
In this way, the compost fermenter for aerobic fermentation of the present invention can easily compost organic waste in cold regions.
[Brief description of the drawings]
1 is a longitudinal sectional view of a compost fermenter of the present invention. FIG. 2 is a sectional view taken along line II-II of FIG. 1. FIG. 3 is a longitudinal sectional view of another compost fermenter of the present invention. Perspective view showing another configuration example of the mixing means.
DESCRIPTION OF SYMBOLS 1 Compost fermentation tank 2 Input part 3 Stirring transfer machine 4 Fermentation processing part 4a Floor 4b Side wall 4c Floor 5 Unloading part 7 Slope 8 Pneumatic means 10 Mixing means 21 Compost fermentation tank 31 Mixing means 32, 33 Auger screw shafts 34, 35 Auger surface A Feedstock B Moisture adjusting material

Claims (3)

有機物原料を投入するための投入部を一方の端に備え、成果物を取出すための搬出部を他方の端に備え、その間をロータリー式等の攪拌移送機によって攪拌移動させることによって有機物を好気発酵して堆肥化するための発酵処理部からなる好気発酵処理用の堆肥発酵槽において、
前記投入部は、投入原料の滲出水分を流下しうる下り勾配の傾斜面と、この傾斜面から温風を吹き出し、または吸引減圧が可能な空圧手段と、添加投入された水分調整材とともに有機物原料を破砕混合する混合手段とを備えることを特徴とする好気発酵処理用の堆肥発酵槽。
At one end, an input section for inputting the organic material is provided, and at the other end, a discharge section for extracting the product is provided. In the compost fermentation tank for aerobic fermentation processing consisting of a fermentation processing section for fermenting and composting,
The charging section includes a slope having a downward slope capable of flowing out the exuded moisture of the input raw material, air pressure means capable of blowing hot air from the slope, or capable of reducing the pressure of suction, and an organic substance together with the added water adjusting material. A compost fermenter for aerobic fermentation, comprising: mixing means for crushing and mixing raw materials.
前記傾斜面は、好気発酵用微生物が高濃度で生息しうる通水性及び通気性を有する材料で形成することを特徴とする請求項1記載の好気発酵処理用の堆肥発酵槽。The compost fermenter for aerobic fermentation treatment according to claim 1, wherein the inclined surface is formed of a material having water permeability and air permeability that allows aerobic fermentation microorganisms to live at a high concentration. 前記混合手段は、対称動作する2つの並列配置のオーガスクリュー軸からなり、各スクリュー軸は、相互に逆方向をなすオーガを直列に形成して左右から目的物を寄せ集めつつ、両軸間で破砕混合することを特徴とする請求項1記載の好気発酵処理用の堆肥発酵槽。The mixing means comprises two auger screw shafts arranged in parallel and operating symmetrically. The compost fermenter for aerobic fermentation according to claim 1, wherein the compost fermenter is crushed and mixed.
JP4332699A 1999-02-22 1999-02-22 Compost fermenter for aerobic fermentation Expired - Fee Related JP3563287B2 (en)

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