JP2758796B2 - Polysaccharide extraction method - Google Patents

Polysaccharide extraction method

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Publication number
JP2758796B2
JP2758796B2 JP30394792A JP30394792A JP2758796B2 JP 2758796 B2 JP2758796 B2 JP 2758796B2 JP 30394792 A JP30394792 A JP 30394792A JP 30394792 A JP30394792 A JP 30394792A JP 2758796 B2 JP2758796 B2 JP 2758796B2
Authority
JP
Japan
Prior art keywords
polysaccharide
cells
added
present
water
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
JP30394792A
Other languages
Japanese (ja)
Other versions
JPH06141877A (en
Inventor
一栄 南迫
恵 小野
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 Zosen KK
Original Assignee
Mitsui Zosen KK
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 Mitsui Zosen KK filed Critical Mitsui Zosen KK
Priority to JP30394792A priority Critical patent/JP2758796B2/en
Publication of JPH06141877A publication Critical patent/JPH06141877A/en
Application granted granted Critical
Publication of JP2758796B2 publication Critical patent/JP2758796B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は多糖類の抽出方法に関
し、さらに詳しくは微細藻体の細胞に含有する色素を効
率よく除去して淡色の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。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a polysaccharide extraction method, and more particularly, to a polysaccharide extraction method capable of efficiently removing pigments contained in cells of microalgae to extract a light-colored polysaccharide. About.

【0002】[0002]

【従来の技術】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
いるが(特開昭58−201993号公報)、多糖類が
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。本出願人は、上記問題を
解決する方法として、特開平4−158794号公報お
よび特開平4−222593号公報において、藻培養液
から分離した湿藻体の細胞を破壊した後にタンパク質分
解酵素および/または脂肪酸エスエル分解酵素により酵
素反応を行う多糖類の抽出方法を提案した。この方法に
よれば、強酸や強アルカリを使用しないため多糖類の低
分子化を防止することができるが、多糖類の回収に多量
のアルコールを必要とするためコスト低下が図れず、ま
た湿藻体に含有する色素を除去することができないため
淡色の多糖類が得られないという欠点があった。
2. Description of the Related Art Conventionally, as a method for extracting polysaccharides from microalgae, a method using a strong acid or a strong alkali has been known (Japanese Patent Application Laid-Open No. 58-201993). There was a problem that some of the molecules were reduced in molecular weight due to hydrolysis with alkali. As a method for solving the above-mentioned problem, the present applicant has disclosed in Japanese Patent Application Laid-Open Nos. 4-158794 and 4-222593 that a cell of a wet alga body separated from an algal culture solution is destroyed and then a protease and / or Alternatively, a method for extracting polysaccharides by performing an enzymatic reaction with fatty acid esterase was proposed. According to this method, a low molecular weight of the polysaccharide can be prevented because a strong acid or a strong alkali is not used. However, since a large amount of alcohol is required to recover the polysaccharide, the cost cannot be reduced, and the wet alga cannot be reduced. There was a drawback that light-colored polysaccharides could not be obtained because pigments contained in the body could not be removed.

【0003】[0003]

【発明が解決しようとする課題】本発明の目的は、前記
従来技術の問題を解決し、淡色の多糖類を低コストで抽
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。
SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned problems of the prior art and to provide a polysaccharide extraction method capable of extracting a light-colored polysaccharide at low cost.

【0004】[0004]

【課題を解決するための手段】本発明は、藻培養液から
分離した湿藻体の細胞を破壊した後、酵素反応を行って
多糖類を抽出する方法において、前記湿藻体に水混和性
有機溶媒を加えて細胞破壊し、細胞内の脂溶性成分を除
去した後、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。
SUMMARY OF THE INVENTION The present invention provides a method for extracting polysaccharides by enzymatic reaction after destroying cells of a wet algal body separated from an algal culture solution. The present invention relates to a method for extracting a polysaccharide, which comprises subjecting cells to destruction by adding an organic solvent, removing fat-soluble components in the cells, and then performing an enzymatic reaction.

【0005】[0005]

【作用】微細藻体細胞中の色素群と多糖類は独立して存
在し、色素群は光合成組織内に、多糖類はデンプン粒ま
たは細胞外に存在する。藻体細胞を水系溶液中で破壊す
ると、多糖類が分子を広げた状態で存在し、この多糖類
に色素がからんだり、多糖類と色素の間に何らかの結合
を生じるため、その後の処理において色素を分離するこ
とは困難である。微細藻体の色素にはクロロフィルなど
の脂溶性色素とフィコエリスリンなどの水溶性色素があ
るが、本発明においては、細胞破壊を水系溶媒ではな
く、水混和性溶媒中で行って多糖類を水混和性溶媒に凝
縮させる一方、細胞内の脂溶性色素を該溶媒に溶解させ
て除去することができるため、その後の処理での多糖類
への色素の沈着を防ぐことができる。
The pigment group and the polysaccharide in the microalgal cells are present independently, the pigment group is present in the photosynthetic tissue, and the polysaccharide is present in the starch granules or extracellularly. When algal cells are destroyed in an aqueous solution, the polysaccharide exists in a state where the molecules are spread, and the pigment is entangled in this polysaccharide and some kind of bond is generated between the polysaccharide and the pigment, so that in the subsequent processing, It is difficult to separate the dye. Microalgae pigments include fat-soluble pigments such as chlorophyll and water-soluble pigments such as phycoerythrin.In the present invention, cell destruction is performed not in an aqueous solvent but in a water-miscible solvent to remove polysaccharides. While condensed in a water-miscible solvent, the intracellular fat-soluble dye can be dissolved in the solvent and removed, thereby preventing the deposition of the dye on the polysaccharide in the subsequent treatment.

【0006】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(Porphyridium cruentum 、海産性)、ポルフィリ
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んでいるために好ま
しい。これらの微細藻体は、公知の方法で培養して用い
られる。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。
[0006] The microalgae used in the present invention are not particularly limited.
, Fresh water) are preferable because they contain a large amount of polysaccharides. These microalgae are used after being cultured by a known method. Extraction of the polysaccharide from the algal culture is performed, for example, as follows.

【0007】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。得られた湿藻体
に水混和性溶媒を加えてホモジナイザー、ボールミル等
により細胞破壊を行う。細胞破壊の方法は湿藻体の状態
によって適宜選択する。水混和性溶剤としては、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。得られた細胞破壊液を遠心分離や濾過などの固液分
離操作により多糖類を含む沈澱物と上清とに分け、沈澱
物に水を加えて沈澱物が充分に溶解するまで25℃〜1
00℃の温度で攪拌する。この水溶液に酵素を加えて酵
素反応を行う。
First, an algal culture is separated into a supernatant and a wet algal body by a solid-liquid separation operation such as centrifugation or filtration. A water-miscible solvent is added to the obtained wet algal cells, and cell destruction is performed using a homogenizer, a ball mill, or the like. The method of cell destruction is appropriately selected depending on the state of the wet algal body. As the water-miscible solvent, alcohols such as ethanol and isopropanol are used. The obtained cell disruption solution is separated into a precipitate containing a polysaccharide and a supernatant by a solid-liquid separation operation such as centrifugation or filtration, and water is added to the precipitate.
Stir at a temperature of 00 ° C. An enzyme is added to this aqueous solution to perform an enzyme reaction.

【0008】酵素反応に用いられる酵素としては、タン
パク質分解酵素や脂肪酸エステル分解酵素などが挙げら
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、各種プロテアーゼなどが
用いられ、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、例えばパクレアチ
ンなどが用いられる。これらの酵素は単独で用いても併
用してもよい。酵素の添加量は、湿藻体100gに対し
てタンパク質分解酵素では通常10,000〜500,
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℃、好ましくは40〜60℃の温度
で、攪拌または振とうを行いながら30分〜24時間程
度行う。反応終了後、1/2〜2倍容量の水混和性溶媒
を加えて浮遊物を析出させ、これを濾過などにより回収
し、充分に溶媒を除いてから乾燥、粉砕して精製多糖を
得る。
[0008] Enzymes used in the enzymatic reaction include proteolytic enzymes and fatty acid ester degrading enzymes. Examples of the protease include papain and various proteases, which are mixed enzyme agents of neutral or weakly alkaline endo- or exo-type proteases, and fatty acid esterases include α- or β-position fatty acids. A lipase that degrades, for example, pacreatin, is used. These enzymes may be used alone or in combination. The amount of the enzyme added is usually 10,000 to 500,
000 U (unit), and usually 7,500 to 30,000 U for fatty acid ester degrading enzyme. The enzymatic reaction is usually performed at a temperature of 30 to 80 ° C., preferably 40 to 60 ° C. for about 30 minutes to 24 hours while stirring or shaking. After completion of the reaction, 1/2 to 2 volumes of a water-miscible solvent is added to precipitate a suspended matter, which is collected by filtration or the like, and after sufficiently removing the solvent, dried and pulverized to obtain a purified polysaccharide.

【0009】本発明の方法によれば、脂溶性色素や脂質
などを水混和性溶媒に溶解させて除去することができる
ため、淡色の多糖類を抽出することができ、また脱色の
ための洗浄等も容易であるため使用する溶剤量を減らす
ことができる。この多糖類は、粘性が高く、流体摩擦抵
抗低減効果を有するほか、増粘剤、分散懸濁安定剤、乳
化剤などに用いることができる。
According to the method of the present invention, since fat-soluble dyes and lipids can be removed by dissolving them in a water-miscible solvent, a light-colored polysaccharide can be extracted, and washing for decolorization can be performed. And the like are easy, so that the amount of solvent used can be reduced. This polysaccharide has a high viscosity, has an effect of reducing fluid frictional resistance, and can be used as a thickener, a dispersion suspension stabilizer, an emulsifier, and the like.

【0010】[0010]

【実施例】以下、本発明を実施例により説明する。 実施例1 微細藻体(ポリフィリジウム・クルエンツム)を培地と
して人工海水培地を使用し、光源としてハロゲンランプ
を使用して5〜10Klxの光照射して培養を行い、藻
培養液を得た。この藻培養液を遠心分離により上清と湿
藻体とに分離し、湿藻体(固形分13重量%)150g
に対して600mlのエタノールを加え、10,000
rpmで2分間ホモジナイズした。その後、吸引濾過に
より固液分離し、沈澱物に100mlエタノールを加え
て10,000rpmで2分間ホモジナイズした。再び
吸引濾過により固液分離し、沈澱物を回収した。この沈
澱物をエタノールで2〜5回洗浄した。エタノール不溶
画分に蒸留水を加えて2重量%溶液とし、充分溶解する
まで90℃で加熱攪拌した。この水溶液に蒸留水を加え
て冷却して1重量%とし、タンパク質分解酵素(プロテ
アーゼA、天野製薬社製)7.5gを加えて50℃で1
晩攪拌して酵素反応を行った。反応終了後、エタノール
を2/3容量加えて多糖類浮遊物を析出させて回収し、
エタノールで洗浄し、充分に溶媒を除去してから40℃
で真空乾燥した。得られた多糖類を粉砕して製品とし
た。この製品の色は淡紅白色であった。また全アルコー
ル使用量は7,200mlであった。
The present invention will be described below with reference to examples. Example 1 An artificial seawater medium was used as a culture medium of microalgae (Polyphyllium kruentum), and culturing was performed by irradiating light of 5 to 10 Klx using a halogen lamp as a light source to obtain an algal culture solution. This algal culture solution was separated into a supernatant and a wet algal body by centrifugation, and 150 g of the wet algal body (solid content 13% by weight)
And add 600 ml of ethanol to the
Homogenized at rpm for 2 minutes. Thereafter, solid-liquid separation was performed by suction filtration, and 100 ml of ethanol was added to the precipitate, followed by homogenization at 10,000 rpm for 2 minutes. The solid was separated again by suction filtration, and the precipitate was recovered. The precipitate was washed with ethanol 2 to 5 times. Distilled water was added to the ethanol-insoluble fraction to make a 2% by weight solution, and the mixture was heated and stirred at 90 ° C. until it was sufficiently dissolved. Distilled water was added to this aqueous solution to cool it to 1% by weight, and 7.5 g of a protease (Protease A, manufactured by Amano Pharmaceutical Co., Ltd.) was added.
The mixture was stirred overnight to perform an enzyme reaction. After completion of the reaction, 2/3 volume of ethanol was added to precipitate and recover the polysaccharide suspension,
After washing with ethanol and removing the solvent sufficiently, 40 ° C
And vacuum dried. The obtained polysaccharide was pulverized into a product. The color of this product was light red and white. The total alcohol consumption was 7,200 ml.

【0011】比較例1 実施例1と同様の操作により得た湿藻体150g(固形
分13重量%)に蒸留水300mlを加えて10,00
0rpmで1分間ホモジナイズした後、80℃で20分
間加熱した。その後室温まで冷却してpH8に調整し、
たんぱく質分解酵素(プロテアーゼA)を7.5g投入
し、50℃で1晩攪拌して酵素反応を行った。反応終了
後、エタノールを等量加えて多糖類を浮遊させて回収
し、多糖類をエタノールで洗浄して充分脱色し、その
後、溶媒を充分除去してから40℃で真空乾燥し、粉砕
して製品とした。得られた製品の色は緑褐色であった。
また全アルコール使用量は10,000mlであった。
Comparative Example 1 To 150 g (13% by weight solids) of wet algal cells obtained by the same operation as in Example 1, 300 ml of distilled water was added, and
After homogenizing at 0 rpm for 1 minute, the mixture was heated at 80 ° C. for 20 minutes. Then cool to room temperature and adjust to pH 8,
7.5 g of proteolytic enzyme (protease A) was charged, and the mixture was stirred at 50 ° C. overnight to perform an enzymatic reaction. After the completion of the reaction, an equal amount of ethanol is added to recover the polysaccharide by floating, and the polysaccharide is washed with ethanol to sufficiently decolorize. Thereafter, the solvent is sufficiently removed, followed by vacuum drying at 40 ° C. and pulverization. The product. The color of the obtained product was greenish brown.
The total amount of alcohol used was 10,000 ml.

【0012】[0012]

【発明の効果】本発明の方法によれば、クロロフィル等
の脂溶性色素をあらかじめ除去することができるため、
抽出多糖類の色素による着色を防ぎ、商品価値の高い多
糖類を得ることができるとともに、洗浄等に使用する溶
媒の量が少なくてすむためコスト低減を図ることができ
る。
According to the method of the present invention, fat-soluble dyes such as chlorophyll can be removed in advance.
Coloring of the extracted polysaccharide by the pigment can be prevented, a polysaccharide having high commercial value can be obtained, and the amount of the solvent used for washing or the like can be reduced, so that the cost can be reduced.

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) C12P 19/04 CA(STN)──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 6 , DB name) C12P 19/04 CA (STN)

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 藻培養液から分離した湿藻体の細胞を破
壊した後、酵素反応を行って多糖類を抽出する方法にお
いて、前記湿藻体に水混和性有機溶媒を加えて細胞破壊
し、細胞内の脂溶性成分を除去した後、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。
1. A method for extracting polysaccharides by destroying cells of a wet alga body separated from an algal culture solution and then performing an enzymatic reaction, wherein the cells are destroyed by adding a water-miscible organic solvent to the wet alga body. The present invention also relates to a method for extracting polysaccharides, which comprises performing an enzymatic reaction after removing fat-soluble components in cells.
JP30394792A 1992-11-13 1992-11-13 Polysaccharide extraction method Expired - Lifetime JP2758796B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30394792A JP2758796B2 (en) 1992-11-13 1992-11-13 Polysaccharide extraction method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30394792A JP2758796B2 (en) 1992-11-13 1992-11-13 Polysaccharide extraction method

Publications (2)

Publication Number Publication Date
JPH06141877A JPH06141877A (en) 1994-05-24
JP2758796B2 true JP2758796B2 (en) 1998-05-28

Family

ID=17927210

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30394792A Expired - Lifetime JP2758796B2 (en) 1992-11-13 1992-11-13 Polysaccharide extraction method

Country Status (1)

Country Link
JP (1) JP2758796B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5597160B2 (en) * 2011-04-15 2014-10-01 株式会社日健総本社 Antiviral agent and production method thereof

Also Published As

Publication number Publication date
JPH06141877A (en) 1994-05-24

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