JPH06239902A - Production of high-purity chitin and chitosan - Google Patents
Production of high-purity chitin and chitosanInfo
- Publication number
- JPH06239902A JPH06239902A JP5271680A JP27168093A JPH06239902A JP H06239902 A JPH06239902 A JP H06239902A JP 5271680 A JP5271680 A JP 5271680A JP 27168093 A JP27168093 A JP 27168093A JP H06239902 A JPH06239902 A JP H06239902A
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- Prior art keywords
- hydrochloric acid
- chitin
- hours
- water
- temperature
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B37/00—Preparation of polysaccharides not provided for in groups C08B1/00 - C08B35/00; Derivatives thereof
- C08B37/0006—Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid
- C08B37/0024—Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid beta-D-Glucans; (beta-1,3)-D-Glucans, e.g. paramylon, coriolan, sclerotan, pachyman, callose, scleroglucan, schizophyllan, laminaran, lentinan or curdlan; (beta-1,6)-D-Glucans, e.g. pustulan; (beta-1,4)-D-Glucans; (beta-1,3)(beta-1,4)-D-Glucans, e.g. lichenan; Derivatives thereof
- C08B37/0027—2-Acetamido-2-deoxy-beta-glucans; Derivatives thereof
- C08B37/003—Chitin, i.e. 2-acetamido-2-deoxy-(beta-1,4)-D-glucan or N-acetyl-beta-1,4-D-glucosamine; Chitosan, i.e. deacetylated product of chitin or (beta-1,4)-D-glucosamine; Derivatives thereof
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- Molecular Biology (AREA)
- Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、キチン及びキトサンの
製造方法に関し、特にカニの甲殻から高分子量を有する
生体臨床医学用の高純度および高白色度キチンを製造す
る方法、および高脱アセチル化度を有する生体臨床医学
用の高分子量キトサンを製造する方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing chitin and chitosan, and more particularly to a method for producing high-purity and high-whiteness chitin having a high molecular weight from crab shells for biomedical use, and high deacetylation. The present invention relates to a method for producing a high molecular weight chitosan having a certain degree for biomedical treatment.
【0002】[0002]
【従来の技術】地球上で繊維素に次いで豊富に入手でき
る多糖類として、キチンは、甲殻類動物の甲殻から工業
的に抽出される高付加価値の生体高分子物質である。か
かるキチンは、水不溶性であるので活用するのに大きな
障害がある。したがって、キチンを脱アセチル化して、
水溶性であるキトサンへ転換され、かかる水溶性キトサ
ンは、工業的にキチンより有用である。Chitin is a high-value-added biopolymer substance industrially extracted from the shells of crustaceans as a polysaccharide which is the most abundant available on earth after fibrin. Since such chitin is insoluble in water, it is a great obstacle to use it. Therefore, deacetylating chitin,
It is converted to chitosan which is water-soluble, and such water-soluble chitosan is industrially more useful than chitin.
【0003】最近、カニ及びエビの大量漁獲によって水
産廃棄物である甲殻の処分に関心が高まるにつれて、甲
殻から抽出されたキチンの多様な用途に関して多くの研
究が行われている。初期には、これらのキチン及びキト
サンは、食品廃棄物から有効物質(例えば、蛋白など)
を回収するための凝集剤として主として用いられたが、
最近は、食品分野;医学分野;機能性膜、酵素及び微生
物の固定化担体などのような生物工学分野;化粧品分
野;農業分野;化学工学分野;環境保護分野などの各分
野で幅広く利用されている。キチンは通常、前処理、脱
蛋白及び脱ミネラル工程からなる方法により甲殻から製
造され、下記の構造式で示される。[0003] Recently, as interest in disposing of shellfish, which is a marine waste, has increased due to the large-scale catch of crabs and shrimp, much research has been conducted on various uses of chitin extracted from shellfish. Initially, these chitins and chitosans were found to be active substances (eg proteins) in food waste.
Was mainly used as a flocculant for recovering
Recently, it has been widely used in various fields such as food field, medical field, biotechnology field such as functional membrane, immobilization carrier for enzymes and microorganisms, cosmetic field, agricultural field, chemical engineering field, environmental protection field. There is. Chitin is usually produced from the shell by a method comprising pretreatment, deproteinization and demineralization steps and is represented by the following structural formula.
【0004】[0004]
【化1】 [Chemical 1]
【0005】キチンを製造するための公知方法として、
甲殻を洗浄して50℃の真空オーブン中で乾燥し;乾燥
した甲殻を粉砕して、10%NaOH溶液に室温で3日
間浸漬して脱蛋白し;脱蛋白した物質をアルカリ成分が
なくなるまで水洗した後、有機溶媒で数回洗浄し;得ら
れた白色生成物を減圧乾燥した後、37%塩酸水溶液中
に−20℃で4時間保持して粗キチンを得;粗キチンを
冷水および有機溶媒で洗浄し;冷塩酸溶液中での浸漬と
洗浄工程を繰返すウィスラー−ベミラー(Whistler & Be
miller) 法がある。Known methods for producing chitin include:
Wash the shell and dry it in a vacuum oven at 50 ° C; crush the dried shell and soak it in 10% NaOH solution at room temperature for 3 days to deproteinize; wash the deproteinized material with water until the alkaline component is gone After that, the product was washed several times with an organic solvent; the obtained white product was dried under reduced pressure and then kept in a 37% aqueous hydrochloric acid solution at -20 ° C for 4 hours to obtain crude chitin; Wash with cold hydrochloric acid solution and repeat washing process Whistler & Bemirror
miller) There is a method.
【0006】他の方法として、甲殻を洗浄して100℃
のオーブン中で乾燥し;乾燥した甲殻を2N塩酸溶液で
室温で5時間処理し;処理した甲殻を洗浄及び乾燥した
後微粉末に粉砕し、該微粉末を2N塩酸溶液で0℃で2
日間撹拌しながら抽出し;抽出したものを水で洗浄した
後、1NNaOH水溶液で100℃で12時間、撹拌し
ながら抽出し;このNaOH水溶液処理工程を4回以上
繰返すハックマン(Hackman) 法がある。一方、キトサン
は、不溶性キチンを脱アセチル化して得られ、下記構造
式で示される。As another method, the shell is washed and the temperature is 100 ° C.
Dried in an oven; treated dry shell with a 2N hydrochloric acid solution at room temperature for 5 hours; washed and dried the treated shell and then pulverized into a fine powder, and the fine powder was treated with a 2N hydrochloric acid solution at 0 ° C. for 2 hours.
There is a Hackman method in which the extract is washed with water, washed with water and then extracted with a 1N NaOH aqueous solution at 100 ° C. for 12 hours with stirring; this NaOH aqueous solution treatment step is repeated four times or more. On the other hand, chitosan is obtained by deacetylating insoluble chitin and is represented by the following structural formula.
【0007】[0007]
【化2】 [Chemical 2]
【0008】キトサンは、繊維素に存在する水酸基の一
つが有機アミノ基で置換されているので、化学的反応性
と化学的改質性において有利である。キトサンは、キチ
ンを一般に30〜50%のNaOH溶液で5〜20時間
脱アセチル化して容易に得られる。Chitosan has an advantage in chemical reactivity and chemical reformability because one of the hydroxyl groups present in the fibrin is substituted with an organic amino group. Chitosan is easily obtained by deacetylating chitin generally with 30-50% NaOH solution for 5-20 hours.
【0009】しかし、前述した従来のキチンの調製方法
は、蛋白及びCaCO3 の含量を減らすために、比較的
激しい反応条件下で行われる。即ち、ウィスラー−ベミ
ラー法の場合には、脱蛋白工程の後で脱CaCO3 工程
が行われるので、分子鎖の切断が増加して高分子量のキ
チンを得ることが困難であり、得られたキチンは、空気
中に放置すると、経時変色し、不純物の含量も高く、ま
た、−20℃の低温で脱CaCO3 工程を行うとして
も、高濃度の塩酸水溶液を用いるので、分子鎖が切断さ
れてしまう。また、ハックマン法の場合にも、脱CaC
O3 工程を塩酸水溶液処理を常温または10℃以上の温
度で行うので、分子鎖が切断されてしまう問題点があっ
た。However, the above-mentioned conventional method for preparing chitin is carried out under relatively vigorous reaction conditions in order to reduce the contents of protein and CaCO 3 . That is, in the case of the Whistler-Bemirer method, since the CaCO 3 removal step is performed after the deproteinization step, it is difficult to obtain a high molecular weight chitin due to an increase in the cleavage of the molecular chain. When it is left in the air, it discolors over time, has a high content of impurities, and even if the CaCO 3 removal step is carried out at a low temperature of −20 ° C., since a high-concentration hydrochloric acid aqueous solution is used, the molecular chain is broken. I will end up. Also, in the case of Hackman method, CaC removal
Since the O 3 process is carried out at room temperature or at a temperature of 10 ° C. or higher, there is a problem that the molecular chain is broken.
【0010】本発明者は、前述の問題点を解消し、高純
度及び高分子量の医薬及び食品用途に適するキチン及び
キトサンを得る方法について研究した結果、塩酸処理時
の処理温度を比較的低温にすることによって分子鎖の切
断を防ぎ、分子量が高くかつCaCO3 含量が低いキチ
ンを得、またNaOH溶液で処理時も、分子鎖の切断を
防ぐために不活性気体を注入しながら3時間ずつ2回処
理することによって、工程を簡素化し、時間を短縮し
た、本発明の方法を完成するに至った。The present inventor has studied the method for obtaining chitin and chitosan having high purity and high molecular weight, which are suitable for pharmaceutical and food applications, by solving the above-mentioned problems, and as a result, the treatment temperature during the hydrochloric acid treatment was relatively low. By doing so, chitin with a high molecular weight and a low CaCO 3 content is obtained by preventing the molecular chain from being cleaved, and even when treated with a NaOH solution, it is injected twice for 3 hours while injecting an inert gas to prevent the molecular chain from being cleaved. The treatment has led to the completion of the method of the invention, which simplifies the process and reduces the time.
【0011】[0011]
【発明が解決しようとする課題】本発明の目的は、高純
度、高分子量及び高白色度のキチンを得る方法を提供す
ることである。本発明のもう一つの目的は、得られたキ
チンから高分子量及び高脱アセチル化度のキトサンを製
造する方法を提供することである。The object of the present invention is to provide a method for obtaining chitin with high purity, high molecular weight and high whiteness. Another object of the present invention is to provide a method for producing chitosan having a high molecular weight and a high degree of deacetylation from the obtained chitin.
【0012】[0012]
【課題を解決するための手段】即ち、本発明は、(イ)
甲殻類の甲殻を乾燥した後粉砕して微粉末を得る工程、
(ロ)該微粉末を0.4〜3MのHCl溶液中、−10
〜10℃の温度で10〜25時間処理する一次塩酸処理
を施し、次いで10〜20℃の温度で2〜8時間浸漬す
る二次塩酸処理を施す工程、(ハ)塩酸処理した物質を
水洗し、ろ過し、有機溶媒で洗浄した後乾燥して粗キチ
ンを得る工程、(ニ)該粗キチンを2〜10重量%のN
aOH溶液に浸漬して加熱する工程、及び(ホ)前記N
aOH処理したキチンを水洗し、ろ過し、有機溶媒で洗
浄した後乾燥する工程からなる高純度キチンの製造方
法、並びに(a)前述方法により得られたキチンを、N
aOH溶液中、80〜100℃の温度で2〜12時間浸
漬して粗キトサンを得る工程、(b)該粗キトサンをろ
過し、水洗し、脱イオン水に浸漬し、ろ過して水混和性
有機溶媒の混合溶液に浸漬した後、ろ過及び乾燥する工
程を繰返す高純度キトサンの製造方法である。That is, the present invention provides (a)
Drying the crustacean crust and then crushing it to obtain a fine powder,
(B) The fine powder was -10 in a 0.4 to 3 M HCl solution.
A step of applying a primary hydrochloric acid treatment for 10 to 25 hours at a temperature of -10 ° C and then a secondary hydrochloric acid treatment for immersing at a temperature of 10 to 20 ° C for 2 to 8 hours, (c) washing the hydrochloric acid-treated substance with water Filtering, washing with an organic solvent and then drying to obtain crude chitin, (d) 2-10 wt% N of the crude chitin.
a step of heating by immersing in an aOH solution, and (e) the N
A method for producing high-purity chitin, which comprises a step of washing aOH-treated chitin with water, filtering, washing with an organic solvent and then drying, and (a) the chitin obtained by the above method
a step of immersing in an aOH solution at a temperature of 80 to 100 ° C. for 2 to 12 hours to obtain crude chitosan, (b) filtering the crude chitosan, rinsing with water, immersing in deionized water, filtering and miscibility with water It is a method for producing high-purity chitosan in which the steps of immersing in a mixed solution of an organic solvent, filtering and drying are repeated.
【0013】以下に、本発明をさらに詳しく説明する。
本発明による高純度キチンの製造方法は、下記三つの工
程からなる。The present invention will be described in more detail below.
The method for producing high-purity chitin according to the present invention comprises the following three steps.
【0014】前処理工程 まず、甲殻を40〜50℃の水中に30分〜1時間浸漬
して熱水処理を施して甲殻から肉質部分を効果的に分離
する。次いで、甲殻を水洗した後、脱水機で乾燥し、常
温でエタノール、メタノール、アセトン、テトラヒドロ
フラン(THF)、ジオキサンまたはメチルエチルケト
ン(MEK)などの有機溶媒中に一定時間、例えば、3
0分〜1時間浸漬した後、日陰で、水分含量が8〜12
%になるまで乾燥する。乾燥した甲殻を直ちに使用しな
い場合、乾燥した甲殻を涼しい場所で保管することが重
要である。保管状態が不良であると、保存時に腐敗して
分子量が低下して高品質のキチンが得られない。肉質が
除去された甲殻は、塩酸処理を効果的にするために粉砕
する。一般に、通常の粉砕機により0.5〜3mmまたは
200〜300メッシュの粗さに粉砕することが好まし
い。 Pretreatment Step First, the shell is dipped in water at 40 to 50 ° C. for 30 minutes to 1 hour and subjected to hot water treatment to effectively separate the fleshy portion from the shell. Then, the shell is washed with water and then dried with a dehydrator, and is kept in an organic solvent such as ethanol, methanol, acetone, tetrahydrofuran (THF), dioxane or methyl ethyl ketone (MEK) at room temperature for a certain time, for example, 3
After soaking for 0 minutes to 1 hour, in the shade, the water content is 8 to 12
Dry until%. If the dried shell is not used immediately, it is important to store the dried shell in a cool place. If the storage condition is poor, it will rot during storage and the molecular weight will decrease, making it impossible to obtain high-quality chitin. The crust from which meat is removed is crushed for effective treatment with hydrochloric acid. Generally, it is preferable to grind to a roughness of 0.5 to 3 mm or 200 to 300 mesh by a common grinder.
【0015】脱ミネラル工程 続いて、粉砕した甲殻(水分含量8〜12%)は、塩酸
処理を施してCaCO3 などのミネラル成分を除去す
る。塩酸処理は、塩酸水溶液を−10〜10℃、好まし
くは−5〜5℃の温度に調整した後、機械的撹拌機で撹
拌した甲殻粉末(通常、水分含量8〜12%)を添加
し、その温度で10〜25時間、好ましくは15〜20
時間処理した後、塩酸水溶液の温度を急激に10〜20
℃、好ましくは12〜18℃に上昇させて2〜8時間、
好ましくは3〜5時間保持することによって行う。この
時、塩酸水溶液は、0.4〜3M濃度が好ましく、機械
的撹拌機は50〜200rpm 、好ましくは100rpm の
速度で撹拌し、処理工程中、適切な時期に新しい塩酸水
溶液と1〜2回交換することが好ましい。また、撹拌速
度が200rpm 以上となると、塩酸処理の効果が低下す
るので注意しなければならない。 Demineralization Step Subsequently, the crushed shell (water content 8 to 12%) is subjected to hydrochloric acid treatment to remove mineral components such as CaCO 3 . In the hydrochloric acid treatment, after adjusting the hydrochloric acid aqueous solution to a temperature of −10 to 10 ° C., preferably −5 to 5 ° C., shell powder (usually water content 8 to 12%) stirred with a mechanical stirrer is added, 10-25 hours at that temperature, preferably 15-20
After treating for a period of time, the temperature of the aqueous hydrochloric acid solution is rapidly increased by 10 to 20
C., preferably 12-18.degree. C. for 2-8 hours,
It is preferably carried out by holding for 3 to 5 hours. At this time, the concentration of the hydrochloric acid aqueous solution is preferably 0.4 to 3M, and the mechanical stirrer is stirred at a speed of 50 to 200 rpm, preferably 100 rpm, and a new hydrochloric acid aqueous solution is added once or twice to a suitable time during the treatment process. It is preferable to replace it. It should be noted that the effect of hydrochloric acid treatment decreases when the stirring speed is 200 rpm or more.
【0016】一方、前記の処理中、塩酸水溶液処理工程
を一段法として、−10〜8℃、好ましくは−5〜5℃
の温度で、20〜60時間、好ましくは30〜50時間
行ってもよい。塩酸処理によりCaCO3 が除去された
甲殻は、水洗により残りの塩酸成分を除去する。水洗の
代わりに、NaOH水溶液を滴下してpH7〜9に調整し
た後、脱イオン水中に、一定時間、例えば1〜6時間浸
漬することもできる。次に、ろ過後、例えばエタノー
ル、メタノール、アセトン、THF、ジオキサン、ME
Kなどの有機溶媒で1〜2回洗浄した後乾燥する。前記
の溶媒洗浄は、甲殻類の甲殻の赤色を除去してキチンの
白色度を上昇させるためのものであり、この溶媒が脱色
剤として作用して、本発明では脱色剤として別の酸化剤
または還元剤を用いなくてもよいという長所がある。On the other hand, during the above treatment, the step of treating the hydrochloric acid aqueous solution as a one-step method is -10 to 8 ° C, preferably -5 to 5 ° C.
The temperature may be 20 to 60 hours, preferably 30 to 50 hours. The shellfish from which CaCO 3 has been removed by the hydrochloric acid treatment is washed with water to remove the remaining hydrochloric acid component. Instead of washing with water, an aqueous solution of NaOH may be added dropwise to adjust the pH to 7-9, and then immersed in deionized water for a certain time, for example, 1-6 hours. Then, after filtration, for example, ethanol, methanol, acetone, THF, dioxane, ME
It is washed with an organic solvent such as K once or twice and then dried. The solvent washing is for removing the red color of the crustacean crustacea and increasing the whiteness of chitin, and this solvent acts as a decolorizing agent, and in the present invention, another oxidizing agent or a decolorizing agent is used. It has the advantage that no reducing agent need be used.
【0017】脱蛋白工程 前記段階で得られた粗キチンを、NaOH水溶液に浸漬
して加熱処理する。NaOH水溶液の濃度は、2〜10
重量%が好ましく、反応温度は80〜100℃の範囲で
あり、加熱時間は2〜4時間が一般的である。この工程
は、不活性ガス、例えば窒素、アルゴン、ヘリウムまた
はネオンガスを連続的に注入しながら行うことが好まし
い。このようにして、キチンの分子鎖の切断を防ぐこと
ができる。次に、粗キチンを脱イオン水で洗浄して、N
aOH水溶液を除去するか、あるいは塩酸溶液を滴下し
て粗キチン浸漬水溶液にpHを7〜8に調整した後、脱イ
オン水中に、一定時間、例えば1〜5時間浸漬する。次
に、キチンをろ過した後、塩酸処理後の後続処理と同じ
ように、例えばエタノール、メタノール、アセトン、T
HF、ジオキサン、MEKなどの有機溶媒で1〜2回洗
浄した後乾燥する。NaOH処理されたキチンの純度を
高め、脱色を促進するために、前述のNaOH処理工程
及び洗浄工程を2回以上繰返すことが好ましい。得られ
たキチンを、白色度を高めるために脱イオン水中に、2
〜5日間浸漬した後、ろ過し、真空乾燥して高純度キチ
ンが得られる。Deproteinization step The crude chitin obtained in the above step is immersed in an aqueous solution of NaOH for heat treatment. The concentration of the NaOH aqueous solution is 2 to 10
% By weight is preferred, the reaction temperature is in the range of 80 to 100 ° C. and the heating time is generally 2 to 4 hours. This step is preferably carried out while continuously injecting an inert gas such as nitrogen, argon, helium or neon gas. In this way, breaking of the chitin molecular chain can be prevented. Then the crude chitin is washed with deionized water to
After removing the aOH aqueous solution or dropping a hydrochloric acid solution to adjust the pH of the crude chitin immersion aqueous solution to 7 to 8, it is immersed in deionized water for a certain time, for example, 1 to 5 hours. Then, after filtering the chitin, as in the subsequent treatment after the hydrochloric acid treatment, for example, ethanol, methanol, acetone, T
It is washed once or twice with an organic solvent such as HF, dioxane or MEK and then dried. In order to enhance the purity of the NaOH-treated chitin and accelerate decolorization, it is preferable to repeat the above-mentioned NaOH treatment step and washing step twice or more. The obtained chitin was added to deionized water to increase the whiteness, and 2
After soaking for ~ 5 days, it is filtered and vacuum dried to obtain high-purity chitin.
【0018】本発明によって得られた高純度キチンから
次のようにして、高分子量で且つ脱アセチル化度が高い
キトサンが得られる。まず、前記方法で調製されたキチ
ンに、例えば、30〜50%のNaOH水溶液を加えて
80〜100℃の温度で2〜12時間加熱する。この
時、例えば窒素、アルゴン、ヘリウムまたはネオンガス
などの不活性ガスを連続的に注入しながら行うことが好
ましい。また、NaOH水溶液の処理時、温度及び時間
が前記の範囲を外れると、分子鎖が切断されるおそれが
あり、好ましくない。次いで、NaOH水溶液で処理し
たキトサンを脱イオン水で洗浄した後、例えばアセト
ン、エタノール、メタノール、イソプロパノール、ジオ
キサン、THF、MEKなどの有機溶媒の混合水溶液
(通常、5〜30重量%の濃度)に浸漬した後、ろ過、
乾燥して、キトサンの白色度を高め、かつ不純物を除去
する。From the high-purity chitin obtained by the present invention, chitosan having a high molecular weight and a high degree of deacetylation can be obtained as follows. First, for example, 30 to 50% NaOH aqueous solution is added to the chitin prepared by the above method and heated at a temperature of 80 to 100 ° C. for 2 to 12 hours. At this time, it is preferable to continuously inject an inert gas such as nitrogen, argon, helium or neon gas. Further, when the temperature and the time are out of the above ranges during the treatment of the NaOH aqueous solution, the molecular chain may be broken, which is not preferable. Then, the chitosan treated with the NaOH aqueous solution is washed with deionized water, and then washed with a mixed aqueous solution of an organic solvent such as acetone, ethanol, methanol, isopropanol, dioxane, THF or MEK (concentration of usually 5 to 30% by weight). After soaking, filtration,
Dry to increase the whiteness of chitosan and remove impurities.
【0019】次いで、乾燥したキトサンを、さらに前述
のNaOH水溶液処理及び有機溶媒処理を繰り返して高
脱アセチル化度の高純度キトサンを得る。好ましくは、
キトサンの脱アセチル化度をさらに高めるために、前述
のNaOH水溶液処理及び有機溶媒処理工程を2回以上
繰返して行うことができる。Then, the dried chitosan is further subjected to the above-mentioned aqueous NaOH treatment and organic solvent treatment to obtain high-purity chitosan having a high degree of deacetylation. Preferably,
In order to further increase the deacetylation degree of chitosan, the above-mentioned NaOH aqueous solution treatment and organic solvent treatment steps can be repeated twice or more.
【0020】[0020]
【実施例】本発明を下記の実施例で更に詳しく説明する
が、本発明はこれに限定されるものではない。実施例中
で、キチン中の残留CaCO3 含量は、800℃で1時
間燃焼した後の強熱減量として測定した。蛋白含量は、
バイオ−ラッド(Bio-Rad) 社の蛋白分析用キットを用い
てブラドフォード(Bradford)法にしたがって米国ヒュー
レット−パッカード(Hewlett-Packard) 社の紫外及び可
視光分光光度計で測定した。また、金属の含量は、セイ
コー電子工業(株)の誘導結合高周波プラズマ発光分光
分析装置及び米国パーキン−エルマー(Perkin-Elmer)社
の原子吸光分析装置を用いて測定した。脱アセチル化度
は、赤外分光光度計を用いて論文〔J. Appl. Polym. Sc
i. 28, 1909(1983) 〕に載せられたミマ(Mima)法によっ
て測定した。経時白色度は、30日以上経た後のキチン
の外観状態を肉眼で判別した。また、粘度は、ブルック
フィールド(Brookfield)粘度計で4番スピンドルを用い
て60rpmで1%酢酸中の0.5%キトサン溶液で測定
した。EXAMPLES The present invention will be described in more detail with reference to the following examples, which should not be construed as limiting the invention thereto. In the examples, the residual CaCO 3 content in chitin was measured as the loss on ignition after burning for 1 hour at 800 ° C. The protein content is
The measurement was carried out with a UV-visible spectrophotometer manufactured by Hewlett-Packard, USA according to the Bradford method using a protein analysis kit manufactured by Bio-Rad. The metal content was measured using an inductively coupled high frequency plasma optical emission spectrophotometer manufactured by Seiko Instruments Inc. and an atomic absorption spectrophotometer manufactured by Perkin-Elmer, USA. The degree of deacetylation was determined using an infrared spectrophotometer [J. Appl. Polym. Sc.
i. 28, 1909 (1983)]. As for the whiteness over time, the appearance state of chitin after 30 days or more was visually judged. Viscosity was also measured with a Brookfield viscometer using a # 4 spindle at 60 rpm with a 0.5% chitosan solution in 1% acetic acid.
【0021】実施例1 ズワイガニ(学名:Chionoecetes opilio)の甲殻300
gを40〜50℃の水浴中に30分間放置した後、カニ
の肉質が完全に除去されるまで水洗した。甲殻を脱水機
で水分を除去し、エタノール浴に1時間浸漬した後、さ
らに脱水機で水分を除去し、日陰で10日間乾燥した乾
燥甲殻(水分含量10%)200gを得た。次いで、乾
燥した甲殻200gを、ディェツ−モトレン社の(Dietz
-Motoren GmbH & Co. KG) 製の粉砕機Mot.WRB
90LB/4Pで粒径0.5〜3mmに粉砕した後、機械
的撹拌機を装着した反応容器に投入し、これに0℃の1
N塩酸水溶液5Lを添加して50rpm の速度で撹拌しな
がら0℃に20時間保持した後、温度を急激に15℃ま
で昇温し、15℃で4時間保持した。塩酸処理した甲殻
をろ過した後、水に浸漬し、5重量%NaOH水溶液で
浸漬液のpHを7〜8に調整した後、6時間放置した。ろ
過した粗キチンをアセトン3Lで2回洗浄した後、ろ過
して30℃の真空オーブン中で36時間乾燥した。 EXAMPLE 1 Shell 300 of snow crab (scientific name: Chionoecetes opilio)
After being left in a water bath at 40 to 50 ° C. for 30 minutes, g was washed with water until the meat quality of the crab was completely removed. After removing water from the shell with a dehydrator and immersing it in an ethanol bath for 1 hour, the water was further removed with a dehydrator to obtain 200 g of dried shell (water content 10%) dried in the shade for 10 days. Then, 200 g of the dried shell was used for the (Dietz-Mottren)
-Motoren GmbH & Co. KG) crusher Mot. WRB
After pulverizing with 90 LB / 4P to a particle size of 0.5 to 3 mm, the mixture was put into a reaction vessel equipped with a mechanical stirrer, and the mixture was added at 0 ° C. to 1
After adding 5 L of N hydrochloric acid aqueous solution and maintaining at 0 ° C. for 20 hours while stirring at a speed of 50 rpm, the temperature was rapidly raised to 15 ° C. and maintained at 15 ° C. for 4 hours. The shell treated with hydrochloric acid was filtered, then immersed in water, the pH of the immersion liquid was adjusted to 7 to 8 with a 5 wt% NaOH aqueous solution, and then left for 6 hours. The filtered crude chitin was washed twice with 3 L of acetone, filtered, and dried in a vacuum oven at 30 ° C. for 36 hours.
【0022】乾燥した粗キチンを5重量%のNaOH水
溶液6Lに浸漬した後、窒素ガスを注入しながら90℃
で3時間加熱した。次いで、2N塩酸水溶液を添加して
粗キチン含有水溶液のpHを7〜8に調整した後、粗キチ
ンをろ過し、脱イオン水6L中に6時間浸漬した後ろ過
した。ろ過した物質をアセトン3Lで2回洗浄した後、
30℃の真空オーブンで12時間乾燥した。得られた乾
燥キチンにさらに前述のNaOH水溶液処理工程を繰返
した。2次NaOH水溶液処理したキチンを脱イオン水
で5〜10回洗浄した後、脱イオン水6L中に3日間浸
漬した後、ろ過及び真空オーブン中で乾燥して、最終的
に高純度キチン50gを得た。The dried crude chitin was immersed in 6 L of a 5% by weight NaOH aqueous solution and then at 90 ° C. while injecting nitrogen gas.
Heated for 3 hours. Then, a 2N aqueous hydrochloric acid solution was added to adjust the pH of the crude chitin-containing aqueous solution to 7 to 8, and then the crude chitin was filtered, immersed in 6 L of deionized water for 6 hours, and then filtered. After washing the filtered material twice with 3 L of acetone,
It was dried in a vacuum oven at 30 ° C. for 12 hours. The dried chitin thus obtained was further subjected to the above-mentioned NaOH aqueous solution treatment step. The chitin treated with the secondary NaOH aqueous solution was washed with deionized water 5 to 10 times, immersed in 6 L of deionized water for 3 days, filtered, and dried in a vacuum oven to finally obtain 50 g of high-purity chitin. Obtained.
【0023】実施例2 塩酸水溶液処理を、0℃の温度に48時間保持すること
により行った以外は、実施例1と同様にしてキチンを製
造した。Example 2 Chitin was produced in the same manner as in Example 1 except that the treatment with the aqueous hydrochloric acid solution was carried out by maintaining the temperature at 0 ° C. for 48 hours.
【0024】実施例3 塩酸水溶液処理を、5℃の温度に、24時間保持するこ
とにより行った以外は、実施例1と同様にしてキチンを
製造した。Example 3 Chitin was produced in the same manner as in Example 1 except that the treatment with the hydrochloric acid aqueous solution was carried out by keeping the temperature at 5 ° C. for 24 hours.
【0025】実施例4 塩酸水溶液処理を、−8℃の温度に40時間保持するこ
とにより行った以外は、実施例1と同様にしてキチンを
製造した。Example 4 Chitin was produced in the same manner as in Example 1 except that the treatment with the aqueous hydrochloric acid solution was carried out by maintaining the temperature at -8 ° C for 40 hours.
【0026】比較例1 塩酸水溶液処理を、15℃の温度に8時間保持すること
により行った以外は、実施例1と同様にしてキチンを製
造した。Comparative Example 1 Chitin was produced in the same manner as in Example 1 except that the treatment with the hydrochloric acid aqueous solution was carried out by keeping the temperature at 15 ° C. for 8 hours.
【0027】比較例2 塩酸水溶液処理を、10℃の温度に24時間保持するこ
とにより行った以外は、実施例1と同様にしてキチンを
製造した。Comparative Example 2 Chitin was produced in the same manner as in Example 1 except that the treatment with the hydrochloric acid aqueous solution was carried out by keeping the temperature at 10 ° C. for 24 hours.
【0028】比較例3 乾燥したズワイガニの甲殻200gを0.5〜3mmに粉
砕し、機械的撹拌機を装着した反応容器に投入した後、
2N塩酸水溶液5Lを添加して撹拌しながら室温で5時
間反応させた。塩酸溶液を0℃に冷却して48時間反応
させた。ろ過後、ろ過物を水洗し、100℃の3.85
wt%NaOH水溶液中に12時間浸漬した。水洗後乾燥
してキチン80gを得た。実施例1〜4と比較例1〜3
の反応条件及び得られたキチンの特性を第1表に示す。Comparative Example 3 200 g of dried snow crab shell was crushed to 0.5 to 3 mm and charged into a reaction vessel equipped with a mechanical stirrer.
5 L of a 2N hydrochloric acid aqueous solution was added, and the mixture was reacted at room temperature for 5 hours with stirring. The hydrochloric acid solution was cooled to 0 ° C. and reacted for 48 hours. After filtration, the filtrated product is washed with water and kept at 100 ° C. for 3.85.
It was immersed in a wt% NaOH aqueous solution for 12 hours. After washing with water and drying, 80 g of chitin was obtained. Examples 1-4 and Comparative Examples 1-3
Table 1 shows the reaction conditions and the characteristics of the obtained chitin.
【0029】[0029]
【表1】 [Table 1]
【0030】実施例5 実施例1で得られたキチン45gを、4L容量の3口フ
ラスコに投入し、更に40重量%のNaOH水溶液3L
を添加した後、窒素ガスを連続的に注入しながら90℃
の温度で7時間加熱した。得られた粗キトサンを洗浄水
のpHが中性になるまで脱イオン水で水洗した後、ろ過し
脱イオン水3L中に2日間浸漬した後、ろ過し、直ちに
3Lの10%エタノール水溶液中に3日間浸漬した。粗
キトサンをろ過して40℃の真空オーブン中で2日間乾
燥した(1次NaOH水溶液処理)。乾燥したキトサン
に40重量%のNaOH水溶液3Lを添加した後、窒素
ガスを連続的に注入しながら90℃の温度で3時間加熱
した。得られたキトサンを洗浄水のpHが中性になるまで
脱イオン水で水洗した後、ろ過し脱イオン水3L中に2
日間浸漬した後、ろ過して、直ちに10%エタノール水
溶液中に3時間浸漬した後、ろ過及び乾燥した(2次N
aOH水溶液処理)。このようにして脱アセチル化度が
90%以上のキトサンを得た。前記の1次及び2次Na
OH水溶液処理を1回さらに繰返して脱アセチル化度が
92%以上のキトサンを得た。Example 5 45 g of chitin obtained in Example 1 was charged into a 4-liter three-necked flask, and 3 L of 40 wt% NaOH aqueous solution was added.
After adding, while continuously injecting nitrogen gas,
Was heated for 7 hours. The obtained crude chitosan was washed with deionized water until the pH of the washing water became neutral, filtered, immersed in 3 L of deionized water for 2 days, filtered, and immediately added to 3 L of 10% aqueous ethanol solution. It was immersed for 3 days. The crude chitosan was filtered and dried in a vacuum oven at 40 ° C. for 2 days (treatment with primary NaOH aqueous solution). After adding 3 L of 40 wt% NaOH aqueous solution to the dried chitosan, it was heated at a temperature of 90 ° C. for 3 hours while continuously injecting nitrogen gas. The resulting chitosan was washed with deionized water until the pH of the washing water became neutral, then filtered and washed with 2 L of 3 L of deionized water.
After soaking for a day, it was filtered, immediately immersed in a 10% aqueous ethanol solution for 3 hours, then filtered and dried (secondary N
aOH aqueous solution treatment). Thus, chitosan having a deacetylation degree of 90% or more was obtained. The above-mentioned primary and secondary Na
The OH aqueous solution treatment was further repeated once to obtain chitosan having a degree of deacetylation of 92% or more.
【0031】実施例6及び比較例4〜7 NaOH水溶液処理の条件を、第2表に示すように行っ
た以外は、実施例5と同様にしてキトサンを製造した。Example 6 and Comparative Examples 4 to 7 Chitosan was produced in the same manner as in Example 5 except that the conditions of the treatment with the aqueous NaOH solution were as shown in Table 2.
【0032】比較例8 比較例1で得られたキチン40gをフラスコに投入し、
更に40重量%NaOH水溶液2.4Lを添加した後、
115℃の温度で6時間加熱した。洗浄及びろ過して真
空オーブンで乾燥した。前記の実施例5〜6及び比較例
4〜8で用いた反応条件及び得られたキトサンの特性を
第2表に示す。Comparative Example 8 40 g of the chitin obtained in Comparative Example 1 was placed in a flask,
After adding further 2.4 L of 40 wt% NaOH aqueous solution,
Heated at a temperature of 115 ° C. for 6 hours. Washed, filtered and dried in a vacuum oven. Table 2 shows the reaction conditions used in Examples 5 to 6 and Comparative Examples 4 to 8 and the properties of the obtained chitosan.
【0033】[0033]
【表2】 [Table 2]
【0034】[0034]
【発明の効果】本発明によれば、温和な塩酸処理条件に
より分子鎖の切断を防止し、塩酸処理後及びNaOH処
理後に有機溶媒を用いることにより、他に脱色剤を用い
なくてもキチンの白色度を高める効果が得られる。また
NaOH処理時、不活性ガスを注入して分子鎖の切断を
防止することにより、高分子量のキチンが得られる。ま
たかかるキチンからNaOH水溶液処理を繰り返すこと
により、高脱アセチル化度の、高純度及び高分子量のキ
トサンが得られる。EFFECTS OF THE INVENTION According to the present invention, it is possible to prevent the cleavage of molecular chains under mild hydrochloric acid treatment conditions, and to use an organic solvent after hydrochloric acid treatment and NaOH treatment, thereby making it possible to remove chitin without using a decolorizing agent. The effect of increasing the whiteness is obtained. Further, during the NaOH treatment, a high molecular weight chitin can be obtained by injecting an inert gas to prevent the molecular chain from breaking. Further, by repeating treatment of such chitin with an aqueous NaOH solution, chitosan having a high degree of deacetylation, high purity and high molecular weight can be obtained.
Claims (13)
て微粉末を得る工程、 (ロ)該微粉末を0.4〜3Mの塩酸溶液中、−10〜
10℃の温度で10〜25時間処理する一次塩酸処理を
施し、次いで10〜20℃の温度で2〜8時間浸漬する
二次塩酸処理を施す工程、 (ハ)塩酸処理した物質を水洗し、ろ過し、有機溶媒で
洗浄した後乾燥して粗キチンを得る工程、 (ニ)該粗キチンを2〜10重量%の水酸化ナトリウム
溶液に浸漬し加熱する工程、及び (ホ)前記水酸化ナトリウム処理したキチンを水洗し、
ろ過し、有機溶媒で洗浄した後乾燥する工程からなる高
純度キチンの製造方法。1. A step of (a) drying a crustacean shell and then pulverizing it to obtain a fine powder, (b) -10 in a 0.4 to 3 M hydrochloric acid solution of the fine powder.
A step of performing primary hydrochloric acid treatment for 10 to 25 hours at a temperature of 10 ° C., and then performing secondary hydrochloric acid treatment for dipping at a temperature of 10 to 20 ° C. for 2 to 8 hours, (c) washing the hydrochloric acid treated material with water, Filtering, washing with an organic solvent and then drying to obtain crude chitin, (d) a step of immersing the crude chitin in a 2 to 10 wt% sodium hydroxide solution and heating, and (e) the sodium hydroxide Wash the treated chitin with water,
A method for producing high-purity chitin, which comprises the steps of filtering, washing with an organic solvent, and then drying.
日陰で水分含量12%以下となるまで行う請求項1記載
の方法。2. Drying the shell in the step (a),
The method according to claim 1, wherein the method is performed in the shade until the water content is 12% or less.
を、−5〜5℃の温度で15〜20時間行い、二次塩酸
処理を12〜18℃の温度で3〜5時間行う請求項1記
載の方法。3. The primary hydrochloric acid treatment in the step (b) is performed at a temperature of −5 to 5 ° C. for 15 to 20 hours, and the secondary hydrochloric acid treatment is performed at a temperature of 12 to 18 ° C. for 3 to 5 hours. The method described.
械的撹拌機により50〜200rpm の速度で撹拌しなが
ら行う請求項1記載の方法。4. The method according to claim 1, wherein the treatment with hydrochloric acid in the step (b) is carried out while stirring with a mechanical stirrer at a speed of 50 to 200 rpm.
媒が、エタノール、メタノール、アセトン、テトラヒド
ロフラン、ジオキサンおよびメチルエチルケトンから選
択される請求項1記載の方法。5. The method according to claim 1, wherein the solvent used in steps (c) and (f) is selected from ethanol, methanol, acetone, tetrahydrofuran, dioxane and methyl ethyl ketone.
ム処理を、不活性気体中で行う請求項1記載の方法。6. The method according to claim 1, wherein the sodium hydroxide treatment in the step (d) is performed in an inert gas.
繰り返し行う請求項1記載の方法。7. The method according to claim 1, wherein the steps (d) and (e) are repeated twice or more.
で−10℃〜8℃の温度で20〜60時間行うことを特
徴とする高純度キチンの製造方法。8. A method for producing high-purity chitin, which comprises performing the hydrochloric acid treatment step (b) of claim 1 in a one-step method at a temperature of −10 ° C. to 8 ° C. for 20 to 60 hours.
で30〜50時間行う請求項8記載の方法。9. The method according to claim 8, wherein the hydrochloric acid treatment step is performed at a temperature of −5 to 5 ° C. for 30 to 50 hours.
法により製造されたキチンを、水酸化ナトリウム溶液で
80〜100℃の温度下、2〜12時間加熱処理して粗
キトサンを得る工程、 (b)該粗キトサンをろ過し、水洗し、脱イオン水に浸
漬し、ろ過して水混和性有機溶媒の混合水溶液に浸漬し
た後、ろ過及び乾燥する工程からなることを特徴とする
高純度キトサンの製造方法。10. (a) The chitin produced by the method according to claim 1 or 8 is heat-treated with a sodium hydroxide solution at a temperature of 80 to 100 ° C. for 2 to 12 hours to obtain crude chitosan. And (b) filtering the crude chitosan, rinsing with water, immersing in deionized water, filtering, immersing in a mixed aqueous solution of a water-miscible organic solvent, and then filtering and drying. A method for producing high-purity chitosan.
う請求項10記載の方法。11. The method according to claim 10, wherein the step (a) is performed in an inert gas.
溶媒を5〜30重量%含有する請求項10記載の方法。12. The method according to claim 10, wherein the mixed aqueous solution in the step (b) contains 5 to 30% by weight of an organic solvent.
ル、メタノール、イソプロパノール、ジオキサン、テト
ラヒドロフランおよびメチルエチルケトンから選択され
る請求項12記載の方法。13. The method of claim 12, wherein the organic solvent is selected from acetone, ethanol, methanol, isopropanol, dioxane, tetrahydrofuran and methyl ethyl ketone.
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Family
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KR (2) | KR970008132B1 (en) |
CA (1) | CA2101079A1 (en) |
FR (1) | FR2701266B1 (en) |
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DE19503465A1 (en) * | 1995-02-03 | 1996-08-08 | Henkel Kgaa | Process for the production of low-viscosity cationic biopolymers |
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DE19604180C2 (en) * | 1996-02-06 | 1997-12-18 | Henkel Kgaa | Process for the production of biopolymers with improved surfactant solubility |
US6444659B1 (en) | 1996-11-28 | 2002-09-03 | Cognis Deutschland Gmbh | Use of mixtures of active substances, containing phytostenols and/or phytostenol esters and potentiators, for the production of hypocholesterolemic agents |
EP0941097B1 (en) | 1996-11-28 | 2002-05-02 | Cognis Deutschland GmbH & Co. KG | Use of mixtures of active substances for the production of hypocholesteremic agents |
DE19710369A1 (en) * | 1997-03-13 | 1998-09-17 | Henkel Kgaa | Process for the production of cross-linked biopolymers |
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WO2000004230A1 (en) | 1998-07-16 | 2000-01-27 | Cognis Deutschland Gmbh | Use of pit emulsions |
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EP1064910B1 (en) | 1999-07-02 | 2005-09-14 | Cognis IP Management GmbH | Microcapsules |
ATE258777T1 (en) | 1999-07-02 | 2004-02-15 | Cognis Iberia Sl | MICRO CAPSULES - II |
DE59912559D1 (en) | 1999-07-02 | 2005-10-20 | Cognis Ip Man Gmbh | Microcapsules - III |
ATE258417T1 (en) | 1999-07-02 | 2004-02-15 | Cognis Iberia Sl | MICRO CAPSULES - I |
GB9929472D0 (en) * | 1999-12-13 | 2000-02-09 | Btg Int Ltd | Polymeric film |
DE10014529A1 (en) | 2000-03-23 | 2001-09-27 | Cognis Deutschland Gmbh | Cosmetic deodorant compositions, comprise chitosan and/or chitosan derivatives in the form of nanoparticles |
DE10018812A1 (en) | 2000-04-15 | 2001-10-25 | Cognis Deutschland Gmbh | Nonionic surfactant granulate, used in surfactant, cosmetic or pharmaceutical formulation or laundry or other detergent, is obtained by granulating and simultaneously drying aqueous surfactant paste in presence of organic polymeric carrier |
FR2814380B1 (en) | 2000-09-25 | 2002-11-08 | Serobiologiques Lab Sa | MICROCAPSULES POWDER AND PROCESS FOR OBTAINING |
DE10105623A1 (en) | 2001-02-08 | 2002-08-14 | Cognis Deutschland Gmbh | Process for antibacterial finishing of fibers or nonwovens |
TW583190B (en) * | 2001-04-04 | 2004-04-11 | Dainichiseika Color Chem | Purified chitins and production process thereof |
NO20015986D0 (en) | 2001-08-02 | 2001-12-06 | Einar J Mustaparta | The product chitosan, as well as the method of manufacture and use of chitosan |
BE1014638A6 (en) * | 2002-02-12 | 2004-02-03 | Univ Liege | Method of preparation of derivatives of cell wall from biomass. |
DE102004007115A1 (en) | 2004-02-13 | 2005-08-25 | Cognis Deutschland Gmbh & Co. Kg | Chitosan-containing wound dressings |
RU2421467C2 (en) * | 2005-06-14 | 2011-06-20 | Дженис Эхф. | Compositions of partially deacetylated chitin derivatives |
CA2927697A1 (en) | 2013-10-23 | 2015-04-30 | Unilever Plc | Anti-perspirant composition |
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GB8824971D0 (en) * | 1988-10-25 | 1988-11-30 | Roberts G A F | Method for production of chitosan |
FR2650282B1 (en) * | 1989-07-26 | 1992-09-04 | Dev Utilisations Cuir | PROCESS FOR THE PREPARATION OF CHITOSAN BY N-DEACETYLATION OF CHITINE |
-
1993
- 1993-02-08 KR KR1019930001687A patent/KR970008132B1/en not_active IP Right Cessation
- 1993-07-21 CA CA002101079A patent/CA2101079A1/en not_active Abandoned
- 1993-07-23 NO NO932662A patent/NO932662L/en unknown
- 1993-08-10 PL PL93300024A patent/PL300024A1/en unknown
- 1993-08-24 IT ITMI931842A patent/IT1270966B/en active IP Right Grant
- 1993-08-31 FR FR9310401A patent/FR2701266B1/en not_active Expired - Fee Related
- 1993-10-29 JP JP5271680A patent/JPH0730123B2/en not_active Expired - Fee Related
-
1997
- 1997-03-13 KR KR1019970008516A patent/KR100190723B1/en not_active IP Right Cessation
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2006057308A1 (en) * | 2004-11-25 | 2006-06-01 | Dainichiseika Color & Chemicals Mfg. Co., Ltd. | Method of determining tropomyosin in chitosan |
JP2006177936A (en) * | 2004-11-25 | 2006-07-06 | Dainichiseika Color & Chem Mfg Co Ltd | Method of measuring tropomyosin in chitosan |
JP2011017724A (en) * | 2004-11-25 | 2011-01-27 | Dainichiseika Color & Chem Mfg Co Ltd | Chitosan subjected to measure for inhibition of allergy expression |
KR100693803B1 (en) * | 2005-09-20 | 2007-03-12 | 노홍균 | Egg preserving agent using the chitosan and producing method thereof |
JP2011515541A (en) * | 2008-03-19 | 2011-05-19 | アグラテック インターナショナル インコーポレイテッド | Chitosan generation method |
CN108239182A (en) * | 2018-01-05 | 2018-07-03 | 佛山市聚成生化技术研发有限公司 | A kind of extracting method of aspongopus chitosan and its application |
Also Published As
Publication number | Publication date |
---|---|
PL300024A1 (en) | 1994-08-22 |
JPH0730123B2 (en) | 1995-04-05 |
KR940019731A (en) | 1994-09-14 |
NO932662L (en) | 1994-08-09 |
ITMI931842A1 (en) | 1995-02-24 |
KR100190723B1 (en) | 1999-06-01 |
IT1270966B (en) | 1997-05-26 |
KR970008132B1 (en) | 1997-05-21 |
FR2701266B1 (en) | 1995-04-21 |
ITMI931842A0 (en) | 1993-08-24 |
CA2101079A1 (en) | 1994-08-09 |
NO932662D0 (en) | 1993-07-23 |
FR2701266A1 (en) | 1994-08-12 |
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