JP3362984B2 - Manufacturing method of non-boiled edible princess mushroom - Google Patents

Manufacturing method of non-boiled edible princess mushroom

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Publication number
JP3362984B2
JP3362984B2 JP29623994A JP29623994A JP3362984B2 JP 3362984 B2 JP3362984 B2 JP 3362984B2 JP 29623994 A JP29623994 A JP 29623994A JP 29623994 A JP29623994 A JP 29623994A JP 3362984 B2 JP3362984 B2 JP 3362984B2
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JP
Japan
Prior art keywords
princess
himematsutake
suspension
mushroom
manufacturing
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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
JP29623994A
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Japanese (ja)
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JPH08149964A (en
Inventor
福佳 中田
Original Assignee
パワフル健康食品株式会社
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Expired - Lifetime legal-status Critical Current

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  • Coloring Foods And Improving Nutritive Qualities (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Medicines Containing Plant Substances (AREA)

Description

【発明の詳細な説明】 【0001】 【産業上の利用分野】本発明は姫マツタケの消化困難な
細胞壁を破砕して、煮沸あるいは抽出操作をすることな
く食用に供することのできる非煮沸可食姫マツタケの製
造法に関する。 【0002】 【従来の技術】姫マツタケは菌糸の集合体であり、ヒト
はその集合体である子実体と呼ばれる茸を食用としてい
る。しかし、姫マツタケの菌糸壁はキチン質及びヘミセ
ルロースで構成されており、極めて消化性が悪く、加熱
しなければ食用に供することができないものであった。 【0003】また、近年、その薬効が注目され、健康食
品として服用することが行われている。しかし、その豊
富な栄養成分及び薬効成分の多くは菌糸壁に蓄積されて
いるため、加熱処理したり、エキス抽出を行っても、こ
れらの成分を充分に取り出すのは困難であり、従って、
有用な成分を含むにもかかわらず、これを充分に利用で
きないのが実状であった。 【0004】 【発明が解決しようとする課題】一方、姫マツタケの菌
糸壁を破砕して、その有効成分を取り出すことが考えら
れるが、これまで、この強靱な菌糸壁を充分に破砕する
方法が知られていなかった。従って、本発明は、姫マツ
タケの菌糸壁を破砕して、その有効成分を充分に利用で
きる食品を提供せんとするものである。 【0005】 【課題を解決するための手段】このような実情におい
て、本発明者は鋭意研究を行った結果、特定の剛体メデ
ィアを使用して破砕すれば上記目的にかなった食品が得
られることを見出し、本発明を完成した。 【0006】すなわち、本発明は、姫マツタケを20〜
100メッシュに粉砕し、得られた姫マツタケ粉末に水
を加えて20〜90重量%の懸濁液となし、この懸濁液
を直径0.5〜1.0mmの剛体メディアが80〜85容
量%満たされたシリンダーに送入し、50℃以下の温度
で回転混和し、得られたスラリーを乾燥することを特徴
とする非煮沸可食姫マツタケの製造法を提供するもので
ある。 【0007】本発明の製造方法を実施するには、まず姫
マツタケを20〜100メッシュに粉砕する。粉砕方法
は特に限定されないが、例えば姫マツタケを80℃程度
で焙煎し、殺菌、乾燥し、水分を5〜10%までとし、
これをアルピネ、ミル等を用いて粉砕する方法が挙げら
れる。また、100メッシュに近い細かい粉末を得るに
は、凍結粉砕が好ましい。 【0008】得られた粉体は、水を加え、濃度20〜9
0重量%の水懸濁液とする。この濃度が20%未満であ
ると、次の工程の作業効率が悪くなり、生産性が低下
し、経済的に不利である。一方、90重量%を超える
と、次工程に用いる密閉シリンダーの中で、摩砕を行う
ための剛体メディアと姫マツタケ水懸濁液とが一緒に回
転してしまい、摩砕が不充分となるため好ましくない。 【0009】姫マツタケ水懸濁液は、剛体メディアが8
0〜85%(容量)満たされているシリンダーに送入さ
れる。この剛体メディアの直径は0.5〜1.0mmであ
り、材質はジルコン又はジルコニアビーズが好ましい。
また剛体メディアはシリンダーの内容積の80〜85重
量%を満たす量を用いるが、この範囲を逸脱すると破砕
効率及び生産性が悪くなり好ましくない。 【0010】姫マツタケ水懸濁液は剛体メディアと共
に、回転羽根により回転・混和する。この回転・混和に
よって、剛体メディアと回転羽根の摩砕作用により姫マ
ツタケ細胞壁が破壊されるが、同時に熱が発生する。こ
れを放置すると、得られる姫マツタケ微粉末の品質が悪
化するため、温度を50℃以下に保たなければならな
い。温度を50℃以下に保つには、前記姫マツタケ水懸
濁液を前もって冷却しておくか、シリンダーの外部に冷
却外套等の冷却装置を設ける等の処置が行われる。な
お、回転羽根の材質は焼入鋼、ステンレススチール、ア
ルミナが好ましく、形状は円盤形で矢じり状の切込みが
入っているものが好ましく、その回転数は2,000〜
3,500rpm とすることが好ましい。 【0011】本発明製造方法を実施する装置としては、
冷却外套を備えた連続湿式微粉砕機が好ましく、市販の
ものとしてはダイノ−ミル(DYNO-MILL, Willy A. Bach
ofenAG Maschinenfabrik )が好適である。ダイノ−ミ
ルを用いる場合は、前記懸濁液の流量を5〜150l/
hrとすることが好ましい。 【0012】以上の如くして、得られた細胞壁破壊姫マ
ツタケのスラリーは、次の乾燥工程を経て、製品化され
る。乾燥は、姫マツタケ微粉末が変質しない方法であれ
ば特に限定されないが、工業的には減圧真空乾燥による
方法が好ましい。なお前記スラリーが粘着性を増してい
るため、乾燥工程中に乾燥機本体に付着し、焦げてしま
うおそれがあるため、付着防止剤、例えばカルボキシメ
チルセルロース(CMC)の微結晶粉体を10〜15%
添加するのが好ましい。また、減圧乾燥機を用いて乾燥
する際の温度は、40〜60℃とすることが好ましい。 【0013】かくして得られる姫マツタケ微粉末は、従
来の方法では全く破壊されなかった細胞壁が破壊されて
おり、その粒径は約90%以上が350メッシュ以下で
ある。 【0014】 【発明の効果】本発明の製造方法によれば、姫マツタケ
の強靱な細胞壁を破壊することができるため、細胞中の
有効成分を充分活用することができる。 【0015】 【実施例】次に、実施例を挙げて本発明を更に詳細に説
明するが、本発明はこれらに限定されるものではない。 【0016】実施例1 採取した姫マツタケ1kgを80℃、120分間焙煎し、
殺菌、乾燥し、水分を11〜12%とし、これをアルピ
スを用いて5分間粉砕を行い5メッシュとした。これを
更にボールミル((株)山本鉄工所製,ミルト2号B
型)を用い、5分間粉砕し、50メッシュの姫マツタケ
粉末を450g得た。なお、クラッシャー粉砕前の姫マ
ツタケ水分を60%として計算すると5%のロスであっ
た。得られた姫マツタケ粉末を電子顕微鏡で観察する
と、まだ姫マツタケ細胞は破壊されていないことが判っ
た。このようにして得られた姫マツタケ粉末に水を加
え、濃度10%の姫マツタケ・水懸濁液を調製し、温度
を10℃にした。次いで直径0.5〜1mmのジルコンビ
ーズを密封シリンダー容量の80%封入したダイノ−ミ
ル中に、前記懸濁液を流量15l/hrにて送入した。密
閉シリンダー中では焼入鋼製の羽根が3200rpmで回
転しており、これにより、ジルコンビーズ及び前記懸濁
液を回転・混和せしめ、姫マツタケ細胞壁を摩砕した。
この時、同時に冷却外套をセットし、温度を調節した。
この結果細胞壁が完全に粉砕された50℃の姫マツタケ
スラリーが連続して得られた。次に冷却機より5℃に冷
却した後、タンクにて貯蔵し、姫マツタケスラリーに1
0%のCMCを付着防止剤として添加した後、減圧低温
乾燥機を使用して、姫マツタケ微粉末を得た。得られた
姫マツタケ微粉末は、その90%以上が350メッシュ
以下であった。 【0017】上記方法における粉砕前の姫マツタケと粉
砕後の姫マツタケについて可溶性無窒素物(糖質)を測
定したところ、粉砕前は27.0g/100gであった
ものが、粉砕後は41.9g/100gに上昇した。こ
のことは本発明方法で得られた姫マツタケ粉末はこれを
服用したときにその成分を有効に利用できることを意味
するものである。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a non-boiled edible crushed edible matsutake mushroom which can be edible without crushing or extracting the cell wall. It relates to a method for producing Hime Matsutake. 2. Description of the Related Art Himematsutake is an aggregate of hyphae, and humans consume mushrooms, which are aggregates, and are called fruiting bodies. However, the mycelial wall of Himematsutake was composed of chitin and hemicellulose, and was extremely poor in digestibility and could not be used for food unless heated. [0003] In recent years, its medicinal properties have attracted attention, and they have been taken as health foods. However, since many of the abundant nutritional and medicinal components are accumulated in the mycelial wall, it is difficult to sufficiently remove these components even by heat treatment or extract extraction.
In spite of the fact that it contains useful components, it has not been possible to make full use of it. [0004] On the other hand, it is conceivable to crush the mycelial wall of Himematsutake to take out the active ingredient, and a method of sufficiently crushing the tough mycelial wall has heretofore been proposed. Was not known. Accordingly, an object of the present invention is to provide a food product in which the mycelial wall of Himematsutake is crushed and its active ingredient can be sufficiently utilized. [0005] Under such circumstances, the present inventors have conducted intensive studies and as a result, it has been found that foods meeting the above-mentioned object can be obtained by crushing using a specific rigid medium. And completed the present invention. [0006] That is, the present invention relates to a method for producing Himematsutake from 20 to
Water was added to the resulting Himematsutake powder to form a suspension of 20 to 90% by weight, and the suspension was crushed into a rigid medium having a diameter of 0.5 to 1.0 mm in an amount of 80 to 85 volumes. %. [0007] In order to carry out the production method of the present invention, Himematsutake is first crushed to 20 to 100 mesh. The crushing method is not particularly limited. For example, princess matsutake is roasted at about 80 ° C., sterilized and dried, and the water content is adjusted to 5 to 10%.
A method of pulverizing this using an alpine, a mill or the like can be used. In order to obtain a fine powder close to 100 mesh, freeze pulverization is preferred. [0008] The obtained powder is added with water to a concentration of 20-9.
A 0% by weight aqueous suspension is obtained. If this concentration is less than 20%, the working efficiency of the next step is lowered, the productivity is reduced, and it is economically disadvantageous. On the other hand, when the content exceeds 90% by weight, the rigid medium for grinding and the water suspension of Himematsutake are rotated together in the closed cylinder used in the next step, and the grinding becomes insufficient. Therefore, it is not preferable. [0009] The water suspension of Himematsutake is composed of 8 rigid media.
It is fed into a cylinder that is 0-85% (volume) full. The diameter of the rigid medium is 0.5 to 1.0 mm, and the material is preferably zircon or zirconia beads.
The rigid medium is used in an amount that satisfies 80 to 85% by weight of the inner volume of the cylinder. However, if the amount is outside this range, the crushing efficiency and productivity will deteriorate, which is not preferable. The Himematsutake water suspension is rotated and mixed with the rigid medium by the rotating blades. This rotation / mixing destroys the Himematsutake cell wall by the grinding action of the rigid medium and the rotating blades, but at the same time generates heat. If left untreated, the quality of the resulting Himematsutake fine powder deteriorates, so the temperature must be kept at 50 ° C. or lower. In order to keep the temperature at 50 ° C. or lower, measures such as cooling the Himematsutake water suspension in advance or providing a cooling device such as a cooling jacket outside the cylinder are performed. The material of the rotating blade is preferably hardened steel, stainless steel, or alumina, and the shape is preferably a disk shape with a barbed cut, and the rotation speed is 2,000 to 2,000.
It is preferred to be 3,500 rpm. The apparatus for carrying out the manufacturing method of the present invention includes:
A continuous wet pulverizer equipped with a cooling jacket is preferred, and commercially available products are DYNO-MILL, Willy A. Bach
ofenAG Maschinenfabrik) are preferred. When using a dyno-mill, the flow rate of the suspension is 5 to 150 l /
hr is preferable. [0012] The slurry of matsutake mushroom obtained as described above is commercialized through the following drying step. Drying is not particularly limited as long as the method does not alter the Himematsutake fine powder, but industrially, vacuum drying is preferred. In addition, since the slurry has increased tackiness, it may adhere to the dryer body during the drying process and burn. Therefore, an anti-adhesion agent such as carboxymethylcellulose (CMC) microcrystalline powder is used for 10 to 15 minutes. %
It is preferred to add. Further, the temperature at the time of drying using a reduced-pressure drier is preferably set to 40 to 60 ° C. The thus obtained fine powder of Himematsutake has a cell wall which has not been destroyed at all by the conventional method, and its particle size is about 90% or more and 350 mesh or less. According to the production method of the present invention, since the tough cell wall of Himematsutake can be destroyed, the active ingredients in the cells can be fully utilized. Next, the present invention will be described in more detail with reference to examples, but the present invention is not limited to these examples. Example 1 1 kg of collected princess matsutake was roasted at 80 ° C. for 120 minutes.
Sterilization and drying were performed to reduce the water content to 11 to 12%, and this was pulverized for 5 minutes using Alpis to obtain 5 mesh. The ball mill (Milt No. 2B, manufactured by Yamamoto Tekkosho Co., Ltd.)
(G), and pulverized for 5 minutes to obtain 450 g of 50-mesh princess matsutake powder. The loss was 5% when calculated assuming that the water content of Himematsutake before crusher crushing was 60%. Observation of the obtained princess matsutake powder with an electron microscope revealed that the princess matsutake cells had not been destroyed yet. Water was added to the princess matsutake mushroom powder thus obtained to prepare a princess matsutake / water suspension having a concentration of 10%, and the temperature was adjusted to 10 ° C. Next, the suspension was fed at a flow rate of 15 l / hr into a dyno-mill in which zircon beads having a diameter of 0.5 to 1 mm were sealed at 80% of the capacity of a sealed cylinder. The hardened steel blades were rotating at 3200 rpm in the closed cylinder, whereby the zircon beads and the suspension were rotated and mixed to grind the Himematsutake cell walls.
At this time, a cooling jacket was set at the same time to adjust the temperature.
As a result, a princess matsutake slurry at 50 ° C. in which the cell walls were completely ground was continuously obtained. Next, after cooling to 5 ° C. from the cooler, it was stored in a tank and added to Himematsutake slurry.
After adding 0% of CMC as an antiadhesive agent, a Himematsutake fine powder was obtained using a reduced-pressure low-temperature dryer. 90% or more of the obtained Himematsutake fine powder had a size of 350 mesh or less. When the soluble nitrogen-free substances (sugars) of the princess matsutake before and after crushing in the above method were measured, it was 27.0 g / 100 g before crushing and 41. It rose to 9 g / 100 g. This means that the Himematsutake powder obtained by the method of the present invention can effectively utilize its components when taken.

Claims (1)

(57)【特許請求の範囲】 【請求項1】 姫マツタケを20〜100メッシュに粉
砕し、得られた姫マツタケ粉末に水を加えて20〜90
重量%の懸濁液となし、この懸濁液を直径0.5〜1.
0mmの剛体メディアが80〜85容量%満たされたシリ
ンダーに送入し、50℃以下の温度で回転混和し、得ら
れたスラリーを乾燥することを特徴とする非煮沸可食姫
マツタケの製造法。
(57) [Claims 1] The princess matsutake is crushed to 20 to 100 mesh, and water is added to the obtained princess matsutake powder to obtain 20 to 90 mesh.
% Suspension, and the suspension is 0.5-1.
A method for producing non-boiling edible princess mushrooms, comprising feeding a 0 mm rigid medium into a cylinder filled with 80 to 85% by volume, rotating and mixing at a temperature of 50 ° C. or less, and drying the obtained slurry. .
JP29623994A 1994-11-30 1994-11-30 Manufacturing method of non-boiled edible princess mushroom Expired - Lifetime JP3362984B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29623994A JP3362984B2 (en) 1994-11-30 1994-11-30 Manufacturing method of non-boiled edible princess mushroom

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29623994A JP3362984B2 (en) 1994-11-30 1994-11-30 Manufacturing method of non-boiled edible princess mushroom

Publications (2)

Publication Number Publication Date
JPH08149964A JPH08149964A (en) 1996-06-11
JP3362984B2 true JP3362984B2 (en) 2003-01-07

Family

ID=17830991

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3362984B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB0110954D0 (en) 2001-05-04 2001-06-27 Marlow Foods Ltd Edible fungi
JP4560145B2 (en) * 2004-09-24 2010-10-13 株式会社 アンフィニ Mycelium processing method of moss
EP4298912A1 (en) * 2022-07-01 2024-01-03 Planetary SA Fungal mycelium-based milk or cream substitute

Also Published As

Publication number Publication date
JPH08149964A (en) 1996-06-11

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