JPH0523193A - Production of high-viscosity cultured product derived from filamentous fungi - Google Patents

Production of high-viscosity cultured product derived from filamentous fungi

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Publication number
JPH0523193A
JPH0523193A JP20150291A JP20150291A JPH0523193A JP H0523193 A JPH0523193 A JP H0523193A JP 20150291 A JP20150291 A JP 20150291A JP 20150291 A JP20150291 A JP 20150291A JP H0523193 A JPH0523193 A JP H0523193A
Authority
JP
Japan
Prior art keywords
culture
cultured
glucan
highly viscous
beta
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.)
Pending
Application number
JP20150291A
Other languages
Japanese (ja)
Inventor
Tomohisa Kotani
智久 小谷
Hiroko Santo
博子 山東
Kazuyoshi Morita
和良 森田
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
Priority to JP20150291A priority Critical patent/JPH0523193A/en
Publication of JPH0523193A publication Critical patent/JPH0523193A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To efficiently and economically obtain high-viscous cultured product such as beta-glucan without exerting adverse influence to hypha by aerobically subjecting a filamentous fungi belonging to the genus Macrophomopsis to liquid culture while stirring the cultured product with a paddle type agitator. CONSTITUTION:A filamentous fungi strain KAB 55 (FERM P-9366) of the genus Macrophomosis, etc., is cultured in a medium for 3 day and planted in a jar fermentor to which a paddle type agitator is fitted and aerobically cultured at 25 deg.C for 4 day to produce highly viscous cultured product and then the cultured product is centrifuged to remove a microbial fungal cell and an organic precipitating agent such as ethanol is added to the supernatant. Thereby the product is subjected to precipitation separation to provide the objective cultured product containing high-viscous beta-glucan, wherein all D-goucopyranosyl residues of the main chain have beta-1,3 bond and branched at C-6 position and D- glucopyranosyl residues of the side chain have beta-1,6 bond in a ratio of 1 based on 4 D-glucopyranosyl residues.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は高粘性のβ−グルカンを
産生するマクロフォモプシス(Macrophomop
sis)属に属する糸状菌培養物の製造方法に関する。
BACKGROUND OF THE INVENTION The present invention relates to a macrophomops which produces highly viscous β-glucan.
The present invention relates to a method for producing a filamentous fungus culture belonging to the genus sis).

【0002】[0002]

【従来の技術及び発明が解決しようとする課題】マクロ
フォモプシス(Macrophomopsis)属に属
する糸状菌を効率良く液体培養するためには多量の通気
と培養系内の均一性を保つことが必要である。本発明者
等は、これまで特願平2−413440号公報に記載の
ごとく、振盪培養や深部通気培養などによる高粘性のβ
−グルカンの製造法を見いだし、提案した。
BACKGROUND OF THE INVENTION In order to efficiently liquid-culture filamentous fungi belonging to the genus Macrophomopsis, it is necessary to maintain a large amount of aeration and homogeneity in the culture system. . As described in Japanese Patent Application No. 2-413440, the present inventors have developed a highly viscous β by shaking culture or deep aeration culture.
-Found and proposed a method for producing glucan.

【0003】しかし、一般に通気量は装置自体の能力の
制約を受ける場合が多く、また過度の通気は培養液の飛
散、蒸発を招き好ましくない。特に本発明の如く、培養
物が高い粘性を有する場合には通気(バブリング)だけ
による攪拌では培養系の均一性が保たれず高効率の培養
は行えない。そこで、均一に攪拌する為に、攪拌翼を使
うことが考えられるが、攪拌翼の形態によっては回転に
伴う剪断力を生じ、菌糸に損傷を与えて菌の増殖にマイ
ナスに作用する。例えばマクロフォモプシス(Macr
ophomopsis)属に属する糸状菌の高粘性の培
養物のタービン型攪拌翼による攪拌では、高速回転させ
ると剪断力による菌糸の損傷から増殖率の低下を招く等
の問題が生じた。
However, in general, the amount of aeration is often restricted by the capacity of the device itself, and excessive aeration is not preferable because it causes scattering and evaporation of the culture solution. In particular, as in the present invention, when the culture has a high viscosity, the homogenization of the culture system cannot be maintained and the highly efficient culture cannot be performed by stirring only by aeration (bubbling). Therefore, it is conceivable to use a stirring blade to uniformly stir, but depending on the form of the stirring blade, a shearing force is generated due to the rotation, which damages the hyphae and negatively affects the growth of bacteria. For example, Macro Phomopsis (Macr
When stirring a highly viscous culture of a filamentous fungus belonging to the genus Ophomopsis) with a turbine-type stirring blade, there was a problem that high-speed rotation caused damage to the hyphae due to shearing force, resulting in a decrease in the growth rate.

【0004】本発明者らは、上記問題点に鑑み鋭意研究
を行った結果、パドル型攪拌翼を用いれば、菌糸を損傷
することなく均一に攪拌できるばかりか、菌体量当りの
β−グルカン生産量が大幅に増加することを見出し本発
明を完成したものであって、その目的とするところは、
効率の良いマクロフォモプシス属に属する糸状菌由来高
粘性培養物の製造方法を確立することにある。
The inventors of the present invention have conducted extensive studies in view of the above problems, and as a result, using a paddle type stirring blade not only can stir mycelia uniformly without damaging the mycelium, but also can produce β-glucan per bacterial cell amount. The present invention has been completed by finding that the production amount is significantly increased, and the purpose is to:
It is to establish an efficient method for producing a highly viscous culture derived from a filamentous fungus belonging to the genus Macrophomopsis.

【0005】[0005]

【課題を解決するための手段】本発明は、マクロフォモ
プシス属に属する糸状菌を液体培養して高粘性培養物を
取得するに際し、パドル型攪拌翼にて培養液を攪拌し、
好気的培養を行うことを特徴とする糸状菌由来高粘性培
養物の製造方法である。
Means for Solving the Problems The present invention, when a filamentous fungus belonging to the genus Macrophomopsis is liquid-cultured to obtain a highly viscous culture, the culture solution is stirred with a paddle type stirring blade,
A method for producing a highly viscous culture derived from a filamentous fungus, which comprises performing aerobic culture.

【0006】以下、本発明の構成の詳細について説明す
る。本発明に用いる微生物としては、例えば、微工研受
託9366号として寄託されたマクロフォモプシスKA
B55株と命名されたもの等があげられる。
The details of the configuration of the present invention will be described below. The microorganism used in the present invention is, for example, Macrophomopsis KA deposited as Micromachine Research Deposit No. 9366.
Examples include those named B55 strain.

【0007】本糸状菌の培養に用いられる炭素源として
は例えば、ブドウ糖、麦芽糖、デンプン、ショ糖、フラ
クトース、糖蜜、及びこれらの混合物等が挙げられる。
上記の糖類を用いた場合、培養物中にはβ−グルカンと
α−グルカンが同時に蓄積されるが、炭素源としてガラ
クトースを骨格として含む糖を用いれば、マクロフォモ
プシス属に属する微生物に、β−グルカンのみを選択的
に培養物中に産生、蓄積させることができ、これによっ
てβ−グルカンを更に容易、且つ安価に回収、利用する
ことができる為、より好ましい。
Examples of the carbon source used for culturing the filamentous fungus include glucose, maltose, starch, sucrose, fructose, molasses, and a mixture thereof.
When the above-mentioned saccharides are used, β-glucan and α-glucan are simultaneously accumulated in the culture, but if a saccharide containing galactose as a skeleton is used as a carbon source, a microorganism belonging to the genus Macrophomopsis has β -It is more preferable because only glucan can be selectively produced and accumulated in the culture, and β-glucan can be recovered and utilized more easily and inexpensively.

【0008】ガラクトースを骨格として含む糖として
は、例えばガラクトース、ラクトース、メリビオース、
ラフィノース、スタキオース等が挙げられるが、収率の
点ではラクトースが特に好ましい。
Examples of sugars containing galactose as a skeleton include galactose, lactose, melibiose,
Raffinose, stachyose and the like can be mentioned, but lactose is particularly preferable in terms of yield.

【0009】窒素源としては、概ね微生物の培養に用い
られる有機体、無機体の窒素源の全てが使用可能であ
り、例えば脱脂綿実粉(Pharmamedia)、コ
ーンスティープリカー、酵母エキス、乾燥酵母、各種ペ
プトン、オートミール肉エキス、カゼイン加水分解物、
アンモニウム塩、硝酸塩などが挙げられる。
As the nitrogen source, it is possible to use all organic and inorganic nitrogen sources generally used for culturing microorganisms, such as absorbent cotton seed flour (Pharmamedia), corn steep liquor, yeast extract, dry yeast, various Peptone, oatmeal meat extract, casein hydrolyzate,
Examples thereof include ammonium salts and nitrates.

【0010】その他添加物として塩化ナトリウム、マグ
ネシウム、カルシウム、りん酸等の無機塩が挙げられ
る。更に該培地には必要に応じて鉄、銅、マンガン等の
金属塩を微量配合してもよい。
Other additives include inorganic salts such as sodium chloride, magnesium, calcium and phosphoric acid. Further, a trace amount of metal salts such as iron, copper and manganese may be added to the medium, if necessary.

【0011】培養条件はpH3.5〜9.0が好まし
く、更に好ましくはpH5.0〜8.0、培養温度は1
0〜40℃が好ましく、更に好ましくは20〜35℃
で、通常3〜7日間で培養する。
The culture conditions are preferably pH 3.5 to 9.0, more preferably pH 5.0 to 8.0, and the culture temperature is 1.
0-40 degreeC is preferable, More preferably, it is 20-35 degreeC.
The culture is usually carried out for 3 to 7 days.

【0012】通気量としては0.5〜4vvmが好まし
く、更に好ましくは1〜3vvmである。0.5vvm
未満では、通気不足によりβ−グルカンの生産性が悪
く、4vvmを越えると、培養液の飛散、蒸発を招き易
く、あまり好ましくない。
The ventilation amount is preferably 0.5 to 4 vvm, more preferably 1 to 3 vvm. 0.5 vvm
If it is less than 4, the productivity of β-glucan is poor due to insufficient ventilation, and if it exceeds 4 vvm, the culture solution tends to be scattered and evaporated, which is not preferable.

【0013】本発明に関係するパドル型攪拌翼は、図
1,図2,図3等のような形態のいずれのものでもよ
く、その他一般に市販されているジャーファメンターに
付属のものでもよい。
The paddle type stirring blade related to the present invention may have any of the configurations shown in FIGS. 1, 2, 3 and the like, or may be attached to other commercially available jar-famenters.

【0014】攪拌条件は最初から一定条件で攪拌を行う
場合には10〜100rpmが好ましい。10rpm未
満では均一攪拌が不十分であり、100rpmを過える
とその剪断力によって菌糸に損傷を与える傾向がある。
また培養液の粘度が数100CPS以上に上昇するに連
れ、連続的にまたは段階的に攪拌条件を70〜250r
pmの範囲で徐々に上げても良い。
The stirring conditions are preferably 10 to 100 rpm when the stirring is carried out under constant conditions from the beginning. If it is less than 10 rpm, uniform stirring is insufficient, and if it exceeds 100 rpm, the shear force tends to damage the hyphae.
Also, as the viscosity of the culture solution rises to several 100 CPS or more, the stirring condition is continuously or stepwise adjusted to 70 to 250 r.
You may raise gradually in the range of pm.

【0015】このようにして本発明の目的物質である糸
状菌由来高粘性培養物が得られるが、これを以下のよう
にして精製することによって、β−グルカンを得ること
ができる。
Thus, a highly viscous culture derived from a filamentous fungus, which is the objective substance of the present invention, can be obtained, and β-glucan can be obtained by purifying it as follows.

【0016】この培養物を、濾過又は遠心分離などの適
当な方法で処理して該微生物菌体を除去する。次に、得
られるろ液または上清に、適当な沈澱剤、例えばエタノ
ール、メタノール、イソプロパノール、プロパノール、
アセトン等の有機沈澱剤を約10〜35重量%加え、β
−グルカンを沈澱させる。この沈澱物を濾過または遠心
分離等の適当な方法で分離しβ−グルカンを得る。更に
水に再溶解させた後、沈澱剤による沈澱を繰り返した
後、透析、凍結乾燥をすることにより、精製β−グルカ
ンを得ることができる。
The culture is treated with an appropriate method such as filtration or centrifugation to remove the microbial cells. Then, the obtained filtrate or supernatant is mixed with a suitable precipitating agent such as ethanol, methanol, isopropanol, propanol,
Add about 10 to 35% by weight of organic precipitant such as acetone,
-Precipitate the glucan. This precipitate is separated by an appropriate method such as filtration or centrifugation to obtain β-glucan. After re-dissolving in water, precipitation with a precipitant is repeated, followed by dialysis and freeze-drying to obtain purified β-glucan.

【0017】以下、実施例と比較例によって本発明を詳
細に説明する。 実施例1 マクロフォモプシス属に属する菌株KAB55(微工研
受諾9366号)を下記表1に示した組成の培地にて3
日間前培養し、これの150mlをパドル型攪拌翼(ミツ
ワバイオ社製、図1)を装着した同組成の培地3 lを入
れた5 l容ジャーファーメンター(ミツワバイオ社製、
形式:KMJ−5B−3U型)に植菌して25℃で4日
間培養を行った。通気量は1vvm、攪拌回転数は70
rpmで本培養を行った。
The present invention will be described in detail below with reference to examples and comparative examples. Example 1 A strain KAB55 belonging to the genus Macrophomopsis (Micromachine Lab. No. 9366) was used in a medium having the composition shown in Table 1 below.
After pre-culturing for 150 days, 150 ml of this was put in a 5 l jar fermenter (manufactured by Mitsuwa Bio Co., Ltd.) containing 3 l of the same composition medium equipped with a paddle type stirring blade (Mitsuwa Bio Co., Ltd., FIG. 1).
(Type: KMJ-5B-3U type) and cultured at 25 ° C. for 4 days. Aeration rate is 1 vvm, stirring speed is 70
Main culture was performed at rpm.

【0018】[0018]

【表1】 [Table 1]

【0019】得られた培養液中のβ−グルカンの定量は
下記条件でHPLCにより分析した。そして、培地中に
残存している糖についてはデジタル糖度計PR−1(ア
タゴ社製)を用いて調べた。また、菌体量は遠心分離し
て得た湿菌体を120℃,17時間乾燥して調べた。
The quantification of β-glucan in the obtained culture broth was analyzed by HPLC under the following conditions. Then, the sugar remaining in the medium was examined using a digital sugar content meter PR-1 (manufactured by Atago Co.). The amount of bacterial cells was examined by drying the wet bacterial cells obtained by centrifugation at 120 ° C. for 17 hours.

【0020】[0020]

【表2】 [Table 2]

【0021】比較例1 パドル型攪拌翼に代えて、タービン型攪拌翼(ミツワバ
イオ社製、図4,(A),(B))2枚を液面下10c
mと18cmの位置に装着して用いる他は、実施例1と
同様にして行った。
Comparative Example 1 In place of the paddle type stirring blade, two turbine type stirring blades (manufactured by Mitsuwa Bio Co., FIG. 4, (A), (B)) 10c below the liquid surface were used.
The same procedure as in Example 1 was carried out except that the device was mounted at the positions of m and 18 cm.

【0022】本培養2日目以降は攪拌翼の回転が培養液
全体に伝わらず、見掛け上、培養液の流動は停止してい
た。尚、β−グルカンの定量、残糖の定量及び菌体量に
ついては実施例1と同様の方法で調べた。
After the second day of main culture, the rotation of the stirring blade was not transmitted to the entire culture solution, and apparently the flow of the culture solution was stopped. The β-glucan was quantified, the residual sugar was quantified, and the bacterial cell amount was examined in the same manner as in Example 1.

【0023】比較例2 マクロフォモプシス属に属する菌株KAB55(微工研
受諾9366号)を実施例と同組成の培地にて3日間前
培養し、これの150mlをタービン型攪拌翼(ミツワバ
イオ社製、図4)を装着した同培地3 lを入れた5 l容
ジャーファーメンター(ミツワバイオ社製、形式:KM
J−5B−3U型)に植菌して25℃で4日間培養を行
った。通気量は1vvm、攪拌回転数は120rpmで
本培養を行った。
Comparative Example 2 A strain KAB55 belonging to the genus Macrophomopsis (Microtechnical Laboratory Acceptance No. 9366) was pre-cultured for 3 days in a medium having the same composition as in Example, and 150 ml of this was stirred with a turbine-type stirring blade (Mitsuwa Bio Co., Ltd.). 5 liter jar fermenter (manufactured by Mitsuwa Bio Co., type: KM) containing 3 liters of the same medium equipped with the product (Fig. 4).
J-5B-3U type) and cultured at 25 ° C. for 4 days. The main culture was performed at an aeration rate of 1 vvm and a stirring rotation speed of 120 rpm.

【0024】本培養3日目以降は攪拌翼の回転が培養液
全体に伝わらず、見掛け上、培養液の流動は停止してい
た。尚、β−グルカンの定量、残糖の定量及び菌体量に
ついては実施例1と同様の方法で調べた。
After the third day of main culture, the rotation of the stirring blade was not transmitted to the entire culture solution, and the flow of the culture solution was apparently stopped. The β-glucan was quantified, the residual sugar was quantified, and the bacterial cell amount was examined in the same manner as in Example 1.

【0025】対照例 マクロフォモプシス属に属する菌株KAB55(微工研
受諾9366号)を実施例と同組成の培地にて3日間前
培養し、これの150mlを同培地3 lを入れた5 l容ジ
ャーファーメンター(ミツオバイオ社製、形式:KMJ
−5B−3U型)に植菌して25℃で4日間培養を行っ
た。通気量は1vvmで本培養を行った。尚、β−グル
カンの定量、残糖の定量及び菌体量については実施例1
と同様の方法で調べた。
Control Example Strain KAB55 belonging to the genus Macrophomopsis (Microtechnical Laboratory Acceptance No. 9366) was pre-cultured for 3 days in a medium having the same composition as that of Example, and 150 ml of this was added to 3 l of the same medium in 5 l. Yong Jar Fermenter (Mitsuo Bio, Model: KMJ
-5B-3U type) and cultured at 25 ° C. for 4 days. The main culture was performed with an aeration rate of 1 vvm. The amount of β-glucan, the amount of residual sugar and the amount of cells were determined in Example 1.
It investigated by the method similar to.

【0026】[0026]

【表3】 [Table 3]

【0027】表3からわかる通り、パドル型攪拌翼を用
いた実施例1は、攪拌を行わない対照例と比べて、菌体
量当りのβ−グルカン生産量が約1.8倍であった。こ
れに対してタービン型攪拌翼を用いた場合(比較例1)
菌体量当りのβ−グルカン生産量は、攪拌しない対照例
とほとんど変わらず、回転数を上げると菌糸の損傷がお
こり(比較例2)かえって生産量が減ってしまった。
As can be seen from Table 3, in Example 1 using the paddle type stirring blade, the amount of β-glucan produced per bacterial cell amount was about 1.8 times that of the control example in which stirring was not performed. . On the other hand, when the turbine type stirring blade is used (Comparative Example 1)
The production amount of β-glucan per cell amount was almost the same as that of the control example without stirring, and when the rotation number was increased, the mycelium was damaged (Comparative Example 2), and the production amount was rather decreased.

【0028】[0028]

【発明の効果】上述の様に、本発明は、高粘性のβ−グ
ルカンを産生するマクロフォモプシス(Macroph
omopsis)属に属する糸状菌培養物の製造方法を
提供するものであり、パドル型攪拌翼を用いることによ
って菌糸に悪影響を与えず、培養系全体が高粘性状態で
も均一に保持され、菌数あたりの高粘性培養物の収量が
大幅に向上する等、効率的で経済的に製造することがで
きる。
INDUSTRIAL APPLICABILITY As described above, according to the present invention, macrophomopsis (Macrophophl) that produces highly viscous β-glucan is produced.
The present invention provides a method for producing a filamentous fungus culture belonging to the genus Omopsis), which does not adversely affect mycelia by using a paddle-type stirring blade, and evenly maintains the entire culture system even in a highly viscous state. The yield of the highly viscous culture can be greatly improved, and the production can be performed efficiently and economically.

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

【図1】実施例1で用いた、パドル型攪拌翼を示す図で
ある。
FIG. 1 is a view showing a paddle type stirring blade used in Example 1.

【図2】パドル型攪拌翼の形態例を示す図である。FIG. 2 is a diagram showing a form example of a paddle type stirring blade.

【図3】パドル型攪拌翼の形態例を示す図である。FIG. 3 is a view showing a form example of a paddle type stirring blade.

【図4】(A)は、比較例1,2で用いた、タービン型
攪拌翼を示す図であり、(B)は同攪拌翼を、a方向か
ら見た図である。
FIG. 4 (A) is a diagram showing a turbine-type stirring blade used in Comparative Examples 1 and 2, and FIG. 4 (B) is a diagram showing the stirring blade as viewed from the direction a.

フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C12R 1:645) Continuation of front page (51) Int.Cl. 5 Identification code Office reference number FI technical display area C12R 1: 645)

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 マクロフォモプシス(Macropho
mopsis)属に属する糸状菌を液体培養して高粘性
培養物を取得するに際し、パドル型攪拌翼にて培養物を
攪拌し、好気的培養を行うことを特徴とする高粘性培養
物の製造方法。
1. Macrophomopsis (Macropho)
When a filamentous fungus belonging to the genus Mopsis) is liquid-cultured to obtain a highly viscous culture, the culture is agitated by a paddle type stirring blade to perform aerobic culture, which is a production of a highly viscous culture. Method.
【請求項2】 高粘性培養物が高粘性β−グルカンを含
有するものであって該高粘性β−グルカンの結合様式
が、主鎖のD−グルコピラノシル残基は全てβ−1,3
結合であり、又主鎖のD−グルコピラノシル残基のC−
6の位置で分岐しており、かつ主鎖であるβ−1,3結
合のD−グルコピラノシル残基4個毎に1個の割合で、
側鎖であるD−グルコピラノシル残基がβ−1,6結合
していることを特徴とする請求項1記載の糸状菌由来高
粘性培養物の製造方法。
2. The highly viscous culture contains a highly viscous β-glucan, and the binding mode of the highly viscous β-glucan is such that all main chain D-glucopyranosyl residues are β-1,3.
C- of the main chain D-glucopyranosyl residue which is a bond
At a ratio of one for every four β-1,3-bonded D-glucopyranosyl residues that are branched at the position 6 and are the main chain,
The method for producing a highly viscous culture derived from a filamentous fungus according to claim 1, wherein a D-glucopyranosyl residue which is a side chain is bound to β-1,6.
JP20150291A 1991-07-15 1991-07-15 Production of high-viscosity cultured product derived from filamentous fungi Pending JPH0523193A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20150291A JPH0523193A (en) 1991-07-15 1991-07-15 Production of high-viscosity cultured product derived from filamentous fungi

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20150291A JPH0523193A (en) 1991-07-15 1991-07-15 Production of high-viscosity cultured product derived from filamentous fungi

Publications (1)

Publication Number Publication Date
JPH0523193A true JPH0523193A (en) 1993-02-02

Family

ID=16442120

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20150291A Pending JPH0523193A (en) 1991-07-15 1991-07-15 Production of high-viscosity cultured product derived from filamentous fungi

Country Status (1)

Country Link
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998050398A1 (en) * 1997-05-07 1998-11-12 Rutgers, The State University Of New Jersey Improved beta-glucan and methods of use
WO1999013052A1 (en) * 1997-09-11 1999-03-18 Shinko Pantec Co., Ltd. Agitation tank for storing yeast solution and method of production of fermented foodstuffs such as beer using the agitation tank
JP2006280290A (en) * 2005-03-31 2006-10-19 Sanei Gen Ffi Inc Gel-like composition
US7872084B2 (en) 2006-08-08 2011-01-18 Nitto Denko Corporation Support for solid-phase synthesis and process for producing the same

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998050398A1 (en) * 1997-05-07 1998-11-12 Rutgers, The State University Of New Jersey Improved beta-glucan and methods of use
WO1999013052A1 (en) * 1997-09-11 1999-03-18 Shinko Pantec Co., Ltd. Agitation tank for storing yeast solution and method of production of fermented foodstuffs such as beer using the agitation tank
JPH1175815A (en) * 1997-09-11 1999-03-23 Shinko Pantec Co Ltd Agitating tank for storing yeast liquid and production of fermented foods of beer or the like using the same tank
JP2006280290A (en) * 2005-03-31 2006-10-19 Sanei Gen Ffi Inc Gel-like composition
US7872084B2 (en) 2006-08-08 2011-01-18 Nitto Denko Corporation Support for solid-phase synthesis and process for producing the same

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