JP2009106828A - Composting treatment method by granule development of organic waste and apparatus therefor - Google Patents

Composting treatment method by granule development of organic waste and apparatus therefor Download PDF

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JP2009106828A
JP2009106828A JP2007279981A JP2007279981A JP2009106828A JP 2009106828 A JP2009106828 A JP 2009106828A JP 2007279981 A JP2007279981 A JP 2007279981A JP 2007279981 A JP2007279981 A JP 2007279981A JP 2009106828 A JP2009106828 A JP 2009106828A
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fermentation
organic
wood
nitrogen
lignin
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JP4153974B1 (en
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Tsutomu Oishi
勉 大石
Mitsuru Sazuka
充 佐塚
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Science KK
Science Inc Japan
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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
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/20Sludge processing
    • 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
    • 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
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/78Recycling of wood or furniture waste

Abstract

<P>PROBLEM TO BE SOLVED: To provide an energy-saving and efficient composting treating method which controls bad odor by adjusting the growing conditions of wood rotting fungi through the ball type granulation and natural fermentation of organic wastes in order to compost organic sludge and pruning branches in a high order. <P>SOLUTION: The composting treatment method of organic wastes comprises granulating a carbon source subjected to the step of reducing the decomposition resistance of lignin and the like by the alkali treatment and the step of permeating a microorganism active liquid thereto, and a nitrogen source such as organic wastes, a foodstuff residue and live stock feces into the ball type by the granulating machine, conducting the low-temperature fermentation at an ordinary temperature region of 20°C-30°C to always assure the ideal C/N ratio under the growing conditions of wood rotten fungi and prevent the elution of nitrogen components to prepare a fertilizer with high soil-value. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、有機汚泥や食品残渣や畜糞等を無臭発酵させるため、チップ化又は綿くず化した木屑を利用し、堆積することなく良質な発酵を施し、悪臭の発生を抑制し、大規模な送気、脱臭装置を不要とした、エネルギーの消費を減少させた堆肥化処理方法及びその処理装置に関するものである。   In order to ferment organic sludge, food residues, livestock excrement, etc. without odor, the present invention uses wood chips made from chips or crushed cotton, performs high-quality fermentation without accumulating, suppresses the generation of bad odors, The present invention relates to a composting method and an apparatus for reducing the energy consumption, which eliminates the need for an air supply and deodorization device.

従来堆肥製造を行う場合、積み重ね方法かスクープ式などの機械化装置による通気、攪拌方式が行われている。いずれも急速な発酵を期するためアンモニアガス、硫化水素等の臭気の発生を余儀なくされ、脱臭のためのエネルギー消費や送気のためのエネルギー消費が処理コストの大半を占めている。すでにEU諸国ではこうした発酵方法は大気環境の負荷が大きいものとして否定的な技術とされている。   Conventionally, when composting is performed, a stacking method or a scooping type aeration / stirring method is used. In both cases, odors such as ammonia gas and hydrogen sulfide are inevitably generated due to rapid fermentation, and energy consumption for deodorization and energy consumption for air occupy most of processing costs. In EU countries, such a fermentation method has already been regarded as a negative technology because it has a heavy load on the atmosphere.

また、林業等の剪定枝や街路樹の剪定枝は、畜産分野では堆肥製造時の水分調整材として利用される場合があるが、半分は焼却処分され再利用が進んでいないバイオマス資源である。その大きな原因は、剪定枝にリグニンと呼ばれる分解しにくい成分が多く含まれ堆肥化に相当の長期間を要することが大きな障害となっている。   In addition, pruning branches for forestry and roadside trees and pruning branches for roadside trees are sometimes used as moisture adjusting materials in compost production, but half of them are biomass resources that have been incinerated and are not being reused. A major cause of this is that the pruned branch contains a lot of components that are difficult to decompose, called lignin, and it takes a long time for composting.

このような分解抵抗が高い有機物は、土壌中においても分解は徐々に進行するはずであり、窒素飢餓その他の害も生じにくい特性を維持できる利点もある。しかし、分解性が低く、微生物の栄養源となりにくい材料の分解促進は従来の手法では困難で、畜糞、ワラ、ヌカなど易分解性有機物、化学肥料などの栄養源を多量に加えても、これらが分解微生物に消費しつくされれば発酵は終息し、剪定枝には作用が及びにくい。そして、リグニンのベンゼン環を完全分解できる細胞外酵素を生成する菌は、きのこの仲間の白色木材腐朽菌だけであり、細菌を含め他の微生物は環の外側部分を少し分解できるが、環そのものは分解できない。こうして土壌に残る難分解性の有機物は、リグニンを中心とした物質になってくる。土壌分解における長期の経過の中では多量のリグニンによる悪影響が起こる可能性もあり、基本的には熟成を進めてリグニンの総量を減少させておくべきである。   Such an organic substance having a high resistance to decomposition should be gradually decomposed even in the soil, and has an advantage that it can maintain a characteristic that hardly causes nitrogen starvation and other harms. However, it is difficult to accelerate the degradation of materials that have low degradability and are unlikely to be a nutrient source for microorganisms, even if a large amount of nutrient sources such as easily degradable organic matter such as livestock dung, straw, and nuka and chemical fertilizers are added. If it is consumed by decomposing microorganisms, the fermentation ends and the pruned branches are hardly affected. And the only fungus that produces an extracellular enzyme that can completely decompose the benzene ring of lignin is the white wood-rotting fungus of the mushroom group, and other microorganisms, including bacteria, can decompose the outer part of the ring a little, but the ring itself Cannot be disassembled. Thus, the hardly decomposable organic matter remaining in the soil becomes a substance centered on lignin. There is a possibility that a large amount of lignin may have an adverse effect in the long-term course of soil degradation. Basically, aging should be promoted to reduce the total amount of lignin.

特許文献1には、回転時に内部に収容の収容物を攪拌する回転ドラムを外周側から加熱する外部加熱機構を有してなり、このパネルヒータがスリップリングの配在下に接続の制御盤における制御で昇温調整を可能にしてなることを特徴とする発酵処理装置が提案されている。この方法は、コンクリートミキサー様の回転ドラム内に収容した生ゴミとバクテリアとを加熱下で攪拌することが可能になり、バクテリアによる生ゴミの分解を効果的に実現し得ることになる。しかし、回転ドラムの傾斜角は上端の開口から収容物Mを漏れさせないようにするのに十分である限り、原則として任意の傾斜角に固定されているため、ボール状造粒に用いる装置には向かない。また、パネルヒータに供給するためのエネルギーが必要である問題点がある。   Patent Document 1 has an external heating mechanism that heats a rotating drum that stirs the contained material inside when rotating from the outer peripheral side, and this panel heater is controlled in a control panel connected to a slip ring. A fermentation treatment apparatus characterized in that the temperature rise can be adjusted by the above-mentioned is proposed. This method makes it possible to stir the garbage and bacteria stored in a rotating drum like a concrete mixer under heating, and can effectively realize the decomposition of the garbage by bacteria. However, as long as the inclination angle of the rotating drum is sufficient to prevent the contents M from leaking from the opening at the upper end, the rotation drum is fixed to an arbitrary inclination angle in principle. Not suitable. In addition, there is a problem that energy for supplying the panel heater is necessary.

特許文献2には、処理物を予め団粒状に造粒して発酵槽31内に収容し、隣接する粒状物の表面間に相互に連通し合う通気空間を形成して発酵させるものである。そして造粒前の処理物の水分率を造粒及び好気性発酵である一次発酵が可能な水分率に調整するとともに、発酵槽31内に収容した処理物に対し、少なくとも当該処理物が目標温度下で一次発酵を継続する温度に至るまで温風を供給する。さらに一次発酵終了後の処理物を、一次発酵を行わしめた発酵槽(32)と同一の発酵槽32内で、嫌気性発酵である二次発酵を行わせる有機廃棄物の発酵処理方法及び装置が提案されている。この方法は、団粒状にすることによって通気性をよくすることがねらいであって、団粒状のまま発酵を待つと言うものではない。また、温風を供給するためのエネルギーや送気のためのエネルギーが必要である問題点がある。   In Patent Document 2, a processed product is granulated in advance and accommodated in a fermenter 31, and an aeration space communicating with each other is formed between the surfaces of adjacent granular materials to be fermented. And while adjusting the moisture content of the processed material before granulation to the moisture content in which the primary fermentation which is granulation and aerobic fermentation is possible, with respect to the processed material accommodated in the fermenter 31, at least the said processed material is target temperature. Warm air is supplied until it reaches the temperature at which primary fermentation is continued. Furthermore, the organic waste fermentation treatment method and apparatus for performing the secondary fermentation, which is anaerobic fermentation, in the same fermentor 32 as the fermenter (32) in which the primary fermentation is performed on the processed product after the end of the primary fermentation. Has been proposed. This method is aimed at improving air permeability by making the aggregate, and does not mean that the fermentation is kept in the aggregate. In addition, there is a problem that energy for supplying hot air and energy for supplying air are necessary.

特許文献3には、砂礫質や粘土質等の粒径を異にする無機物質材3からなる粒体を有機植物繊維等からなる有機物質剤2に絡み付かせるとともに、結合剤4によって粒状に固結することにより多孔質の固粒構造を有してなる人工団粒体及びその製造方法が提案されている。この方法は、植物栽培用の人工土壌や汚濁水等の浄化媒体等として好適に用いられるともに資源の有効利用を図る人工団粒体及びその製造方法であり、加温や送気のためのエネルギーを必要としない優れた処理法であるが、樹枝チップ等が未処理のままであるため、土壌に残る難分解性の有機物リグニンが蓄積することとなる問題点がある。   In Patent Document 3, particles made of an inorganic substance material 3 having different particle sizes such as gravel and clay are entangled with an organic substance agent 2 made of organic plant fibers and the like, and are made granular by a binder 4. Artificial aggregates having a porous solid grain structure by consolidation and a method for producing the same have been proposed. This method is an artificial aggregate that is preferably used as a purification medium for artificial soil for plant cultivation, polluted water, etc. and that also makes effective use of resources, and a method for producing the same. Although it is an excellent treatment method that does not need to be used, there is a problem that the hard-to-decompose organic lignin that remains in the soil accumulates because the dendron chips and the like remain untreated.

特許文献4には、堆肥材料堆積層3の底部に配設される吸引管4と、該吸引管4の吸引側端部に入口側が接続され、出口側にアンモニアトラップ8の入口側が接続される第1のドレイントラップ6と、該アンモニアトラップ8の出口側に入口側が接続され、出口側に吸引ファン12の吸引側が接続される第2のドレイントラップ10と、該第2のドレイントラップ10の排出側から残った気体を外部に排出する吸引ファン12とを備える。アンモニアトラップ8の充填材8aにより回収されたアンモニアは固形肥料として利用する。悪臭の揮散を低減する堆肥化処理方法及び装置が提案されている。しかし、臭気を発生させることは発酵条件が不備であり、かつ、それを除去するために複雑、過大な手間とエネルギーが必要である問題点がある。
特開2001−79525号公報 特開2001−170693号公報 特開2001−204245号公報 特開2005−35811号公報
In Patent Document 4, the suction pipe 4 disposed at the bottom of the compost material deposition layer 3, the inlet side is connected to the suction side end of the suction pipe 4, and the inlet side of the ammonia trap 8 is connected to the outlet side. A first drain trap 6, a second drain trap 10 whose inlet side is connected to the outlet side of the ammonia trap 8, and a suction side of the suction fan 12 is connected to the outlet side, and discharge of the second drain trap 10 And a suction fan 12 for discharging the gas remaining from the side to the outside. Ammonia recovered by the filler 8a of the ammonia trap 8 is used as a solid fertilizer. A composting method and apparatus for reducing odor emission have been proposed. However, the generation of odor has a problem that fermentation conditions are inadequate and complicated and excessive labor and energy are required to remove it.
JP 2001-79525 A Japanese Patent Laid-Open No. 2001-170693 JP 2001-204245 A JP 2005-35811 A

静岡県内から産業廃棄物として、有機汚泥(下水汚泥として約180千m)や剪定枝(山林と街路樹で約60万トン)が排出されている。畜産分野では、堆肥製造時の窒素原料や水分調整材として利用される場合があるが、半分は焼却処分され、再利用が進んでいないバイオマス資源である。その大きな原因は、アンモニアガスや硫化水素等の発生、また、剪定枝にはリグニンと呼ばれる分解しにくい成分が多く含まれ、堆肥化には年単位の時間が必要なことがある。
本発明が解決しようとする課題は、リグニン分解を伴う常温自然発酵を行い、悪臭の発生を抑制するものであり、かつ、不要なエネルギーの使用を減じようとするものである。
Organic sludge (approximately 180,000 m 3 as sewage sludge) and pruned branches (approximately 600,000 tons in mountain forests and street trees) are discharged from Shizuoka Prefecture as industrial waste. In the livestock field, there are cases where it is used as a nitrogen raw material or moisture adjusting material during compost production, but half of it is a biomass resource that has been incinerated and has not been reused. The major causes are the generation of ammonia gas, hydrogen sulfide, etc., and the pruned branches contain a lot of components that are difficult to decompose called lignin, and composting may require annual time.
The problem to be solved by the present invention is to perform natural fermentation at room temperature accompanied by lignin decomposition, to suppress the generation of malodor, and to reduce the use of unnecessary energy.

そこで本発明は、有機汚泥から悪臭の発生を抑制する発酵方式とするものであり、堆積させないから高温発酵しない。汚泥のみの発酵でなくチップ化又は綿くず化した木屑をアルカリ処理によって分解の障壁となるフェノール性物質の被覆を緩め、またセルロースを膨潤させて分解抵抗を低める処理を施し、C/N比のバランスを長期にわたり維持させ、そして微生物が必要とするミネラルを補給して良好な発酵を促すこと、さらに団粒化させた形状とすることによる低温発酵で悪臭の発生を防ぎ、団粒化した形状により外部から乾燥させ内部の臭気を外部に出さない、有機廃棄物のボール状造粒による無臭発酵処理とそれに用いる装置を提供することを目的とする。   Therefore, the present invention is a fermentation system that suppresses the generation of malodor from organic sludge, and does not accumulate, so high temperature fermentation is not performed. The processing of reducing the degradation resistance by swelling the cellulose with a phenolic substance that becomes a decomposition barrier by alkali treatment of the wood chips made into chips or cotton scrap instead of only sludge fermentation, Maintaining the balance over a long period of time, replenishing minerals required by microorganisms to promote good fermentation, and preventing odors from occurring by low-temperature fermentation by forming the aggregated shape, and the aggregated shape An object of the present invention is to provide an odorless fermentation treatment by ball-shaped granulation of organic waste and an apparatus used therefor, which are dried from the outside and do not emit an internal odor to the outside.

上記の目的を達成するために請求項1に記載した造粒物形成方法は、有機汚泥や食品残渣や畜糞等を無臭発酵させる造粒物形成において、チップ化又は綿くず化した木屑をアルカリ処理により分解の障壁となるリグニン等の分解抵抗を低める工程と、微生物活性液を浸潤させる工程を施した炭素源と、有機汚泥や食品残渣や畜糞等の窒素源とを、造粒処理装置によって微生物資材と混練し、粘着力によりボール状に造粒することを特徴とする造粒物形成方法である。   In order to achieve the above object, the granulated product forming method according to claim 1 is an alkali treatment of chipped or cotton-scraped wood waste in forming a granulated product for odorless fermentation of organic sludge, food residue, livestock dung, etc. The carbon source that has been subjected to the process of lowering the degradation resistance of lignin, etc., which becomes a barrier to degradation by the process, and the process of infiltrating the microorganism active liquid, and the nitrogen source such as organic sludge, food residues and livestock excreta, It is a granulated material forming method characterized by kneading with a material and granulating into a ball shape by adhesive force.

この発明は、フンコロガシ(甲虫;スカラベ)が動物の糞をボール玉にして運び、その中へ卵を産み付けることを知り、ボール玉を取ってみると外側は乾燥しているため臭気はなく、中は水分が残されており幼虫が餌としていることを知った。こうした自然界で行われていることを応用して、簡易で、臭気の発生を抑制した有機廃棄物の造粒物形成方法を構築し、畜産排泄物の堆肥化の実用性の検証を行ってきたところである。   This invention knows that dung beetle (beetle; scarab) carries animal dung in a ball and lays eggs in it, and when the ball is taken out, the outside is dry and there is no odor. Knew that there was water left and the larvae were feeding. By applying what is being done in the natural world, we have constructed a simple method for forming granulated organic waste that suppresses the generation of odors, and verified the practicality of composting livestock excreta By the way.

課題の有機汚泥と剪定枝を高次元で堆肥化処理する場合、難分解性のリグニンの分解が非常に重要な要素であり、分解性が低く、微生物栄養となりにくい材料の分解促進は、在来の手法では困難であるため薬品による前処理を試みた結果、苛性ソーダが持続性のある効果を示し、アルカリ処理が適していることがわかった。苛性ソーダ濃度は2%〜4%で効果が顕著となる。   When composting organic sludge and pruned branches at a high level, the degradation of persistent lignin is a very important factor, and it is natural to promote the degradation of materials that have low degradability and are difficult to become microbial nutrients. As a result, it was found that caustic soda showed a lasting effect and that alkali treatment was suitable. The caustic soda concentration is 2% to 4%, and the effect becomes remarkable.

また発明者らは、先に提案した特開2006−28406号公報の微生物活性液を原液の500倍程度に希釈して、アルカリ処理後の乾燥させたチップ化又は綿くず化した木屑に浸潤させ、低温発酵におけるリグニンの分解促進を図った結果、30日〜45日の発酵期間を経てから農地へ施肥するのが効果的である見解を得た。   In addition, the inventors dilute the microbial activity solution of the previously proposed Japanese Patent Application Laid-Open No. 2006-28406 to about 500 times the stock solution, and infiltrate the dried chip-formed or cotton-scraped wood chips after alkali treatment. As a result of promoting the decomposition of lignin in low-temperature fermentation, an opinion that it is effective to apply fertilization to farmland after a fermentation period of 30 to 45 days was obtained.

請求項2に記載の堆肥化処理方法は、ボール状に造粒された請求項1の炭素源と窒素源を、20℃〜30℃の常温域で低温発酵させて、木材腐朽菌の繁殖条件下で、常に理想的なC/N比率を確保し、窒素成分の流出を防止し、土壌的価値の高い肥料とすることを特徴とする堆肥化処理方法である。   The composting method according to claim 2 is characterized in that the carbon source and nitrogen source of claim 1 granulated in a ball shape are fermented at a low temperature in a room temperature range of 20 ° C. to 30 ° C., and the conditions for the growth of wood-rotting fungi Below, it is a composting method characterized by always ensuring an ideal C / N ratio, preventing the outflow of nitrogen components, and producing fertilizer with high soil value.

この発明は、木材腐朽菌の繁殖条件である適度の水分、温度、酸素、栄養分で木材含水率が20%以上、温度は20〜30℃で酸素を必要とし、栄養分は木材に含まれるリグニン、セルロース、ヘミセルロースである木材腐朽菌の繁殖条件に適合させるため、ボール状に造粒された形成物の中で木材腐朽菌を活性させ、常に理想的なC/N比率を確保し、窒素成分の流出を防止することを実現しているのである。   The present invention requires that the moisture content of wood is 20% or more at a proper moisture, temperature, oxygen, and nutrients, which are the breeding conditions of wood-rotting fungi, and the oxygen is required at a temperature of 20 to 30 ° C. The nutrient is lignin contained in the wood, In order to adapt to the growth conditions of the wood-rotting fungi, which are cellulose and hemicellulose, the wood-rotting fungi are activated in the ball-granulated formation, always ensuring an ideal C / N ratio, It prevents the outflow.

請求項3に記載の造粒処理装置は、ミキサーの回転ドラム部の傾斜角が回転動作中に変更可能な機構を有し、水分率の変動に対し傾斜角を変更することで、造粒径の大きさを制御することを特徴とする造粒処理装置である。   The granulation processing apparatus according to claim 3 has a mechanism in which the tilt angle of the rotating drum portion of the mixer can be changed during the rotation operation, and the granulation particle size is changed by changing the tilt angle with respect to fluctuations in moisture content. It is the granulation processing apparatus characterized by controlling the magnitude | size of.

この発明は、請求項1で使用する造粒処理装置であるため、コンポスト化装置のように発酵物を長期間滞留する必要はない。そこで、ミキサーの回転ドラム部の傾斜角が回転動作中に変更可能な機構とし、投入初期には傾斜角を高くし、積極的に団子化状態を誘発させて造粒物の径の拡大を図り造粒を促進させる。一部の発酵物が規定の造粒径に達した場合、径の大きい物は上層に上がるため、ミキサーの回転ドラム部の傾斜角を低くし、外部に移送すると共に等量の新規発酵物を投入する。この様にミキサーの回転ドラム部の傾斜角が回転動作中に変更可能な機構とすることにより、流動的造粒動作を可能とする。   Since this invention is the granulation processing apparatus used in Claim 1, it is not necessary to retain a fermented material for a long period of time unlike a composting apparatus. Therefore, a mechanism that can change the tilt angle of the rotating drum part of the mixer during the rotation operation is set to increase the tilt angle at the initial stage of injection, and the diameter of the granulated material is increased by actively inducing a dumpling state. Promote granulation. When some of the fermented products reach the specified particle size, the larger ones rise to the upper layer, so the tilt angle of the rotating drum part of the mixer is lowered and transferred to the outside and an equal amount of new fermented product is added. throw into. In this way, a fluid granulation operation can be performed by using a mechanism in which the inclination angle of the rotating drum portion of the mixer can be changed during the rotation operation.

以上説明したように請求項1の発明によれば、自然界で行われている現象を応用して再現し、有機汚泥と剪定枝を高次元で堆肥化処理するための造粒物形成が可能となる。   As described above, according to the invention of claim 1, it is possible to form a granule for reproducing organic sludge and pruned branches in a high-dimensional manner by applying a phenomenon that occurs in nature. Become.

請求項2の発明によれば、ボール状に造粒された形成物の中で木材腐朽菌の繁殖条件が整うため、常に理想的なC/N比率を確保し、窒素成分の流出を防止することを実現し、リグニンの総量を減少させ、土壌的価値の高い肥料とすることが可能となる。   According to the invention of claim 2, since the breeding conditions of the wood-rotting fungi are adjusted in the ball-granulated formation, the ideal C / N ratio is always ensured and the outflow of nitrogen components is prevented. This makes it possible to reduce the total amount of lignin and to make a fertilizer with high soil value.

請求項3の発明によれば、ミキサーの回転ドラム部の傾斜角が回転動作中に変更可能な機構とすることにより、造粒径の大きさを制御することに加え、回転方向を変えずに造粒物を取り出すことが可能となり、作業時間の短縮ができる。   According to the invention of claim 3, in addition to controlling the size of the particle size by changing the tilt angle of the rotary drum portion of the mixer during the rotation operation, the rotation direction is not changed. The granulated product can be taken out, and the working time can be shortened.

以下、本発明の実施形態を図1〜図2を参照して詳細に説明する。図1は本発明のボール状に造粒された有機物の断面図、図2は本発明の有機廃棄物をボール状に造粒する造粒処理装置の構造を示す内部透視線を付加した斜視図である。   Hereinafter, embodiments of the present invention will be described in detail with reference to FIGS. FIG. 1 is a cross-sectional view of an organic material granulated into a ball shape according to the present invention, and FIG. 2 is a perspective view with an internal perspective line showing the structure of a granulation processing apparatus for granulating the organic waste according to the present invention into a ball shape. It is.

産業廃棄物として、有機汚泥2や食品残渣3や畜糞4等の窒素源や剪定枝等5(6)の炭素源がある。これらの廃棄物を図1のボール状の造粒物1として常温自然発酵を行い、土壌的価値の高い肥料とすることにより、産業廃棄物から有機肥料に造り替えることができる。   As industrial waste, there are nitrogen sources such as organic sludge 2, food residue 3 and livestock dung 4 and carbon sources such as pruned branches 5 (6). These wastes are subjected to natural fermentation at normal temperature as the ball-shaped granulated material 1 in FIG. 1 to produce fertilizers with high soil value, so that industrial wastes can be replaced with organic fertilizers.

有機汚泥2や食品残渣3や畜糞4等の窒素源を利用する場合、十分に水分を除去した有機汚泥2に、3mm程度に破砕した食品残渣3や畜糞4等を混ぜ、先に提案した特開2006−28406号公報の微生物活性液を原液の500倍程度に希釈して、重量比0.5%程度混入する。この微生物活性液により有機汚泥に含まれる金属とリン、イオウなどをキレート錯体化して微生物が利用しやすくさせるものである。   When using a nitrogen source such as organic sludge 2, food residue 3 or livestock dung 4, etc., the food sludge 2 or livestock dung 4 crushed to about 3 mm is mixed with organic sludge 2 from which water has been sufficiently removed. The microorganism active solution disclosed in Kaikai 2006-28406 is diluted to about 500 times the stock solution and mixed with about 0.5% by weight. This microorganism active solution makes the metal contained in organic sludge chelate-complexed with phosphorus, sulfur, etc. to make it easier for microorganisms to use.

剪定枝5(6)を炭素源として利用する場合、衝撃力を主な破砕成分とするハンマータイプの破砕機によって、長さ60mm〜120mm、幅1mm〜2mm厚み0.2mm〜0.8mmの綿くず化した状態の破砕物A(10mm×5mm×0.5mm程度の圧縮破砕物Bを含む)にする。破砕物の形態や寸法は破砕機によって変化するため、有機肥料の使用用途に合わせて選択すればよい。この破砕の目的は、微生物が分解作用を発揮し易いように粗く砕くのが目的であり、破砕機の構造や破砕物の形態や寸法を特定するものではない。   When the pruned branch 5 (6) is used as a carbon source, a hammer type crusher whose impact force is a main crushing component is used to make cotton 60 to 120 mm long, 1 to 2 mm wide and 0.2 to 0.8 mm thick. A crushed material A (including a compressed crushed material B of about 10 mm × 5 mm × 0.5 mm) is formed. Since the form and dimensions of the crushed material vary depending on the crusher, it may be selected according to the intended use of the organic fertilizer. The purpose of this crushing is to crush roughly so that microorganisms can easily exert a decomposing action, and does not specify the structure of the crusher or the form and size of the crushed material.

破砕された炭素源は、アルカリ処理によって分解の障壁となるフェノール性物質の被覆を緩め、またセルロースを膨潤させて分解抵抗を低めるため、種々の濃度の苛性ソーダを用いて分解持続性の特性を調べた結果、濃度が2%〜4%で10日〜15日浸潤後、硫酸でPH7に中和し、減圧下で乾燥処理した物が持続性のある効果を示し、アルカリ処理が適していることがわかった。従来は石灰処理が行われていたが、添加量は1%以下であり、樹体の酸性を中和し、微生物の生育環境を整えることが主目的であったため、難分解性のリグニンに対して持続性のある効果が発揮できなかったものと思われる。作用として、苛性ソーダによるアルカリ処理により、ポリフェノール、リグニン、ヘミセルロースなどが溶解し、微生物の分解作用が向上すると共に、セルロースも膨潤して分解作用が向上するものと思われる。上記のアルカリ処理は、苛性ソーダを用いた例であるが、濃度が15%〜22%の消石灰を用いても有効性を示す。しかし、処理温度や樹種で有効性が大きく変化するため、条件を配慮した運用が望まれる。   The crushed carbon source is subjected to alkali treatment to loosen the coating of phenolic substances that become a decomposition barrier, and to swell cellulose to reduce decomposition resistance. As a result, after infiltration for 10 to 15 days at a concentration of 2% to 4%, the product neutralized with sulfuric acid to PH7 and dried under reduced pressure shows a durable effect, and alkali treatment is suitable I understood. In the past, lime treatment was performed, but the amount added was 1% or less, and the main purpose was to neutralize the acidity of the tree and to adjust the growth environment of microorganisms. It seems that the long-lasting effect could not be demonstrated. As an action, it is considered that polyphenol, lignin, hemicellulose and the like are dissolved by alkali treatment with caustic soda, and the decomposition action of microorganisms is improved, and cellulose is also swollen to improve the decomposition action. The above alkali treatment is an example using caustic soda, but the effectiveness is exhibited even when slaked lime having a concentration of 15% to 22% is used. However, the effectiveness varies greatly depending on the treatment temperature and tree species, so operation with consideration for conditions is desired.

アルカリ処理された炭素源は、先に提案した特開2006−28406号公報の微生物活性液を原液の500倍程度に希釈して、アルカリ処理後の乾燥させたチップ化又は綿くず化した木屑に浸潤させ、低温発酵におけるリグニンの分解促進を図る。この微生物活性液を木屑に浸潤させた処理における作用は解明に至っていないが、一定の効果は確認されている。   The alkali-treated carbon source is obtained by diluting the microbial activity solution of the previously proposed Japanese Patent Application Laid-Open No. 2006-28406 to about 500 times the stock solution, and drying it into chips or cotton scraps that have been dried after alkali treatment. Infiltrate and promote decomposition of lignin in low temperature fermentation. Although the action in the treatment in which the microbial active liquid is infiltrated into the wood chips has not been elucidated, a certain effect has been confirmed.

各処理工程を経た窒素源と炭素源は、図2に示す造粒処理装置9に微生物資材と共に投入される。この発明による造粒処理装置9は、回転時に内部に投入された窒素源と炭素源を攪拌する回転ドラム10と、駆動モーター11と、投入排出機構12とそれらを固定する可動板13と、地面に設置する固定版14と、可動板13の角度を変化させる可変機構15により構成されている。   The nitrogen source and the carbon source that have passed through each processing step are input together with the microbial material into the granulation processing apparatus 9 shown in FIG. A granulating apparatus 9 according to the present invention includes a rotating drum 10 that stirs a nitrogen source and a carbon source that are input into the interior at the time of rotation, a drive motor 11, a charging / discharging mechanism 12, a movable plate 13 that fixes them, a ground surface And a variable mechanism 15 that changes the angle of the movable plate 13.

尚、可動板13と固定版14とは回転体16を経由して接続されているため、可変機構15の先端が伸びたり縮んだりすることにより、可動板13に固定されている回転ドラム10の傾斜角が変化する。この傾斜角の変更は、回転ドラム10の回転中も自由にコントロールできる。この傾斜角を変化させる目的は、造粒径の大きさを制御することに加え、回転方向を変えずに造粒物を取り出すことを可能にするのが目的であり、可変機構15がパンタグラフ式、歯車方式、シリンダー方式等の構造を有する機構であればよく、機構を特定するものではない。   Since the movable plate 13 and the fixed plate 14 are connected via the rotating body 16, the tip of the variable mechanism 15 extends or contracts, so that the rotary drum 10 fixed to the movable plate 13 is fixed. The tilt angle changes. The change of the tilt angle can be freely controlled even while the rotary drum 10 is rotating. The purpose of changing the inclination angle is to control the size of the granulated particle size and to allow the granulated product to be taken out without changing the rotation direction. Any mechanism having a structure such as a gear system or a cylinder system may be used, and the mechanism is not specified.

回転ドラム10は、周知のスクリュー付のコンクリートミキサー機構である。回転ドラム10内部に付設されたブレード17は、回転ドラム10本体が軸芯線を中心にして回転するときに併せて旋回するが、周知のように回転ドラム10本体の回転方向によって、回転ドラム10本体内の投入物(窒素源や炭素源)を、回転ドラム10本体の底部側18に押し込むように、あるいは、開口部側19に排出するように機能する。回転ドラム10本体の底部側18に押し込むように回転するとき、行き場がなくなった投入物を回転ドラム10本体の軸線方向に直行する方向に攪拌することになる。   The rotating drum 10 is a well-known concrete mixer mechanism with a screw. The blade 17 attached to the inside of the rotating drum 10 turns together when the rotating drum 10 main body rotates around the axial center line. As is well known, depending on the rotation direction of the rotating drum 10 main body, the rotating drum 10 main body is rotated. It functions so as to push the input material (nitrogen source or carbon source) into the bottom side 18 of the main body of the rotary drum 10 or to discharge it into the opening side 19. When the rotary drum 10 is rotated so as to be pushed into the bottom side 18 of the rotating drum 10 main body, the input material having no place to go is stirred in a direction orthogonal to the axial direction of the rotating drum 10 main body.

攪拌に伴う傾斜角は、攪拌効率から水平線に対して5度〜12度に設定されるのが好ましい。攪拌動作進行に伴い、一部の投入物が丸まり小径の造粒物を形成し、次第に成長し大型化していく。造粒径の大きさを強制的に制御する場合、進行状況に合わせて傾斜角が15度〜25度に設定される。   It is preferable that the inclination angle accompanying stirring is set to 5 to 12 degrees with respect to the horizontal line from the stirring efficiency. As the stirring operation proceeds, a part of the input material is rounded to form a granulated product having a small diameter, which gradually grows and becomes larger. When forcibly controlling the size of the particle size, the inclination angle is set to 15 to 25 degrees according to the progress.

そして、ボール状の造粒物1が外形で30mm〜50mmの大きさに達したら、造粒物を取り出す動作に移行する。ボール状の造粒物1は、投入物全般の上部に浮上滞留するため、傾斜角を水平線に対して5度以下に設定すれば、回転方向を反転しなくても、完成したボール状の造粒物1は、オーバーフローして開口部側19の下端部を通過して、排出口21に排出される。   Then, when the ball-shaped granulated product 1 reaches a size of 30 mm to 50 mm in outer shape, the operation proceeds to an operation of taking out the granulated product. Since the ball-shaped granulated product 1 floats and stays at the upper part of the whole of the input material, if the inclination angle is set to 5 degrees or less with respect to the horizontal line, the completed ball-shaped granulated product can be obtained without reversing the rotation direction. The granular material 1 overflows, passes through the lower end portion of the opening side 19, and is discharged to the discharge port 21.

ボール状の造粒物1の排出動作により、回転ドラム10内部の投入物総量が減少するため、傾斜角を水平線に対して5度〜12度に戻し、排出量に相当する投入物を投入口20に投入すれば、回転方向を反転しなくても連続運転動作が可能となる。   Since the total amount of the charged material in the rotary drum 10 is reduced by the discharging operation of the ball-shaped granulated material 1, the inclination angle is returned to 5 to 12 degrees with respect to the horizontal line, and the input corresponding to the discharged amount is input to the charging port. If it is set to 20, continuous operation is possible without reversing the direction of rotation.

投入排出機構12は、回転ドラム10の開口部側19を横方向から覆うように配設されており、上部に投入口20と下部に排出口21を有し、投入口20に投入物を投入すると受け板22上に落下する。落下してきた投入物は、送りブレード23により回転ドラム10本体の底部側18に押し込むように送り込まれる。また、回転ドラム10内の投入物を全て排出する場合は回転方向を逆転すれば、開口部側19の下端部を通過して投入排出機構12の排出口21に排出するように機能する。   The charging / discharging mechanism 12 is disposed so as to cover the opening 19 of the rotary drum 10 from the lateral direction, and has a charging port 20 at the top and a discharging port 21 at the bottom, and loads the charging material into the charging port 20. Then, it falls on the receiving plate 22. The dropped input material is fed by the feed blade 23 so as to be pushed into the bottom side 18 of the rotary drum 10 main body. Further, when all of the input in the rotary drum 10 is discharged, it functions so as to pass through the lower end portion of the opening side 19 and discharge to the discharge port 21 of the input / discharge mechanism 12 if the rotation direction is reversed.

排出されたボール状の造粒物1は、ボール状に造粒された有機物の断面図の図1に示す如く、有機汚泥と蓄糞の混合物7と食品残渣A3−1や食品残渣B3−2から溶出した物質と混ざり合った粘着力を持つ物質を作り出し、投入物全体を覆う粘着層8を形成する。このボール状の造粒物1の形成により、有機汚泥2や食品残渣3や畜糞4等の窒素源と剪定枝5(6)の炭素源が混然一体となり理想的な形状になる。   As shown in FIG. 1 of the sectional view of the organic material granulated in a ball shape, the discharged ball-shaped granulated product 1 is a mixture 7 of organic sludge and feces, food residue A3-1 and food residue B3-2. A substance having an adhesive force mixed with the substance eluted from is produced, and an adhesive layer 8 covering the entire input is formed. By forming this ball-shaped granulated product 1, the nitrogen source such as the organic sludge 2, the food residue 3 and the livestock dung 4 and the carbon source of the pruned branch 5 (6) are mixed together to form an ideal shape.

ボール状の造粒物1として完成した有機廃棄物は、平コンテナーで表面乾燥後、コンテナーへ移して通気性の良い所で貯蔵熟成を行う。2〜3日程度で表面が固まり、約1週間で内部に白いものが確認される。この時期は、糖やアミノ酸などの易分解性物質が好気的に分解され、生育の早い糸状菌や好気細菌が主として活動する。このとき積み込み処理していれば、呼吸熱によって発熱が起こり温度が60〜70℃に上昇しますが、ボール状の造粒物1を重ねないで貯蔵熟成を行うことにより、20℃〜30℃の常温域で糸状菌優先のまま推移し、約2週間でボール状の造粒物1の内部は真っ白となる。この状態を過ぎればやがて菌層が変化して、酸素を盛んに消費するためボール状の造粒物1の内部が酸素不足となり、そこに嫌気性のセルロース分解菌が働き、好気性菌と嫌気性菌の役割分担が成り立ち、繊維質の分解が進む。こうして、食べるエサが少なくなる頃、分解されて軟らかくなった繊維組織を食べるいろいろな細菌が増えてくる。このころ木材腐朽菌の繁殖条件となるため、リグニンの分解が始まり温度も低下して、先に活動した菌体の死骸や排泄した酵素により他の微生物も繁殖し、さらにリグニンの分解が促進される。この段階で臭気はなく約45日〜90日貯蔵熟成が行われて完成品となる。   The organic waste completed as a ball-shaped granulated product 1 is surface-dried in a flat container, transferred to a container, and stored and aged in a place with good ventilation. The surface hardens in about 2 to 3 days, and a white thing is confirmed in about 1 week. During this period, easily degradable substances such as sugars and amino acids are aerobically decomposed, and fast-growing filamentous fungi and aerobic bacteria are mainly active. If it is loaded at this time, heat is generated due to breathing heat and the temperature rises to 60-70 ° C. However, storage aging without stacking the ball-shaped granulated product 1 results in 20-30 ° C. In the normal temperature range, the filamentous fungi remain preferential and the inside of the ball-shaped granulated product 1 becomes pure white in about 2 weeks. When this state is passed, the fungus layer will eventually change and oxygen will be actively consumed, so the inside of the ball-shaped granulated product 1 becomes deficient in oxygen, and anaerobic cellulose-degrading bacteria work there, aerobic bacteria and anaerobic The role sharing of the sex bacteria is established, and the degradation of the fiber progresses. Thus, when less food is eaten, the number of bacteria that eat fiber tissue that has been degraded and softened increases. At this time, the conditions for the growth of wood-rotting fungi were such that the decomposition of lignin began and the temperature decreased, and other microorganisms also propagated due to the dead bodies of the previously activated cells and the excreted enzymes, further promoting the decomposition of lignin. The At this stage, there is no odor and storage aging is carried out for about 45 to 90 days to give a finished product.

有機栄養微生物にとって有機物さえあればよいのだろうか。有機物のなかには、ブドウ糖(グルコース)、砂糖、でん粉、セルロースなどの糖のように、炭素、水素、酸素しかないものがある。こうした糖だけをエサにしたときは、エネルギー源としてのATPは合成されるが、菌体の増殖はほとんど起きない。これは細胞成分のうちの糖、有機酸、脂肪などしかつくれないからである。細胞成分のアミノ酸やタンパク質をつくるには窒素とイオウ、核酸をつくるにはリンも必要である。したがって糖をエサにしたときには、窒素、リン、イオウなどを無機物で与える必要がある。   Is it only necessary to have organic matter for organic nutrient microorganisms? Some organic substances have only carbon, hydrogen, and oxygen, such as sugars such as glucose (glucose), sugar, starch, and cellulose. When only these sugars are used as food, ATP is synthesized as an energy source, but there is little growth of bacterial cells. This is because only cell components such as sugar, organic acid and fat can be produced. Nitrogen and sulfur are needed to make amino acids and proteins, and phosphorus is also needed to make nucleic acids. Therefore, when sugar is used as feed, it is necessary to provide nitrogen, phosphorus, sulfur, etc. as inorganic substances.

炭素以外の元素を無機物からとることは、すべての微生物に共通することである。ただし、有機栄養微生物は、もしも有機物中にこれらの元素が含まれていれば、それも利用する。有機物中の元素だけで不足なら、無機物中の元素で補充して細胞成分を合成(有機化)し、有機物中の元素が必要量以上にあれば、無機態として元素を放出(無機化)する。しかし有機炭素源だけでは、やがて無機態窒素が枯渇する。この状態で約45日〜90日貯蔵熟成が行われてボール状の造粒物1の完成となる。   Taking elements other than carbon from inorganic substances is common to all microorganisms. However, organic vegetative microorganisms use these elements if they are contained in organic matter. If only the elements in the organic matter are insufficient, they are supplemented with the elements in the inorganic matter to synthesize cell components (organize), and if the amount of the elements in the organic matter exceeds the required amount, the elements are released in an inorganic state (inorganic). . However, organic nitrogen sources will eventually deplete inorganic nitrogen. In this state, storage aging is performed for about 45 days to 90 days, and the ball-shaped granulated product 1 is completed.

完成されたボール状の造粒物1を粉砕して農地に鋤き込ませれば、土壌中で無機態窒素を補給し、微生物はまた増加しいわゆる芳香的な匂いがする状態となる。植物が吸収するのは窒素、燐酸、カリの三大要素だけでなく、土壌中のミネラルや微生物が作り出すアミノ酸、ホルモン、ビタミン、核酸等が供給されることに現代農業では重要な意義付けがなされている。   If the completed ball-shaped granulated product 1 is pulverized and sown into the farmland, inorganic nitrogen is replenished in the soil, and microorganisms increase again, giving a so-called aromatic smell. Plants absorb not only the three major elements of nitrogen, phosphoric acid, and potash, but also the fact that amino acids, hormones, vitamins, nucleic acids, etc. produced by minerals and microorganisms in the soil are supplied, which is important in modern agriculture. ing.

本発明のボール状に造粒された有機物の断面図である。It is sectional drawing of the organic substance granulated by the ball shape of this invention. 本発明の有機廃棄物をボール状に造粒する造粒処理装置の構造を示す内部透視線を付加した斜視図である。It is the perspective view which added the internal perspective line which shows the structure of the granulation processing apparatus which granulates the organic waste of this invention to ball shape.

符号の説明Explanation of symbols

1 ボール状の造粒物
2 有機汚泥
3−1 食品残渣A
3−2 食品残渣B
4 蓄糞
5 破砕物A
6 圧縮破砕物B
7 有機汚泥と蓄糞の混合物
8 粘着層
9 造粒処理装置
10 回転ドラム
11 駆動モーター
12 投入排出機構
13 可動板
14 固定板
15 可変機構
16 回転体
17 ブレード
18 底部側
19 開口部側
20 投入口
21 排出口
22 受け板
23 送りブレード

1 Ball-shaped granules 2 Organic sludge 3-1 Food residue A
3-2 Food residue B
4 Feces 5 Crushed material A
6 Compression crush B
7 Mixture of organic sludge and feces 8 Adhesive layer 9 Granulation processing device 10 Rotating drum 11 Drive motor 12 Loading / discharging mechanism 13 Movable plate 14 Fixed plate 15 Variable mechanism 16 Rotating body 17 Blade 18 Bottom side 19 Opening side 20 Input port 21 Discharge port 22 Back plate 23 Feed blade

Claims (3)

有機汚泥や食品残渣や畜糞等を無臭発酵させる造粒物形成において、チップ化又は綿くず化した木屑を、アルカリ処理により分解の障壁となるリグニン等の分解抵抗を低める工程と、微生物活性液を浸潤させる工程を施した炭素源と、有機汚泥や食品残渣や畜糞等の窒素源とを、造粒処理装置によって微生物資材と混練し、粘着力によりボール状に造粒することを特徴とする造粒物形成方法。   In the formation of granules for odorless fermentation of organic sludge, food residues, livestock excrement, etc., a process to reduce degradation resistance such as lignin, which becomes a decomposition barrier by chipping or scrapping wood chips, and a microorganism active liquid A carbon source that has been infiltrated and a nitrogen source such as organic sludge, food residue, and livestock excreta are kneaded with microbial materials using a granulator and granulated into a ball shape with adhesive strength. Granule formation method. ボール状に造粒された請求項1の炭素源と窒素源を、20℃〜30℃の常温域で低温発酵させて、木材腐朽菌の繁殖条件下で、常に理想的なC/N比率を確保し、窒素成分の流出を防止し、土壌的価値の高い肥料とすることを特徴とする堆肥化処理方法。   The carbon source and nitrogen source of claim 1 granulated in a ball shape are subjected to low-temperature fermentation in a room temperature range of 20 ° C. to 30 ° C., and an ideal C / N ratio is always obtained under the breeding conditions of wood-rotting fungi. A composting method characterized in that the fertilizer has a high soil value by securing and preventing the outflow of nitrogen components. 請求項1で使用する造粒処理装置は、ミキサーの回転ドラム部の傾斜角が回転動作中に変更可能な機構を有し、水分率の変動に対し傾斜角を変更することで、造粒径の大きさを制御することを特徴とする造粒処理装置。
The granulation processing apparatus used in claim 1 has a mechanism in which the inclination angle of the rotating drum portion of the mixer can be changed during the rotation operation, and by changing the inclination angle with respect to fluctuations in moisture content, The granulation processing apparatus characterized by controlling the magnitude | size.
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