JP2013237018A - Fermentation and drying method for waste mushroom bed having property of producing antibacterial substance by hypha - Google Patents

Fermentation and drying method for waste mushroom bed having property of producing antibacterial substance by hypha Download PDF

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JP2013237018A
JP2013237018A JP2012112014A JP2012112014A JP2013237018A JP 2013237018 A JP2013237018 A JP 2013237018A JP 2012112014 A JP2012112014 A JP 2012112014A JP 2012112014 A JP2012112014 A JP 2012112014A JP 2013237018 A JP2013237018 A JP 2013237018A
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fermentation
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mushroom waste
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bed
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Tadaaki Shimizu
忠明 清水
Kazuhiko Takizawa
和彦 瀧澤
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SANKO DOBOKU KK
Niigata University NUC
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SANKO DOBOKU KK
Niigata University NUC
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Abstract

PROBLEM TO BE SOLVED: To provide a method for fermenting and drying a waste mushroom bed of Flammulina veluptipes or the like having a property of producing an antibacterial substance by hyphae within a short time by a simple method.SOLUTION: A fermentation starting auxiliary agent of 15 pts.mass or more is mixed with 100 pts.mass of a waste mushroom bed and stored in a heat insulated container and air is allowed to flow into the heat insulated container to perform a first fermentation. In a second fermentation and after, 30 pts.mass or more of a fermented product obtained by the preceding fermentation is mixed with 100 pts.mass of a new waste mushroom bed and stored in the heat insulated container and air is allowed to flow the heat insulated container to perform fermentation.

Description

本発明は、菌糸が抗菌物質を産生する性質を持つキノコ廃菌床の発酵乾燥方法に関する。   The present invention relates to a method for fermenting and drying a mushroom waste fungus bed having the property that mycelia produce an antibacterial substance.

近年、廃棄物処理や地球温暖化といった問題を解決すべく、農業系廃棄物の有効利用が望まれている。中でも、キノコ廃菌床は、バイオマス発生量の相当量を占め、現在では飼料化や堆肥化などにより利用されているが、その需要量にも限りがあることから廃棄物系バイオマス燃料としての利活用が期待されている。また、キノコ廃菌床はリン、カリウムの含有量が多く、燃焼後の焼却灰は食品製造原料由来であるため、重金属などを含まない優良な肥料原料としてそのまま利用することが期待できる。リン資源の枯渇が問題となっている昨今、廃菌床の焼却灰はリン資源の確保にも繋がると考えられている。しかし、キノコ廃菌床は含水率が約55%と高いので、燃焼前には自燃可能かつ熱回収が見込まれる含水率30〜40%程度に乾燥させなければならない。したがって、キノコ廃菌床のエネルギー資源化には低エネルギー、低コストでの乾燥法を確立する必要がある。   In recent years, effective use of agricultural waste has been desired in order to solve problems such as waste disposal and global warming. Among them, the waste mushroom bed occupies a considerable amount of biomass generation and is currently used for feed and composting, but its demand is limited, so it is useful as a waste biomass fuel. Utilization is expected. In addition, the waste mushroom bed contains a large amount of phosphorus and potassium, and the incinerated ash after combustion is derived from food production raw materials. Therefore, it can be expected to be used as it is as an excellent fertilizer raw material containing no heavy metals. In recent years, when phosphorus resources are depleted, incineration ash in waste beds is thought to lead to securing phosphorus resources. However, the mushroom waste fungus bed has a high moisture content of about 55%, and therefore it must be dried to a moisture content of about 30 to 40%, which allows self-combustion and heat recovery, before combustion. Therefore, it is necessary to establish a low-energy, low-cost drying method for energy resource utilization of mushroom waste fungus beds.

乾燥法には種類が多く存在するが、熱風を通風するといった直接乾燥法では熱風を作り出すのにエネルギーがかかり、熱効率も低い。赤外線、高周波などの電気的乾燥法もあるが、いずれの場合も照射のエネルギーを必要とする。加熱以外のバイオマスの乾燥法には発酵乾燥法が挙げられる。堆肥化に伴う微生物発酵による発熱を乾燥熱源として利用する発酵乾燥法は、外部から加えるエネルギーが機械的動力のみであることからエネルギーにかかるコストを抑えることができ、また常温に近い運転条件なので設備投資も他の乾燥法に比べると安価になる。全体として、低コストでの乾燥が期待できる。さらに、発酵乾燥は操作においても加熱炉などを使わないことから非常に安全性が高いと言える。   There are many types of drying methods, but direct drying methods, such as passing hot air, require energy to produce hot air and have low thermal efficiency. There are electrical drying methods such as infrared and high frequency, but in any case, irradiation energy is required. As a method for drying biomass other than heating, a fermentation drying method may be mentioned. The fermentation drying method that uses the heat generated by microbial fermentation accompanying composting as a drying heat source can reduce the cost of energy because the energy applied from the outside is only mechanical power. Investment is also cheaper than other drying methods. Overall, low cost drying can be expected. Furthermore, it can be said that fermentation drying is very safe because it does not use a heating furnace in operation.

しかし、特許文献1に開示されるような従来のバイオマスの発酵乾燥法では、1処理あたりの所要時間が数十日間と長いという問題があった。また、発酵乾燥を発酵槽内で行い、槽内への空気導入を行うことで小規模かつ高速でバイオマスを乾燥する装置及び方法が特許文献2に開示されている。しかし、1処理毎に発酵開始菌(種菌)を投入するため、種菌の調達、確保のコスト上昇が避けられないという問題があった。   However, the conventional fermentation and drying method for biomass as disclosed in Patent Document 1 has a problem that the time required for one treatment is as long as several tens of days. Further, Patent Document 2 discloses an apparatus and method for drying biomass on a small scale and at high speed by performing fermentation and drying in a fermentation tank and introducing air into the tank. However, since fermentation start bacteria (inoculum) are introduced for each treatment, there has been a problem that the cost of procurement and securing of the inoculum is inevitable.

さらに、この発酵乾燥法を用いて菌糸が抗菌物質を産生する性質を持つために抗菌物質を含有するキノコ廃菌床(例えばエノキポジンを含有するエノキタケ廃菌床)を乾燥しようとすると、抗菌物質により発酵を行う細菌が死滅するため、安定した発酵乾燥は不可能であるという問題があった。   Furthermore, when using this fermentative drying method, the hyphae have the property of producing antibacterial substances, so if you try to dry mushroom waste fungus beds containing antibacterial substances (eg enokitake mushroom waste fungus beds containing enokipodin), There is a problem that stable fermentation and drying is impossible because the bacteria that perform fermentation are killed.

特開2011−189268号公報JP 2011-189268 A 特開2009−178712号公報JP 2009-178712 A

そこで、本発明は、上記問題点を解決し、簡易な方法で、短時間において、菌糸が抗菌物質を産生する性質を持つエノキタケなどのキノコの廃菌床を発酵乾燥する方法を提供することを目的とする。   Therefore, the present invention provides a method for solving the above-mentioned problems and fermenting and drying a waste fungus bed of mushrooms such as enokitake mushrooms having the property that mycelia produce an antibacterial substance in a short time. Objective.

本発明の菌糸が抗菌物質を産生する性質を持つキノコ廃菌床の発酵乾燥方法は、キノコ廃菌床100質量部に対して15質量部以上の発酵開始助剤を混合して断熱容器内に収容し、この断熱容器内に空気を流通させて1回目の発酵を行うとともに、2回目以降の発酵において、新たなキノコ廃菌床100質量部に対して30質量部以上の前回の発酵で得られた発酵生成物を混合して断熱容器内に収容し、この断熱容器内に空気を流通させて発酵を行うことを特徴とする。   The method for fermenting and drying a mushroom waste fungus bed having the property that the mycelium of the present invention produces an antibacterial substance is prepared by mixing 15 parts by mass or more of a fermentation start aid with 100 parts by mass of the mushroom waste fungus bed in an insulated container. Accommodates and conducts the first fermentation by circulating air in this insulated container, and in the second and subsequent fermentations, it is obtained in the previous fermentation of 30 parts by mass or more with respect to 100 parts by mass of the new waste mushroom bed. The obtained fermentation product is mixed and accommodated in an insulated container, and air is circulated in the insulated container to perform fermentation.

また、前記発酵開始助剤は、好気性発酵微生物を含むものであることを特徴とする。   Moreover, the said fermentation start adjuvant is a thing containing an aerobic fermentation microorganisms, It is characterized by the above-mentioned.

また、前記発酵開始助剤は、発酵鶏糞堆肥、EM発酵資材、乾燥牛糞、発酵牛糞堆肥、発酵豚糞堆肥のいずれかであることを特徴とする。   Moreover, the said fermentation start adjuvant is any one of fermented chicken manure compost, EM fermentation material, dry cow manure, fermented cow manure compost, and fermented pig manure compost.

また、前記キノコ廃菌床は、エノキタケ廃菌床であることを特徴とする。   Further, the mushroom waste fungus bed is an enokitake mushroom waste fungus bed.

本発明の菌糸が抗菌物質を産生する性質を持つキノコ廃菌床の発酵乾燥方法によれば、簡易な方法で、短時間において、菌糸が抗菌物質を産生する性質を持つエノキタケなどのキノコの廃菌床を発酵乾燥することができる。   According to the method for fermenting and drying a mushroom waste fungus bed having the property that the mycelium of the present invention produces an antibacterial substance, waste of mushrooms such as enokitake having the property that the mycelium produces an antibacterial substance in a short time in a simple manner. The fungus bed can be fermented and dried.

実施例1における第1回目のエノキタケ廃菌床の発酵において、発酵開始助剤の添加量と発酵時の温度上昇の関係を示すグラフである。It is a graph which shows the relationship between the addition amount of a fermentation start adjuvant, and the temperature rise at the time of fermentation in fermentation of the 1st enokitake mushroom bed in Example 1. 実施例1における実験手順と結果を示す説明図である。It is explanatory drawing which shows the experimental procedure and result in Example 1. FIG. 実施例1におけるひよこ発酵鶏糞を用いた場合の発酵時の温度上昇を示すグラフである。It is a graph which shows the temperature rise at the time of fermentation at the time of using the chick fermented chicken dung in Example 1. 実施例1におけるEM発酵資材を用いた場合の発酵時の温度上昇を示すグラフである。It is a graph which shows the temperature rise at the time of fermentation at the time of using the EM fermentation material in Example 1. 実施例1における乾燥牛糞を用いた場合の発酵時の温度上昇を示すグラフである。It is a graph which shows the temperature rise at the time of fermentation at the time of using the dry cow dung in Example 1. 実施例1におけるペレット化牛糞堆肥を用いた場合の発酵時の温度上昇を示すグラフである。It is a graph which shows the temperature rise at the time of fermentation at the time of using the pelletized cow dung compost in Example 1.

本発明の菌糸が抗菌物質を産生する性質を持つキノコ廃菌床の発酵乾燥方法は、はじめに、キノコ廃菌床と発酵開始助剤を混合して断熱容器内に収容し、この断熱容器内に空気を流通させて1回目の発酵を行う。ここで、安定した発酵を継続させるために、キノコ廃菌床100質量部に対して、15質量部以上の発酵開始助剤を混合するのが好ましい。   The method for fermenting and drying a mushroom waste fungus bed having the property that the mycelium of the present invention produces an antibacterial substance is first prepared by mixing a mushroom waste fungus bed and a fermentation start auxiliary agent and storing the mixture in a heat insulation container. The first fermentation is performed by circulating air. Here, in order to continue stable fermentation, it is preferable to mix 15 mass parts or more of fermentation start adjuvant with respect to 100 mass parts of waste mushroom beds.

そして、2回目以降の発酵において、新たなキノコ廃菌床と前回の発酵で得られた発酵生成物を混合して断熱容器内に収容し、この断熱容器内に空気を流通させて発酵を行う。すなわち、2回目以降の発酵においては、前回の発酵生成物を発酵開始助剤の代わりに用いるものである。ここで、安定した発酵を継続させるために、新たなキノコ廃菌床100質量部に対して、前回の発酵で得られた発酵生成物30質量部以上を混合するのが好ましい。   In the second and subsequent fermentations, a new mushroom waste fungus bed and a fermentation product obtained in the previous fermentation are mixed and accommodated in an insulated container, and air is circulated in the insulated container for fermentation. . That is, in the second and subsequent fermentations, the previous fermentation product is used instead of the fermentation start aid. Here, in order to continue stable fermentation, it is preferable to mix 30 parts by mass or more of the fermentation product obtained in the previous fermentation with 100 parts by mass of the new waste mushroom bed.

発酵開始助剤としては、好気性発酵微生物を含むものを用いることができ、堆肥又は発酵微生物含有剤が好適に用いられる。堆肥としては、例えば、発酵鶏糞、乾燥牛糞、発酵牛糞堆肥が好適に用いられ、発酵微生物含有剤としては、例えば、有用微生物群(EM)を含むEM発酵資材が好適に用いられる。   As the fermentation start aid, those containing aerobic fermentation microorganisms can be used, and compost or fermenting microorganism-containing agents are preferably used. As the compost, for example, fermented chicken dung, dried cow dung, and fermented cow dung compost are preferably used. As the fermenting microorganism-containing agent, for example, EM fermentation material containing a useful microorganism group (EM) is preferably used.

キノコ廃菌床としては、特定のものに限定されるものではないが、例えば、抗菌物質であるエノキポジンを産生する性質を持つエノキタケ廃菌床を用いることができる。   The mushroom waste fungus bed is not limited to a specific one, but for example, an enokitake mushroom waste fungus bed having the property of producing an antibacterial substance enokipodin can be used.

断熱容器としては、本発明の方法により発酵を行ったときの最高温度が60℃以上に到達する程度の断熱性を有すればよく、特定の構造のものに限定されるものではない。   The heat insulating container is not limited to a specific structure as long as it has heat insulating properties such that the maximum temperature when fermentation is performed by the method of the present invention reaches 60 ° C. or higher.

発酵時に断熱容器に導入する空気の量は、キノコ廃菌床の温度、断熱容器内外の空気の湿度や温度に応じて適宜調整すればよい。   What is necessary is just to adjust suitably the quantity of the air introduce | transduced into a heat insulation container at the time of fermentation according to the temperature of the mushroom waste microbial bed, and the humidity and temperature of the air inside and outside a heat insulation container.

断熱容器内へ空気を導入する際は、断熱容器内の空気層に導入してもよく、キノコ廃菌床の充填層に導入してもよい。空気層に導入する場合は、空気がキノコ廃菌床に良く触れるように撹拌又は切り返しを行うことが望ましい。撹拌又は切り返しは連続的、間歇的どちらでもよく、キノコ廃菌床の温度上昇と乾燥に適した条件を選定すればよい。なお、キノコ廃菌床の充填層内に送気パイプ等を用いて空気を導入する場合には撹拌、切り返しが不要なこともある。   When air is introduced into the heat insulating container, it may be introduced into the air layer in the heat insulating container or may be introduced into the packed bed of the mushroom waste fungus bed. When introduced into the air layer, it is desirable to perform stirring or turning over so that the air is in good contact with the mushroom waste fungus bed. Agitation or reversal may be either continuous or intermittent, and conditions suitable for temperature rise and drying of the mushroom waste fungus bed may be selected. In addition, when air is introduced into the packed bed of the mushroom waste fungus bed using an air supply pipe or the like, stirring and turning over may not be necessary.

本発明の菌糸が抗菌物質を産生する性質を持つキノコ廃菌床の発酵乾燥方法によれば、外部からの加熱を要せずに、断熱容器内に空気を流通させて発酵を行うという簡易な方法で、発酵熱を利用して、48〜60時間という短時間において、含水率が約55%であって菌糸が抗菌物質を産生する性質を持つエノキタケなどのキノコの廃菌床を、自燃可能かつ熱回収が見込まれる含水率30〜40%程度にまで発酵乾燥することができる。   According to the method for fermenting and drying a mushroom waste fungus bed having the property that the mycelium of the present invention produces an antibacterial substance, a simple method of performing fermentation by circulating air in a heat insulating container without requiring heating from the outside. The method can self-combust waste mushroom beds such as enokitake mushrooms, which have the property that the moisture content is about 55% and the mycelium produces antibacterial substances in a short period of 48 to 60 hours using fermentation heat. And it can be fermented and dried to a water content of about 30 to 40% where heat recovery is expected.

また、外部からの加熱を要しないこと、発酵乾燥用の装置を簡単に構成できること、発酵開始助剤の添加は1回目だけでよいことから、低コストにてキノコ廃菌床を発酵乾燥することができる。   In addition, since no external heating is required, the apparatus for fermentation and drying can be easily configured, and the addition of the fermentation start aid is only required for the first time, the mushroom waste bacterial bed is fermented and dried at low cost. Can do.

本発明の方法は、菌糸が抗菌物質を産生する性質を持つキノコ廃菌床のほか、湿潤有機廃棄物一般にも適用可能である。   The method of the present invention can be applied not only to mushroom waste fungus beds having the property of producing antibacterial substances, but also to wet organic waste in general.

以下、本発明の具体的実施例について説明する。なお、本発明は以下の実施例に限定されるものではなく、本発明の思想を逸脱しない範囲で種々の変形実施が可能である。   Hereinafter, specific examples of the present invention will be described. The present invention is not limited to the following examples, and various modifications can be made without departing from the spirit of the present invention.

本発明の方法を用いてキノコ廃菌床の乾燥を行うために、固定層発酵実験を行った。実験装置は、断熱性に優れたステンレス製デュワー瓶であり、ふたの部分には断熱材(発泡スチロール板)で断熱を施した。この中に所定量の種となる発酵開始助剤をあらかじめ混合したエノキタケ廃菌床(組成を表1に示す)を入れ、所定量の空気を流通させて発酵を行った。空気送風量は毎分0.2リットルとした。発酵途中では、廃菌床の中の温度を測定するとともに、生成ガス中の水分を冷却凝縮して捕集し量を測定した。また、生成したガス中の二酸化炭素濃度を測定した。発酵終了後は、廃菌床を取り出して乾燥し、その際の重量変化から含水率を求めた。   In order to dry the mushroom waste fungus bed using the method of the present invention, a fixed bed fermentation experiment was conducted. The experimental apparatus was a stainless steel dewar with excellent heat insulation, and the lid was insulated with a heat insulating material (a foamed polystyrene plate). An enokitake mushroom waste bed (composition shown in Table 1) preliminarily mixed with a fermentation initiation aid serving as a predetermined amount of seeds was placed therein, and fermentation was performed by circulating a predetermined amount of air. The air blowing rate was 0.2 liters per minute. During the fermentation, the temperature in the waste microbial bed was measured, and the moisture in the product gas was cooled and condensed, and the amount collected was measured. Moreover, the carbon dioxide concentration in the produced | generated gas was measured. After completion of the fermentation, the waste microbial bed was taken out and dried, and the moisture content was determined from the weight change at that time.

用いた発酵開始助剤は、A)ひよこ発酵鶏糞((株)東商)、B)EM発酵資材(商品名:ウルトラボカシ1000;(株)コンパル)、C)乾燥牛糞((株)こうじや)、D)ペレット化牛糞堆肥を用いた。A)ひよこ発酵鶏糞については、廃菌床およそ400gに対して、添加物なし、10%添加、20%添加の3水準で実験を行った。ここで10%添加の際は廃菌床400gに対して発酵開始助剤40gを、20%添加の際には廃菌床400gに対して発酵開始助剤80gを、それぞれ添加した。また、1回目発酵終了後の発酵生成物である発酵廃菌床を次の発酵の助剤として用いることを行った。1回目発酵終了後の発酵廃菌床混合比としては、新しい廃菌床100に対し、質量比で20〜40の割合でそれぞれ添加した。また、2回目以降の発酵終了後の廃菌床を次の発酵の助剤として用いることを繰り返して行い、徐々に初期開始助剤濃度を下げることを行った。   Fermentation start aids used were: A) chick fermented chicken manure (Tosho Co., Ltd.), B) EM fermented material (trade name: Ultra Bocashi 1000; Compal Corp.), C) dried beef manure (Kojiya Co., Ltd.) D) Pelletized cow manure compost was used. A) For the chick-fermented chicken manure, experiments were conducted at three levels of no additive, 10% addition, and 20% addition to about 400 g of waste bacterial bed. Here, at the time of 10% addition, 40 g of fermentation start assistant was added to 400 g of the waste bacteria bed, and at the time of 20% addition, 80 g of fermentation start assistant was added to 400 g of the waste bacteria bed. Moreover, it performed using the fermentation waste microbial bed which is a fermentation product after completion | finish of 1st fermentation as an auxiliary agent of the next fermentation. As a mixing ratio of the fermented waste microbial bed after the end of the first fermentation, each mass was added to the new waste microbial bed 100 at a rate of 20 to 40. Moreover, it repeatedly performed using the waste microbial bed after completion | finish of the second and subsequent fermentation as an auxiliary | assistant of the next fermentation, and performed the initial stage auxiliary | assistant auxiliary | assistant density | concentration gradually.

ひよこ発酵鶏糞を発酵開始助剤として1回目発酵させた場合の温度変化を図1に示す。発酵開始剤添加量が20%の時には発酵開始後24時間程度で60℃以上に到達し48時間後にはほぼ発酵が終了したが、発酵開始助剤添加量が10%の時には発酵温度が最高になるまで40時間以上を必要とし、また最高温度も55℃に至らなかった。したがって、1回目発酵させた場合の発酵開始助剤添加量は20%程度を必要とすることが確認された。   FIG. 1 shows the temperature change when the chick-fermented chicken dung was fermented for the first time as a fermentation start aid. When the addition amount of the fermentation initiator is 20%, the temperature reaches 60 ° C. or more in about 24 hours after the start of the fermentation, and the fermentation is almost finished after 48 hours. However, when the addition amount of the fermentation start assistant is 10%, the fermentation temperature becomes the highest. It took 40 hours or more to become, and the maximum temperature did not reach 55 ° C. Therefore, it was confirmed that about 20% of the fermentation start auxiliary agent addition amount in the case of the first fermentation was required.

次に、発酵開始助剤添加割合20%で約50時間1回目発酵を行った後の発酵生成物を2回目以降の発酵開始助剤として用いた場合での、発酵時温度上昇に及ぼす1回目発酵生成物添加量の影響を調べた。図2に結果を示す。第1回目発酵生成物を20%添加したときには50℃までしか温度が上昇しなかったが、40%添加したものについては60℃強まで温度上昇が見られた。したがって、2回目の発酵には1回目の発酵生成物を40%程度添加する必要があることが分かる。さらに3回目の発酵に2回目発酵生成物を40%程度添加して用いた場合でも同様に60℃強まで温度上昇が見られた。   Next, the first effect on the temperature rise during fermentation in the case where the fermentation product after performing the first fermentation for about 50 hours at a fermentation initiation assistant addition ratio of 20% is used as the fermentation initiation assistant for the second and subsequent times. The effect of fermented product addition was investigated. The results are shown in FIG. When 20% of the first fermentation product was added, the temperature increased only up to 50 ° C., but when 40% was added, the temperature increased to over 60 ° C. Therefore, it is understood that about 40% of the first fermentation product needs to be added for the second fermentation. Further, even when about 40% of the second fermentation product was added to the third fermentation, the temperature was similarly increased to a little over 60 ° C.

以上より、1回目の発酵では発酵開始剤を20%添加し、2回目以降では前回発酵生成物を40%添加することが安定した発酵のために望ましいことが確認されたので、異なった堆肥あるいは発酵開始用微生物含有剤を発酵開始剤として用いた場合でもこの方式が適用できるかどうかを検討した。結果を図3〜6に示す。2回目以降の温度がいずれも最高で60℃を超え、かつ2回目以降安定して同様な温度変化曲線が得られた。したがって、本発明の方法によって安定して継続的に発酵乾燥ができることが確認された。   From the above, it was confirmed that the addition of 20% of the fermentation initiator in the first fermentation and the addition of 40% of the previous fermentation product in the second and subsequent fermentations was desirable for stable fermentation. It was examined whether this method can be applied even when a microorganism-containing agent for initiating fermentation is used as a fermentation initiator. The results are shown in FIGS. The temperature after the second time exceeded 60 ° C. at the maximum, and the same temperature change curve was obtained stably after the second time. Therefore, it was confirmed that the fermentation drying can be stably and continuously performed by the method of the present invention.

Figure 2013237018
Figure 2013237018

Claims (4)

キノコ廃菌床100質量部に対して15質量部以上の発酵開始助剤を混合して断熱容器内に収容し、この断熱容器内に空気を流通させて1回目の発酵を行うとともに、2回目以降の発酵において、新たなキノコ廃菌床100質量部に対して30質量部以上の前回の発酵で得られた発酵生成物を混合して断熱容器内に収容し、この断熱容器内に空気を流通させて発酵を行うことを特徴とする菌糸が抗菌物質を産生する性質を持つキノコ廃菌床の発酵乾燥方法。 At least 15 parts by mass of a fermentation start aid is mixed with 100 parts by mass of the mushroom waste microbial bed, and the mixture is accommodated in a heat-insulated container. In the subsequent fermentation, the fermentation product obtained in the previous fermentation of 30 parts by mass or more is mixed with 100 parts by mass of the new mushroom waste fungus bed, accommodated in the insulated container, and air is contained in the insulated container. A method for fermenting and drying a mushroom waste fungus bed, wherein the mycelia produce an antibacterial substance, characterized by being fermented by circulation. 前記発酵開始助剤は、好気性発酵微生物を含むものであることを特徴とする請求項1記載のキノコ廃菌床の発酵乾燥方法。 The method for fermenting and drying a mushroom waste fungus bed according to claim 1, wherein the fermentation initiation aid contains aerobic fermentation microorganisms. 前記発酵開始助剤は、発酵鶏糞堆肥、EM発酵資材、乾燥牛糞、発酵牛糞堆肥、発酵豚糞堆肥のいずれかであることを特徴とする請求項2記載のキノコ廃菌床の発酵乾燥方法。 The method for fermenting and drying a mushroom waste fungus bed according to claim 2, wherein the fermentation start assistant is any one of fermented chicken manure compost, EM fermented material, dried cow manure, fermented cow manure compost, and fermented pig manure compost. 前記キノコ廃菌床は、エノキタケ廃菌床であることを特徴とする請求項1〜3のいずれか1項記載のキノコ廃菌床の発酵乾燥方法。 The method for fermenting and drying a mushroom waste fungus bed according to any one of claims 1 to 3, wherein the mushroom waste fungus bed is an enokitake mushroom waste fungus bed.
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* Cited by examiner, † Cited by third party
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JPH01270584A (en) * 1988-04-20 1989-10-27 Hisakazu Ikeda Soil-conditioning fertilizer and production thereof
JPH08181A (en) * 1994-06-17 1996-01-09 Noboru Yamamoto Production of feed, fertilizer, etc., using waste mushroom cultivation medium
JP2004314051A (en) * 2003-04-01 2004-11-11 Tsuguo Aramaki Treating agent for organic waste, method of manufacturing the agent and method of treating dung and urine
JP2006116529A (en) * 2004-09-21 2006-05-11 Hisakazu Ikeda Drying method for organic matter, product by the method and its drying device
JP2006182579A (en) * 2004-12-27 2006-07-13 Ichimura:Kk Manufacturing method of compost
JP2009017695A (en) * 2007-07-05 2009-01-22 Chugoku Electric Power Co Inc:The Power feed system of receiving equipment
JP2009062531A (en) * 2007-08-13 2009-03-26 Hisakazu Ikeda Method for manufacturing dried organic material fuel and its apparatus
JP2009178712A (en) * 2007-12-31 2009-08-13 Shinyodo:Kk Container apparatus for fermenting/drying work and method for drying wet organic matter
JP2010203906A (en) * 2009-03-03 2010-09-16 National Agriculture & Food Research Organization Ventilation resistance measuring device
JP2012001667A (en) * 2010-06-18 2012-01-05 S Science:Kk Solid fuel and method for manufacturing the same

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01270584A (en) * 1988-04-20 1989-10-27 Hisakazu Ikeda Soil-conditioning fertilizer and production thereof
JPH08181A (en) * 1994-06-17 1996-01-09 Noboru Yamamoto Production of feed, fertilizer, etc., using waste mushroom cultivation medium
JP2004314051A (en) * 2003-04-01 2004-11-11 Tsuguo Aramaki Treating agent for organic waste, method of manufacturing the agent and method of treating dung and urine
JP2006116529A (en) * 2004-09-21 2006-05-11 Hisakazu Ikeda Drying method for organic matter, product by the method and its drying device
JP2006182579A (en) * 2004-12-27 2006-07-13 Ichimura:Kk Manufacturing method of compost
JP2009017695A (en) * 2007-07-05 2009-01-22 Chugoku Electric Power Co Inc:The Power feed system of receiving equipment
JP2009062531A (en) * 2007-08-13 2009-03-26 Hisakazu Ikeda Method for manufacturing dried organic material fuel and its apparatus
JP2009178712A (en) * 2007-12-31 2009-08-13 Shinyodo:Kk Container apparatus for fermenting/drying work and method for drying wet organic matter
JP2010203906A (en) * 2009-03-03 2010-09-16 National Agriculture & Food Research Organization Ventilation resistance measuring device
JP2012001667A (en) * 2010-06-18 2012-01-05 S Science:Kk Solid fuel and method for manufacturing the same

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