明 細 書 Specification
茸栽培用殺菌菌床組成物の製造法及び茸栽培法 Method for producing sterilizing fungal bed composition for mushroom cultivation and method for cultivating mushroom
技術分野 Technical field
[0001] 本発明は、設備費及びエネルギーコストを大幅に削減できる茸栽培用殺菌菌床組 成物の製造方法及び茸栽培法に関するものである。 The present invention relates to a method for producing a bactericidal bed composition for cultivating mushrooms and a method for cultivating mushrooms, which can greatly reduce equipment costs and energy costs.
背景技術 Background art
[0002] 近年、ォガ粉 (おが屑)を主成分とし、フスマ、米ぬか、粉砕玉蜀黍及び粉砕大豆の 中の少なくとも 1種よりなる栄養成分及び水よりなる菌床組成物を用いる茸類の栽培 が広く行われてレ、る。この菌床組成物は茸培養袋又はボトルに充填された状態で茸 菌を植菌されるが、植菌に先立って殺菌処理して雑菌を排除しておく必要がある。 [0002] In recent years, cultivation of mushrooms using a bacterial bed composition comprising oga flour (sawdust) as a main component and at least one nutrient component of bran, rice bran, crushed corn, and crushed soybean and water has been promoted. Widely performed. The fungal bed composition is inoculated with mushrooms in a state filled in a mushroom culture bag or bottle, but it is necessary to sterilize and remove various bacteria prior to inoculation.
[0003] 殺菌は通常水蒸気加熱により行う。菌床の形状及び大きさにもよるが、例えば実公 昭 57— 22518号に開示された構造の雑菌遮断通気性茸菌培養体袋に 20cm X 12 cm X高さ 15cm (3. 6リツター)の菌床を充填したものの場合、菌床ブロックの中心ま で殺菌温度に上昇させ必要時間維持しょうとすると高圧殺菌釜を用い 125°Cの加圧 水蒸気で 5時間を要する。 125°Cの加圧水蒸気で処理するためにはボイラーも殺菌 釜も耐圧仕様にしなければならず割高になると共に、処理時間が長いので装置の利 用効率が悪い。 95°Cの常圧水蒸気を用レ、ることも出来るが、殺菌処理の所要時間が 倍増するので決して効率がよいとは言えなレ、。また水蒸気処理した袋入り又はボトノレ 入りの菌床組成物に茸菌を植菌する前に常温まで冷却する必要がある。冷却は通常 放冷で行われるので、やはり時間がかかる。 [0003] Sterilization is usually performed by steam heating. Although it depends on the shape and size of the bacterial bed, for example, a bag of 20 cm X 12 cm X 15 cm (3.6 litters) is placed in a bag for cultivating a fungus-blocking and air-permeable mushroom having the structure disclosed in Japanese Utility Model Publication No. 57-22518. In the case of a bed filled with a bacterial bed, it is necessary to raise the sterilizing temperature to the center of the bacterial bed block and maintain it for the required time by using a high-pressure sterilizing oven and 5 hours with pressurized steam at 125 ° C. In order to treat with pressurized steam at 125 ° C, both the boiler and the sterilization pot must be pressure-resistant, which is expensive and the treatment time is long, resulting in inefficient use of the equipment. Although it is possible to use steam at 95 ° C under normal pressure, the time required for sterilization processing is doubled, so it is not efficient. In addition, it is necessary to cool to room temperature before inoculating the fungus bed composition into the steam-treated bag-containing or bottle-filled bacterial bed composition. Cooling is usually done by cooling, which also takes time.
特許文献 1 :実公昭 57— 22518号公報 Patent Document 1: Japanese Utility Model Publication No. 57-22518
[0004] 本発明者は、主成分であるォガ粉と、栄養成分であるフスマ、米ぬか、粉砕玉蜀黍 又は粉砕大豆とでは加熱殺菌処理の難易度に差があり、ォガ粉に伴われてくる雑菌 は 1 oo°cの常圧水蒸気を用レ、た熱処理でも比較的短時間で死滅すると言う認識及 び粉体とそれを容器に充填したブロック体とでは熱の通り方が違うという認識のもとに 検討を重ねた結果、本発明を完成した。 [0004] The inventor of the present invention has found that there is a difference in the degree of difficulty in heat sterilization treatment between oga flour as the main component and bran, rice bran, ground corn or ground soybean as the nutritional components. Recognition that germs can be killed in a relatively short time by heat treatment under atmospheric pressure of 1 oo ° c, and that heat flow between powder and block filled with the container is different. As a result of repeated investigations based on the above, the present invention was completed.
発明の開示
発明が解決しょうとする課題 Disclosure of the invention Problems the invention is trying to solve
[0005] 本発明は、設備費及びエネルギーコストを大幅に削減できる茸栽培用殺菌菌床組 成物の製造方法及び茸栽培法を提供することを目的とする。 An object of the present invention is to provide a method for producing a bactericidal bed composition for cultivating mushrooms and a method for cultivating mushrooms, which can greatly reduce equipment costs and energy costs.
課題を解決するための手段 Means for solving the problem
[0006] 本発明に関わる茸栽培用殺菌菌床組成物の製造方法は、ォガ粉を主成分とし、フ スマ、米ぬか、粉砕玉蜀黍及び粉砕大豆の中の少なくとも 1種よりなる栄養成分及び 水よりなる茸栽培用菌床組成物の製造において、栄養成分に水及び過酸化水素を 加えて混合し接触させることよりなる栄養成分殺菌工程、前記栄養成分殺菌工程の 生成物にォガ粉を加え撹拌しつつ常圧の水蒸気と直接接触させて 60°C以上までカロ 熱するォガ粉殺菌工程、並びに前記ォガ粉殺菌工程の生成物を撹拌しつつ殺菌冷 風と直接接触させて常温まで冷却する冷却工程よりなることを特徴とする。なお栄養 成分殺菌工程として、栄養成分に水及び過酸化水素を加えて混合し接触させ次い で超音波による振動を与えても良い。 [0006] The method for producing a bactericidal bed composition for cultivating mushrooms according to the present invention comprises a nutrient component comprising oga flour as a main component, at least one of bran, rice bran, ground corn and ground soybean, and water. In the production of a fungal bed composition for cultivating a mushroom comprising a nutrient component, water and hydrogen peroxide are added to a nutrient component, mixed and contacted, and oga powder is added to the product of the nutrient component sterilization process. Oga powder sterilization process in which the product of the agar powder sterilization process is heated to 60 ° C or more by direct contact with steam at normal pressure while stirring, and the product of the above-mentioned oga powder sterilization process is directly contacted with sterilizing cold air while stirring to reach room temperature. It is characterized by comprising a cooling step of cooling. In the nutrient sterilization step, water and hydrogen peroxide may be added to the nutrient, mixed and brought into contact, and then subjected to ultrasonic vibration.
[0007] これらの栄養成分殺菌工程、ォガ粉殺菌工程及び冷却工程は、同一の密閉式撹 拌機内で順次行うことが、工程の簡素化、横持ち費用の節減、雑菌による再汚染防 止などの点から望ましい。 [0007] The nutrient component sterilizing step, oga powder sterilizing step, and cooling step can be sequentially performed in the same closed-type stirrer to simplify the process, reduce the cost of lateral holding, and prevent re-contamination by various bacteria. It is desirable from such points.
[0008] 冷却工程を終えた殺菌菌床組成物は、その段階で密閉式撹拌機から抜き出して茸 栽培用袋又はボトルに充填し植菌し茸を栽培してもよいが、密閉式撹拌機内で常温 まで冷却後、同じ密閉式撹拌機内で得られた茸栽培用殺菌菌床組成物に所望の茸 の種菌を添加し混合する植菌工程、植菌工程の生成物を茸栽培用袋又はボトルに 充填する充填工程、前記充填工程で得られた充填物を茸菌の培養条件下に保持す る菌糸体培養工程、並びに茸子実体の発生工程を順次行って茸を栽培しても良い。 発明の効果 [0008] The sterilized bacterial bed composition after the cooling step may be extracted from the closed stirrer at that stage, filled in a mushroom cultivation bag or bottle, and inoculated to grow the mushrooms. After cooling to room temperature in the same closed stirrer, the desired mushroom inoculum is added to and mixed with the sterilized fungus bed composition for mushroom cultivation obtained in the same closed stirrer. A mushroom may be grown by sequentially performing a filling step of filling a bottle, a mycelium culture step of maintaining the filling obtained in the filling step under culture conditions of mushrooms, and a step of generating mushroom fruit bodies. . The invention's effect
[0009] 本発明の茸栽培用殺菌菌床組成物の製造法又は茸栽培法は、現在人工菌床で 栽培されている、又は栽培されようとしている各種の茸、例えば、椎茸、舞茸、山伏茸 、しめじ、なめこ、エノキ茸、はなびら茸、ァガリタスなどに適用できる。 [0009] The method for producing the bactericidal bed composition for cultivating mushrooms of the present invention or the method for cultivating mushrooms includes various mushrooms currently cultivated or about to be cultivated on artificial bed, for example, shiitake mushroom, maitake mushroom, Applicable to Yamabushi mushroom, shimeji mushroom, nameko mushroom, enoki mushroom, flower mushroom, agaritas, etc.
発明を実施するための最良の形態
[0010] 菌床における主成分であるォガ粉と栄養成分との好ましい比率は、茸の種類、菌種 の違いによって同じではないが、標準的には重量比で前者 (含水物) 92 ± 2:後者 8 ± 2の範囲が適当である。また最終的に得られる菌床組成物中の水分の量は 63重 量%前後が適当である。 BEST MODE FOR CARRYING OUT THE INVENTION [0010] The preferable ratio of oga flour, which is the main component in the fungal bed, to the nutritional component is not the same depending on the type of mushroom and the type of fungus, but is typically the weight ratio of the former (hydrous) 92 ± 2: The latter range of 8 ± 2 is appropriate. The amount of water in the finally obtained bacterial bed composition is suitably around 63% by weight.
[0011] 栄養成分殺菌工程における過酸化水素の使用量は、 H O在り姿(35%水溶液) で栄養成分に対し:!〜 7重量%、通常は 2〜3重量%程度が適当である。処理時間 は 10〜20分程度でよい。殺菌効果を促進するため、過酸化水素処理後超音波(20 KHz前後)処理を行うことが望ましい。超音波処理時間は 20〜60分程度である。超 音波処理を行うには水分の存在が重要である。最終的な菌床組成物中の水分は 63 %前後が適当であることは前段落で述べたが、ォガ粉中に存在する水分及びォガ粉 殺菌工程で吹き込まれた水蒸気の凝集分を考慮して不足分は過酸化水素と共に栄 養成分に加えておく方がよい。過酸化水素の使用はコストアップ要因になる力 使用 対象は全体の 1割程度である栄養成分で、その 2〜3重量%程度が過酸化水素の使 用量であるから、菌床組成物の全体量に対しては 0. 2〜0. 3重量%程度である。 [0011] The amount of hydrogen peroxide to be used in the nutrient component sterilization step is appropriate for the nutrient component in the form of H 2 O (35% aqueous solution):! To 7% by weight, usually about 2 to 3% by weight. Processing time may be about 10 to 20 minutes. In order to promote the sterilization effect, it is desirable to perform an ultrasonic treatment (around 20 KHz) after the hydrogen peroxide treatment. The sonication time is about 20 to 60 minutes. The presence of moisture is important for sonication. Although it is mentioned in the previous paragraph that the water content in the final bacterial bed composition is appropriate around 63%, the moisture content in the oga powder and the coagulated water Considering the shortage, it is better to add it to nutrients together with hydrogen peroxide. The use of hydrogen peroxide is a factor that increases costs. The target is about 10% of the total nutritional components, and about 2 to 3% by weight of hydrogen peroxide is used. The amount is about 0.2 to 0.3% by weight.
[0012] ォガ粉殺菌工程では、その前工程である栄養成分殺菌工程の生成物にォガ粉を 加え撹拌しながら常圧の水蒸気を吹き込んで加熱する。プラスチック袋入り又はボト ル入りの菌床組成物を容器の外部から加熱する従来法と異なり、粉体を撹拌しなが ら直接水蒸気と接触させるのであるから加熱効率は極めて優れてレ、る。菌床組成物 の温度が 60°Cの場合は 120〜180分、 80°Cの場合は 60〜90分、菌床組成物の温 度が 90°Cの場合は 30〜60分で良レ、。 [0012] In the oga powder sterilization step, oga powder is added to the product of the nutrient component sterilization step, which is the preceding step, and the mixture is heated by blowing steam at normal pressure with stirring. Unlike the conventional method in which the bacterial bed composition in a plastic bag or a bottle is heated from the outside of the container, the powder is brought into direct contact with steam while stirring, so that the heating efficiency is extremely excellent. 120-180 minutes when the temperature of the bacterial bed composition is 60 ° C, 60-90 minutes when the temperature is 80 ° C, and 30-60 minutes when the temperature of the bacterial bed composition is 90 ° C. ,.
[0013] 冷却工程では、その前工程であるォガ粉殺菌工程の生成物を撹拌しながら殺菌し た冷風と接触させる。 [0013] In the cooling step, the product of the oga powder sterilization step, which is the preceding step, is brought into contact with sterilized cold air while stirring.
実施例 1 Example 1
[0014] 密閉式横型攪拌機に、フスマ 8Kg、過酸化水素水 (濃度 35%) 0. 2Kg及び水 30 Kgを投入し 20分間混合した。次いで広葉樹(ぶな)のォガ粉 92Kgをカ卩ぇ撹拌しな 力 Sら常圧水蒸気を撹拌機内に直接送入し粉体温度 90°Cで 60分維持した。水蒸気 の凝縮分は 16Kgと計算された。次いで水蒸気の送入を停止し、殺菌常圧空気を送 入して 20°Cまで冷却した。この冷却された殺菌菌床組成物に撹拌機内で舞茸の種
菌を添加して混合し、実公昭 57— 22518号に開示された構造の雑菌遮断通気性茸 菌培養体袋に 2. 5Kg充填し、約 45日後菌床内に菌糸体が十分に成長した段階で 袋の上部を切り取り大気中に解放して舞茸の子実体を成長させ 12日後に 0. 7Kgの 舞茸を収穫した。 8 kg of bran, 0.2 kg of aqueous hydrogen peroxide (35% concentration) and 30 kg of water were charged into a closed horizontal stirrer and mixed for 20 minutes. Then, 92 kg of ogre flour of broadleaf tree (buna) was fed directly into the stirrer under the pressure of stirring without kneading. The powder temperature was maintained at 90 ° C for 60 minutes. The water vapor condensate was calculated to be 16 kg. Then, the supply of steam was stopped, and sterilized normal-pressure air was supplied to cool the mixture to 20 ° C. The mushroom seeds are added to the cooled sterilized bacterial bed composition in a stirrer. Bacteria were added and mixed, and 2.5 kg was filled in a bag of a fungus-blocking and breathable mushroom fungus having the structure disclosed in Japanese Utility Model Publication No. 57-22518. After about 45 days, the mycelium grew sufficiently in the bacterial bed At the stage, the upper part of the bag was cut off and released into the atmosphere to grow the fruit body of Maitake mushrooms. After 12 days, 0.7 kg of Maitake mushrooms were harvested.
産業上の利用可能性 Industrial applicability
茸の人工栽培における設備費やエネルギーコストが大幅に節減され、また設備の 利用効率も高まるので、茸の製造コストが下がる。
The equipment and energy costs for artificial cultivation of mushrooms are greatly reduced, and the utilization efficiency of the equipment is increased, so that the production cost of mushrooms is reduced.