JP6588710B2 - Method for producing liquid manure and co-products from compostable surplus organic matter - Google Patents

Method for producing liquid manure and co-products from compostable surplus organic matter Download PDF

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JP6588710B2
JP6588710B2 JP2015047802A JP2015047802A JP6588710B2 JP 6588710 B2 JP6588710 B2 JP 6588710B2 JP 2015047802 A JP2015047802 A JP 2015047802A JP 2015047802 A JP2015047802 A JP 2015047802A JP 6588710 B2 JP6588710 B2 JP 6588710B2
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森田 剛
剛 森田
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森田 剛
剛 森田
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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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel
    • 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
    • Y02W30/20Waste processing or separation
    • 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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  • Processing Of Solid Wastes (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Treatment Of Sludge (AREA)
  • Crushing And Pulverization Processes (AREA)
  • Fertilizers (AREA)

Description

本発明は、メタン発酵消化液と堆肥化可能余剰有機物から液肥とコプロダクツを生産する方法に関する。 The present invention relates to a method for producing liquid fertilizer and co-products from methane fermentation digestive liquid and compostable surplus organic matter.

現在の堆肥化可能有機廃棄物から液肥を製造するためには複雑な工程が含まれているので、経済性に富んだものではない。また現在の方法では、その工程をおこなうために、高価な設備、機械を必要とする。その結果、現在の方法や工程は、堆肥化可能有機廃棄物から液肥を製造することは困難で、実際的ではなく、経済的に実行、利用することが難しい。 Producing liquid fertilizer from current compostable organic waste is not economical because it involves complicated processes. In addition, the current method requires expensive equipment and machines in order to perform the process. As a result, current methods and processes make it difficult to produce liquid manure from compostable organic waste, which is impractical and difficult to implement and use economically.

一方、メタン発酵消化液の有効利用には特開2006−265052号公報に貯蔵技術が開示されているが、メタン発酵消化液の保存についてのものであり、有効利用についてのものではない。 On the other hand, although the storage technique is disclosed by Unexamined-Japanese-Patent No. 2006-265052 for effective utilization of methane fermentation digestive liquid, it is about preservation | save of methane fermentation digestive liquid, and is not about effective utilization.

特開2006−265052号公報JP 2006-265052 A

現在の堆肥化可能有機廃棄物から液肥を製造するためには複雑な工程が含まれているので、経済性に富んだものではない。また現在の方法では、その工程をおこなうために、高価な設備、機械を必要とする。その結果、現在の方法や工程は、堆肥化可能有機廃棄物から液肥を製造することは困難で、実際的ではなく、経済的に実行、利用することが難しい。 Producing liquid fertilizer from current compostable organic waste is not economical because it involves complicated processes. In addition, the current method requires expensive equipment and machines in order to perform the process. As a result, current methods and processes make it difficult to produce liquid manure from compostable organic waste, which is impractical and difficult to implement and use economically.

本発明は、堆肥化可能有機性廃棄物から、次のステップにより、液体肥料(液肥)と、同時並行的にコプロダクツを作り出す方法に関するものであり、1.堆肥化可能有機性廃棄物を堆肥化できない廃棄物より分別し、2.分別された堆肥化可能有機性廃棄物の大きさを小さくし、3.事前にきめられた量のメタン発酵消化液をタンク・貯水槽に投入し、4.そのメタン発酵消化液の入ったタンク・貯水槽に上述の小さくなった分別済の堆肥化可能有機性廃棄物をある比率にて投入し、5.そのメタン発酵消化液の入ったタンク貯水槽に上述の小さくなって投入された堆肥化可能有機性廃棄物を攪拌し、6.その結果得られる製品(液肥)と副生産物を集荷、分別するものである。 The present invention relates to a method for producing co-products in parallel with liquid fertilizer (liquid fertilizer) from compostable organic waste by the following steps: 1. Separate compostable organic waste from waste that cannot be composted; 2. Reduce the size of sorted compostable organic waste; 3. A predetermined amount of methane fermentation digestive juice is put into the tank / water tank. 4. Put the above-mentioned reduced sorted compostable organic waste in a certain ratio into the tank / water tank containing the methane fermentation digestive liquid. 5. Stir the compostable organic waste introduced into the tank reservoir containing the methane fermentation digestive juice into a small amount as described above. The resulting product (liquid fertilizer) and by-products are collected and separated.

第1の発明は、堆肥化可能余剰有機物の大きさを縮小し、メタン発酵消化液に対して一定の決められた比率の範囲内の堆肥化可能有機物をタンク内のメタン発酵消化液中に投入し、堆肥化可能有機物とメタン発酵消化液の混合液を攪拌し、熟成させ、最終製品と同時並行して生産される副生産物を分別、集荷する堆肥化可能余剰有機物から液肥とコプロダクツを生産する方法である。
第2の発明は、メタン発酵消化液と堆肥化可能余剰有機物から液肥とコプロダクツを生産する方法であって、以下に示す工程よりなる。
堆肥化不可廃棄物と堆肥化可能余剰有機物を分別する工程
分別された堆肥化可能余剰有機物の大きさを縮小する工程
事前に決められた量のメタン発酵消化液を、タンク・貯水槽に投入する工程
そのタンク・貯水槽に一定の決められた比率の範囲内の分別され微細化した堆肥化可能余剰有機物を一定の間隔で(日々)投入する工程
その分別され微細化した堆肥化可能余剰有機物とメタン発酵消化液の貯水槽の混合液を一定の間隔で(日々)攪拌する工程
そして、最終製品と同時並行して生産される副生産物を集荷、分別する工程
第3の発明は、第1または第2の発明において、タンク・貯水槽における混合液のPHを中性域(PH6―8)に維持する堆肥化可能余剰有機物から液肥とコプロダクツを生産する方法である。
第4の発明は、第2または第3の発明において、メタン発酵消化液に対する堆肥化可能余剰有機物量を0.1−20質量%の範囲とする堆肥化可能余剰有機物から液肥とコプロダクツを生産する方法である。
第5の発明は、第2〜第4のいずれかの発明において、メタン発酵消化液に対する堆肥化可能余剰有機物量を0.1−10質量%の範囲とする堆肥化可能余剰有機物から液肥とコプロダクツを生産する方法である。
第6の発明は、第2〜第5のいずれかの発明において、タンク・貯水槽における、濃縮されたメタン発酵消化液と堆肥化可能余剰有機物に0.1−10質量%の範囲で水分を加えて実行する堆肥化可能余剰有機物から液肥とコプロダクツを生産する方法である。
第7の発明は、第1〜第6のいずれかの発明において、堆肥化可能余剰有機物を切断機(シュレッダー)または/および、粉砕機(クラッシャー)により、細かくする堆肥化可能余剰有機物から液肥とコプロダクツを生産する方法である。
第8の発明は、第1〜第7のいずれかの発明において、メタン発酵消化液はアルコール工場の廃液と汚泥からつくられる堆肥化可能余剰有機物から液肥とコプロダクツを生産する方法である。
第9の発明は、第1〜第8のいずれかの発明において、メタン発酵消化液はアルコール工場の廃液と汚泥からつくられる堆肥化可能余剰有機物から液肥とコプロダクツを生産する方法である。
第10の発明は、第1〜第9のいずれかの発明において、副生産物はミミズ堆肥製造の原料としてミミズ培地で餌となる堆肥化可能余剰有機物から液肥と副生産物を生産する方法である。
第11の発明は、第1〜第10のいずれかの発明において、副生産物は水生動物の餌となるウジである堆肥化可能余剰有機物から液肥とコプロダクツを生産する方法である。
1st invention reduces the magnitude | size of the compostable surplus organic substance, and throws into the methane fermentation digestive liquid in a tank the compostable organic substance in the range of the fixed ratio fixed with respect to the methane fermentation digestive liquid. Then, the mixture of compostable organic matter and methane fermentation digestion liquid is stirred and aged, and the by-product produced in parallel with the final product is separated and collected. It is a production method.
The second invention is a method for producing liquid fertilizer and co-products from methane fermentation digestive liquid and compostable surplus organic matter, and includes the following steps.
A process for separating non-compostable waste and compostable surplus organic matter A process for reducing the size of the separated compostable surplus organic matter A predetermined amount of methane fermentation digestive liquid is put into a tank / water tank. The process of supplying the fractionated and refined compostable surplus organic matter in a certain fixed ratio range to the tank / water tank at regular intervals (daily) The fractionated and refined compostable surplus organic matter and The step of stirring the mixed liquid of the methane fermentation digestive fluid storage tank at regular intervals (daily) and the step of collecting and separating by-products produced in parallel with the final product. Alternatively, in the second invention, the liquid fertilizer and the co-products are produced from the compostable surplus organic matter that maintains the pH of the mixed liquid in the tank / water tank in a neutral region (PH 6-8).
4th invention produces liquid fertilizer and a co-product from the compostable surplus organic substance which makes compostable surplus organic substance quantity with respect to methane fermentation digestive liquid the range in 0.1-20 mass% in 2nd or 3rd invention It is a method to do.
5th invention is liquid fertilizer and co-fertilizer from compostable surplus organic substance which makes the amount of surplus organic substance compostable with respect to methane fermentation digestive liquid in the range of 0.1-10 mass% in any one of 2nd-4th invention. It is a method of producing products.
The sixth invention is the invention according to any one of the second to fifth inventions, wherein the concentrated methane fermentation digestive liquid and the compostable surplus organic matter in the tank / water tank are supplied with water in a range of 0.1-10% by mass. In addition, it is a method to produce liquid fertilizer and co-products from compostable surplus organic matter.
According to a seventh invention, in any one of the first to sixth inventions, the compostable surplus organic matter is made fine from the compostable surplus organic matter by a cutting machine (shredder) and / or a crusher (crusher). This is a method for producing co-products.
The eighth invention is a method for producing liquid fertilizer and co-products from compostable surplus organic matter produced from waste liquid and sludge of an alcohol factory in any one of the first to seventh inventions.
A ninth invention is a method for producing liquid fertilizer and co-products from compostable surplus organic matter produced from waste liquid and sludge of an alcohol factory in any one of the first to eighth inventions.
A tenth invention is a method of producing liquid fertilizer and a by-product from compostable surplus organic matter serving as a feed in an earthworm medium as a raw material for earthworm compost production in any one of the first to ninth inventions. is there.
The eleventh invention is a method for producing liquid fertilizer and co-products from compostable surplus organic matter, which is a maggot as a feed for aquatic animals, in any one of the first to tenth inventions.

本発明は液肥を製造する一般的な方法であるが、非常に稀有なことは、安く、簡単に、効率よく堆肥化可能有機廃棄物から液肥とコプロダクツが製造出来ることである。 Although the present invention is a general method for producing liquid fertilizer, what is very rare is that liquid fertilizer and co-products can be produced from organic waste that is cheap, simple and efficient.

図1は本発明の堆肥化可能有機廃棄物より液肥とコプロダクツを生産する一般的な工程図である。FIG. 1 is a general process diagram for producing liquid manure and co-products from the compostable organic waste of the present invention. 図2は本発明の堆肥化可能有機廃棄物より生産された液肥とコプロダクツがどのように生産されるかを示した図である。FIG. 2 is a diagram showing how liquid fertilizer and co-products produced from the compostable organic waste of the present invention are produced. 図3は、本発明を実行するためのタンク・貯水槽の様子を示した図である。FIG. 3 is a diagram showing a state of a tank / water tank for carrying out the present invention.

本発明の第一の目的は、堆肥化可能有機廃棄物から液肥を製造する簡単で、効率よく、安価な方法とすることで、上述した現在の方法の技術的問題点、非効率性を解決するものである。このように、本発明では、簡単に設置し、維持管理ができる堆肥製造用のタンク、貯水槽だけが必要で、高価で複雑な設備、機械は必要としない。 The first object of the present invention is to solve the technical problems and inefficiencies of the above-mentioned current method by producing a simple, efficient and inexpensive method for producing liquid manure from compostable organic waste. To do. Thus, in the present invention, only a compost production tank and a water storage tank that can be easily installed and maintained are required, and expensive and complicated equipment and machines are not required.

本発明の次の目的は、現在利用されている方法では悪臭を生じさせるが堆肥化可能有機廃棄物から、液肥・コプロダクツ15を作り出し方法でメタン発酵消化液によって、堆肥化可能有機廃棄物10は短期間に簡単に効率よく分解されることで、悪臭を周辺に出すことを抑制することができる。 The next object of the present invention is to produce compostable organic waste from compostable organic waste that produces malodor in the currently used method, but compostable organic waste 10 by using a methane fermentation digestion solution in the method. Can be easily and efficiently decomposed in a short period of time, thereby suppressing the occurrence of bad odors in the vicinity.

更に、本発明は、堆肥化可能有機廃棄物より、液肥(LIQUID)・コプロダクツ( CO-PRODUCTS) 15を簡単に作ることができるものである。これらの、本発明が、より優れていることが添付された図によって明らかで、また詳細に理解できるであろう。 Furthermore, the present invention can easily produce liquid manure (LIQUID) and co-products (CO-PRODUCTS) 15 from compostable organic waste. These and other advantages of the present invention will become apparent and more fully understood from the accompanying drawings.

図解の図1に関して、堆肥化可能有機廃棄物10から、液肥(LIQUID)・コプロダクツ15は図1に示したようなステップで製造される。下記はそれを示したものである。
a.堆肥化不可有機性廃棄物と堆肥化可能有機性廃棄物を分別する。
(SEGRIGATION) 11
b.粉砕機、切断機によって、分離された堆肥化可能有機性廃棄物の大きさを細かくする (CRUSHING/SCHREDDING) 12
c.メタン発酵消化液が投入された堆肥製造用のタンク、貯水槽に細かくなった分離済み堆肥化可能有機性廃棄物を事前に決められた率で投入する (FEEDING INTO COMPOST TANK POND/DRUMS) 13
d.最終の製品(液肥)・コプロダクツ15を分離回収する(SEPARATING/COLLECTING) 14
With reference to FIG. 1 of the illustration, from a compostable organic waste 10, a liquid manure (LIQUID) coproduct 15 is manufactured in steps as shown in FIG. The following is an illustration of this.
a. Separate non-compostable organic waste from compostable organic waste.
(SEGRIGATION) 11
b. Reduce the size of compostable organic waste separated by crusher and cutting machine (CRUSHING / SCHREDDING) 12
c. Compost production tanks with fermented methane fermented digestion and water storage tanks that are separated into compostable organic waste at a predetermined rate (FEEDING INTO COMPOST TANK POND / DRUMS) 13
d. Separate and recover the final product (liquid fertilizer) and co-products 15 (SEPARATING / COLLECTING) 14

図2は堆肥化可能有機廃棄物10から製造された液肥・コプロダクツ 15の講成を示したものである。
主生産品は嫌気性活動(開放系であり、完全な嫌気性環境ではない)によって生成された高品質の液肥16である。これは、浮遊物(FLOATINGS)17とウジ(MAGGOTS)18が同時に生産される。
FIG. 2 shows a course for liquid fertilizer / co-products 15 manufactured from compostable organic waste 10.
The main product is high quality liquid fertilizer 16 produced by anaerobic activity (open system, not a complete anaerobic environment). As for this, the floating substance (FLOATINGS) 17 and the maggot (MAGGOTS) 18 are produced simultaneously.

浮遊物17はミミズ培地(FEED TO VERMICULTURE)19に与えられる。詳しくいうと、浮遊物は,ミミズ堆肥肥料(COMPOST FERTILIZER) 20を生産するミミズ培地に、その餌として与えられ、ミミズが消化することの出来る餌である。 The suspended matter 17 is fed to an earthworm medium (FEED TO VERMICULTURE) 19. More specifically, the suspended matter is a feed that can be digested by the earthworm that is fed to the earthworm medium that produces the COMPOST FERTILIZER 20.

主たる生産物である、高品質の液肥16は、主として農作物、特に農場や庭(FERTILIZER FOR HOME/GARDEN)21 で,生産される果実、野菜などに利用される。一方、ウジ(MAGGOTS)18については、養殖池(FISH POND)22の餌として利用される。 The main product, high-quality liquid fertilizer 16, is mainly used for crops, especially fruits and vegetables produced in farms and gardens (FERTILIZER FOR HOME / GARDEN) 21. On the other hand, the maggot 18 is used as food for the fish pond 22.

本発明の方法を開始するにあたり、図3で示したようなタンク・貯水槽Pを準備する。タンク・貯水槽Pは、コンクリートの床B、底の部分F、側壁Wから構成され,上部は開放式Tとなっている。タンク・貯水槽Pを清掃するための排水口が側壁Wの一つにつけられる(図では記載なし)堆肥化用のタンク・貯水槽Pは、コンクリート製で、屋根付の設備があることが望ましい。 In starting the method of the present invention, a tank / water tank P as shown in FIG. 3 is prepared. The tank / water tank P is composed of a concrete floor B, a bottom portion F, and a side wall W, and an upper portion is an open type T. A drain outlet for cleaning the tank / water tank P is attached to one of the side walls W (not shown in the figure). The composting tank / water tank P is preferably made of concrete and has a roofed facility. .

本発明では、メタン発酵消化液には、例えば、サトウキビからの抽出液をアルコール発酵を行った廃液をメタン発酵を行った消化液が使用できる。この場合は、組成のバラツキか少ないメタン発酵消化液が大量に得られる。その他、家庭、飲食店、食堂、ホテル、小売り店(スーマーマーケット、コンビニエンスストア等)卸売店、食品加工工場、各種の市場(青果物市場、魚市場)からの廃棄物、農場、畜産場、娯楽施設からの堆肥化可能有機廃棄物をメタン発酵させた消化液が使用できることももちろんである。 In the present invention, as the methane fermentation digestive liquid, for example, a digested liquid obtained by subjecting a waste liquid obtained by alcohol fermentation to an extract from sugarcane to methane fermentation can be used. In this case, a large amount of methane fermentation digestive juice with little variation in composition can be obtained. Others, households, restaurants, restaurants, hotels, retail stores (summer markets, convenience stores, etc.) wholesale stores, food processing factories, waste from various markets (fruits and vegetables market, fish market), farms, livestock farms, entertainment facilities Of course, it is possible to use digestive juice obtained by methane fermentation of compostable organic waste.

本発明では、堆肥化可能有機廃棄物10から,液肥・コプロダクツ15を生産するために家庭、飲食店、食堂、ホテル、小売り店(スーマーマーケット、コンビニエンスストア等)、食品加工工場、各種の市場(青果物市場、魚市場)からの廃棄物、農場、畜産場、娯楽施設からの堆肥化可能有機廃棄物を集荷することから始まる。また、それから、人手を使って、または、従来型の機械による選別によって、堆肥化不可廃棄物を取り除く。その分別された堆肥化可能有機廃棄物10は効果的なプロセスと分解のために小さなサイズにする必要がある。これは粉砕、切断の設備によって実行されるのが好ましいが、人力または従来型の粉砕、切断機でも構わない。 In the present invention, in order to produce liquid manure / co-products 15 from compostable organic waste 10, households, restaurants, canteens, hotels, retail stores (smart markets, convenience stores, etc.), food processing factories, various markets It begins with the collection of compostable organic waste from farms, livestock farms and recreational facilities (from the fruit and vegetable market, fish market). Also, non-compostable waste is removed manually or by sorting with conventional machines. The sorted compostable organic waste 10 needs to be sized for effective process and decomposition. This is preferably carried out by crushing and cutting equipment, but may also be manual or conventional crushing and cutting machines.

次の工程は、事前に決められた量のメタン発酵消化液を、タンク・貯水槽Pに満たすことである。メタン発酵消化液がタンク・貯水槽Pが満たされていたら、そこに、細かくなった堆肥化可能有機廃棄物10を投入する。 The next step is to fill the tank / water tank P with a predetermined amount of methane fermentation digestive juice. If the tank and the water storage tank P are filled with the methane fermentation digestive liquid, the compostable organic waste 10 that has become finer is put therein.

本発明では、事前に準備投入されたメタン発酵消化液に対して決められた比率の堆肥化可能有機廃棄物を一定の間隔で(日々)投入するものである。そして、一定の間隔で攪拌するものである。 In the present invention, a compostable organic waste in a predetermined ratio with respect to the methane fermentation digestive liquid prepared and input in advance is input at regular intervals (daily). And it stirs at a fixed interval.

重要なことは、最終の液肥・コプロダクツ15を作り出すために、タンク・貯水槽Pの菌の活動を維持する必要があるので、一定の間隔で決められた比率の堆肥化可能有機廃棄物10を投入することが求められる。 Importantly, in order to produce the final liquid fertilizer / co-products 15, it is necessary to maintain the fungal activity in the tank / water tank P, so that the compostable organic waste 10 at a fixed ratio can be determined at regular intervals. Is required.

結果として発生する製品、液肥・コプロダクツ15は、高品質の液肥16、浮遊物17、ウジ18で、これらは直ぐに使用するのであれば日々、収穫、更には分別が必要となる。液肥・コプロダクツ15の収穫は人力または、これまで従来からの機械によって行っても良い。 The resulting product, liquid fertilizer / co-products 15 are high-quality liquid fertilizer 16, suspended matter 17 and maggot 18, and if they are used immediately, they need to be harvested and separated daily. The harvesting of the liquid fertilizer / co-products 15 may be performed manually or by a conventional machine.

更に重要なことは、タンク・貯水槽Pにおける混合物のPHが中性域(PH6−8)であることで、この判定は、これまでの従来の方法で行われる。PHはメタン発酵消化液と、それに対する一定の比率にて投入される堆肥化可能有機廃棄物の比率に左右される。 More importantly, the PH of the mixture in the tank / water tank P is in the neutral range (PH6-8), and this determination is performed by the conventional method so far. PH depends on the ratio of methane fermentation digestive liquid and compostable organic waste that is input at a fixed ratio.

PHは原料となる堆肥化可能有機廃棄物の状態により変化するが、この範囲内に維持することが好ましい。PHが6未満の場合、また、PHが8を超える場合は、反応が遅くなる。そのため、PHが6〜8の範囲に入るようにすることが好ましいが、やや酸性、アルカリ性の場合(PHが5〜9)でも、反応は進行する。メタン発酵消化液のPHは機器による測定、または、表面状態(泡の発生状態等)により推測する。 Although PH changes with the state of the compostable organic waste used as a raw material, it is preferable to maintain within this range. When PH is less than 6 or when PH exceeds 8, the reaction is slowed down. For this reason, it is preferable that the pH is in the range of 6 to 8, but the reaction proceeds even if the pH is slightly acidic or alkaline (PH is 5 to 9). The PH of the methane fermentation digestion liquid is estimated by measurement with an instrument or the surface state (such as the state of foam generation).

本発明における、もう一つの指標は、メタン発酵消化液に対する堆肥化可能有機廃棄物10の実用範囲を0.1質量%から20質量%とすることである。例えば、タンク・貯水槽Pにメタン発酵消化液を、1,000kg準備すれば、(1〜)200kg以内の堆肥化可能有機廃棄物10を、そのタンク貯水槽Pに一定の間隔で投入して攪拌することである。この量の上下限は配合する堆肥化可能有機廃棄物10の組成により異なる。農産物廃棄系(葉菜、オクラ等)の植物性堆肥化可能有機廃棄物の場合の上限が200kgであり、畜産系の廃棄物の割合が増加すると、上限値は低くなる。 Another index in the present invention is to set the practical range of the compostable organic waste 10 to 0.1% by mass to 20% by mass with respect to the methane fermentation digestive juice. For example, if 1,000 kg of methane fermentation digestive liquid is prepared in a tank / water tank P, (1) up to 200 kg of compostable organic waste 10 is introduced into the tank water tank P at regular intervals. To stir. The upper and lower limits of this amount depend on the composition of the compostable organic waste 10 to be blended. The upper limit in the case of organic waste that can be composted from agricultural products (leaf vegetables, okra, etc.) is 200 kg, and the upper limit decreases as the proportion of livestock waste increases.

植物性堆肥化可能有機廃棄物に、畜産系の廃棄物の割合が増加すると、PHが上がるため、投入の上限値は低くなる。この場合の指標は、メタン発酵消化液に対する堆肥化可能有機廃棄物10の実用範囲を0.1質量%から10質量%とすることである。例えば、タンク・貯水槽Pにメタン発酵消化液を、1,000kg準備すれば、(1〜)100kg以内の堆肥化可能有機廃棄物10を、そのタンク貯水槽に一定の間隔で投入して攪拌することである。下限値の0.1%は、それ以下の場合は、表面状態がメタン発酵は進まないため、および、生産性を維持するための値である。 When the proportion of livestock waste increases in plant compostable organic waste, the PH increases, so the upper limit of input becomes lower. The index in this case is that the practical range of the compostable organic waste 10 with respect to the methane fermentation digestive juice is 0.1 mass% to 10 mass%. For example, if 1,000 kg of methane fermentation digestive liquid is prepared in a tank / water tank P, (1) 100 kg of compostable organic waste 10 is introduced into the tank water tank at regular intervals and stirred. It is to be. When the lower limit is 0.1% or less, the surface state is a value for maintaining the productivity because methane fermentation does not proceed.

本発明におけるメタン発酵消化液はアルコール製造からの廃液、残渣に由来していることが望ましい。メタン発酵消化液は最終製品である液肥・コプロダクツ15を生産するための、堆肥化可能有機廃棄物10を分解する微生物群を含んでいる。堆肥化用タンク・貯水槽Pのなかで、メタン発酵消化液と堆肥化可能余剰有機物10の混合物の濃度が上昇した場合の調整は、メタン発酵消化液に対して、事前に決められた率の水を混合物に投入することが、本発明の方法である。堆肥化可能余剰有機物の混合物の濃度が上がりすぎると、反応速度が低下する。水の比率は、事前に決められたメタン発酵消化液の0.1−10質量%の範囲である。 It is desirable that the methane fermentation digestive liquid in the present invention is derived from waste liquid and residue from alcohol production. The methane fermentation digestive fluid contains a group of microorganisms that decompose the compostable organic waste 10 to produce the final product, liquid fertilizer / co-products 15. Adjustment when the concentration of the mixture of methane fermentation digestion liquid and compostable surplus organic matter 10 in the composting tank / water storage tank P is increased with respect to the methane fermentation digestion liquid at a predetermined rate. It is the method of the present invention that water is introduced into the mixture. If the concentration of the compostable surplus organic material is too high, the reaction rate decreases. The ratio of water is in the range of 0.1-10% by weight of the predetermined methane fermentation digestive fluid.

水の比率は、事前に決められたメタン発酵消化液の0.1−10質量%の範囲は、10質量%以上の投入では希釈されすぎ、反応速度が低下する。下限値の0.1質量%は、実質的な作業能率を考慮した値である。なお、投入は複数回に分けて行うこと、攪拌しつつ行うことが好ましい。 As for the ratio of water, a predetermined range of 0.1-10% by mass of the methane fermentation digestive juice is excessively diluted when 10% by mass or more is added, and the reaction rate decreases. The lower limit of 0.1% by mass is a value in consideration of substantial work efficiency. In addition, it is preferable to perform charging in a plurality of times and with stirring.

これまでに述べて来たタンク・貯水槽Pにおける、メタン発酵消化液と堆肥化可能余剰有機物10の混合液の濃度は伝統的な方法にて調べることも可能であるし、混合物において泡の発生が減少することでも、判断が可能である。タンク・貯水槽Pの中の濃度は、嫌気性発酵(完全な嫌気性環境ではない)を維持して、求める液肥・コプロダクツ15が発生するものでなければならない。 The concentration of the mixed liquid of methane fermentation digestive liquid and compostable surplus organic matter 10 in the tank / reservoir P described so far can be examined by a traditional method, and generation of bubbles in the mixture Judgment is also possible by a decrease in. The concentration in the tank / water tank P must be such that the required liquid fertilizer / co-products 15 are generated while maintaining anaerobic fermentation (not a complete anaerobic environment).

本発明をより優位にするために変更することは、この方式においては可能である。本発明は、幅広い便利性をもっているので、本件でしめされた事例にこだわらない。すなわち、本件で示された基本的な考え方から逸脱しない限り、修正をすることは可能である。 Modifications can be made in this manner to make the invention more advantageous. Since the present invention has a wide range of convenience, it does not stick to the case shown in this case. In other words, modifications can be made without departing from the basic idea shown in this case.

メタン発酵消化液には、アルコール工場の廃液と汚泥からの抽出液を用いたが、これにかぎられるものではない。アルコール工場の対象物は、トウモロコシ、サトウキビ、各種醸造工場の廃液、汚泥からの抽出液も使用可能である。 For the methane fermentation digestive juice, the waste liquid from the alcohol factory and the extract from sludge were used, but this is not the only option. As the target of the alcohol factory, corn, sugar cane, effluent from various breweries, and extract from sludge can be used.

分解能力の確認のために連続投入はせずに、設定後の変化と、その液体での農業利用、ミミズが生息できる土壌が確保されているかどうか(oecdの化学物質の残存度の影響調査の方式に近い方法で)を行なった。(試験A)
結果を表1〜表6に示す。
In order to confirm the decomposition ability, without continuous input, changes after setting, agricultural use with the liquid, and whether soil where earthworms can inhabit have been secured (inspection effect of oecd's chemical residue In a manner close to the method). (Test A)
The results are shown in Tables 1-6.

結果を纏めると以下のようになる。
1.生ゴミを粉砕してメタン発酵消化液に投入すると、分解が進む。
2.その状況は泡の発生という形で確認できる。
3.繊維質は主として浮遊物となって分解に時間がかかるが、柔らかくなる。ことによってミミズの餌として利用できることが確認された。
4.浮遊物を順じ利用してゆくことで、メタン発酵消化液の濃度は下がり連続投入への応用が見えてきた。
5.農産物の施肥にも、問題がないようであることが確認された。
6.25日で泡の発生が少なくなっていることは、メタン発酵発電の投入比率と似たような数値である。これから連続投入の量を考えると4−5%が一つの指標になると思われる。
The results are summarized as follows.
1. When raw garbage is crushed and put into methane fermentation digestive liquid, decomposition proceeds.
2. The situation can be confirmed in the form of bubbles.
3. The fiber is mainly suspended and takes time to decompose, but becomes soft. It was confirmed that it can be used as food for earthworms.
4). By using the suspended matter one after another, the concentration of methane fermentation digestion liquid decreased, and the application to continuous input became visible.
5. It was confirmed that there was no problem in fertilizing agricultural products.
It is a numerical value similar to the input ratio of methane fermentation power generation that generation | occurrence | production of foam has decreased in 6.25 days. Considering the amount of continuous input from now on, 4-5% would be an indicator.

実施例1(試験A)の結果より連続投入による結果と泡の発生、PHの変化をテストする。(試験B)その結果を表7、表8に示す。 From the result of Example 1 (Test A), the result of continuous charging, the generation of bubbles, and the change in PH are tested. (Test B) The results are shown in Tables 7 and 8.

実施例1(試験A)をふまえて、通常の家庭よりの生ゴミ(各種のものが混じっている)を分解テストした。粉砕機は、小型のもので、ペースト状にはならず、切断されたような状態である。結果を表9、表10に示す。 Based on Example 1 (Test A), the garbage from normal households (mixed with various items) was subjected to a decomposition test. The pulverizer is small, does not become a paste, and is in a state of being cut. The results are shown in Tables 9 and 10.

上記の3つの試験結果(実施例1〜3)より、以下の結論を得た。
1.生ゴミ、余剰有機物をメタン発酵消化液で分解すことは可能である。
2.分解が可能な物質を分別して、できることならばペースト状にすりつぶすことが望ましいが、機械の設置の問題などで、切断だけでも行うことで効果がある。
3.メタン発酵消化液と物質の接触面積を増やすために切断、粉砕が必要であるが、同時に適度な攪拌をすることは必要である。
4.分解の活動は泡が発生していることで確認することが出来る。分解が進んで完了すると、泡の発生が止まる。再度投入をすると、泡の活性が再開することも確認できている(別途)。
5.PHを中性域に保つことで、分解の状態を保つことができる。
6.取り出した余剰メタン消化液(拡大したもの)は、液体肥料として野菜などに与えた場合に、通常の発電から発生するメタン発酵消化液と同等の効果が見られる。
7.浮遊物はミミズ培地で有効な餌となる。これは適度に残った繊維質が空気層を作ってミミズの侵入に効果てきであることと、ミミズが好むPHのレベルにあることである。腐敗菌などが多い場合はPHは酸性が強く、ゴミの山にミミズを放っても中には入り込まない。ミミズが入り込むこと自体が、すでに堆肥製造の有効な原料となっていることを示していると考えられる。
The following conclusions were obtained from the above three test results (Examples 1 to 3).
1. It is possible to decompose raw garbage and surplus organic matter with methane fermentation digestive juice.
2. It is desirable to separate the decomposable substance, and if possible, to grind it into a paste, but it can be effective by cutting alone because of problems such as machine installation.
3. Cutting and crushing are necessary to increase the contact area between the methane fermentation digestive juice and the substance, but it is necessary to carry out appropriate stirring at the same time.
4). The activity of decomposition can be confirmed by the occurrence of bubbles. When decomposition proceeds and completes, the generation of bubbles stops. It has also been confirmed that the foam activity resumes when charged again (separately).
5. By maintaining the pH in a neutral range, the decomposition state can be maintained.
6). When the extracted excess methane digested liquid (enlarged) is given to vegetables as a liquid fertilizer, the same effect as the methane fermentation digested liquid generated from normal power generation is seen.
7). Suspensions are an effective bait in earthworm medium. This is because the moderately remaining fiber forms an air layer and is effective for the invasion of earthworms, and is at the PH level preferred by earthworms. When there are many spoilage bacteria etc., PH is strong acidity, and even if it releases a worm to a pile of garbage, it does not enter inside. The entry of earthworms is considered to indicate that it is already an effective raw material for compost production.

5m×1.1m×1.2m(液体の深さは0.8m)のタンク・貯水槽Pにサトウキビからのアルコール工場からの廃液、残渣からなるメタン発酵消化液(PH7.5)を4,400リットル投入した。その後、粉砕したオクラくずを、攪拌しつつ200kgを毎日投入した。その後の1日毎のPHは、7.5で変化はなかった。最初の投入後から20日後にオクラくずを攪拌しつつ700kg投入した。その結果、PHは5.5を計測し泡の発生が減少した.不純物として石灰が混入し、PHが8.5になり泡の発生が減少した。(反応速度が低下した。) 4400 methane fermentation digestive fluid (PH7.5) consisting of waste liquid from alcohol factory from sugarcane and residue in tank / water tank P of 5m × 1.1m × 1.2m (liquid depth is 0.8m) Added liters. Thereafter, 200 kg of crushed okra waste was added daily with stirring. Thereafter, the daily PH was 7.5, unchanged. After 20 days from the first charging, 700 kg of okra waste was added with stirring. As a result, PH was measured to be 5.5 and foam generation decreased. Lime was mixed as an impurity, PH became 8.5 and foam generation decreased. (Reaction rate decreased.)

その後、タンク・貯水槽P内より、液肥・コプロダクツ15を抽出後、野菜(キャベツ):100Kg、オクラ:200Kg、水産工場からの廃棄物(魚のあら):100Kgを投入した。この場合には、濃度が上昇したため、泡の発生が減少した。そのため水:100kgを投入し、平常状態に復帰させた。
Thereafter, liquid fertilizer / co-products 15 were extracted from the tank / water tank P, and then vegetables (cabbage): 100 kg, okra: 200 kg, and waste from fisheries factory (fish outline): 100 kg were introduced. In this case, since the concentration increased, the generation of bubbles decreased. Therefore, 100 kg of water was added to restore the normal state.

生物系廃棄物の利用産業を盛んにできる。 The industry that uses biological waste can flourish.

10 堆肥化可能有機廃棄物
11 分別(SEGRIGATION)
12 粉砕、切断(CRUSHING/SCHREDDING) 12
13 投入 (FEEDING INTO COMPOST TANK POND/DRUMS)
14 分離回収(SEPARATING/COLLECTING)
15 液肥(LIQUID)・コプロダクツ(CO-PRODUCTS)
16 液肥(LIQUID)
17 浮遊物(FLOATINGS)
18 ウジ(MAGGOTS)
19 ミミズ培地(FEED TO VERMICULTURE)
20 ミミズ堆肥肥料(COMPOST FERTILIZER)
21 農場や庭(FERTILIZER FOR HOME/GARDEN)
22 養殖池(FISH POND)
P タンク・貯水槽
B コンクリートの床
F タンク・貯水槽の底の部分
W タンク・貯水槽の側壁
T タンク・貯水槽の開放部
10 Compostable organic waste 11 Separation (SEGRIGATION)
12 Crushing and cutting (CRUSHING / SCHREDDING) 12
13 Input (FEEDING INTO COMPOST TANK POND / DRUMS)
14 Separation / Recovery (SEPARATING / COLLECTING)
15 Liquid fertilizer (LIQUID), Co-products (CO-PRODUCTS)
16 Liquid fertilizer (LIQUID)
17 FLOATINGS
18 Uzi (MAGGOTS)
19 FEED TO VERMICULTURE
20 Earthworm Compost Fertilizer (COMPOST FERTILIZER)
21 FERTILIZER FOR HOME / GARDEN
22 Aquaculture Pond (FISH POND)
P tank, water tank
B Concrete floor F Bottom of tank / water tank W Side wall of tank / water tank T Open part of tank / water tank

Claims (3)

メタン発酵消化液と、メタン発酵消化液に対して一定の決められた比率の範囲内の量の堆肥化可能余剰有機物とをタンク内に投入し、前記堆肥化可能余剰有機物と前記メタン発酵消化液の混合物を撹拌し、嫌気性発酵をさせ、液肥とコプロダクツを生産する方法において、前記コプロダクツは、ミミズの餌、または/および、ウジであるの液肥とコプロダクツを生産する方法。 A methane fermentation digestion liquid and a compostable surplus organic substance in an amount within a predetermined ratio range with respect to the methane fermentation digestion liquid are put into a tank, and the compostable surplus organic substance and the methane fermentation digestion liquid A method for producing liquid fertilizer and co-products by stirring the mixture of the fertilizer and anaerobic fermentation to produce liquid manure and co-products. 前記タンクは、上部が開放された形状である請求項1に記載の液肥とコプロダクツを生産する方法。 The method for producing liquid fertilizer and co-products according to claim 1, wherein the tank has a shape with an open top. 前記堆肥化可能余剰有機物の量を前記メタン発酵消化液の量の0.1〜20%とする請求項1または2に記載の液肥とコプロダクツを生産する方法。 The method for producing liquid fertilizer and co-products according to claim 1 or 2, wherein the amount of surplus organic matter that can be composted is 0.1 to 20% of the amount of the methane fermentation digestive liquid.
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JPS60147642U (en) * 1984-03-12 1985-10-01 コダマ樹脂工業株式会社 Lid for composting container
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JP3639543B2 (en) * 2001-05-24 2005-04-20 川崎重工業株式会社 Organic waste treatment method and apparatus
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