JP2866157B2 - Method for producing cellooligosaccharide - Google Patents

Method for producing cellooligosaccharide

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Publication number
JP2866157B2
JP2866157B2 JP18525490A JP18525490A JP2866157B2 JP 2866157 B2 JP2866157 B2 JP 2866157B2 JP 18525490 A JP18525490 A JP 18525490A JP 18525490 A JP18525490 A JP 18525490A JP 2866157 B2 JP2866157 B2 JP 2866157B2
Authority
JP
Japan
Prior art keywords
cellulase
reaction
cellooligosaccharides
cellooligosaccharide
glucose
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 - Fee Related
Application number
JP18525490A
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Japanese (ja)
Other versions
JPH0475594A (en
Inventor
吉紀 青柳
謙二 飛河
仙太郎 中谷
豊文 美矢
忠行 日野
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.)
Kojin Co Ltd
Original Assignee
Kojin Co Ltd
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Filing date
Publication date
Application filed by Kojin Co Ltd filed Critical Kojin Co Ltd
Priority to JP18525490A priority Critical patent/JP2866157B2/en
Publication of JPH0475594A publication Critical patent/JPH0475594A/en
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Publication of JP2866157B2 publication Critical patent/JP2866157B2/en
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Expired - Fee Related 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] 本発明はセロビオース等のセロオリゴ糖の製造方法に
関するものであり、更に詳しくはセロオリゴ糖の酵素的
製造方法に関する。セロオリゴ糖とは、例えば、セロビ
オース、セロトリオース、セロテトラオース、セロペン
タオース、セロヘキサオース等のグルコースがβ−1,4
結合した比較的低重合の少糖類であり、セルラーゼの基
質または阻害剤や合成品の出発原料その他一般試薬とし
て用いられている。更に、近年は、その機能性が注目さ
れており、食品添加物としての用途も期待されている。
The present invention relates to a method for producing cellooligosaccharides such as cellobiose, and more particularly, to an enzymatic method for producing cellooligosaccharides. Cellooligosaccharides include, for example, glucose such as cellobiose, cellotriose, cellotetraose, cellopentaose, cellohexaose, and β-1,4.
It is a relatively low-polymerized oligosaccharide that is bound and is used as a substrate or inhibitor of cellulase, a starting material for synthetic products, and other general reagents. Furthermore, in recent years, its functionality has been attracting attention, and its use as a food additive is also expected.

[従来の技術] セロオリゴ糖を酵素的に製造するには、セルロースに
セルラーゼを作用させる方法、及び、セルロースにセロ
オリゴ糖を好収率で生成する極めて特異性の高い特殊な
セルラーゼを作用する方法が知られていた(特開平1−
256394号)。
[Prior Art] In order to produce cellooligosaccharides enzymatically, a method of reacting cellulase with cellulose and a method of reacting cellulose with a highly specific special cellulase that produces cellooligosaccharide at a high yield are known. It was known (Japanese Unexamined Patent Publication No.
256394).

[本発明が解決しようとする課題] しかしながら、市販のセルラーゼを用いた酵素法で
は、生成したセロオリゴ糖が更に分散されてグルコース
に分解され、目的とするセロオリゴ糖の収率が極めて低
いという欠点があった。又、特異性が高い特殊なセルラ
ーゼを作用する方法はそのセルラーゼを得るためにその
生産菌を培養しなければならず、又限外濾過反応器等の
設備が必要でありかつ反応時間も長い等の欠点を有して
いる。
[Problems to be Solved by the Invention] However, the enzymatic method using a commercially available cellulase has a disadvantage that the produced cellooligosaccharide is further dispersed and decomposed into glucose, and the yield of the target cellooligosaccharide is extremely low. there were. In addition, a method of acting a special cellulase having a high specificity requires culturing the producing bacteria to obtain the cellulase, requires equipment such as an ultrafiltration reactor, and requires a long reaction time. Has the disadvantage of

[課題を解決するための手段] 本発明は、以上のような問題点を解決し、一般に市販
されている入手容易なセルラーゼ製剤を利用して且つ高
収率でセロオリゴ糖を工業的に製造する方法を提供する
ことを目的とする。即ち、本発明者らは上記の欠点を解
消するため鋭意検討した結果、一般に市販されている入
手容易なセルラーゼ製剤を用いてのバッチ式酵素反応に
より、セロオリゴ糖を効率良く生成蓄積せしめる方法を
見いだし本発明を達成したものである。即ち、本発明
は、セルロース系物質からセルラーゼの作用によりセロ
オリゴ糖を製造する方法において、その反応をグルコノ
ラクトン及び/またはグルコン酸の存在下で行うことを
特徴とするセロオリゴ糖の製造方法である。以下に本発
明を詳細に説明する。
[Means for Solving the Problems] The present invention solves the above-mentioned problems, and industrially produces cellooligosaccharides in high yields using generally available cellulase preparations which are generally commercially available. The aim is to provide a method. That is, the present inventors have conducted intensive studies to solve the above-mentioned disadvantages, and as a result, have found a method for efficiently producing and accumulating cellooligosaccharides by a batch-type enzymatic reaction using an easily available cellulase preparation which is generally commercially available. The present invention has been achieved. That is, the present invention relates to a method for producing cellooligosaccharides from cellulosic substances by the action of cellulase, wherein the reaction is carried out in the presence of gluconolactone and / or gluconic acid. . Hereinafter, the present invention will be described in detail.

本発明に用いるセルラーゼは特に限定する必要はな
く、市販セルラーゼ製剤のいずれでも用いることが出来
る。また主原料としてのセルロース系物質としては特に
限定されないが、脱リグニンされパウダー化された物の
方がより好ましい。またパルプ製造工程で副成する短繊
維や古紙再生工程で発生する再生不可能なセルロース等
も用いることが出来る。反応は、グルコノラクトン及び
/またはグルコン酸及び酵素と主原料を含む水懸濁状態
で行う。この時のグルコノラクトン及び/またはグルコ
ン酸の反応液中の濃度は0.1〜5W/W%、好ましくは0.5〜
2W/W%の範囲である。酵素の反応液中濃度は0.01〜5W/W
%、好ましくは0.1〜1W/W%、また主原料の反応液中濃
度は0.1〜15W/W%、好ましくは1〜10W/W%の範囲であ
り、これらを適宜組み合わせて用いる。また反応液のpH
は3〜6、好ましくは4〜5の範囲で、また反応温度は
30〜60℃、好ましくは45℃〜55℃の範囲で行う。反応時
間はセロオリゴ糖の生成が最大になった時点で終了する
のが好ましいが、大方1〜10時間の範囲である。酵素反
応終了後遠心分離及びケイソウ土濾過等により未反応残
査を除去して清澄液を得る。次に、イオン交換樹脂によ
る脱イオン処理を行い減圧濃縮し冷却してセロオリゴ糖
の結晶を得ることが出来る。更に再結晶を繰り返せば極
微量共存するグルコースを完全に除去する事が出来る。
尚、結晶収率を向上させる為にエタノール等のアルコー
ルを添加して冷却する方法も適用出来る。
The cellulase used in the present invention need not be particularly limited, and any commercially available cellulase preparation can be used. The cellulosic material as the main raw material is not particularly limited, but a delignified and powdered material is more preferable. Also, short fibers produced as a by-product in the pulp manufacturing process, non-renewable cellulose generated in the used paper recycling process, and the like can be used. The reaction is carried out in an aqueous suspension containing gluconolactone and / or gluconic acid, an enzyme and a main raw material. At this time, the concentration of gluconolactone and / or gluconic acid in the reaction solution is 0.1 to 5 W / W%, preferably 0.5 to 5 W / W%.
It is in the range of 2W / W%. The enzyme concentration in the reaction solution is 0.01 to 5 W / W
%, Preferably 0.1 to 1 W / W%, and the concentration of the main raw material in the reaction solution is in the range of 0.1 to 15 W / W%, preferably 1 to 10 W / W%, and these are used in appropriate combination. The pH of the reaction solution
Is in the range of 3-6, preferably 4-5, and the reaction temperature is
The reaction is carried out at 30 to 60 ° C, preferably at 45 to 55 ° C. The reaction time is preferably terminated when the production of cellooligosaccharide is maximized, but is generally in the range of 1 to 10 hours. After completion of the enzymatic reaction, the unreacted residue is removed by centrifugation, diatomaceous earth filtration or the like to obtain a clear liquid. Next, deionization treatment with an ion exchange resin is performed, concentration is performed under reduced pressure, and cooling is performed to obtain cellooligosaccharide crystals. Further, if recrystallization is repeated, a trace amount of coexisting glucose can be completely removed.
In addition, a method of adding an alcohol such as ethanol and cooling in order to improve the crystal yield can also be applied.

[作用] 本発明によるセルラーゼ反応に於てセロオリゴ糖が生
成する機構については明かでないが以下のようなことが
推定された。セルラーゼはセルロース成分をグルコース
やセロオリゴ糖に分解する酵素として一般に知られてい
るが、その中にC1酵素活性、CX酵素活性、及びβ−グル
コシダーゼ活性等を含むとされている。セルロースが分
解される過程は先ずC1酵素活性やCX酵素活性が働きセロ
オリゴ糖を生成しこれにβ−グルコシダーゼ活性が働き
セルロースの最小単位であるグルコースに分解するとさ
れている。セルラーゼ反応を行う際にグルコノラクトン
及び/またはグルコン酸を加えると、これによりβ−グ
ルコシダーザ活性が阻害され従ってセロオリゴ糖が蓄積
されたものと考えられる。
[Action] The mechanism of cellooligosaccharide formation in the cellulase reaction according to the present invention is not clear, but the following was presumed. Cellulase is generally known as an enzyme that decomposes a cellulose component into glucose and cellooligosaccharide, and is said to contain C1 enzyme activity, CX enzyme activity, β-glucosidase activity and the like. In the process of cellulose degradation, it is said that C1 enzyme activity and CX enzyme activity act first to produce cellooligosaccharides, and β-glucosidase activity acts on these to decompose to glucose, which is the minimum unit of cellulose. It is considered that when gluconolactone and / or gluconic acid was added during the cellulase reaction, the β-glucosidase activity was inhibited thereby, and cellooligosaccharides were accumulated.

[実施例] 以下実施例を挙げて本発明を更に詳しく説明する。EXAMPLES Hereinafter, the present invention will be described in more detail with reference to examples.

尚、実施例におけるセロオリゴ糖の分離定量方法は下
記に示す高速液体クロマトグラフィー(以下HPLCと略
す)により行った。
The method for separating and quantifying cellooligosaccharides in the examples was performed by the following high performance liquid chromatography (hereinafter abbreviated as HPLC).

(1)測定機器 HPLC用ポンプ:ウオーターズ製MODEL 510 示差屈折率検出器:昭和電工(株)製SHODEX RI SE −6
1 クロマトデーター処理装置:日立製833A形 (2)測定条件 カラム:4.6mm ID×25cm 充填剤:東ソー(株)製TSKge1Amide−80(5μm) カラム温度:80℃ 溶出溶媒:アセトニトリル/水=6/4 流速:1ml/min 注入量:10μl 実施例1 セルラーゼ(商品名:メイセラーゼ、明治製菓株式会
社製)2g、セルロースパウダー(商品名:K・S・パウダ
ー100メッシュ、株式会社興人製)20g、及び10gのグル
コノラクトンを1Lの0.1M酢酸緩衝液pH5に添加し、50℃
に加温し攪拌しながら酵素反応を行った。4時間反応
後、遠心分離により上澄液を得た。上澄液は更にラジオ
ライト#500を用いるケイソウ土濾過により清澄化し清
澄液960mlを得た。この清澄液の糖組成はHPLC分析の結
果グルコース1.04mg/ml、セロビオース6.29mg/ml、セロ
トリオース0.22mg/mlであった。次にこの清澄液を樹脂
量50mlのダイヤイオンSKIB(H型、三菱化成製)カラム
及び樹脂量100mlのダイヤイオンWA30(OH型、三菱化成
製)カラムに連続的に通液した(SV=5)。得られた通
過液はエバポレーターにより減圧濃縮(40℃)して約12
ml(Bx約60度)とした。これにエタノールを4ml添加し
4℃で放置した。一液放置後白色結晶4.5gを得た。次
に、これを約9mlの熱水に溶解し先と同様に冷却して再
結晶品約3.1gを得た。この再結晶品をHPLCで分析した結
果は第1図のようであった。即ち、標準物質との比較か
らセロビオース96.6%、セロトリオース3.4%であっ
た。また、得られた結晶は、アーモンドβ−グルコシダ
ーゼ(シグマ製)により完全にグルコースに分解された
ことからこれはセロオリゴ糖であるといえる。
(1) Measuring instrument HPLC pump: Waters MODEL 510 Differential refractive index detector: Showa Denko KK SHODEX RISE-6
1 Chromatographic data processing device: Hitachi 833A type (2) Measurement conditions Column: 4.6 mm ID × 25 cm Filler: TSKge1Amide-80 (5 μm) manufactured by Tosoh Corporation Column temperature: 80 ° C. Elution solvent: acetonitrile / water = 6 / 4 Flow rate: 1 ml / min Injection volume: 10 μl Example 1 2 g of cellulase (trade name: Meisserase, manufactured by Meiji Seika Co., Ltd.), 20 g of cellulose powder (trade name: KS powder 100 mesh, manufactured by Kojin Co., Ltd.), And 10 g of gluconolactone were added to 1 L of 0.1 M acetate buffer pH 5, and the temperature was adjusted to 50 ° C.
, And the enzyme reaction was carried out with stirring. After the reaction for 4 hours, a supernatant was obtained by centrifugation. The supernatant was further clarified by diatomaceous earth filtration using Radiolite # 500 to obtain 960 ml of a clear solution. As a result of HPLC analysis, the sugar composition of the clarified solution was glucose 1.04 mg / ml, cellobiose 6.29 mg / ml, and cellotriose 0.22 mg / ml. Next, the clarified solution was continuously passed through a column of Diaion SKIB (H type, manufactured by Mitsubishi Kasei) having a resin amount of 50 ml and a column of Diaion WA30 (OH type, manufactured by Mitsubishi Kasei) having a resin amount of 100 ml (SV = 5). ). The eluate obtained was concentrated under reduced pressure (40 ° C) by an evaporator to about 12
ml (Bx about 60 degrees). To this was added 4 ml of ethanol, and the mixture was allowed to stand at 4 ° C. After standing for one solution, 4.5 g of white crystals were obtained. Next, this was dissolved in about 9 ml of hot water and cooled in the same manner as above to obtain about 3.1 g of a recrystallized product. The result of HPLC analysis of this recrystallized product was as shown in FIG. That is, cellobiose was 96.6% and cellotriose was 3.4% as compared with the standard substance. In addition, the obtained crystals were completely decomposed into glucose by almond β-glucosidase (manufactured by Sigma), which means that they were cellooligosaccharides.

実施例2 セルラーゼとしてセルラーゼオノズカ(株式会社ヤク
ルト製)を、またグルコノラクトンの代わりにグルコン
酸を用いた以外は実施例1と全く同一条件で反応を行い
この反応液より実施例1と同様の方法により清澄液955m
lを得た。この清澄液の糖組成はHPLC分析の結果グルコ
ース0.82mg/ml、セロビオース5mg/ml、セロトリオース
0.17mg/mlであった。その後も実施例1と同様の処理を
行い、再結晶品2gを得た。このものの糖組成も、HPLC分
析の結果実施例1とほぼ同様であった。
Example 2 A reaction was carried out under exactly the same conditions as in Example 1 except that cellulase Onozuka (produced by Yakult Co., Ltd.) was used as cellulase and gluconic acid was used instead of gluconolactone. 955m clear liquid by the method of
got l. The sugar composition of this clarified solution was determined by HPLC analysis to be glucose 0.82 mg / ml, cellobiose 5 mg / ml, cellotriose
It was 0.17 mg / ml. Thereafter, the same treatment as in Example 1 was performed to obtain 2 g of a recrystallized product. The saccharide composition of this product was almost the same as in Example 1 as a result of HPLC analysis.

比較例1 グルコノラクトンを添加しないこと以外は実施例1と
全く同じ条件で反応を行った。次にこの反応液より実施
例1と同様の方法により清澄液965mlを得た。の清澄液
の糖組成はHPLC分析の結果グルコース5.71mg/ml、セロ
ビオース0.96mg/mlであった。このように目的とするセ
ロビオースの収率は低く、多くはグルコースに変化して
しまっていた。
Comparative Example 1 The reaction was carried out under exactly the same conditions as in Example 1 except that gluconolactone was not added. Next, 965 ml of a clear solution was obtained from the reaction solution in the same manner as in Example 1. As a result of HPLC analysis, the sugar composition of the clarified solution was 5.71 mg / ml for glucose and 0.96 mg / ml for cellobiose. Thus, the yield of the target cellobiose was low, and most of the cellobiose had been converted to glucose.

[発明の効果] 比較例1からも明らかなように市販セルラーゼ製剤を
そのまま用いるセルラーゼ反応ではセロオリゴ糖の生成
が極めて低くセロオリゴ糖の製造方法として不適である
が、本発明の方法を用いれば一般に入手容易な市販セル
ラーゼ製剤によってもセロオリゴ糖の製造が可能であ
る。従って、特殊なセルラーゼを特に必要としない。ま
た限外濾過反応器等の設備も特に必要ではなく、かつ反
応時間も短い等セロオリゴ糖の工業的製造方法として極
めて有効である。
[Effects of the invention] As is clear from Comparative Example 1, in the cellulase reaction using a commercially available cellulase preparation as it is, the production of cellooligosaccharides is extremely low, which is unsuitable as a method for producing cellooligosaccharides. Cellooligosaccharides can also be produced by easy commercial cellulase preparations. Therefore, no special cellulase is required. In addition, equipment such as an ultrafiltration reactor is not particularly required, and the reaction time is short. Thus, it is extremely effective as an industrial production method of cellooligosaccharide.

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

第1図は実施例1において得られた最終生成物の糖組成
を示すHPLCのクロマトグラムである。
FIG. 1 is an HPLC chromatogram showing the sugar composition of the final product obtained in Example 1.

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) C12P 19/14 CA(STN)──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 6 , DB name) C12P 19/14 CA (STN)

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】セルロース系物質からセルラーゼの作用に
よりセロオリゴ糖を製造する方法において、その反応を
グルコノラクトン及び/またはグルコン酸の存在下で行
うことを特徴とするセロオリゴ糖の製造方法。
1. A method for producing cellooligosaccharides from cellulosic substances by the action of cellulase, wherein the reaction is carried out in the presence of gluconolactone and / or gluconic acid.
JP18525490A 1990-07-16 1990-07-16 Method for producing cellooligosaccharide Expired - Fee Related JP2866157B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18525490A JP2866157B2 (en) 1990-07-16 1990-07-16 Method for producing cellooligosaccharide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18525490A JP2866157B2 (en) 1990-07-16 1990-07-16 Method for producing cellooligosaccharide

Publications (2)

Publication Number Publication Date
JPH0475594A JPH0475594A (en) 1992-03-10
JP2866157B2 true JP2866157B2 (en) 1999-03-08

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ID=16167600

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Country Link
JP (1) JP2866157B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014142325A1 (en) 2013-03-15 2014-09-18 国立大学法人長岡技術科学大学 Variant of cellulase-producing fungus, cellulase manufacturing method, and cello-oligosaccharide manufacturing method
CN104805137B (en) * 2014-01-24 2018-11-23 华东理工大学 A kind of method of bioconversion lignocellulosic production gluconic acid

Also Published As

Publication number Publication date
JPH0475594A (en) 1992-03-10

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