JPH05317073A - Production of cellooligosaccharide - Google Patents
Production of cellooligosaccharideInfo
- Publication number
- JPH05317073A JPH05317073A JP12889992A JP12889992A JPH05317073A JP H05317073 A JPH05317073 A JP H05317073A JP 12889992 A JP12889992 A JP 12889992A JP 12889992 A JP12889992 A JP 12889992A JP H05317073 A JPH05317073 A JP H05317073A
- Authority
- JP
- Japan
- Prior art keywords
- cellulase
- cellulose
- lignin
- cellooligosaccharide
- cellobiose
- 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.)
- Granted
Links
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- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
Description
【0001】[0001]
【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。TECHNICAL FIELD The present invention relates to a method for producing cellooligosaccharides such as cellobiose.
【0002】[0002]
【従来の技術】従来、ダイエット甘味料としてセロビオ
ース,セロトリオース,セロテトラオース等のセロオリ
ゴ糖が知られている。このセロオリゴ糖は一般にセルロ
ースをセルラーゼ(酵素)の作用により加水分解させる
ことにより得られる。2. Description of the Related Art Cello-oligosaccharides such as cellobiose, cellotriose, and cellotetraose have been known as diet sweeteners. This cellooligosaccharide is generally obtained by hydrolyzing cellulose by the action of cellulase (enzyme).
【0003】この加水分解反応においてセルラーゼがで
きるだけ働き易い環境を作るために次のような技術が提
案されている。 (1)特公昭57−53801号公報;原料としてのセ
ルロースを濃塩酸と濃硫酸との混液中で処理することに
よりそのセルロースをセルラーゼに分解され易いセルロ
ースに加工する。 (2)特開平1−256394号公報;反応系に限外濾
過反応器を配設してその限外濾過反応器において反応阻
害物を除去する。The following techniques have been proposed in order to create an environment in which cellulase works as easily as possible in this hydrolysis reaction. (1) Japanese Examined Patent Publication No. 57-58001; cellulose as a raw material is treated in a mixed solution of concentrated hydrochloric acid and concentrated sulfuric acid to process the cellulose into cellulose that is easily decomposed into cellulase. (2) JP-A 1-256394; An ultrafiltration reactor is provided in the reaction system to remove reaction inhibitors in the ultrafiltration reactor.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、これら
の技術は、(1)セルロースに加工を施さなければなら
ない、(2)反応阻害物が除去されるため、セルラーゼ
による加水分解反応が阻害されることを抑止することは
できるが、選択的にセロオリゴ糖を得ることができな
い、ため、セロオリゴ糖を安価に大量生産することは困
難である。この結果、セロオリゴ糖が非常に高価なもの
となっている。However, in these techniques, (1) cellulose must be processed, and (2) reaction inhibitors are removed, so that the hydrolysis reaction by cellulase is inhibited. However, it is difficult to mass-produce cellooligosaccharides at low cost because cellooligosaccharides cannot be selectively obtained. As a result, cellooligosaccharides are very expensive.
【0005】本発明は前記問題点に鑑みてなされたもの
であって、セロオリゴ糖を安価かつ簡便に得ることがで
きるセロオリゴ糖の製造方法を提供することを目的とす
る。The present invention has been made in view of the above problems, and an object of the present invention is to provide a method for producing cellooligosaccharides, which allows cellooligosaccharides to be obtained inexpensively and conveniently.
【0006】[0006]
【課題を解決するための手段】本発明者らは、(1)結
晶性セルロースはその結晶性セルロースを構成するグル
コース単位間の水素結合力が強いため、この結晶性セル
ロースのセルラーゼによる加水分解速度は遅い。また、
この加水分解においてセルラーゼの中に含まれるβ−グ
ルコシダーゼの作用によりグルコースを多く含む加水分
解物(生成物)が得られる、(2)非結晶性セルロース
はセルラーゼにより容易に加水分解され、この加水分解
によりセロオリゴ糖,グルコースが得られるが、この加
水分解においてセルラーゼの中に含まれるβ−グルコシ
ダーゼの作用によりセロオリゴ糖よりもグルコースが多
く得られる、(3)β−グルコシダーゼはリグニンに吸
着されることにより不活性となる、(4)前記加水分解
反応にて生成されるセロビオースはセルラーゼに対する
分解阻害性を有する、という事象に基づいて、非結晶性
セルロースを多く含むセルロース原料にセルラーゼを作
用させるとともに、このセルラーゼの中のβ−グルコシ
ダーゼをリグニンに吸着させてそのβ−グルコシダーゼ
の作用を抑止させ、この加水分解反応により生成される
セロオリゴ糖のうち少なくともセロビオースを随時その
反応液から採取することにより選択的にセロオリゴ糖が
得られるという知見を得た。MEANS FOR SOLVING THE PROBLEMS The present inventors have found that (1) crystalline cellulose has a strong hydrogen bonding force between glucose units constituting the crystalline cellulose. Therefore, the hydrolysis rate of this crystalline cellulose by cellulase is high. Is slow. Also,
In this hydrolysis, a glucose-rich hydrolyzate (product) is obtained by the action of β-glucosidase contained in cellulase. (2) Amorphous cellulose is easily hydrolyzed by cellulase, and this hydrolysis Although cellooligosaccharide and glucose are obtained by this method, more glucose is obtained than cellooligosaccharide by the action of β-glucosidase contained in cellulase in this hydrolysis. (3) β-glucosidase is adsorbed by lignin Based on the phenomenon that (4) cellobiose produced by the hydrolysis reaction has an inhibitory effect on cellulase decomposition, cellulase is caused to act on a cellulose raw material containing a large amount of amorphous cellulose, and Β-glucosidase in cellulase to lignin It was found that cello-oligosaccharides can be selectively obtained by adsorbing them to inhibit the action of β-glucosidase and collecting at least cellobiose from the reaction solution at any time among the cellooligosaccharides produced by this hydrolysis reaction. .
【0007】したがって、本発明のセロオリゴ糖の製造
方法は、非結晶性セルロースを多く含むセルロース原料
をセルラーゼの作用により加水分解してセロオリゴ糖を
生成する加水分解反応をリグニンの存在のもとに行わせ
るとともに、この加水分解反応により生成されるセロオ
リゴ糖のうち少なくともセロビオースを随時その反応液
から採取することを特徴とする。Therefore, in the method for producing cellooligosaccharides of the present invention, a hydrolysis reaction in which a cellulosic material containing a large amount of amorphous cellulose is hydrolyzed by the action of cellulase to produce cellooligosaccharides is carried out in the presence of lignin. At the same time, at least cellobiose among the cellooligosaccharides produced by this hydrolysis reaction is optionally collected from the reaction solution.
【0008】[0008]
【作用】本発明のセロオリゴ糖の製造方法によれば、非
結晶性セルロースを多く含むセルロース原料がセルラー
ゼの作用により加水分解されてセロオリゴ糖が生成され
る。この際、セルラーゼの中でセロオリゴ糖からグルコ
ースを生成するβ−グルコシダーゼはリグニンに吸着さ
れて不活性化されるため、セルラーゼの中のエンド形酵
素のセルロース原料への作用が優位となる。また、生成
されたセロビオースがその反応液から採取されることに
よりセルラーゼの分解反応が阻害されるのが抑止され
る。この結果、選択的にセロオリゴ糖が生成される。な
お、この反応系においては、セルロース原料が非結晶性
セルロースを多く含むほど加水分解反応が進行し易くな
るとともに選択的にセロビオースが得られる。According to the method for producing cellooligosaccharides of the present invention, the cellulose raw material containing a large amount of non-crystalline cellulose is hydrolyzed by the action of cellulase to produce cellooligosaccharides. At this time, β-glucosidase, which produces glucose from cellooligosaccharide in cellulase, is inactivated by being adsorbed by lignin, so that the action of the endo-type enzyme in cellulase on the cellulose raw material becomes dominant. Further, the cellobiose thus produced is collected from the reaction solution, thereby inhibiting the cellulase decomposition reaction from being inhibited. As a result, cellooligosaccharides are selectively produced. In this reaction system, as the cellulose raw material contains a larger amount of non-crystalline cellulose, the hydrolysis reaction proceeds more easily and cellobiose is selectively obtained.
【0009】[0009]
【実施例】次に、本発明の具体的な一実施例について説
明する。EXAMPLE A specific example of the present invention will be described below.
【0010】本発明の一実施例のセロオリゴ糖の製造方
法は、まず、例えばパルプ製造工程途中の生産物として
得られる未晒しパルプ(非結晶性セルロースとリグニン
とを含む。)を原料としてその未晒しパルプの2wt%
スラリー液を作成する。このスラリー液を攪拌しつつそ
のスラリー液に酢酸を添加することによりそのスラリー
液のpHを5.5に調整した後、このスラリー液を45
℃に加温する。この温度を保持しつつそのスラリー液に
対して0.1wt%のセルラーゼ(Trichoderma viride
起源)を添加して20min攪拌することにより、セル
ロースにセルラーゼを作用させてそのセルロースを加水
分解する。In the method for producing cellooligosaccharides according to one embodiment of the present invention, first, for example, unbleached pulp (containing amorphous cellulose and lignin) obtained as a product during the pulp production process is used as a raw material. 2 wt% of bleached pulp
Create a slurry liquid. The pH of the slurry liquid was adjusted to 5.5 by adding acetic acid to the slurry liquid while stirring the slurry liquid, and then the slurry liquid was adjusted to 45
Warm to ℃. While maintaining this temperature, 0.1 wt% of cellulase (Trichoderma viride
(Origin) is added and stirred for 20 minutes to cause cellulase to act on the cellulose to hydrolyze the cellulose.
【0011】この加水分解反応液を例えば限外濾過膜に
て濾過すると、セロビオースが80%以上を占める糖液
が採取された。When this hydrolysis reaction solution was filtered through, for example, an ultrafiltration membrane, a sugar solution in which cellobiose accounted for 80% or more was collected.
【0012】次に、比較例としてKCフロックW−50
(セルロース原料;山陽国策パルプ株式会社製)を原料
として、前記実施例と同様な加水分解反応を行った。こ
の比較例において反応液を前記限外濾過膜にて濾過する
と、セロビオースが20%以下の糖液が採取された。前
記加水分解反応をさらに1.5h継続してその反応液を
同様に限外濾過膜にて濾過すると、グルコースがほとん
どを占める糖液が採取された。Next, as a comparative example, KC Flock W-50
(Cellulose raw material; manufactured by Sanyo Kokusaku Pulp Co., Ltd.) was used as a raw material to carry out the same hydrolysis reaction as in the above-mentioned Examples. When the reaction solution in this comparative example was filtered through the ultrafiltration membrane, a sugar solution having a cellobiose content of 20% or less was collected. The hydrolysis reaction was continued for a further 1.5 hours, and the reaction solution was filtered through an ultrafiltration membrane in the same manner. As a result, a sugar solution containing mostly glucose was collected.
【0013】[0013]
【発明の効果】以上のように構成された本発明によれ
ば、セルラーゼの中のβ−グルコシダーゼをリグニンに
吸着させて不活性化させるとともに加水分解反応により
生成されるセロオリゴ糖のうちセロビオースを随時その
反応液から採取することにより、安価で簡便にセロオリ
ゴ糖を得ることができる。EFFECTS OF THE INVENTION According to the present invention constituted as described above, cellobiose is optionally included in the cellooligosaccharides produced by the hydrolysis reaction by adsorbing β-glucosidase in cellulase to lignin to inactivate it. Cellooligosaccharides can be obtained inexpensively and easily by collecting from the reaction solution.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 越島 哲夫 大阪市淀川区加島4丁目6番23号 日本化 学機械製造株式会社内 (72)発明者 都宮 孝彦 大阪市淀川区加島4丁目6番23号 日本化 学機械製造株式会社内 (72)発明者 笹谷 昌見 大阪市淀川区加島4丁目6番23号 日本化 学機械製造株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Tetsuo Koshishima 4-6-23 Kashima, Yodogawa-ku, Osaka City, Japan Chemical Machinery Manufacturing Co., Ltd. (72) Inventor Takahiko Tsunomiya 4-chome, Kashima, Yodogawa-ku, Osaka No. 23 In Japan Chemical Machinery Manufacturing Co., Ltd. (72) Inventor Masami Sasaya 4-6-23 Kashima, Yodogawa-ku, Osaka City Japan Chemical Machinery Manufacturing Co., Ltd.
Claims (1)
ス原料をセルラーゼの作用により加水分解してセロオリ
ゴ糖を生成する加水分解反応をリグニンの存在のもとに
行わせるとともに、この加水分解反応により生成される
セロオリゴ糖のうち少なくともセロビオースを随時その
反応液から採取することを特徴とするセロオリゴ糖の製
造方法。1. A cellulosic material containing a large amount of non-crystalline cellulose is hydrolyzed by the action of cellulase to produce a cellooligosaccharide in the presence of lignin, and is produced by this hydrolysis reaction. A method for producing cellooligosaccharides, characterized in that at least cellobiose of the cellooligosaccharides is optionally collected from the reaction solution.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12889992A JPH0695943B2 (en) | 1992-05-21 | 1992-05-21 | Method for producing cellooligosaccharide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12889992A JPH0695943B2 (en) | 1992-05-21 | 1992-05-21 | Method for producing cellooligosaccharide |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH05317073A true JPH05317073A (en) | 1993-12-03 |
JPH0695943B2 JPH0695943B2 (en) | 1994-11-30 |
Family
ID=14996112
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12889992A Expired - Lifetime JPH0695943B2 (en) | 1992-05-21 | 1992-05-21 | Method for producing cellooligosaccharide |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0695943B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006112316A1 (en) * | 2005-04-13 | 2006-10-26 | Matsutani Chemical Industry Co. Ltd. | Purification method and production method for cellobiose |
US7947656B2 (en) | 2004-07-27 | 2011-05-24 | Asahi Kasei Chemicals Corporation | Processes for producing cellooligosaccharide |
JP6255119B1 (en) * | 2017-01-12 | 2017-12-27 | 新日鉄住金エンジニアリング株式会社 | Method and apparatus for producing a saccharifying enzyme for saccharifying lignocellulosic biomass, and use thereof |
-
1992
- 1992-05-21 JP JP12889992A patent/JPH0695943B2/en not_active Expired - Lifetime
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7947656B2 (en) | 2004-07-27 | 2011-05-24 | Asahi Kasei Chemicals Corporation | Processes for producing cellooligosaccharide |
WO2006112316A1 (en) * | 2005-04-13 | 2006-10-26 | Matsutani Chemical Industry Co. Ltd. | Purification method and production method for cellobiose |
JP2006290831A (en) * | 2005-04-13 | 2006-10-26 | Matsutani Chem Ind Ltd | Method for purifying cellobiose and method for producing the same |
GB2438573A (en) * | 2005-04-13 | 2007-11-28 | Matsutani Kagaku Kogyo Kk | Purification method and production method for cellobiose |
GB2438573B (en) * | 2005-04-13 | 2009-08-26 | Matsutani Kagaku Kogyo Kk | Purification method and production method for cellobiose |
KR100939551B1 (en) * | 2005-04-13 | 2010-02-03 | 마쓰다니가가꾸고오교가부시끼가이샤 | Purification method and production method for cellobiose |
US8580955B2 (en) | 2005-04-13 | 2013-11-12 | Matsutani Chemical Industry Co., Ltd. | Purification method and production method for cellobiose |
JP6255119B1 (en) * | 2017-01-12 | 2017-12-27 | 新日鉄住金エンジニアリング株式会社 | Method and apparatus for producing a saccharifying enzyme for saccharifying lignocellulosic biomass, and use thereof |
WO2018131653A1 (en) * | 2017-01-12 | 2018-07-19 | 新日鉄住金エンジニアリング株式会社 | Method and apparatus for producing saccharification enzyme for saccharifying lignocellulosic biomass, and uses of said method and apparatus |
Also Published As
Publication number | Publication date |
---|---|
JPH0695943B2 (en) | 1994-11-30 |
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