JPH074266B2 - Extraction method of polysaccharides - Google Patents

Extraction method of polysaccharides

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Publication number
JPH074266B2
JPH074266B2 JP28646190A JP28646190A JPH074266B2 JP H074266 B2 JPH074266 B2 JP H074266B2 JP 28646190 A JP28646190 A JP 28646190A JP 28646190 A JP28646190 A JP 28646190A JP H074266 B2 JPH074266 B2 JP H074266B2
Authority
JP
Japan
Prior art keywords
polysaccharide
added
polysaccharides
ethanol
molecular weight
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
JP28646190A
Other languages
Japanese (ja)
Other versions
JPH04158794A (en
Inventor
一栄 南迫
彰男 林
龍男 中谷
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.)
Mitsui Engineering and Shipbuilding Co Ltd
Original Assignee
Mitsui Engineering and Shipbuilding Co Ltd
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Priority to JP28646190A priority Critical patent/JPH074266B2/en
Publication of JPH04158794A publication Critical patent/JPH04158794A/en
Publication of JPH074266B2 publication Critical patent/JPH074266B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は多糖類の抽出方法に関し、さらに詳しくは強酸
または強アルカリを使用せずに微細藻体から多糖類を抽
出することができる多糖類の抽出方法に関する。
Description: TECHNICAL FIELD The present invention relates to a method for extracting a polysaccharide, and more specifically, a polysaccharide capable of extracting a polysaccharide from a microalgae without using a strong acid or a strong alkali. Regarding the extraction method of.

〔従来の技術〕[Conventional technology]

従来、微細藻体から多糖類を抽出する方法として、強酸
や強アルカリを使用する方法が知られている(特開昭58
−201993号公報)。しかしながら、この方法で回収され
る多糖類は、強酸や強アルカリで加水分解を受けて分子
の一部が低分子化するという問題があった。またアルカ
リ処理中には硫酸基等の官能基が脱離したり、アンヒド
ロ結合を形成するおそれがあった。
Conventionally, as a method for extracting a polysaccharide from a microalgae, a method using a strong acid or a strong alkali is known (JP-A-58).
-201993). However, there is a problem that the polysaccharide recovered by this method is hydrolyzed by a strong acid or a strong alkali to lower a part of the molecule. Further, during the alkali treatment, there is a risk that functional groups such as sulfate groups may be eliminated or that anhydro bonds may be formed.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

本発明の目的は、前記従来技術の問題を解決し、強酸や
強アルカリを使用せずに微細藻体から多糖類を抽出する
ことができる多糖類の抽出方法を提供することにある。
An object of the present invention is to solve the above-mentioned problems of the prior art and to provide a method for extracting a polysaccharide that can extract a polysaccharide from a microalgae without using a strong acid or a strong alkali.

〔課題を解決するための手段〕[Means for Solving the Problems]

本発明は、藻培養液中の湿藻体から多糖類を抽出するに
際し、上記湿藻体の細胞を破壊した後、タンパク質分解
酵素および/または脂肪酸エステル分解酵素により酵素
反応を行うことを特徴とする多糖類の抽出方法に関す
る。
The present invention is characterized in that, when a polysaccharide is extracted from a wet algal body in an algal culture solution, after destroying the cells of the wet algal body, an enzymatic reaction is carried out with a proteolytic enzyme and / or a fatty acid ester degrading enzyme. The present invention relates to a method for extracting a polysaccharide.

本発明に用いられる微細藻体には特に制限はないが、紅
藻類に属するポルフィリジウム・クルエンツム(Porphy
ridium cruentum海産性)、ポルフィルジウム・アイロ
ギニュウム(Porphyridium aerugineum淡水性)などが
多糖類を多く含むために好ましい。これらの微細藻体
は、通常、公知の方法で培養して用いられる。
The microalgae used in the present invention are not particularly limited, but Porphyridium kruentum (Porphy
ridium cruentum marine), Porphyridium aerugineum (freshwater) and the like are preferable because they contain a large amount of polysaccharides. These microalgae are usually used by culturing by a known method.

本発明に用いられるタンパク質分解酵素としては、例え
ば、中性または弱アルカリ性のエンド型またはエキソ型
プロテアーゼの混合酵素剤である、パパイン、プロテア
ーゼN「アマノ」(天野製薬社製商品名)などが挙げら
れる。
Examples of the proteolytic enzyme used in the present invention include papain, protease N “Amano” (trade name of Amano Pharmaceutical Co., Ltd.), which is a mixed enzyme agent of neutral or weakly alkaline endo-type or exo-type protease. To be

本発明に用いられる脂肪酸エステル分解酵素としては、
α位またはβ位の脂肪酸を分解するリパーゼ、パクレア
チンなどが挙げられる。
Examples of the fatty acid ester-degrading enzyme used in the present invention include
Examples thereof include lipases and pacreatins that decompose fatty acids at the α-position or β-position.

藻培養液から多糖類を抽出するには、例えば次のように
して行うことができる。
The polysaccharide can be extracted from the algae culture solution, for example, as follows.

まず、藻培養液を遠心分離、濾過等の固液分離操作によ
り上清と湿藻体に分ける。
First, the alga culture solution is separated into a supernatant and a wet algal body by solid-liquid separation operations such as centrifugation and filtration.

得られた湿藻体を密閉容器に入れて5〜7倍容の水を加
えた後、加熱および/またはホモジナイザー、ボールミ
ル等により細胞破壊を行う。細胞破壊の方法は藻体の状
態によって適宜選択されるが、細胞内の色素タンパクを
変性し、後述する酵素反応を容易にするためには加熱す
るのが好ましい。しかし、高温で長時間細胞破壊を行う
と細胞内の多糖類が分解されて低分子化するおそれがあ
るため、70〜120℃の温度で10分〜60分間程度で行うこ
とが好ましく、より好ましくは120℃で10分ないしは70
℃で30分加熱を行う。加熱の前後にホモジナイザー、ボ
ールミル等で充分破壊するのがさらに好ましい。
The obtained wet algal cells are placed in a closed container, 5 to 7 volumes of water are added, and then cells are heated and / or disrupted by a homogenizer, a ball mill or the like. The method of cell disruption is appropriately selected depending on the state of the algal cells, but heating is preferable in order to denature the intracellular pigment protein and facilitate the enzymatic reaction described later. However, when the cells are destroyed at a high temperature for a long time, the intracellular polysaccharides may be decomposed to lower the molecular weight, so it is preferable to perform the treatment at 70 to 120 ° C. for about 10 to 60 minutes, and more preferably At 120 ° C for 10 minutes or 70
Heat at ℃ for 30 minutes. Before and after heating, it is more preferable to sufficiently destroy with a homogenizer, a ball mill or the like.

次に破壊された細胞にタンパク質分解酵素および/また
は脂肪酸エステル分解酵素を添加して酵素反応を行う。
タンパク質分解酵素と脂肪酸エステル分解酵素は単独で
用いても、併用して用いてもよい。併用する場合には別
々に添加しても同時に添加してもよい。湿藻体100mlに
対する添加量は、タンパク質分解酵素では通常10,000〜
50,000U(ユニット)であり、脂肪酸エステル分解酵素
では通常7,500〜30,000Uである。酵素反応は、通常30〜
80℃、より好ましくは40〜60℃の温度で、撹拌または振
とうを行いながら30分〜24時間程度行う。
Next, a proteolytic enzyme and / or a fatty acid ester degrading enzyme is added to the destroyed cells to carry out an enzymatic reaction.
The proteolytic enzyme and the fatty acid ester degrading enzyme may be used alone or in combination. When used in combination, they may be added separately or simultaneously. The amount added to 100 ml of wet algal cells is usually 10,000-
It is 50,000 U (unit), and it is usually 7,500 to 30,000 U for fatty acid ester degrading enzyme. Enzyme reaction is usually 30 ~
It is carried out at a temperature of 80 ° C., more preferably 40 to 60 ° C., with stirring or shaking for about 30 minutes to 24 hours.

酵素反応終了後、水混和性有機溶媒を反応物の2〜3倍
容になるまで加え、多糖類を浮遊物として析出させる。
水混和性有機溶媒としては、エタノール、イソプロパノ
ール等のアルコールなどが用いられる。浮遊物の回収は
濾過等の手段により行う。浮遊物を回収した後、必要に
応じて水への再溶解工程および水混和性有機溶媒による
浮遊物の回収工程を数回繰り返し、多糖類の精製を行
う。さらに必要に応じて透析等による脱塩を行った後、
乾燥する。乾燥は、通常の真空乾燥、スプレー乾燥、凍
結乾燥等の方法により行う。
After the completion of the enzymatic reaction, a water-miscible organic solvent is added until the volume becomes 2 to 3 times that of the reaction mixture, and the polysaccharide is precipitated as a suspension.
As the water-miscible organic solvent, alcohols such as ethanol and isopropanol are used. The suspended matter is collected by means such as filtration. After recovering the suspended matter, the process of redissolving in water and the step of recovering the suspended matter using a water-miscible organic solvent are repeated several times to purify the polysaccharide. After desalting by dialysis, etc., if necessary,
dry. Drying is performed by a usual method such as vacuum drying, spray drying or freeze drying.

本発明の方法により得られる多糖類は、強酸および強ア
ルカリを使用しないため、多糖の分子が壊されることが
なく、高分子量の多糖を多く含む。この高分子量の多糖
を多く含む多糖類は、流体摩擦の抵抗低減効果に優れ、
種々の流体摩擦低減剤として有用である。
The polysaccharide obtained by the method of the present invention does not use a strong acid and a strong alkali, so that the molecule of the polysaccharide is not broken and contains a large amount of high molecular weight polysaccharide. Polysaccharides containing a large amount of high molecular weight polysaccharides are excellent in reducing the resistance to fluid friction,
It is useful as various fluid friction modifiers.

〔実施例〕〔Example〕

以下、本発明を実施例により詳しく説明する。 Hereinafter, the present invention will be described in detail with reference to Examples.

実施例1 微小藻体(ポリフィリジウム・クルエンツム)を、培地
としてASWを使用し、光源としてハロゲンランプを使用
して5〜10klxの光を照射し、25℃において、約2週
間、CO25%を含む空気を通気しながら培養を行い、藻培
養液を得た。
Example 1 A microalgae (Polyphyridium kruentum) was irradiated with 5 to 10 klx of light using ASW as a medium and a halogen lamp as a light source, and CO 2 5 at 25 ° C. for about 2 weeks. Culturing was carried out while aerating air containing 10% to obtain an alga culture solution.

得られた藻培養液を遠心分離にかけ、上清と湿藻体に分
離した。湿藻体(固形分13重量%)1kgに対し、蒸留水
5を加えて10,000rpmで5分間ホモジナイズした。次
にこれを80℃で10分間加熱した後、40℃に冷却し、タン
パク質分解酵素であるパパイン(天野製薬社製)を13g
加え、50℃で24時間酵素反応を行った。反応終了後、エ
タノールを等量加え、浮遊する多糖類をナイロンメッシ
ュで濾過し、水およびエタノールを除去した。得られた
多糖類を再び蒸留水5に溶解させ、パパインを13g加
え、50℃で24時間酵素反応を充分に行った。その後、エ
タノールを等量加えて浮遊する多糖類を回収した。この
多糖類をエタノールで充分洗浄し、真空乾燥法で乾燥し
た。
The obtained alga culture solution was centrifuged to separate into a supernatant and a wet algal body. Distilled water 5 was added to 1 kg of wet alga body (solid content 13% by weight), and the mixture was homogenized at 10,000 rpm for 5 minutes. Next, this is heated at 80 ° C for 10 minutes, then cooled to 40 ° C, and 13 g of papain (manufactured by Amano Pharmaceutical Co., Ltd.), which is a protease,
In addition, the enzyme reaction was carried out at 50 ° C for 24 hours. After the reaction was completed, ethanol was added in an equal amount, and the floating polysaccharide was filtered with a nylon mesh to remove water and ethanol. The obtained polysaccharide was again dissolved in distilled water 5, 13 g of papain was added, and the enzyme reaction was sufficiently carried out at 50 ° C. for 24 hours. Then, ethanol was added in an equal amount to collect the floating polysaccharides. The polysaccharide was thoroughly washed with ethanol and dried by a vacuum drying method.

得られた多糖類の分子量分布を、GPC(gel permeation
chromatohraphy)を用いて測定し、結果を第1図に示し
た。
The molecular weight distribution of the obtained polysaccharide was analyzed by GPC (gel permeation
chromatohraphy) and the results are shown in FIG.

比較例1 藻体を含む培養液にNaOHを加えてpH10〜12に調整し、10
0℃で1〜2時間加熱した。これを室温まで冷却した
後、HClを加えてpH2〜4に調整し、エタノールを2〜3
倍容加え、浮遊した多糖を回収した。回収した多糖を2M
のCaCl2を含む蒸留水に溶解させた。その後、90℃で多
糖が完全に溶解するまで撹拌し、溶解したら、35℃まで
冷却し、これにさらにエタノールを2〜3倍容加えて多
糖類を回収し、40℃で真空乾燥させた。
Comparative Example 1 pH was adjusted to 10 to 12 by adding NaOH to a culture solution containing algal cells,
Heat at 0 ° C. for 1-2 hours. After cooling it to room temperature, add HCl to adjust the pH to 2-4 and add ethanol to 2-3.
Double the volume was added and the floating polysaccharides were collected. 2M of recovered polysaccharide
Was dissolved in distilled water containing CaCl 2 . Then, the mixture was stirred at 90 ° C. until the polysaccharide was completely dissolved, and when it was dissolved, it was cooled to 35 ° C., and ethanol was added to this in an amount of 2 to 3 times to recover the polysaccharide, and vacuum dried at 40 ° C.

得られた多糖類の分子量分布を実施例1と同様にして測
定し、その結果を第3図に示した。
The molecular weight distribution of the obtained polysaccharide was measured in the same manner as in Example 1, and the results are shown in FIG.

第1図と第3図の比較から、本発明の方法で得られた多
糖類は、酸・アルカリ処理による場合よりも、高分子量
の多糖を多く含むことがわかった。
From the comparison between FIG. 1 and FIG. 3, it was found that the polysaccharide obtained by the method of the present invention contained a larger amount of high molecular weight polysaccharide than that obtained by the acid / alkali treatment.

実施例2 実施例1で用いた藻培養液を遠心分離にかけて上清と湿
藻体に分離した。得られた湿藻体1kgに対して蒸留水3
を加え、100℃で30分間加熱した。加熱後、蒸留水を
3加え、さらにプロテアーゼN「アマノ」(天野製薬
社製商品名)25gを加えて40℃で24時間酵素反応を行っ
た。反応後、エタノール7を加えて浮遊する多糖類を
濾過により回収した。この多糖類を再び蒸留水に溶解
し、プロテアーゼN「アマノ」を25gを加えて24時間酵
素反応を充分に行った。その後、エタノールを加えて多
糖類を浮遊させ、濾過により回収した。この多糖類を蒸
留水に再溶解し、水に対して4℃において48時間透析を
行い、その後凍結乾燥させた。
Example 2 The alga culture solution used in Example 1 was centrifuged to separate into a supernatant and a wet algal cell. 3 kg of distilled water for 1 kg of the obtained wet alga
Was added and heated at 100 ° C. for 30 minutes. After heating, 3 g of distilled water was added, 25 g of Protease N “Amano” (trade name of Amano Pharmaceutical Co., Ltd.) was further added, and the enzyme reaction was carried out at 40 ° C. for 24 hours. After the reaction, ethanol 7 was added and the floating polysaccharides were collected by filtration. This polysaccharide was dissolved again in distilled water, 25 g of protease N "Amano" was added, and the enzyme reaction was sufficiently carried out for 24 hours. Then, ethanol was added to suspend the polysaccharide, and the polysaccharide was collected by filtration. This polysaccharide was redissolved in distilled water, dialyzed against water at 4 ° C. for 48 hours and then freeze-dried.

得られた多糖類の分子量分布を実施例1と同様にして測
定したが、本発明の方法で得られた多糖類は、比較例1
と比較して高分子量の多糖を多く含むことがわかった。
The molecular weight distribution of the obtained polysaccharide was measured in the same manner as in Example 1, but the polysaccharide obtained by the method of the present invention was compared to Comparative Example 1.
It was found that it contained a large amount of high-molecular-weight polysaccharides as compared with.

実施例3 実施例1で用いた藻培養液を遠心分離にかけて上清と湿
藻体に分離した。湿藻体1kgに対し、蒸留水5を加え
て10,000rpmで5分間ホモジナイズし、その後、80℃で1
0分間加熱した。これを20℃に冷却した後、リパーゼ
(天野製薬社製)を35g加え、30℃で24時間反応させ
た。反応終了後、エタノールを等量加えて浮遊する多糖
類をナイロンメッシュで濾過し、水およびエタノールを
除去した。得られた多糖類を再び水5に充分溶解させ
た後、パパイン13gを加え、50℃で24時間酵素反応を充
分に行い、エタノールを等量加えて浮遊する多糖類を回
収した。これをエタノールで充分に洗浄し、室温で真空
乾燥した。
Example 3 The alga culture solution used in Example 1 was centrifuged to separate it into a supernatant and wet algal cells. Distilled water 5 was added to 1 kg of wet alga and homogenized at 10,000 rpm for 5 minutes, and then 1 hour at 80 ° C.
Heated for 0 minutes. After cooling this to 20 ° C., 35 g of lipase (manufactured by Amano Pharmaceutical Co., Ltd.) was added and reacted at 30 ° C. for 24 hours. After completion of the reaction, an equal amount of ethanol was added and the floating polysaccharide was filtered through a nylon mesh to remove water and ethanol. The obtained polysaccharide was sufficiently dissolved again in water 5, 13 g of papain was added, the enzyme reaction was sufficiently carried out at 50 ° C. for 24 hours, and ethanol was added in an equal amount to collect the floating polysaccharide. This was thoroughly washed with ethanol and vacuum dried at room temperature.

得られた多糖類の分子量分布を実施例1と同様に測定
し、結果を第2図に示したが、本発明の方法で得られた
多糖類は、比較例1と比較して高分子量の多糖を多く含
むことがわかった。
The molecular weight distribution of the obtained polysaccharide was measured in the same manner as in Example 1, and the result is shown in FIG. 2. The polysaccharide obtained by the method of the present invention has a higher molecular weight than that of Comparative Example 1. It was found to contain a large amount of polysaccharides.

実施例4 実施例1で用いた藻培養液を遠心分離にかけて上清と湿
藻体に分離した。湿藻体1kgに対し、蒸留水2を加
え、80℃で20分間加熱を行った。その後、7000rpmで5
分間ホモジナイズし、蒸留水2を加えて撹拌した。30
℃に冷却させた後、パンクレアチン(天野製薬社製)50
gを加えて40℃で24時間反応を行った。反応終了後、等
量のエタノールを加えて浮遊する多糖類をナイロンメッ
シュで濾過し、水とエタノールを除去した。回収した多
糖類にさらに蒸留水5を加えて溶解し、パンクレアチ
ン50gを加え、40℃24時間反応を行った。再びエタノー
ルを等量加えて多糖類を回収し、水に対して透析を4℃
で48時間行った後、凍結乾燥した。
Example 4 The alga culture solution used in Example 1 was centrifuged to separate into a supernatant and wet algal cells. Distilled water 2 was added to 1 kg of wet alga and heated at 80 ° C. for 20 minutes. After that, 5 at 7000 rpm
Homogenize for 1 minute, add distilled water 2 and stir. 30
After cooling to ℃, pancreatin (Amano Pharmaceutical Co., Ltd.) 50
g was added and the reaction was carried out at 40 ° C. for 24 hours. After the reaction was completed, an equal amount of ethanol was added and the floating polysaccharides were filtered through a nylon mesh to remove water and ethanol. Distilled water 5 was further added to the recovered polysaccharide to dissolve it, 50 g of pancreatin was added, and the reaction was carried out at 40 ° C. for 24 hours. Equal amount of ethanol is added again to recover the polysaccharide, and dialyzed against water at 4 ° C.
After 48 hours, it was freeze-dried.

得られた多糖類を実施例1と同様にして分子量分布を測
定したが、本発明の方法で得られた多糖類は、比較例1
と比較して高分子量の多糖を多く含むことがわかった。
The obtained polysaccharide was measured for molecular weight distribution in the same manner as in Example 1, but the polysaccharide obtained by the method of the present invention was compared with Comparative Example 1.
It was found that it contained a large amount of high-molecular-weight polysaccharides as compared with.

〔発明の効果〕〔The invention's effect〕

本発明の抽出方法によれば、強酸や強アルカリを使用し
ないため、多糖類の分子を損なうことなく、高分子量の
多糖を多く含む多糖類を回収することができる。この高
分子量の多糖を多く含む多糖類は流体摩擦低減効果に優
れるため、種々の流体摩擦低減剤として有用である。
According to the extraction method of the present invention, since a strong acid or a strong alkali is not used, it is possible to recover a polysaccharide containing a large amount of high molecular weight polysaccharide without damaging the molecule of the polysaccharide. This polysaccharide containing a large amount of high molecular weight polysaccharides is excellent in the effect of reducing fluid friction and is therefore useful as various fluid friction reducing agents.

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

第1図は、プロテアーゼで酵素処理して得られた多糖類
の分子量分布曲線、第2図は、リパーゼとプロテアーゼ
で酵素処理して得られた多糖類の分子量分布曲線、第3
図は、酸およびアルカリ処理して得られた多糖類の分子
量分布曲線である。
FIG. 1 is a molecular weight distribution curve of a polysaccharide obtained by enzymatic treatment with protease, and FIG. 2 is a molecular weight distribution curve of a polysaccharide obtained by enzymatic treatment with lipase and protease.
The figure is a molecular weight distribution curve of a polysaccharide obtained by acid and alkali treatment.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】藻培養液中の湿藻体から多糖類を抽出する
に際し、上記湿藻体の細胞を破壊した後、タンパク質分
解酵素および/または脂肪酸エステル分解酵素により酵
素反応を行うことを特徴とする多糖類の抽出方法。
1. When extracting a polysaccharide from a wet alga body in an alga culture solution, after destroying the cells of the wet alga body, an enzymatic reaction is carried out with a protein degrading enzyme and / or a fatty acid ester degrading enzyme. Extraction method of polysaccharides.
JP28646190A 1990-10-24 1990-10-24 Extraction method of polysaccharides Expired - Lifetime JPH074266B2 (en)

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JPH04158794A JPH04158794A (en) 1992-06-01
JPH074266B2 true JPH074266B2 (en) 1995-01-25

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104938762A (en) * 2015-02-12 2015-09-30 南昌大学 Preparation method of duckweed protein powder for fermentation

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100810135B1 (en) * 2006-09-08 2008-03-06 (주)완도해조생약마을 Method for preparing enzyme hydrolyzed solution of layer or sea lettuce

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104938762A (en) * 2015-02-12 2015-09-30 南昌大学 Preparation method of duckweed protein powder for fermentation

Also Published As

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