Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0681570B2 - Manufacturing method of culture medium for mushroom cultivation - Google Patents
[go: Go Back, main page]

JPH0681570B2 - Manufacturing method of culture medium for mushroom cultivation - Google Patents

Manufacturing method of culture medium for mushroom cultivation

Info

Publication number
JPH0681570B2
JPH0681570B2 JP2090698A JP9069890A JPH0681570B2 JP H0681570 B2 JPH0681570 B2 JP H0681570B2 JP 2090698 A JP2090698 A JP 2090698A JP 9069890 A JP9069890 A JP 9069890A JP H0681570 B2 JPH0681570 B2 JP H0681570B2
Authority
JP
Japan
Prior art keywords
medium
pressure
culture
time
retort
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP2090698A
Other languages
Japanese (ja)
Other versions
JPH0387120A (en
Inventor
貴夫 原田
寿公 富岡
筒井  秀也
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kanebo Ltd
Original Assignee
Kanebo Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kanebo Ltd filed Critical Kanebo Ltd
Publication of JPH0387120A publication Critical patent/JPH0387120A/en
Publication of JPH0681570B2 publication Critical patent/JPH0681570B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Mushroom Cultivation (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、きのこ栽培用培養基の製法に係り、更に詳細
にはレトルト殺菌処理における殺菌処理時間の短縮と均
一殺菌とを培地含水量を変化させずに実施することが可
能であるきのこ栽培用培養基の製法に関するものであ
る。
TECHNICAL FIELD The present invention relates to a method for producing a culture medium for mushroom cultivation, and more specifically, to shorten the sterilization time in retort sterilization treatment and uniform sterilization to change the medium water content. The present invention relates to a method for producing a culture medium for mushroom cultivation, which can be carried out without performing it.

(従来の技術) 従来より、しいたけのようなきのこ栽培に用いる榾木
を、工場等で人工的かつ大量に生産する、所謂、きのこ
栽培用培養基の生産が実施されている。例えば、しいた
けのようなきのこ栽培においては、おがくず、米糠等の
培地原料を用いてきのこ栽培用培養基をつくり、このき
のこ栽培用培養基にしいたけ種菌を植菌し、培養してし
いたけを量産することが行われている。また、ひらた
け,えのきたけではビン栽培が行われている。この一連
の工程を、より詳しく説明すると、きのこ栽培用培地基
は、第1図に示すようにおがくず,米糠等の培地原料
(1)を、ポリプロピレン製の培養袋(4)に所定量充
填し、袋の開口部を通気口部(3)を有するねじ蓋
(2)で閉塞し、あるいはポリプロピレン製瓶に充填
し、その状態でレトルト釜に収納し、110〜130℃の条件
でレトルト殺菌を施すことにより、製造されている。ま
た、本発明者らは、レトルト釜本体とそれに一体化接続
された真空装置とによって、レトルト殺菌処理の前に、
レトルト釜内を減圧状態にする方法(特開昭63-209516
号公報)を提案している。
(Prior Art) Conventionally, a so-called mushroom cultivation medium for producing mushrooms such as shiitake mushrooms grown in mushrooms artificially and in large quantities has been carried out. For example, in mushroom cultivation such as shiitake mushrooms, it is possible to make a culture medium for mushroom cultivation using sawdust, rice bran and other medium raw materials, inoculate the mushroom culture medium for mushroom cultivation, incubate and culture shiitake mushrooms. Has been done. In addition, bottle cultivation is carried out in hiratake and enokitake. This series of steps will be described in more detail. As for the mushroom culture medium base, a polypropylene culture bag (4) is filled with a predetermined amount of the culture medium raw material (1) such as sawdust and rice bran as shown in FIG. The bag opening is closed with a screw lid (2) having a vent (3) or filled in a polypropylene bottle, and stored in a retort kettle in that state, and retort sterilized at 110 to 130 ° C. It is manufactured by applying. In addition, the present inventors, before the retort sterilization process, by the retort kettle body and the vacuum device integrally connected thereto,
Method of reducing the pressure inside the retort kettle (Japanese Patent Laid-Open No. 63-209516)
Issue gazette).

しかしながら、一般に培地はおがくず,米糠等を原料と
しており、培地の充填された培養容器内には空気が残存
している。このため、レトルト殺菌処理工程での高圧下
において、この培養容器内の空気が脱気せず残存した空
気の断熱作用により、培養容器内の温度が上昇し難い。
また、培養容器の形状は円柱形等の塊状が一般的であ
り、培養容器内の中心部は熱伝導の面からも昇温し難
い。すなわち、レトルト釜内をレトルト殺菌処理に先立
って減圧状態にするという方法も含め、培養容器内の空
気が充分に脱気されず、培養容器内が昇温しにくいの
で、レトルト殺菌処理に1〜5時間という長時間を要し
ているのが現状である。また、培養容器内の中心部の温
度が周辺部に比べ上昇しにくいので、均一なレトルト殺
菌処理ができず、未殺菌の部分が培養容器内に生じる危
険が大きい。この結果、後の培養工程において、雑菌汚
染の確率が高くなり、不良培養基の発生率が高くなる。
However, the medium is generally made of sawdust, rice bran, etc., and air remains in the culture container filled with the medium. Therefore, under high pressure in the retort sterilization process, the temperature in the culture container is unlikely to rise due to the adiabatic action of the air remaining in the culture container without being deaerated.
Further, the shape of the culture container is generally a lump such as a columnar shape, and it is difficult to raise the temperature in the center of the culture container from the viewpoint of heat conduction. That is, including the method of reducing the pressure inside the retort kettle prior to the retort sterilization treatment, the air in the culture container is not sufficiently degassed, and the temperature inside the culture container is difficult to rise. At present, it takes a long time of 5 hours. Further, since the temperature of the central part in the culture container is less likely to rise than that of the peripheral part, uniform retort sterilization treatment cannot be performed, and there is a great risk that an unsterilized part is generated in the culture container. As a result, in the subsequent culturing step, the probability of contamination of various bacteria increases, and the incidence of defective culture medium increases.

このように、従来のレトルト殺菌処理方法では、レトル
ト殺菌処理が長時間に亘るため、大量生産を行う工場に
おいては生産効率の低下に繋がり、また、培養容器内の
不均一な加熱のため、歩留りの低下にも繋がっている。
培養容器内の空気を脱気させ、速やかに内部を均一昇温
させ、処理時間を短縮する方法がまだ開発されていない
のが現状である。
As described above, in the conventional retort sterilization treatment method, since the retort sterilization treatment takes a long time, it leads to a decrease in production efficiency in a factory where mass production is performed, and because of uneven heating in the culture vessel, the yield is high. It also leads to a decrease in
At present, a method for deaerating the air in the culture vessel to quickly raise the temperature inside the culture vessel to shorten the treatment time has not been developed.

(発明が解決しようとする課題) 本発明は、このような事情に鑑みなされたもので、その
目的とするところは、レトルト殺菌処理の迅速化と均一
化がなされるとともに、培地含水量を保持し得るきのこ
栽培用培養基の製法を提供するにある。
(Problems to be Solved by the Invention) The present invention has been made in view of such circumstances, and an object of the present invention is to speed up and homogenize retort sterilization treatment, and to maintain a medium water content. It is to provide a method for producing a cultivating substrate for mushroom cultivation that can be performed.

(課題を解決するための手段) 上記目的は、きのこ栽培用の培地原料を充填した容器を
レトルト釜中に入れてレトルト殺菌を施すに際し、レト
ルト釜内を減圧して上記培地の充填された容器内部の空
気を脱気する工程と、レトルト釜内に100℃以上の蒸気
を10kg/cm2以下の圧力で供給し容器内部へ蒸気を送入さ
せる工程とを順次繰り返して行い、該2回目以降のレト
ルト釜内を減圧するときの圧力を、その時点での培地品
温に対する飽和蒸気圧、あるいはそれより若干高い圧力
にすることを特徴とするきのこ栽培用培養基の製法によ
って達成される。
(Means for Solving the Problem) The above-mentioned object is to put a container filled with a medium raw material for mushroom cultivation in a retort kettle to perform retort sterilization, decompress the inside of the retort kettle and fill the container with the above medium. The process of degassing the internal air and the process of supplying steam of 100 ° C or higher to the retort kettle at a pressure of 10 kg / cm 2 or less and sending the steam into the container are sequentially repeated, and the second and subsequent times. The method for producing a culture medium for mushroom cultivation is characterized in that the pressure for depressurizing the inside of the retort kettle is set to a saturated vapor pressure with respect to the medium temperature at that time, or a pressure slightly higher than that.

すなわち、本発明の製法は、レトルト殺菌処理中に、レ
トルト釜内を減圧状態にして培養容器内より強制的に空
気を脱気させることと、レトルト釜内へ蒸気を供給して
培養容器内の空気を速やかに蒸気に置換させることとを
繰り返して昇温を行い、この場合、2回目以降のレトル
ト釜内の減圧状態を、その時点での培地品温に対する飽
和蒸気圧、あるいはそれより若干高い圧力にすることに
より、短時間で均一に、かつ、培地含水量を保持しなが
ら、レトルト殺菌処理を施すものである。
That is, the manufacturing method of the present invention, during the retort sterilization treatment, forcibly deaerating the air from the culture container by reducing the pressure in the retort kettle, and supplying steam to the retort kettle in the culture container. Rapidly replacing air with steam is repeated to raise the temperature, and in this case, the pressure reduction state in the retort kettle after the second time is saturated vapor pressure with respect to the culture medium temperature at that time, or slightly higher. By applying a pressure, the retort sterilization treatment is performed uniformly in a short time while maintaining the water content of the medium.

以下、本発明を図面に基づき詳細に説明する。Hereinafter, the present invention will be described in detail with reference to the drawings.

第3図は、本発明に用いるレトルト殺菌・真空吸引装置
の一例を示す説明図である。
FIG. 3 is an explanatory view showing an example of the retort sterilization / vacuum suction device used in the present invention.

同図において、(5)は釜本体、(12)はその天井部に
設けられた蒸気吹出用パイプである。(10)はその吹出
用パイプ(12)に蒸気を供給するスチームパイプであ
り、中間に開閉弁(11)が設けられている。(13)は釜
本体(5)の底部に開口を有する真空吸引パイプであ
り、真空ポンプ(7)に連結され、間に開閉弁(14)が
設けられている。(17)は釜本体(5)の天井部に開口
を有する空気取入パイプであり、間に雑菌汚染防止のた
めに空気を洗浄する除菌フィルター(19)と開閉弁(1
8)が設けられている。なお、(15)は間に開閉弁(1
6)が設けられたドレン排出パイプである。また、
(6)は入口扉である。(8)は釜本体(5)内に形成
されたレールであり、このレール(8)によって台車
(9),(9)′が釜本体(5)内に案内されるように
なっている。
In the figure, (5) is a pot main body, and (12) is a steam blowing pipe provided on the ceiling thereof. (10) is a steam pipe for supplying steam to the blow-out pipe (12), and an opening / closing valve (11) is provided in the middle. Reference numeral (13) is a vacuum suction pipe having an opening at the bottom of the pot main body (5), which is connected to the vacuum pump (7) and provided with an opening / closing valve (14) therebetween. (17) is an air intake pipe having an opening in the ceiling of the pot main body (5), between which a sterilization filter (19) and an opening / closing valve (1) for washing air to prevent contamination of various bacteria are provided.
8) is provided. In addition, (15) is an open / close valve (1
It is a drain discharge pipe provided with 6). Also,
(6) is an entrance door. Reference numeral (8) is a rail formed in the shuttle body (5), and the rails (8) guide the carriages (9), (9) 'into the shuttle body (5).

このようなレトルト殺菌・真空吸引装置を用いて、本発
明によるレトルト殺菌は、例えば、次のようにして行
う。すなわち、おがくず,米糠等の培地原料が従来公知
の方法で充填され、開口部が封されたポリプロピレン製
等の培養袋を上記台車(9)に、多段に積層する。次
に、これを釜本体(5)内に収納する。その状態で入口
扉(6)を閉じ、スチームパイプ(10)および空気取入
パイプ(17)は閉状態にし、まず、真空吸引パイプ(1
3)の開閉弁(14)を開き、真空ポンプ(7)を稼働さ
せ、釜本体(5)内を減圧状態にする。このときの減圧
状態は大気圧より低い状態であればよい。次に、真空吸
引パイプ(13)を閉状態にし、スチームパイプ(10)の
開閉弁(11)を開き、釜本体(5)内に、100℃以上で1
0kg/cm2以下、すなわち、100〜180℃で1.03〜10kg/c
m2、好ましくは1.5〜2.7kg/cm2の圧力の飽和蒸気を供給
する。そして、釜本体(5)内を100℃以上、好ましく
は110〜130℃の状態で数分間保持する。その後、再び、
スチームパイプ(10)を閉状態にし、真空吸引パイプ
(13)の開閉弁(14)を開き、真空ポンプ(7)を稼働
させ、釜本体(5)内を減圧状態にする。
Using such a retort sterilization / vacuum suction device, the retort sterilization according to the present invention is performed, for example, as follows. That is, a culture bag made of polypropylene or the like, which is filled with a raw material for culture medium such as sawdust and rice bran by a conventionally known method, and the opening of which is sealed is laminated on the trolley (9) in multiple stages. Next, this is stored in the shuttle body (5). In that state, the inlet door (6) is closed, the steam pipe (10) and the air intake pipe (17) are closed, and first, the vacuum suction pipe (1
The on-off valve (14) of 3) is opened, the vacuum pump (7) is operated, and the inside of the shuttle main body (5) is depressurized. The depressurized state at this time may be lower than atmospheric pressure. Next, close the vacuum suction pipe (13), open the on-off valve (11) of the steam pipe (10), and put it inside the pot body (5) at 100 ° C or higher.
0 kg / cm 2 or less, that is, 1.03 to 10 kg / c at 100 to 180 ° C
Saturated steam is supplied at a pressure of m 2 , preferably 1.5 to 2.7 kg / cm 2 . Then, the inside of the kettle body (5) is kept at 100 ° C. or higher, preferably 110 to 130 ° C. for several minutes. Then again
The steam pipe (10) is closed, the opening / closing valve (14) of the vacuum suction pipe (13) is opened, the vacuum pump (7) is operated, and the inside of the pot body (5) is depressurized.

このときの釜本体(5)内の適正減圧条件は、培地品温
との関係が深く、減圧時点での培地品温に対する飽和蒸
気圧、あるいはそれより若干高い圧力にすることが肝要
である。培地品温に対する飽和蒸気圧未満に減圧した場
合、培地品温は真空圧力下の水沸点もしくは真空中で最
も低温な部分のいずれか高温側の温度迄冷却される。こ
れは真空中で培地水分が蒸発する時の潜熱を培地から奪
っていく事によって生じる冷却で真空冷却と呼ばれる。
真空冷却の生じる減圧条件にした場合、培地含水量が変
化し培養工程以後で不良が発生するだけでなく、加熱殺
菌に必要な熱エネルギーのロスが大きくなると共に処理
時間が長くなる。したがって、このときの圧力は、減圧
時点での培地品温に対する飽和蒸気圧と同じか、または
飽和蒸気圧の好ましくは1.3倍以内の圧力にすると好結
果が得られる。
At this time, the proper depressurization condition in the kettle body (5) has a deep relationship with the medium product temperature, and it is important to set the saturated vapor pressure to the medium product temperature at the time of depressurization or a pressure slightly higher than that. When the pressure is reduced below the saturated vapor pressure with respect to the medium product temperature, the medium product temperature is cooled to either the boiling point of water under vacuum pressure or the lowest temperature part in vacuum, whichever is higher. This is cooling that occurs by removing latent heat from the medium when the medium moisture evaporates in a vacuum, and is called vacuum cooling.
When a reduced pressure condition that causes vacuum cooling is used, not only the water content of the medium changes and defects occur after the culturing step, but also the loss of heat energy required for heat sterilization increases and the processing time increases. Therefore, good results can be obtained when the pressure at this time is the same as the saturated vapor pressure with respect to the medium temperature at the time of depressurization or preferably within 1.3 times the saturated vapor pressure.

次に再度、前回と同様にして蒸気を釜本体(5)内に充
満させる。以上のような培養袋内の空気の脱気と、蒸気
の送入とを必要に応じて数回繰り返し、レトルト殺菌を
施す。
Next, the steam main body (5) is filled with steam again in the same manner as the previous time. The degassing of the air in the culture bag and the feeding of steam as described above are repeated several times as needed to perform retort sterilization.

なお、上記の減圧状態や各回の圧力差,蒸気等の条件
は、培養基の形状や重量,培地品温または装置能力等に
より異なるものであるので都度、適切な設定を行うこと
が好ましい。また、上記条件は圧力制御だけでなく時間
制御によって行ってもよい。
It should be noted that the conditions such as the reduced pressure state, the pressure difference at each time, and the steam vary depending on the shape and weight of the culture medium, the temperature of the culture medium, the capacity of the apparatus, and the like. The above conditions may be controlled not only by pressure control but also by time control.

上記のようにしてレトルト殺菌処理を行った後、釜内を
常圧に戻し、従来公知の方法に従って、冷却を行うこと
により、きのこ栽培用培養基が得られる。
After performing the retort sterilization treatment as described above, the pressure in the kettle is returned to normal pressure, and the culture medium for mushroom cultivation is obtained by cooling according to a conventionally known method.

上記レトルト殺菌時に、釜本体(5)内に収納された培
地原料が充填された培養袋は、第2図に示すような挙動
を示す。すなわち、真空ポンプを稼働させ、釜本体
(5)内を減圧状態にしたとき、培養袋内部の圧力が外
部の圧力より高くなるために、第2図(a)に示すよう
に培養袋内部の空気が外部へ出ようとするため、培養袋
内面全体を押す。この結果、培養袋が膨張すると同時に
培養袋内部の空気がねじ蓋等の通気口を通って脱気され
る。次に、釜本体(5)内に蒸気を吹き込むと、培養袋
外部の圧力が内部の圧力より高くなるために、第2図
(b)に示すように、培養袋外部より培養袋全体を圧縮
するような方向に力が働くと同時に、外部の蒸気がねじ
蓋等の通気口を通って培養袋内部へ侵入する。このよう
な減圧・蒸気供給操作を繰り返すことにより、培養袋内
部の空気が徐々に脱気され希薄になっていくとともに、
蒸気が侵入し、培養袋内部全体の温度が急激にかつ均一
に上昇する。この時、特に培養基の容器がポリプロピレ
ン製袋の如き柔軟性に富んだ容器の場合、第2図に示す
ように、容器が膨張・収縮を繰り返し、あたかも生物が
呼吸しているかのような挙動を示し、その効果は顕著と
なる。
At the time of the above-mentioned retort sterilization, the culture bag filled with the medium raw material stored in the kettle body (5) behaves as shown in FIG. That is, when the vacuum pump is operated and the inside of the kettle body (5) is depressurized, the pressure inside the culture bag becomes higher than the pressure outside, so that as shown in FIG. As the air tries to come out, the whole inner surface of the culture bag is pushed. As a result, at the same time when the culture bag is inflated, the air inside the culture bag is deaerated through the vent hole such as the screw lid. Next, when steam is blown into the kettle body (5), the pressure outside the culture bag becomes higher than the pressure inside, so that the entire culture bag is compressed from outside the culture bag as shown in FIG. 2 (b). At the same time, a force acts in such a direction that outside steam enters the culture bag through a vent such as a screw lid. By repeating such depressurization and steam supply operations, the air inside the culture bag is gradually degassed and becomes leaner,
Steam penetrates and the temperature inside the culture bag rises rapidly and uniformly. At this time, especially when the culture medium container is a highly flexible container such as a polypropylene bag, as shown in FIG. 2, the container repeatedly expands and contracts and behaves as if an organism were breathing. The effect is remarkable.

また、第4図は、培養袋内の中心部と周辺部の温度変化
パターンを示す説明図である。第4図(a)は、従来公
知のレトルト殺菌(真空殺菌)法による場合を表し、同
図(b)は、本発明の殺菌法による場合を表している。
なお、同図(a),(b)の時間及び温度の単位は同一
である。図より、第4図(b)での培養袋内の温度は、
第4図(a)よりも急激に上昇し、かつ、中心部の温度
も周辺部に遅れることなく上昇することを示している。
Further, FIG. 4 is an explanatory view showing temperature change patterns of the central portion and the peripheral portion in the culture bag. FIG. 4 (a) shows the case of the conventionally known retort sterilization (vacuum sterilization) method, and FIG. 4 (b) shows the case of the sterilization method of the present invention.
The units of time and temperature in FIGS. 9A and 9B are the same. From the figure, the temperature in the culture bag in FIG.
It shows that the temperature rises more rapidly than in FIG. 4 (a), and that the temperature of the central portion also rises to the peripheral portion without delay.

更に、レトルト釜内の減圧を、その時点での培地品温に
相当する飽和蒸気圧、あるいはそれより若干高い圧力に
するため、培地内に含有される水分の蒸発はない。
Further, since the reduced pressure in the retort kettle is set to a saturated vapor pressure corresponding to the medium temperature at that time or a pressure slightly higher than that, there is no evaporation of water contained in the medium.

また、本発明において、釜本体内を減圧状態にする装置
としては、上記に示した装置以外に、例えば、従来公知
のレトルト殺菌機に真空冷却装置を接続一体化した装置
を用いて行ってもよい。また、レトルト釜本体内を減圧
状態にする方法としては、真空ポンプに限る必要はな
く、例えば、エゼクター等の吸引装置を用いてもよい。
また、真空装置の前にコンデンサーを設置することによ
り真空能力は大幅に向上する。
Further, in the present invention, as a device for reducing the pressure inside the pot main body, for example, a device in which a vacuum cooling device is integrally connected to a conventionally known retort sterilizer may be used in addition to the above-mentioned device. . Further, the method of reducing the pressure inside the retort kettle body is not limited to the vacuum pump, and for example, a suction device such as an ejector may be used.
Also, the vacuum capacity is greatly improved by installing a condenser in front of the vacuum device.

更に、本発明で使用する培養容器の材質はポリプロピレ
ン製に限るものではなく、耐熱性のある材質であれば他
の材質の袋でも良く、またガラスびんや樹脂製容器を用
いたものでも効果は得られる。また、培養容器の開口部
は、培養容器内外に何らかの手段によって通気経路を有
する状態であれば、ねじ蓋等で蓋をするといった培養容
器形態のみに限られるものではなく、たとえば袋の先端
を部分的にヒートシールを行ったような半密閉状の培養
容器形態のようなものでもよい。
Further, the material of the culture container used in the present invention is not limited to polypropylene, but may be a bag of other material as long as it is a heat resistant material, and the effect using a glass bottle or a resin container is also not effective. can get. Further, the opening of the culture container is not limited to the culture container form in which the inside and outside of the culture container have a ventilation path by some means and is covered with a screw lid or the like. It may be in the form of a semi-hermetically sealed culture vessel that has been heat-sealed.

(発明の効果) 以上のように、本発明のきのこ栽培用培養基の製法で
は、レトルト殺菌処理に要する時間が従来の1〜5時間
よりも大幅に短縮され、0.5時間程度にて行う事が可能
となる。更に、培地含水量がレトルト殺菌処理後も保持
される。すなわち、従来より生産工場等のきのこ栽培用
培養基の量産化を図る際の最大の阻害要因であったレト
ルト殺菌処理工程が、本発明を実施することによって、
レトルト殺菌機の増設等の大がかりな費用をかけずにレ
トルト殺菌処理時間の短縮が可能となり、生産効率の向
上が成されるとともに、培地含水量の変化による培養工
程での不良が生じない。
(Effect of the invention) As described above, in the method for producing a culture medium for mushroom cultivation of the present invention, the time required for the retort sterilization treatment is significantly shortened compared to the conventional 1 to 5 hours, and can be performed in about 0.5 hours. Becomes Further, the water content of the medium is retained after the retort sterilization treatment. That is, the retort sterilization treatment step, which has been the largest inhibiting factor when mass-producing the culture medium for mushroom cultivation in a production plant, etc. by carrying out the present invention,
The retort sterilization process time can be shortened without incurring a large cost such as the addition of a retort sterilizer, and the production efficiency is improved, and defects in the culture process due to changes in the water content of the medium do not occur.

更には、昇温しにくい性質のある培養袋内部の中心部が
周辺部に遅れることなく昇温することにより、培養袋内
全体が均一に殺菌処理される。この結果、後の培養工程
において、殺菌不充分による雑菌汚染率が大幅に低下
し、工程の品質面の向上も図ることが可能となる。
Furthermore, the temperature inside the culture bag, which has the property of being difficult to raise the temperature, is raised without delaying to the peripheral portion, so that the inside of the culture bag is uniformly sterilized. As a result, in the subsequent culturing step, the contamination rate of miscellaneous bacteria due to insufficient sterilization is significantly reduced, and the quality of the step can be improved.

すなわち、本発明により、きのこ栽培用培養基の生産工
場において製品の生産効率と歩留りとを飛躍的に向上さ
せることができる。
That is, according to the present invention, it is possible to dramatically improve the production efficiency and yield of products in a plant for producing a culture medium for mushroom cultivation.

以下、実施例に基づいて本発明を具体的に説明する。Hereinafter, the present invention will be specifically described based on Examples.

<実施例1> おがくず40重量部,米糠1重量部に加水し、含水率を70
%になるように調整した培地原料1kgを、ポリプロピレ
ン製培養袋に充填して円柱状に成形し、培養袋開口部に
第1図に示すように通気口を有する市販肩口キャップを
装着した。
<Example 1> 40 parts by weight of sawdust and 1 part by weight of rice bran were hydrated to a water content of 70
1 kg of the culture medium raw material adjusted to be 100% was filled in a polypropylene culture bag and formed into a cylindrical shape, and a commercially available shoulder cap having a vent hole was attached to the opening of the culture bag as shown in FIG.

次に、上述したレトルト殺菌・真空吸引装置を用い、レ
トルト殺菌を行った。このとき、最初の釜本体内の減圧
状態を60Torr、2回目を培地品温が61℃であった為160T
orr、3回目を培地品温が72℃であった為260Torr、4回
目を培地品温が80℃であった為360Torrとして真空吸引
装置を稼働させた。釜本体内に供給する蒸気は2.5kg/cm
2の圧力に設定し、保持温度は121℃に設定し、蒸気充満
時の保持時間は、それぞれ2分間とした。
Next, retort sterilization was performed using the retort sterilization / vacuum suction device described above. At this time, the first depressurized state in the pot body was 60 Torr, and the second was 160 T because the medium temperature was 61 ° C.
The vacuum suction device was operated at ortor for the third time at 260 Torr because the medium product temperature was 72 ° C. and for the fourth time at 360 Torr because the medium product temperature was 80 ° C. The steam supplied to the pot body is 2.5 kg / cm
The pressure was set to 2 , the holding temperature was set to 121 ° C., and the holding time when the steam was filled was 2 minutes.

この結果、レトルト殺菌処理は、35分で完了した。ま
た、レトルト殺菌処理前後での培地含水量の変化は認め
られなかった。
As a result, the retort sterilization treatment was completed in 35 minutes. In addition, no change in the water content of the medium was observed before and after the retort sterilization treatment.

<実施例2> 実施例1と同様にして調製した培地原料を0.5kg充填し
た培養袋を用いて、レトルト殺菌を行った。
<Example 2> Retort sterilization was performed using a culture bag filled with 0.5 kg of the medium raw material prepared in the same manner as in Example 1.

最初の減圧状態を60Torr、2回目を培地品温が80℃であ
った為360Torrとして真空吸引装置を稼働させた。供給
する蒸気の圧力、ならびに保持温度は実施例1の設定と
同一とし、減圧状態間の蒸気充満時の保持時間は0分間
とした。
The first vacuum condition was 60 Torr, and the second time the medium product temperature was 80 ° C., so 360 Torr was set and the vacuum suction device was operated. The pressure of the supplied steam and the holding temperature were the same as those in Example 1, and the holding time when the steam was filled between the depressurized states was 0 minutes.

この結果、レトルト殺菌処理は、30分で完了した。ま
た、レトルト殺菌処理前後での培地含水量の変化は認め
られなかった。
As a result, the retort sterilization treatment was completed in 30 minutes. In addition, no change in the water content of the medium was observed before and after the retort sterilization treatment.

<実施例3> 実施例2と同様に培地原料を0.5kg充填した培養袋を用
い、最初の減圧状態を60Torr、2回目を培地品温が72℃
であった為260Torrとして真空吸引装置を稼働させた。
このとき、真空吸引装置の稼働に要した時間はそれぞれ
2分,3分であった。また、この間の蒸気の圧力、ならび
に保持温度は実施例1の設定と同一とし、保持時間は3
分間とした。
<Example 3> As in Example 2, using a culture bag filled with 0.5 kg of medium raw material, the first depressurized state was 60 Torr, and the second time the medium temperature was 72 ° C.
Therefore, the vacuum suction device was operated at 260 Torr.
At this time, the time required to operate the vacuum suction device was 2 minutes and 3 minutes, respectively. In addition, the pressure of the steam and the holding temperature during this period were the same as those in Example 1, and the holding time was 3
Minutes.

この結果、レトルト殺菌処理時間は36分となった。ま
た、レトルト殺菌処理前後での培地含水量の変化は認め
られなかった。
As a result, the retort sterilization treatment time was 36 minutes. In addition, no change in the water content of the medium was observed before and after the retort sterilization treatment.

<実施例4> 実施例2と同様に培地原料を0.5kg充填した培養袋を用
いて、供給する蒸気の圧力ならびに保持温度を実施例3
と同一に設定し、釜本体内を減圧状態にする真空ポンプ
の稼働を圧力計を用いずにタイマーを設置して時間で制
御した。つまり、実施例3の条件と同一の減圧状態にす
るために真空ポンプの稼働を2分間とし、次の釜本体内
への蒸気の保持を3分間、2回目の真空ポンプ稼働を3
分間というように時間で制御した。
<Example 4> As in Example 2, using a culture bag filled with 0.5 kg of medium raw material, the pressure of steam to be supplied and the holding temperature were set in Example 3.
The operation of the vacuum pump, which was set to be the same as the above, to depressurize the inside of the kettle body, was controlled by time by installing a timer without using a pressure gauge. In other words, the vacuum pump is operated for 2 minutes in order to obtain the same reduced pressure condition as the condition of the third embodiment, the steam is kept in the pot body for the next 3 minutes, and the second vacuum pump is operated for 3 minutes.
Controlled by time, such as minutes.

この結果、時間制御によっても実施例3と同様の結果が
得られた。
As a result, the same result as in Example 3 was obtained by the time control.

<比較例1> 実施例2と同様に培地原料を0.5kg充填した培養袋を用
い、供給する蒸気の圧力および保持温度の設定も同一と
し、従来公知の方法であるレトルト殺菌に先立ち釜本体
内を減圧状態にする方法を行った。つまり、上記の実施
例と同じレトルト殺菌真空吸引装置を用いて、同じ方法
で釜本体内に培地原料を充填した培養袋を収納した。そ
の後、真空ポンプを稼働させ、釜本体内の減圧状態を60
Torrとした後、蒸気を供給し、レトルト殺菌処理を行っ
た。
<Comparative Example 1> As in the case of Example 2, a culture bag filled with 0.5 kg of a medium raw material was used, the pressure of steam to be supplied and the holding temperature were set to be the same, and the inside of the pot main body was set before the retort sterilization which is a conventionally known method. A method of reducing pressure was performed. That is, the same retort sterilization vacuum suction device as that used in the above example was used to store the culture bag filled with the medium raw material in the pot body in the same manner. Then, operate the vacuum pump to reduce the pressure inside the kettle body to 60
After setting to Torr, steam was supplied to perform retort sterilization.

この結果、レトルト殺菌処理時間は60分間を要した。As a result, the retort sterilization treatment time required 60 minutes.

<比較例2> 実施例2と同様に培地原料を0.5kg充填した培養袋を用
い、供給する蒸気の圧力および保持温度の設定も同一と
した。最初のレトルト釜内減圧を60Torr、2回目も培地
品温は80℃であったが60Torrまで減圧を行った。このと
き、培地品温は42℃となった。その後再度蒸気を供給し
レトルト殺菌処理を行った。
<Comparative Example 2> As in Example 2, a culture bag filled with 0.5 kg of the culture medium raw material was used, and the pressure of the supplied steam and the holding temperature were set to be the same. The first depressurization in the retort kettle was 60 Torr, and the medium product temperature was 80 ° C. in the second time as well, but the pressure was reduced to 60 Torr. At this time, the medium temperature was 42 ° C. After that, steam was supplied again to perform retort sterilization treatment.

この結果処理時間は42分となり、レトルト殺菌処理後の
含水率は66.7%と変化した。
As a result, the treatment time was 42 minutes, and the water content after the retort sterilization treatment was 66.7%.

上記実施例1〜4及び比較例1〜2のごとくレトルト殺
菌処理が行われて得られた培養基各3000個にしいたけの
種菌を植菌し、培養を行った。
The retort sterilization treatment was carried out as in Examples 1 to 4 and Comparative Examples 1 to 2 described above, and 3,000 seeds of each of the culture media were inoculated with the inoculum of mushrooms and cultivated.

これら殺菌処理条件,雑菌汚染率等の結果を第1表にあ
わせて示す。なお、雑菌汚染率は殺菌不充分によるもの
を示している。
The results of these sterilization conditions and the contamination ratio of various bacteria are also shown in Table 1. In addition, the contamination ratio of various bacteria is due to insufficient sterilization.

この結果、実施例1〜4及び比較例2の培養基のうち殺
菌不充分により雑菌汚染された培養基は全くなかった。
これに対して比較例1の培養基のうち殺菌不充分により
雑菌汚染された培養基は3000個中18個(0.6%)であっ
た。
As a result, none of the culture mediums of Examples 1 to 4 and Comparative Example 2 were contaminated with bacteria due to insufficient sterilization.
On the other hand, among the culture media of Comparative Example 1, the culture media contaminated with various bacteria due to insufficient sterilization was 18 out of 3000 (0.6%).

また培養不良となった培養基は、実施例1〜4及び比較
例1で3000個中60〜90個(2〜3%)であるのに対し、
比較例2では720個(24%)にも達した。
In addition, the number of culture media that failed culture was 60 to 90 out of 3000 (2 to 3%) in Examples 1 to 4 and Comparative Example 1, whereas
In Comparative Example 2, the number reached 720 (24%).

以上の結果より、本発明の製法は、製品の生産効率と歩
留りを大きく向上させることができる。また、真空ポン
プ等の制御を圧力のみならず、時間によって制御するこ
ともできるので、例えば、予め時間プログラムを作って
殺菌工程を管理することも可能である。
From the above results, the production method of the present invention can greatly improve the production efficiency and yield of products. Further, since the control of the vacuum pump and the like can be controlled not only by the pressure but also by the time, it is possible to manage the sterilization process by creating a time program in advance.

従って、生産工場の生産規模,人員,装置等に合わせ
て、制御方法を設定できるので殺菌工程における省力
化,省人化,迅速化が可能となる。
Therefore, the control method can be set according to the production scale of the production factory, the number of personnel, the device, etc., so that labor saving, labor saving, and speedup in the sterilization process can be achieved.

【図面の簡単な説明】[Brief description of drawings]

第1図は一般的なきのこ栽培用培養基の説明図、第2図
は本発明の基本原理を示す説明図、第3図は本発明に用
いるレトルト殺菌・真空吸引装置の一例を示す説明図、
第4図は培養袋内部の中心部と周辺部の温度変化パター
ンを示す説明図である。 (1)……培地原料、(2)……ねじ蓋、(3)……通
気口部、(4)……培養袋、(5)……釜本体、(7)
……真空ポンプ、(12)……蒸気吹出用パイプ、(13)
……真空吸引パイプ、(17)……空気取入パイプ、(1
9)……除菌フィルター。
FIG. 1 is an explanatory view of a general culture medium for mushroom cultivation, FIG. 2 is an explanatory view showing the basic principle of the present invention, and FIG. 3 is an explanatory view showing an example of a retort sterilization / vacuum suction device used in the present invention,
FIG. 4 is an explanatory diagram showing a temperature change pattern in the central portion and the peripheral portion inside the culture bag. (1) ... medium material, (2) ... screw lid, (3) ... vent hole, (4) ... culture bag, (5) ... pot body, (7)
...... Vacuum pump, (12) …… Steam blowing pipe, (13)
…… Vacuum suction pipe, (17) …… Air intake pipe, (1
9) …… Sterilization filter.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】きのこ栽培用の培地原料を充填した容器を
レトルト釜内に入れてレトルト殺菌を施すに際し、レト
ルト釜内を減圧して上記培地の充填された容器内部の空
気を脱気する工程と、レトルト釜内に100℃以上の蒸気
を10kg/cm2以下の圧力で供給し、容器内部へ蒸気を送入
させる工程とを順次繰り返して行い、該2回目以降のレ
トルト釜内を減圧するときの圧力を、その時点での培地
品温に対する飽和蒸気圧、あるいはそれより若干高い圧
力にすることを特徴とするきのこ栽培用培養基の製法。
1. A step of depressurizing the inside of a container filled with the above medium by depressurizing the inside of the retort kettle when putting a container filled with a raw material for a medium for mushroom cultivation into a retort kettle to perform retort sterilization. And the step of supplying steam of 100 ° C. or higher at a pressure of 10 kg / cm 2 or less into the retort kettle and sending the steam into the container are sequentially repeated to reduce the pressure in the retort kettle after the second time. A method for producing a culture medium for mushroom cultivation, characterized in that the pressure at that time is set to a saturated vapor pressure with respect to the medium temperature at that time or a pressure slightly higher than that.
JP2090698A 1989-06-30 1990-04-05 Manufacturing method of culture medium for mushroom cultivation Expired - Lifetime JPH0681570B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP1-170382 1989-06-30
JP17038289 1989-06-30

Publications (2)

Publication Number Publication Date
JPH0387120A JPH0387120A (en) 1991-04-11
JPH0681570B2 true JPH0681570B2 (en) 1994-10-19

Family

ID=15903902

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2090698A Expired - Lifetime JPH0681570B2 (en) 1989-06-30 1990-04-05 Manufacturing method of culture medium for mushroom cultivation

Country Status (1)

Country Link
JP (1) JPH0681570B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09253266A (en) * 1996-03-21 1997-09-30 Toshihiko Kaneda Glove

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4530954B2 (en) * 2005-08-08 2010-08-25 有限会社コンペックス Method for producing sterilized fungus bed for straw cultivation

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09253266A (en) * 1996-03-21 1997-09-30 Toshihiko Kaneda Glove

Also Published As

Publication number Publication date
JPH0387120A (en) 1991-04-11

Similar Documents

Publication Publication Date Title
JPS6012018B2 (en) Continuous hot water heating sterilization method and its equipment
CA1080646A (en) Method for vessel cultivation of lentinus edodes
JP2002051639A (en) Method for producing liquid spawn of mushroom and apparatus for inoculation of liquid spawn
JPH0681570B2 (en) Manufacturing method of culture medium for mushroom cultivation
JPH09172992A (en) Preparation of asepticaly packed cooked rice
CN106676018B (en) Agaricus bisporus strain breeding method suitable for standardized factory
CN103190288B (en) Edible mushroom vertical bag is planted and carries mouth cultivation fruiting method
GB2508946A (en) Method of producing bean sprouts
JP5241024B2 (en) Mushroom bed cultivation equipment
CN206481644U (en) Button mushroom kind system and device is bred in one kind standardization
JPH0775442A (en) Method of culturing mushroom mycelia
CN116555244A (en) Yellow series morchella multi-spore fusion separation method
CN215122714U (en) A kind of antler mushroom edible mushroom bag disinfection device
CN108739066A (en) A kind of lentinus edodes strain stick high pressure steam sterilization method
CN108782012A (en) A kind of White mushroom implantation methods
KR20190056328A (en) Production method of mushroom using mushroom cultivation bag with micropore
JP2003153632A (en) Method for cultivating mushroom
CN102972202A (en) Sterilization method of edible fungus culture medium
JP4060153B2 (en) Sterilizer, sterilization method, and culture method
JPH06209651A (en) Method for raising &#39;shiitake&#39; mushroom
CN206260761U (en) Strain koji machine
JPH053724A (en) Culture vessel for mushroom
CN112265228A (en) Edible fungus bag production system and process
KR960004964B1 (en) Cultivation container and cultivation method of edible mushrooms
CN106819974A (en) Canned strawberry and strawberry vacuum-pumping method