JPH057496A - Production of oligosaccharide - Google Patents

Production of oligosaccharide

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Publication number
JPH057496A
JPH057496A JP16184091A JP16184091A JPH057496A JP H057496 A JPH057496 A JP H057496A JP 16184091 A JP16184091 A JP 16184091A JP 16184091 A JP16184091 A JP 16184091A JP H057496 A JPH057496 A JP H057496A
Authority
JP
Japan
Prior art keywords
oligosaccharide
chitin
glucosamine
chitinase
acetylglucosamine
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
Application number
JP16184091A
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Japanese (ja)
Other versions
JP2810255B2 (en
Inventor
Hiroshi Miyoshi
洋 三好
Tamami Boku
玉美 朴
Toru Chiba
徹 千葉
Kimitsuna Watanabe
公綱 渡辺
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.)
Shin Etsu Chemical Co Ltd
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Shin Etsu Chemical Co Ltd
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Priority to JP16184091A priority Critical patent/JP2810255B2/en
Publication of JPH057496A publication Critical patent/JPH057496A/en
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Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To efficiently produce a homo-oligosaccharide and a heterooligosaccharide both comprising high mol.wt. glucosamine and N- acetylglucosamine and having high physiological activities by hydrolyzing uniformly and partially deacetylated chitin with chitinase. CONSTITUTION:The powder of chitin is dissolved in an alkali solution and uniformly and partially deacetylated. The reaction product is dissolved in lactic acid, etc., and the solution is dropped in acetone to produce the precipitates of the partially deacetylated chitin lactic acid salt. The precipitates are filtered out, dried, dissolved in water, hydrolyzed with chitinase at 20-50 deg.C for 24hrs or longer, and subsequently heated to stop the hydrolytic reaction. The chitinase is removed by an ultrafiltration method, and the remaining reaction solution is treated with a cation exchange resin to make the partially deacetylated chitin adsorbed and removed the lactic acid. The resin is treated with diluted hydrochloric acid to elute a hetero-oligosaccharide comprising glucosamine and N-acetylglucosamine having high mol.wts. and glucosamine homo- oligosaccharide.

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、キチン及びキトサンを
分解して得られる生理活性が高い高重合度のキチンオリ
ゴ糖及びキトサンオリゴ糖の製造方法に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing chitin oligosaccharides and chitosan oligosaccharides having a high degree of polymerization and having a high physiological activity, which are obtained by degrading chitin and chitosan.

【0002】[0002]

【従来の技術】近年、キチンやキトサンを分解すること
により生理活性が高いオリゴ糖が見い出されている。生
理活性が高いオリゴ糖は比較的重合度の高いオリゴ糖で
ある。例えばキチンオリゴ糖のヘキサN−アセチルキト
ヘキサオース(重合度6のN−アセチルグルコサミン)
は、免疫機能亢進効果が著しい(鈴木茂生ら、第2回キ
チン、キトサンシンポジジウム講演要旨集、3-6、198
5)。また、キトサンオリゴ糖のヘプタキトヘプタオー
ス(重合度7のグルコサミン)は、フサリウム ソラニ
(Fusarium solani )の成育を阻害し(D.F.Kendra et.
al.,Exp.Mycology,8,276-281,1984) 、トマトの葉のプ
ロテアーゼ阻害剤を合成するために有用である(M.Walke
r-Simmons et.al.,Plant physiol.,76, 787-790,198
4)。
2. Description of the Related Art Recently, oligosaccharides having high physiological activity have been found by degrading chitin and chitosan. An oligosaccharide having a high physiological activity is an oligosaccharide having a relatively high degree of polymerization. For example, chitin oligosaccharide hexaN-acetylchitohexaose (N-acetylglucosamine with a degree of polymerization of 6)
Have a remarkable effect on enhancing immune function (Suzuki Shigeo et al., 2nd chitin, chitosan symposium abstracts, 3-6, 198)
Five). In addition, the chitosan oligosaccharide heptachitoheptaose (glucosamine with a degree of polymerization of 7) inhibits the growth of Fusarium solani (DFKendra et.
al., Exp. Mycology, 8, 276-281 , 1984), useful for synthesizing tomato leaf protease inhibitors (M. Walke
r-Simmons et.al., Plant physiol., 76, 787-790,198
Four).

【0003】一方、生理活性が高いオリゴ糖を得る方法
は酸加水分解や酵素分解が試みられているが、これまで
に効率のよい方法は見い出されていない。例えばキチン
を塩酸で加水分解しN−アセチルグルコサミンのオリゴ
糖を得ることができるが、分解物中における重合度が高
いオリゴ糖の割合は塩酸の濃度、温度及び反応時間など
に大きく影響される。この場合、加水分解を限定的に行
うと分解物中における高重合度のオリゴ糖の割合は増加
するが、分解物全体の収量が少ない。逆に、加水分解を
ほぼ完全に行うと分解物全体の収量は多くなるが、分解
物中の高重合度のオリゴ糖の割合が著しく減少する。ま
た、キトサンの酸加水分解によるグルコサミンのオリゴ
糖の生成についても同様であり、高重合度のオリゴ糖を
効率よく得る方法は確立されていない(坂井和雄、キチ
ン、キトサンの開発と応用、工業技術会、111-134、198
7)。
On the other hand, acid hydrolysis or enzymatic decomposition has been tried as a method for obtaining an oligosaccharide having a high physiological activity, but an efficient method has not been found so far. For example, chitin can be hydrolyzed with hydrochloric acid to obtain oligosaccharides of N-acetylglucosamine, but the ratio of oligosaccharides having a high degree of polymerization in the decomposed product is greatly affected by the concentration of hydrochloric acid, temperature, reaction time, and the like. In this case, if hydrolysis is limitedly carried out, the proportion of oligosaccharides having a high degree of polymerization in the degradation product increases, but the yield of the entire degradation product is low. On the other hand, if the hydrolysis is almost completely performed, the yield of the entire hydrolyzate increases, but the proportion of the oligosaccharides having a high degree of polymerization in the hydrolyzate significantly decreases. The same applies to the production of oligosaccharides of glucosamine by acid hydrolysis of chitosan, and a method for efficiently obtaining oligosaccharides with a high degree of polymerization has not been established (Kazuo Sakai, development and application of chitin and chitosan, industrial technology Kai, 111-134, 198
7).

【0004】酵素分解による方法では、キチンをキチナ
ーゼで分解してN−アセチルグルコサミンのオリゴ糖を
得た場合、分解物が殆ど二糖であった(大宝明、昭和6
1年日本農芸化学会西日本支部大会要旨集、12、1986
)。また、キトサンをキトサナーゼで分解しグルコサ
ミンのオリゴ糖を得る場合も分解物は殆ど二糖から五糖
であり、その中でも五糖以上の重合度のオリゴ糖は少な
い(M.Izumi et.al.,Agric.Biol.Chem.,51,1189-1191,1
987) 。
In the enzymatic decomposition method, when chitin was decomposed with chitinase to obtain oligosaccharides of N-acetylglucosamine, most of the decomposition products were disaccharides (Daihomei, Showa 6).
1st Annual Meeting of the Japanese Society of Agricultural Chemistry, West Japan Chapter, 12, 1986
). Further, when degrading chitosan with chitosanase to obtain oligosaccharides of glucosamine, most of the degradation products are disaccharides to pentasaccharides, and among them oligosaccharides having a degree of polymerization of pentasaccharides or higher are small (M.Izumi et.al., Agric.Biol.Chem., 51, 1189-1191,1
987).

【0005】その他、高重合度のオリゴ糖を得る方法
は、N−アセチルグルコサミンの四糖にキチナーゼを作
用させて糖転移反応を利用してN−アセチルグルコサミ
ンの六糖を得ることができるが、原料である四糖のN−
アセチルグルコサミン自体が得られにくい(F.Nanjo e
t.al.,Agric.Biol.Chem.,53,2189-2195,1989)。また、
分子内に20〜35%程度のN−アセチルグルコサミン
残基が不均一に分布した部分脱アセチル化キチンをキチ
ナーゼで分解してオリゴ糖を得ることもできるが、分解
物は二糖、三糖及び四糖に限られる(A.Ohtakara et.a
l.,Agric.Biol.Chem.,52,3181-3182,1988)。
In addition, as a method for obtaining an oligosaccharide having a high degree of polymerization, a chitinase is allowed to act on the tetrasaccharide of N-acetylglucosamine to utilize the transglycosylation reaction to obtain the hexasaccharide of N-acetylglucosamine. N- of the raw material tetrasaccharide
Acetylglucosamine itself is difficult to obtain (F. Nanjo e
t.al., Agric. Biol. Chem., 53, 2189-2195 , 1989). Also,
A partially deacetylated chitin in which about 20 to 35% of N-acetylglucosamine residues are unevenly distributed in the molecule can be decomposed with chitinase to obtain an oligosaccharide, but the decomposition products are disaccharide, trisaccharide and Limited to tetrasaccharides (A. Ohtakara et.a
L., Agric. Biol. Chem., 52 , 3181-3182, 1988).

【0006】[0006]

【発明が解決しようとする課題】本発明は前記の課題を
解決するためなされたもので、生理活性が高いグルコサ
ミンオリゴ糖及びN−アセチルグルコサミンオリゴ糖の
効率の良い製造方法を提供することを目的とする。
The present invention has been made to solve the above problems, and an object thereof is to provide a method for efficiently producing glucosamine oligosaccharides and N-acetylglucosamine oligosaccharides having high physiological activity. And

【0007】[0007]

【課題を解決するための手段】前記の目的を達成するた
めになされた本発明のオリゴ糖の製造方法は、均一に部
分脱アセチル化されたキチンをキチナーゼにより加水分
解し、高重合度のグルコサミン及びN−アセチルグルコ
サミンからなるヘテロオリゴ糖、及びグルコサミンのホ
モオリゴ糖を得る。キチンのキチナーゼによる加水分解
は透析膜の内部で行い、同時に透析膜の外部に陽イオン
交換樹脂を配置して透析を行うことが好ましい。尚、使
用するキチンは甲殻類、または糸状菌から得られるもの
が好ましい。
Means for Solving the Problems The method for producing an oligosaccharide of the present invention, which has been made to achieve the above-mentioned object, is a method of uniformly hydrolyzing partially deacetylated chitin with chitinase to give glucosamine having a high degree of polymerization. Hetero-oligosaccharides consisting of and N-acetylglucosamine and homo-oligosaccharides of glucosamine are obtained. Hydrolysis of chitin by chitinase is preferably performed inside the dialysis membrane, and at the same time, cation exchange resin is arranged outside the dialysis membrane to perform dialysis. The chitin used is preferably one obtained from crustaceans or filamentous fungi.

【0008】均一に部分脱アセチル化されたキチンは、
N−アセチルグルコサミン残基が分子中に均一に分布し
たものであればよく、脱アセチル化の割合は70〜95
%程度、特に80〜90%が好ましい。
Chitin, which is uniformly partially deacetylated, is
It is sufficient that the N-acetylglucosamine residues are evenly distributed in the molecule, and the deacetylation ratio is 70 to 95.
%, Especially 80 to 90% is preferable.

【0009】キチンを均一に部分脱アセチル化する方法
としては、甲殻類のキチンであればキチン粉末を高濃度
のアルカリ溶液に溶解してアルカリキチンとして部分脱
アセチル化を行う(T.Sannan et.al.,Makromal.Chem.,1
77,3589-3600,1976 )。糸状菌のキチンは、菌体をアル
カリ処理した後、酢酸抽出を行えば脱アセチル化された
キチンが調整できる(小林丘ら、日本農芸化学会誌、6
2 10、1988)。甲殻類のキチンよりも糸状菌のキチンの
方が調整法としては容易である。甲殻類のキチンは部分
脱アセチル化の際にアルカリキチンにすることが煩雑で
あり、高濃度のアルカリ廃液の処理が面倒である(キチ
ン、キトサン研究会編、キチン、キトサン実験マニュア
ル、技報堂出版、16-21、1991) 。
As a method for uniformly partially deacetylating chitin, in the case of shellfish chitin, chitin powder is dissolved in a high-concentration alkaline solution to carry out partial deacetylation as alkaline chitin (T. Sannan et. al., Makromal. Chem., 1
77, 3589-3600 , 1976). For filamentous fungus chitin, deacetylated chitin can be prepared by subjecting the bacterial cells to alkali treatment and then extracting with acetic acid (Kobayashioka et al., Journal of the Japan Society for Agricultural Chemistry, 6
2 , 10 , 1988). Filamentous fungus chitin is easier to prepare than crustacean chitin. It is cumbersome to make chitin of crustacean into alkaline chitin at the time of partial deacetylation, and it is troublesome to treat a high-concentration alkaline waste solution (chitin, chitosan study group edition, chitin, chitosan experimental manual, Gihodo Publishing, 16-21, 1991).

【0010】キチナーゼは、部分脱アセチル化キチン分
子中のN−アセチルグルコサミン残基を認識し分解する
エンド型キチナーゼであれば良く、できればキトビアー
ゼ(β−N−アセチルグルコサミナーゼ)活性を除去し
た精製品が好ましい。前記キチナーゼとしては、例えば
寶酒造製のトリコデルマ sp.AF6-T8 (Trichodermasp.AF
6-T8)、シグマ ケミカル社(SIGMA CHEMICAL COMPAN
Y)製のストレプトミセス グリソイス( Streptomyces
griseus )が挙げられる。
The chitinase may be an endo-type chitinase that recognizes and decomposes N-acetylglucosamine residues in a partially deacetylated chitin molecule, and if possible, a chitobiase (β-N-acetylglucosaminase) activity-removed purified enzyme. Products are preferred. Examples of the chitinase include Trichoderma sp.AF6-T8 (Trichoderma sp.AF) manufactured by Takara Shuzo.
6-T8), SIGMA CHEMICAL COMPAN
Y) Streptomyces
griseus).

【0011】透析膜は分画分子量が1000〜1500
0程度、特に2000〜8000が好ましい。市販品で
は、例えばスペクトラ/ピーオーアール(SPECTR
A/POR)社製の透析膜が挙げられる。
The dialysis membrane has a molecular weight cutoff of 1000 to 1500.
About 0, especially 2000 to 8000 is preferable. With commercial products, for example, SPECTRA / PORTR
A / POR) dialysis membrane.

【0012】陽イオン交換樹脂は、予めH+ のイオンに
変えた強酸性型であれば良い。市販品としては、例えば
ダウ ケミカル社(DOW CHEMICAL COMPANY)製のDOW
EX50WやDOWEX HGRが挙げられる。
The cation exchange resin may be a strong acid type which has been converted into H + ions in advance. Examples of commercially available products include DOW manufactured by DOW CHEMICAL COMPANY.
EX50W and DOWEX HGR are mentioned.

【0013】[0013]

【作用】部分脱アセチル化キチンはN−アセチルグルコ
サミン残基が分子中に均一に分布し、キチナーゼがN−
アセチルグルコサミン残基の部分を優先的に切断するた
め、効率よく高重合度のオリゴ糖を得ることができる。
[Function] In partially deacetylated chitin, N-acetylglucosamine residues are uniformly distributed in the molecule, and chitinase is N-.
Since the portion of the acetylglucosamine residue is preferentially cleaved, an oligosaccharide having a high degree of polymerization can be efficiently obtained.

【0014】また、透析膜の内部で加水分解しながら透
析膜外部に陽イオン交換樹脂を配置して透析を行うと、
より効率的に加水分解でき、加水分解終了後の処理を省
くことができる。
When cation exchange resin is placed outside the dialysis membrane while performing hydrolysis while hydrolyzing inside the dialysis membrane,
The hydrolysis can be carried out more efficiently, and the treatment after completion of the hydrolysis can be omitted.

【0015】[0015]

【実施例】以下、本発明の実施例を説明するが、これに
限定されるものではない。
EXAMPLES Examples of the present invention will be described below, but the invention is not limited thereto.

【0016】キチンを均一に部分脱アセチル化した後、
これを乳酸に溶解して均一に溶解する。乳酸は、部分脱
アセチル化キチン1gに対して、2〜20容積%好まし
くは5〜10容積%の乳酸を20〜200ml好ましく
は60〜100ml加える。前記溶液をアセトンに滴下
すると、部分脱アセチル化キチン乳酸塩がゲル状沈殿物
として生成する。アセトンは前記溶液100ml当たり
900ml以上使用するのが好ましい。生成したゲル状
沈殿物を濾過し、アセトンで数回洗浄を行って乳酸を完
全に除去した後、減圧で乾燥し、部分脱アセチル化キチ
ン乳酸塩を得る。
After partially deacetylating the chitin uniformly,
This is dissolved in lactic acid and dissolved uniformly. As for lactic acid, 20 to 200 ml, preferably 60 to 100 ml of lactic acid of 2 to 20% by volume, preferably 5 to 10% by volume is added to 1 g of partially deacetylated chitin. When the solution is dropped into acetone, partially deacetylated chitin lactate is produced as a gel-like precipitate. Acetone is preferably used in an amount of 900 ml or more per 100 ml of the solution. The produced gel-like precipitate is filtered, washed with acetone several times to completely remove lactic acid, and then dried under reduced pressure to obtain partially deacetylated chitin lactate.

【0017】得られた部分脱アセチル化キチン乳酸塩を
水に溶解し、0.1〜1重量%の水溶液とする。前記乳
酸塩水溶液にキチナーゼを添加し、20〜50℃で24
時間以上加水分解を行う。キチナーゼは、乳酸塩水溶液
10ml中に1〜10ユニット(units)のキチナ
ーゼを含む濃度に調整し、前記濃度のキチナーゼ水溶液
は乳酸塩水溶液の容積の1/500〜1/10倍を添加
する。加水分解を24時間以上行った後、熱処理により
加水分解を停止し、反応液からキチナーゼを限外濾過で
除去する。
The partially deacetylated chitin lactate obtained is dissolved in water to give an aqueous solution of 0.1 to 1% by weight. Add chitinase to the aqueous lactate solution and add 24 at 20-50 ° C.
Hydrolyze for more than an hour. The chitinase is adjusted to a concentration containing 1 to 10 units (units) of chitinase in 10 ml of the aqueous lactate solution, and 1/500 to 1/10 times the volume of the aqueous lactate solution is added to the chitinase aqueous solution having the above concentration. After the hydrolysis is performed for 24 hours or more, the hydrolysis is stopped by heat treatment, and the chitinase is removed from the reaction solution by ultrafiltration.

【0018】キチナーゼを除去した反応液は陽イオン交
換樹脂に吸着させた後、陽イオン交換樹脂を蒸留水で洗
浄し遊離した乳酸を除去する。樹脂に吸着した部分脱ア
セチル化キチンの加水分解物は希塩酸で溶出し、蒸発乾
固する。生成物質はグルコサミン及びN−アセチルグル
コサミンのヘテロオリゴ糖、及びグルコサミンのホモオ
リゴ糖の塩酸塩である。
The reaction solution from which chitinase has been removed is adsorbed on a cation exchange resin, and then the cation exchange resin is washed with distilled water to remove free lactic acid. The partially deacetylated chitin hydrolyzate adsorbed on the resin is eluted with dilute hydrochloric acid and evaporated to dryness. The products are glucosamine and N-acetylglucosamine heterooligosaccharides, and glucosamine homooligosaccharide hydrochlorides.

【0019】また、透析膜内部で加水分解を行う場合
は、キチナーゼを添加した部分脱アセチル化キチン乳酸
塩水溶液を透析膜の内部に入れ、透析膜の外側から陽イ
オン交換樹脂を分散した蒸留水で透析しながら、前記と
同様に20〜50℃で加水分解を24時間以上行う。蒸
留水に分散する陽イオン交換樹脂は、部分脱アセチル化
キチン乳酸塩100mg当たり陽イオン交換樹脂10〜
50mlの割合である。透析に使用する陽イオン交換樹
脂を分散した蒸留水の容量は、キチナーゼを添加した乳
酸塩水溶液の容量の10〜100倍であることが好まし
い。加水分解を24時間以上行った後、透析膜外側の陽
イオン交換樹脂を集めて蒸留水で洗浄後、分解物を希塩
酸で溶出し蒸発乾固する。前記と同様にグルコサミン及
びN−アセチルグルコサミンのヘテロオリゴ糖、及びグ
ルコサミンのホモオリゴ糖の塩酸塩が生成する。
When hydrolysis is carried out inside the dialysis membrane, a partially deacetylated chitin lactate aqueous solution containing chitinase is put inside the dialysis membrane, and distilled water in which a cation exchange resin is dispersed from the outside of the dialysis membrane. Hydrolysis is carried out for 24 hours or more at 20 to 50 ° C in the same manner as described above while dialyzing with. The cation exchange resin dispersed in distilled water is 10 to 10 parts of the cation exchange resin per 100 mg of partially deacetylated chitin lactate.
It is a ratio of 50 ml. The volume of distilled water in which the cation exchange resin used for dialysis is dispersed is preferably 10 to 100 times the volume of the aqueous lactate solution containing chitinase. After hydrolysis for 24 hours or more, the cation exchange resin on the outside of the dialysis membrane is collected and washed with distilled water, and then the decomposed product is eluted with dilute hydrochloric acid and evaporated to dryness. Glucosamine and N-acetylglucosamine heterooligosaccharides and glucosamine homooligosaccharide hydrochlorides are produced in the same manner as described above.

【0020】実施例1 甲殻類のキチン市販試薬(和光純薬製)を T.San
nan et.al.,Makromol.Che
m.,177,3589−3600,1976に記載の
方法で部分脱アセチル化を行う。得られた脱アセチル化
度が87%の部分脱アセチル化キチン2.0gを5容積
%の乳酸160mlに加えて均一に溶解する。前記溶液
を1800mlのアセトンに滴下して部分脱アセチル化
キチン乳酸塩の沈殿物を生成し、これを500ミクロン
のふるいで濾過した。回収した部分脱アセチル化キチン
乳酸塩は減圧下、室温で乾燥した。収量は2.02gで
あった。
Example 1 A commercially available reagent for chitin of crustacean (manufactured by Wako Pure Chemical Industries, Ltd.) was used. San
nan et. al. , Makromol. Che
m. , 177, 3589-3600 , 1976 for partial deacetylation. 2.0 g of the partially deacetylated chitin having a deacetylation degree of 87% thus obtained is added to 160 ml of 5% by volume lactic acid and uniformly dissolved. The solution was added dropwise to 1800 ml of acetone to form a partially deacetylated chitin lactate precipitate, which was filtered through a 500 micron sieve. The recovered partially deacetylated chitin lactate was dried at room temperature under reduced pressure. The yield was 2.02g.

【0021】得られた部分脱アセチル化キチン乳酸塩1
00.0mgを14.6mlの蒸留水に溶解し、20unit
s/mlのキチナーゼ(寶酒造製、Trichoderma sp.AF6-T8、
活性10units/mg) の水溶液を400μl加え、37℃で
加水分解反応を行った。48時間加水分解した後、90℃
で5分間熱処理を行って反応を停止する。反応液は分離
分子量20000の限外濾過によりキチナーゼを除去し
た後、陽イオン交換樹脂(バイオ−ラッド(Bio-Rad )
社製、AG50W−X8、H+ 型)30mlに吸着させ
る。樹脂を蒸留水で洗浄後、5.5規定の塩酸で溶出
し、溶出液は40℃でエバポレータにより蒸発乾固した。
63.0mgの分解物の塩酸塩が得られ、収率78%で
あった。
The partially deacetylated chitin lactate obtained 1
Dissolve 00.0 mg in 14.6 ml distilled water and add 20 units.
s / ml chitinase (Taboo Shuzo, Trichoderma sp.AF6-T8,
400 μl of an aqueous solution having an activity of 10 units / mg) was added, and a hydrolysis reaction was carried out at 37 ° C. After hydrolysis for 48 hours, 90 ℃
Then, heat treatment is performed for 5 minutes to stop the reaction. After removing the chitinase from the reaction solution by ultrafiltration with a molecular weight of 20000, a cation exchange resin (Bio-Rad) was used.
(Manufactured by AG50W-X8, H + type). The resin was washed with distilled water and eluted with 5.5 N hydrochloric acid, and the eluate was evaporated to dryness at 40 ° C with an evaporator.
63.0 mg of the hydrolyzate of the decomposition product was obtained, and the yield was 78%.

【0022】得られた分解物の塩酸塩を高性能液体クロ
マトグラフィ(以下、HPLCと記す)で分析した結果
を図1に示す。図中における各グルコサミンオリゴ糖塩
酸塩(GlcN.HCln :nは2〜6の整数、実施例
2以下も同様に示す)の位置は各々、以下の市販試薬で
決定した。キトビアーゼ ヒドロクロライド、キトトリ
オース ヒドロクロライド、キトテトラーゼ ヒドロク
ロライド、キトペンタオーゼ ヒドロクロライド、キト
ヘキサオース ヒドロクロライド(ChitobioseHydrochl
oride, Chitotriose Hydrochloride, Chitotetraose Hy
drochloride,Chitopentaose Hydrochloride, Chitohexa
ose Hydrochloride,生化学工業製)。
FIG. 1 shows the results of high performance liquid chromatography (hereinafter referred to as HPLC) analysis of the hydrochloride of the obtained decomposition product. The position of each glucosamine oligosaccharide hydrochloride (GlcN.HCl n : n is an integer of 2 to 6, the same applies to Example 2 and the following) in the figure was determined by the following commercially available reagents. Chitobiase Hydrochloride, Chitotriose Hydrochloride, Chitotetolase Hydrochloride, Chitopentaose Hydrochloride, Chitohexaose Hydrochloride
oride, Chitotriose Hydrochloride, Chitotetraose Hy
drochloride, Chitopentaose Hydrochloride, Chitohexa
ose Hydrochloride, manufactured by Seikagaku Corporation).

【0023】分解物のうちグルコサミン及びN−アセチ
ルグルコサミンのヘテロオリゴ糖は直接に分析できない
ため、分解物の塩酸塩全体をN−アセチル化し、N−ア
セチルグルコサミンオリゴ糖として重合度を調べた。分
解物の塩酸塩をN−アセチル化する反応は、トリエチル
アミンを添加した蒸留水−メタノール混合溶媒中で、分
解物塩酸塩を無水酢酸と反応させて行った。得られたN
−アセチル化物のHPLCによる分析結果を図2に示
す。図中でGlcNAcn (nは1〜8の整数)は、重
合度が1〜8である各々のN−アセチルグルコサミンオ
リゴ糖を表す(実施例2以下も同様に示す)。
Among the degradation products, the heterooligosaccharides of glucosamine and N-acetylglucosamine cannot be directly analyzed. Therefore, the entire hydrochloride of the degradation product was N-acetylated, and the degree of polymerization was examined as N-acetylglucosamine oligosaccharides. The reaction for N-acetylating the hydrochloride of the decomposition product was carried out by reacting the hydrochloride of the decomposition product with acetic anhydride in a mixed solvent of distilled water-methanol containing triethylamine. Obtained N
-The analysis result of the acetylated product by HPLC is shown in FIG. In the figure, GlcNAc n (n is an integer of 1 to 8) represents each N-acetylglucosamine oligosaccharide having a degree of polymerization of 1 to 8 (the same applies to Example 2 and the following).

【0024】更に、図2の分析結果をN−アセチルグル
コサミンオリゴ糖標準試薬の検量線法により分析し、分
解物中の各オリゴ糖の重量割合を求めた。結果は図3に
示す。図3より分解物中において重合度が4以上のオリ
ゴ糖の割合は65%で、重合度が5以上のオリゴ糖の割
合は36%であり、高重合度のオリゴ糖が効率よく製造
できたといえる。
Further, the analysis results of FIG. 2 were analyzed by a calibration curve method of N-acetylglucosamine oligosaccharide standard reagent to determine the weight ratio of each oligosaccharide in the decomposed product. The results are shown in Figure 3. As shown in FIG. 3, the ratio of oligosaccharides having a degree of polymerization of 4 or more in the decomposed product was 65%, and the ratio of oligosaccharides having a degree of polymerization of 5 or more was 36%, indicating that oligosaccharides having a high degree of polymerization could be efficiently produced. I can say.

【0025】実施例2 実施例1で調整した部分脱アセチル化キチン乳酸塩100.
07mgを14.6mlの蒸留水に溶解し、実施例1と同じキチナ
ーゼで濃度が20units/mlの水溶液を400μl加えた。
この溶液を分画分子量が8000の透析チューブ(SPEC
TRA/POR 社製、NO.132116 )に入れ、透析チューブの外
部から実施例1と同じ陽イオン交換樹脂20mlを分散
させた蒸留水200mlで透析を行いながら、37℃で
加水分解を行った。48時間加水分解した後、透析チュ
ーブの外部にある陽イオン交換樹脂を回収し、樹脂を蒸
留水で洗浄する。樹脂に吸着した分解物を5.5規定の
塩酸で溶出し、溶出液は40℃でエバポレータにより蒸発
乾固する。49.3mgの分解物塩酸塩が得られ、収率
61%であった。
Example 2 Partially deacetylated chitin lactate 100 prepared in Example 1.
07 mg was dissolved in 14.6 ml of distilled water, and 400 μl of the same chitinase as in Example 1 and a concentration of 20 units / ml was added.
A dialysis tube with a molecular weight cut off of 8000 (SPEC
TRA / POR manufactured by NO.132116), and hydrolyzed at 37 ° C. while dialyzing from outside the dialysis tube with 200 ml of distilled water in which 20 ml of the same cation exchange resin as in Example 1 was dispersed. After hydrolyzing for 48 hours, the cation exchange resin outside the dialysis tube is collected and the resin is washed with distilled water. The decomposition product adsorbed on the resin is eluted with 5.5N hydrochloric acid, and the eluate is evaporated to dryness at 40 ° C with an evaporator. 49.3 mg of decomposition product hydrochloride was obtained, and the yield was 61%.

【0026】得られた分解物塩酸塩のHPLCによる分
析結果を図4に示す。図中のグルコサミンオリゴ糖の塩
酸塩の位置は、実施例1と同じ試薬で決定した。
The results of HPLC analysis of the obtained decomposition product hydrochloride are shown in FIG. The position of the glucosamine oligosaccharide hydrochloride in the figure was determined using the same reagents as in Example 1.

【0027】実施例1と同様にして分解物をN−アセチ
ル化し、N−アセチルグルコサミンオリゴ糖をHPLC
により分析した結果を図5に示す。図5の結果をN−ア
セチルグルコサミンオリゴ糖標準試薬の検量線法により
分析し、分解物中の各オリゴ糖の重量割合を求めた。結
果は図6に示す。
The degradation product was N-acetylated in the same manner as in Example 1, and the N-acetylglucosamine oligosaccharide was analyzed by HPLC.
The result of the analysis is shown in FIG. The results of FIG. 5 were analyzed by the calibration curve method of the N-acetylglucosamine oligosaccharide standard reagent to determine the weight ratio of each oligosaccharide in the decomposed product. The results are shown in Figure 6.

【0028】実施例1と比較すると分解物塩酸塩の収量
は61%に減少したが、分解物中において重合度が4以
上のオリゴ糖の割合は67%、重合度が5以上のオリゴ
糖の割合は47%であり、高重合度オリゴ糖の割合が高
くなった。従って、透析膜を使用することでより効率的
に高重合度オリゴ糖が製造できたといえる。
Compared with Example 1, the yield of hydrolyzate as a degradation product was reduced to 61%, but the proportion of oligosaccharides having a degree of polymerization of 4 or more in the degradation product was 67%, and that of oligosaccharides having a degree of polymerization of 5 or more was 67%. The proportion was 47%, and the proportion of high-polymerization degree oligosaccharides was high. Therefore, it can be said that by using the dialysis membrane, the highly polymerized oligosaccharide could be produced more efficiently.

【0029】実施例3 糸状菌(アブシディア コエルレア(Absidia coerule
a):IFO NO.5301) を用いて小林丘らにより日本農芸化
学会誌、62、10、1988に記載された方法で、脱アセチル化
度が86%の部分脱アセチル化キチンを得た。前記部分
脱アセチル化キチン0.81gを5容積%の乳酸80mlに
加えて均一に溶解し、この溶液を720ml のアセトンに滴
下して糸状菌の部分脱アセチル化キチン乳酸塩の沈殿物
を生成する。沈殿物を500 ミクロンのふるいで濾過し、
減圧下、室温で乾燥した。1.01g の部分脱アセチル化キ
チン乳酸塩が得られた。
Example 3 Filamentous fungus (Absidia coerule
a): IFO NO.5301) was used to obtain partially deacetylated chitin with a degree of deacetylation of 86% by the method described by Kobayashioka et al., Journal of Japan Society of Agricultural Chemistry, 62, 10 , 1988. 0.81 g of the partially deacetylated chitin was added to 80 ml of 5% by volume lactic acid and uniformly dissolved, and the solution was added dropwise to 720 ml of acetone to form a precipitate of partially deacetylated chitin lactate of filamentous fungi. . Filter the precipitate through a 500 micron sieve,
It was dried at room temperature under reduced pressure. 1.01 g of partially deacetylated chitin lactate was obtained.

【0030】糸状菌の部分脱アセチル化キチン乳酸塩1
00.09mgを14.6mlの蒸留水に溶解し、20un
its/mlの実施例1と同じキチナーゼの水溶液を400μ
l加えて37℃で加水分解を行った。48時間の加水分解
後、90℃で5分間の熱処理で加水分解を停止し、分離
分子量20000の限外濾過によりキチナーゼを除去し
た。キチナーゼを除去した溶液を実施例1と同じ陽イオ
ン交換樹脂30mlに吸着させた後、蒸留水で洗浄し
た。樹脂に吸着した分解物を5.5規定の塩酸で溶出
し、溶出液を40℃でエバポレータにより蒸発乾固し
た。分解物の塩酸塩が43.5mgが得られ、収率は5
4%であった。
Partial deacetylated chitin lactate of filamentous fungi 1
Dissolve 0.09 mg in 14.6 ml distilled water and add 20un
400 μl of its / ml chitinase solution in Example 1
1 was added and hydrolysis was carried out at 37 ° C. After the hydrolysis for 48 hours, the hydrolysis was stopped by heat treatment at 90 ° C. for 5 minutes, and the chitinase was removed by ultrafiltration with a molecular weight of 20000. The solution from which chitinase had been removed was adsorbed on 30 ml of the same cation exchange resin as in Example 1 and then washed with distilled water. The decomposition product adsorbed on the resin was eluted with 5.5 N hydrochloric acid, and the eluate was evaporated to dryness at 40 ° C. with an evaporator. The hydrolyzate of the decomposition product was 43.5 mg, and the yield was 5
It was 4%.

【0031】得られた分解物の塩酸塩をHPLCで分析
し、図7はその結果である。図中のグルコサミンオリゴ
糖の塩酸塩の位置は、実施例1と同じ試薬によって決定
した。
The hydrochloride of the obtained decomposition product was analyzed by HPLC, and FIG. 7 shows the result. The position of the hydrochloride of glucosamine oligosaccharide in the figure was determined by the same reagent as in Example 1.

【0032】実施例1と同様にして分解物をN−アセチ
ル化し、N−アセチルグルコサミンオリゴ糖をHPLC
により分析した結果を図8に示す。図8の結果をN−ア
セチルグルコサミンオリゴ糖標準試薬の検量線法により
分析し、分解物中の各オリゴ糖の重量割合を求めた。結
果は図9に示す。図9に示す通り、分解物中における重
合度が4以上のオリゴ糖の割合は67%、重合度が5以
上のオリゴ糖の割合は40%であり、この割合は実施例
1以上である。
The degradation product was N-acetylated in the same manner as in Example 1, and the N-acetylglucosamine oligosaccharide was analyzed by HPLC.
The result of the analysis is shown in FIG. The results of FIG. 8 were analyzed by the calibration curve method of the N-acetylglucosamine oligosaccharide standard reagent to determine the weight ratio of each oligosaccharide in the decomposed product. The results are shown in Figure 9. As shown in FIG. 9, the ratio of oligosaccharides having a degree of polymerization of 4 or more in the decomposed product was 67%, the ratio of oligosaccharides having a degree of polymerization of 5 or more was 40%, and this ratio was in Example 1 or more.

【0033】実施例4 実施例3で使用した糸状菌の部分脱アセチル化キチン乳
酸塩100.04mgを14.6mlの蒸留水に溶解
し、濃度が20units/mlの実施例1で使用したキチナーゼ
の水溶液を400μl加えた。前記溶液を分画分子量8
000の透析チューブ(SPECTRA/POR 社製、NO.13211
6)に入れ、透析チューブの外側から実施例1と同じ陽
イオン交換樹脂20mlを分散させた蒸留水200mlで透
析を行いながら、37℃で加水分解を行った。48時間
の加水分解後、透析膜外部の陽イオン交換樹脂を回収し
蒸留水で洗浄した。樹脂に吸着した分解物を5.5規定
の塩酸で溶出し、溶出液を40℃でエバポレータにより
蒸発乾固した。24.8mgの分解物塩酸塩が得られ、
収率は31%であった。
Example 4 100.04 mg of the partially deacetylated chitin lactate of the filamentous fungus used in Example 3 was dissolved in 14.6 ml of distilled water to obtain the chitinase used in Example 1 at a concentration of 20 units / ml. 400 μl of the aqueous solution was added. The solution was cut to a molecular weight of 8
000 dialysis tubing (SPECTRA / POR, NO.13211
The solution was placed in 6) and hydrolyzed at 37 ° C. while dialyzing from the outside of the dialysis tube with 200 ml of distilled water in which 20 ml of the same cation exchange resin as in Example 1 was dispersed. After hydrolysis for 48 hours, the cation exchange resin outside the dialysis membrane was collected and washed with distilled water. The decomposition product adsorbed on the resin was eluted with 5.5 N hydrochloric acid, and the eluate was evaporated to dryness at 40 ° C. with an evaporator. 24.8 mg of hydrolyzate hydrochloride were obtained,
The yield was 31%.

【0034】得られた分解物塩酸塩をHPLCにより分
析した結果を図10に示す。図中のグルコサミンオリゴ
糖の塩酸塩の位置は実施例1と同じ試薬により決定し
た。
The result of HPLC analysis of the obtained hydrolyzate of the decomposition product is shown in FIG. The position of the hydrochloride of glucosamine oligosaccharide in the figure was determined by the same reagent as in Example 1.

【0035】実施例1と同様にして分解物をN−アセチ
ル化し、N−アセチルグルコサミンオリゴ糖をHPLC
により分析した結果を図11に示す。図11の結果をN
−アセチルグルコサミンオリゴ糖標準試薬の検量線法に
より分析し、分解物中の各オリゴ糖の重量割合を求め
た。結果は図12に示す。
The degradation product was N-acetylated in the same manner as in Example 1, and the N-acetylglucosamine oligosaccharide was analyzed by HPLC.
The result of analysis by is shown in FIG. The result of FIG.
-Acetylglucosamine oligosaccharide standard analysis was performed by a calibration curve method to determine the weight ratio of each oligosaccharide in the degradation product. Results are shown in FIG.

【0036】実施例3と比較すると分解物塩酸塩の収量
が31%に減少したが、図12に示す通り分解物中にお
ける重合度が4以上のオリゴ糖の割合は68%、重合度
が5以上のオリゴ糖の割合は45%である。従って、透
析膜を使用することで、より効率的に高重合度のオリゴ
糖を生成することができた。
Compared with Example 3, the yield of the hydrolyzate of the degradation product was reduced to 31%, but as shown in FIG. 12, the ratio of oligosaccharides having a degree of polymerization of 4 or more in the degradation product was 68% and the degree of polymerization was 5%. The ratio of the above oligosaccharides is 45%. Therefore, by using the dialysis membrane, oligosaccharides having a high degree of polymerization could be produced more efficiently.

【0037】[0037]

【発明の効果】以上、詳細に説明したように本発明のオ
リゴ糖の製造方法でキチンを分解すれば、確実に生理活
性が高い高重合度のオリゴ糖を得ることができる。ま
た、加水分解するときに透析膜を使用すれば、より簡単
で効率的に高重合度のオリゴ糖を得ることができる。従
って、簡単に入手できるキチンから生理活性が高いオリ
ゴ糖が得られるので、医療等の研究にも大いに有用であ
る。
As described above in detail, if chitin is decomposed by the method for producing an oligosaccharide of the present invention, an oligosaccharide having a high degree of polymerization and a high physiological activity can be reliably obtained. Further, if a dialysis membrane is used during hydrolysis, an oligosaccharide having a high degree of polymerization can be obtained more easily and efficiently. Therefore, oligosaccharides having high physiological activity can be obtained from easily obtainable chitin, which is also very useful for medical research.

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

【図1】実施例1のグルコサミンオリゴ糖塩酸塩の分析
結果を表す図。
FIG. 1 is a diagram showing the analysis results of glucosamine oligosaccharide hydrochloride of Example 1.

【図2】実施例1のN−アセチル化オリゴ糖の分析結果
を表す図。
FIG. 2 is a view showing the analysis result of N-acetylated oligosaccharides of Example 1.

【図3】実施例1のキチン分解物の各オリゴ糖の重量割
合を表す図。
FIG. 3 is a view showing the weight ratio of each oligosaccharide of the degradation product of chitin of Example 1.

【図4】実施例2のグルコサミンオリゴ糖塩酸塩の分析
結果を表す図。
FIG. 4 is a view showing the analysis result of glucosamine oligosaccharide hydrochloride of Example 2.

【図5】実施例2のN−アセチル化オリゴ糖の分析結果
を表す図。
FIG. 5 shows the analysis results of N-acetylated oligosaccharides of Example 2.

【図6】実施例2のキチン分解物の各オリゴ糖の重量割
合を表す図。
FIG. 6 is a view showing the weight ratio of each oligosaccharide of the degradation product of chitin of Example 2.

【図7】実施例3のグルコサミンオリゴ糖塩酸塩の分析
結果を表す図。
FIG. 7 is a diagram showing the analysis result of glucosamine oligosaccharide hydrochloride of Example 3.

【図8】実施例3のN−アセチル化オリゴ糖の分析結果
を表す図。
FIG. 8 shows the analysis results of N-acetylated oligosaccharides of Example 3.

【図9】実施例3のキチン分解物の各オリゴ糖の重量割
合を表す図。
FIG. 9 is a view showing the weight ratio of each oligosaccharide of the degradation product of chitin of Example 3.

【図10】実施例4のグルコサミンオリゴ糖塩酸塩の分
析結果を表す図。
FIG. 10 shows the analysis results of glucosamine oligosaccharide hydrochloride of Example 4.

【図11】実施例4のN−アセチル化オリゴ糖の分析結
果を表す図。
FIG. 11 shows the analysis results of N-acetylated oligosaccharides of Example 4.

【図12】実施例4のキチン分解物の各オリゴ糖の重量
割合を表す図。
FIG. 12 is a view showing the weight ratio of each oligosaccharide of the degradation product of chitin of Example 4.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 千葉 徹 神奈川県川崎市高津区坂戸100−1 信越 化学工業株式会社コーポレートリサーチセ ンター内 (72)発明者 渡辺 公綱 東京都渋谷区恵比寿南3−11−17−308   ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Toru Chiba             Shin-Etsu 100-1 Sakado, Takatsu-ku, Kawasaki, Kanagawa Prefecture             Chemical Industry Co., Ltd. Corporate Research Center             In the center (72) Inventor Watanabe Kotsuna             3-11-17-308, Ebisu Minami, Shibuya-ku, Tokyo

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 均一に部分脱アセチル化されたキチンを
キチナーゼにより加水分解して高重合度のグルコサミン
及びN−アセチルグルコサミンからなるヘテロオリゴ
糖、及びグルコサミンのホモオリゴ糖を得ることを特徴
とするオリゴ糖の製造方法。
1. An oligosaccharide characterized by obtaining a heterooligosaccharide composed of glucosamine and N-acetylglucosamine having a high degree of polymerization and a homooligosaccharide of glucosamine by hydrolyzing uniformly partially deacetylated chitin with chitinase. Manufacturing method.
【請求項2】 前記加水分解を透析膜の内部で行い、同
時に透析膜の外部に陽イオン交換樹脂を配置して透析を
行い、高重合度のグルコサミン及びN−アセチルグルコ
サミンからなるヘテロオリゴ糖、及びグルコサミンのホ
モオリゴ糖を得ることを特徴とする請求項1に記載のオ
リゴ糖の製造方法。
2. The hydrolysis is performed inside a dialysis membrane, and at the same time, a cation exchange resin is placed outside the dialysis membrane to perform dialysis, and a heterooligosaccharide composed of glucosamine and N-acetylglucosamine having a high degree of polymerization, and The method for producing an oligosaccharide according to claim 1, wherein a homooligosaccharide of glucosamine is obtained.
【請求項3】 前記キチンは甲殻類、または糸状菌から
得られることを特徴とする請求項1に記載のオリゴ糖の
製造方法。
3. The method for producing an oligosaccharide according to claim 1, wherein the chitin is obtained from crustaceans or filamentous fungi.
JP16184091A 1991-07-02 1991-07-02 Method for producing oligosaccharide Expired - Fee Related JP2810255B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16184091A JP2810255B2 (en) 1991-07-02 1991-07-02 Method for producing oligosaccharide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16184091A JP2810255B2 (en) 1991-07-02 1991-07-02 Method for producing oligosaccharide

Publications (2)

Publication Number Publication Date
JPH057496A true JPH057496A (en) 1993-01-19
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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5998173A (en) * 1996-02-20 1999-12-07 The University Of Bristish Columbia Process for producing N-acetyl-D-glucosamine
WO2002044397A1 (en) * 2000-12-01 2002-06-06 Kabushiki Kaisha Hayashibara Seibutsu Kagaku Kenkyujo Process for producing substance positive in elson-morgan reaction and use thereof
KR100483847B1 (en) * 2002-07-11 2005-04-20 주식회사 건풍바이오 The chitin/chitosan oligosaccharide which mitigating the cold symptoms of hands and foot
WO2005056525A3 (en) * 2003-12-09 2005-10-13 Bio Tech Resources Deacetylation of n-acetylglucosamine
KR100735826B1 (en) * 2005-09-30 2007-07-06 주식회사 키토라이프 Preparation Method of N-Acetyl-D-Glucosamine Using Enzyme Degradation
JP2012031107A (en) * 2010-07-30 2012-02-16 Koyo Chemical Kk Method for producing hetero disaccharide, chitobiose, and di-n-acetyl chitobiose, and their applications
CN103913532A (en) * 2014-04-14 2014-07-09 南京林业大学 Method for measuring N-acetylglucosamine by utilizing ion exchange chromatography

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5998173A (en) * 1996-02-20 1999-12-07 The University Of Bristish Columbia Process for producing N-acetyl-D-glucosamine
AU723674B2 (en) * 1996-02-20 2000-08-31 University Of British Columbia, The Process for producing N-acetyl-D-glucosamine
WO2002044397A1 (en) * 2000-12-01 2002-06-06 Kabushiki Kaisha Hayashibara Seibutsu Kagaku Kenkyujo Process for producing substance positive in elson-morgan reaction and use thereof
KR100483847B1 (en) * 2002-07-11 2005-04-20 주식회사 건풍바이오 The chitin/chitosan oligosaccharide which mitigating the cold symptoms of hands and foot
WO2005056525A3 (en) * 2003-12-09 2005-10-13 Bio Tech Resources Deacetylation of n-acetylglucosamine
KR100735826B1 (en) * 2005-09-30 2007-07-06 주식회사 키토라이프 Preparation Method of N-Acetyl-D-Glucosamine Using Enzyme Degradation
JP2012031107A (en) * 2010-07-30 2012-02-16 Koyo Chemical Kk Method for producing hetero disaccharide, chitobiose, and di-n-acetyl chitobiose, and their applications
CN103913532A (en) * 2014-04-14 2014-07-09 南京林业大学 Method for measuring N-acetylglucosamine by utilizing ion exchange chromatography

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