JPS6040224A - Manufacture of formed article of chitosan - Google Patents
Manufacture of formed article of chitosanInfo
- Publication number
- JPS6040224A JPS6040224A JP58148742A JP14874283A JPS6040224A JP S6040224 A JPS6040224 A JP S6040224A JP 58148742 A JP58148742 A JP 58148742A JP 14874283 A JP14874283 A JP 14874283A JP S6040224 A JPS6040224 A JP S6040224A
- Authority
- JP
- Japan
- Prior art keywords
- chitosan
- strength
- threads
- solution
- aqueous solution
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/36—Feeding the material to be shaped
- B29C44/46—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length
- B29C44/50—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length using pressure difference, e.g. by extrusion or by spraying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2096/00—Use of specified macromolecular materials not provided for in a single one of main groups B29K2001/00 - B29K2095/00, as moulding material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
- B29L2031/00—Other particular articles
- B29L2031/731—Filamentary material, i.e. comprised of a single element, e.g. filaments, strands, threads, fibres
Landscapes
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Artificial Filaments (AREA)
Abstract
Description
【発明の詳細な説明】
本発明はキトサンからすぐれた物性の糸、フィルムその
他の成形物を効率的に製造する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for efficiently producing threads, films and other molded articles with excellent physical properties from chitosan.
従来、キチンの加水分解生成物であるキトサンの有効利
用について多くの研究が為されており、キトサン糸、キ
トサンフィルム等のキトサン成形物を得る方法も幾つか
知られている。Conventionally, much research has been conducted on the effective use of chitosan, which is a hydrolysis product of chitin, and several methods for obtaining chitosan molded products such as chitosan threads and chitosan films are known.
例えばキトサン糸に関してはキトサンの水性溶液を調製
し、これから紡糸する方法であるが、従来の紡糸方法で
は、キトサンは低分子圀のものであり且つ低濃度でも高
い粘度を示すため、その使用限界濃度が約8重量φ程度
であり、これ以」二の濃度のキトサン水性溶液を使用し
てキトサン糸を得ることは不可能であり、分子J)(の
高いキトサンの場合は更に高粘度であり、使用限界濃度
は一層低くなるものであった。従って、従来のキトサン
糸は通常は3〜8重量%という低濃度の紡糸原液を使用
して紡糸するため、紡糸ノズルから出た直後の糸は殆ど
強度が無く、直ちに凝固浴中に導入し凝固させねば糸の
形状を保持し得ないものであった。また、このようにし
て湿式紡糸しても紡糸原液の低濃度という面から紡糸効
率は低く且つ実用的な強度およびヤング率を有する糸を
得ることができないという問題があった。For example, for chitosan thread, the method is to prepare an aqueous solution of chitosan and then spin it.However, in the conventional spinning method, chitosan is a low-molecular-weight product and exhibits high viscosity even at low concentrations, so its use limit concentration is is about 8 weight φ, and it is impossible to obtain chitosan thread using a chitosan aqueous solution with a higher concentration than this, and chitosan with a high molecule J) has an even higher viscosity. The limit concentration for use has been lowered.Therefore, since conventional chitosan yarns are usually spun using a spinning stock solution with a low concentration of 3 to 8% by weight, most of the yarns immediately after coming out of the spinning nozzle are It lacked strength, and the shape of the yarn could not be maintained unless it was immediately introduced into a coagulation bath and coagulated.Furthermore, even with wet spinning in this way, the spinning efficiency was low due to the low concentration of the spinning stock solution. Another problem was that it was not possible to obtain a yarn with practical strength and Young's modulus.
本発明者は上述の如き従来技術の問題点を解決すべく鋭
意研究の結果、10重!、 %以上のキトサン水性溶液
を紡糸原液として使用し、加圧下に成形ノズルから押出
成形することによって上述の彷来技術の欠点が十分に解
決され、すぐれた物性のキトサン糸あるいはキトサン成
形物が得られることを知見して本発明を完成した。The inventor of the present invention has conducted extensive research to solve the problems of the prior art as described above, and has found a 10-fold solution! By using an aqueous solution of chitosan with a concentration of at least 10% as a spinning stock solution and extruding it from a molding nozzle under pressure, the drawbacks of the conventional technology described above can be fully solved, and chitosan threads or chitosan molded products with excellent physical properties can be obtained. The present invention was completed based on the knowledge that
すなわち、本発明は、キトサンを10重量%以上含有す
るキトサン水性溶液を調製し、該水性溶液を加圧下に押
出成形することを特徴とするキトサン成形物の製造方法
である。That is, the present invention is a method for producing a chitosan molded article, which is characterized by preparing an aqueous chitosan solution containing 10% by weight or more of chitosan, and extruding the aqueous solution under pressure.
本発明の詳細な説明すると、本発明において使用するキ
トサンとは、えび、かに、昆虫その他甲殻類の外殻等中
に存在する天然高分子であるキチンをアルカリ加水分解
することによって得られ、2一番アミノー2−デオキシ
ーD−グルコースを構成却位とする塩基性多糖類であυ
、このようなキトサンそれ自体はすでに工業的に製造さ
れ市場から入手し得るものである。このようなキトサン
は、例えば稀酢酸等に溶解可能であるが、低分子邪のも
のであってもその濃度が約8重月°チ以上となると溶液
が非常に高粘度となり、従来のキトサン紡糸技術におい
ては約8重量%以上の高濃度の溶液はイ史用されたこと
がない。本発明においては、このようなキトサンを酢酸
、塩酸、スルファミン酸その他の稀酸水溶液中に10重
量−〜801旧チ、好ましくは約15重量%〜40重間
係の濃度に溶解した高濃度溶液を使用することを1つの
特金としている。本発明においては、このようなキトサ
ン水性溶液の調製に際して、稀酸水溶液中に水と相溶性
のある揮発性有機溶剤、例えばメタノール、エタノール
、インプロパツール、アセトン等を水100重量部あた
シO〜100重fi+部の割合で添加し、後の成形時の
乾燥を併進させることができる。また、キトサン水性溶
液中に各種の添加剤、例えば酵素、酵母、その他の有用
徹牛物、各種医薬、着色剤、香料等も心壁に応じて添加
することができる。To explain the present invention in detail, the chitosan used in the present invention is obtained by alkaline hydrolysis of chitin, a natural polymer present in the outer shells of shrimp, crabs, insects, and other crustaceans. It is a basic polysaccharide whose constituent position is 2-amino-2-deoxy-D-glucose.
, such chitosan itself has already been produced industrially and is available on the market. Such chitosan can be dissolved in, for example, dilute acetic acid, but even if it is a low molecular weight chitosan, if the concentration exceeds about 80%, the solution becomes extremely viscous, making it difficult to use conventional chitosan spinning. Highly concentrated solutions of more than about 8% by weight have never been used in the art. In the present invention, a highly concentrated solution is prepared by dissolving such chitosan in an aqueous solution of acetic acid, hydrochloric acid, sulfamic acid, or other dilute acid to a concentration of 10% by weight to 801% by weight, preferably about 15% by weight to 40% by weight. One special feature is the use of . In the present invention, when preparing such an aqueous chitosan solution, a volatile organic solvent that is compatible with water, such as methanol, ethanol, impropatol, acetone, etc., is added to the dilute acid aqueous solution per 100 parts by weight of water. It can be added in a proportion of 0 to 100 parts by weight to simultaneously accelerate drying during subsequent molding. In addition, various additives such as enzymes, yeast, other useful beef extracts, various medicines, coloring agents, fragrances, etc. can also be added to the chitosan aqueous solution depending on the heart wall.
本発明の成形物の製造方法は、上記の如き高濃度キトサ
ン水性溶液を紡糸ノズルまたはその他の成形ノズルを通
して加圧下に押出成形することも%9とする。この際の
成形圧力は10〜500に9 /’ crA 、好まし
くは20−50 Kt/crlの圧力である。本発明者
の詳細な研究によれば、このような圧力下で高濃度のキ
トサン水性溶液を押出成形することによって、押出時に
キトサン分子が高度に配向し、その結果特に凝固浴を使
用しないでも、また成形直後であってもかなシの強度を
有する成形物、例えば糸が形成されることを知見した。The method for producing a molded article of the present invention also involves extruding the above-described high-concentration chitosan aqueous solution under pressure through a spinning nozzle or other molding nozzle. The molding pressure at this time is 10 to 500 to 9/' crA, preferably 20 to 50 Kt/crl. According to the inventor's detailed research, by extruding a highly concentrated chitosan aqueous solution under such pressure, chitosan molecules become highly oriented during extrusion, and as a result, even without using a coagulation bath, It has also been found that a molded product, such as a thread, having a certain strength can be formed even immediately after molding.
従って、本発明方法においては、従来技術における如き
複雑な組成の凝固浴や強い薬剤の使用は不要となり、例
えば、単に空中に押出し、成形物中の揮発成分を除去し
、後に成形物中に包含されている少量の酸を中和するの
みで目的とする成形物を得ることができる。なお、押出
直後またはその後に押出した糸を約2〜10倍程度に延
伸処理することによって得られる糸の強度や弾性率を飛
躍的に向上させることができる。勿論、他の雰囲気、例
えば不活性ガスやアンモニアガス等の雰囲気中に押出す
ことも可能であシ、またアルカリ性の中和浴中に押出す
ことも好ましい方法である。すなわち、本発明方法にお
いては、上述の如き技術構成により、従来技術における
如き凝固浴の使用は実質上不要となっている。Therefore, in the method of the present invention, there is no need to use a coagulation bath with a complicated composition or strong chemicals as in the prior art. The desired molded product can be obtained by simply neutralizing the small amount of acid present. In addition, the strength and elastic modulus of the obtained yarn can be dramatically improved by stretching the extruded yarn by about 2 to 10 times immediately after or after extrusion. Of course, it is also possible to extrude into other atmospheres, such as inert gas or ammonia gas, and extrusion into an alkaline neutralization bath is also a preferred method. That is, in the method of the present invention, the use of a coagulation bath as in the prior art is substantially unnecessary due to the above-mentioned technical configuration.
以上の如き本発明によれば、キトサンの成形にあたり、
従来技術では考えられない程の高濃度キトラン水性溶液
あるいは高分子量のキトサン水性溶液を使用し圧力下に
押出成形することによって、成形時にキトサンの高度の
分子配向が認められ、その結果従来方法における如き煩
雑な凝固浴は実質上不要となシ、強度および弾性率にす
ぐれたキトサン成形物が効率良く提供される。According to the present invention as described above, when molding chitosan,
By extrusion molding under pressure using a highly concentrated chitran aqueous solution or a high molecular weight chitosan aqueous solution unimaginable with conventional techniques, a high degree of molecular orientation of chitosan is observed during molding, resulting in a high degree of molecular orientation compared to conventional methods. A complicated coagulation bath is substantially unnecessary, and chitosan molded articles with excellent strength and elastic modulus can be efficiently provided.
以上においては本発明方法を主として糸の成形を対象に
して説明したが、本発明方法は、糸以外の成形物、例え
ばロンド、フィルム、シートその他の形状の成形物の製
造にも同様に適用できるものである。Although the method of the present invention has been explained above mainly for forming threads, the method of the present invention can be similarly applied to the production of molded products other than threads, such as rondos, films, sheets, and other shapes. It is something.
次に実施例をあげて本発明を具体的に説明する。Next, the present invention will be specifically explained with reference to Examples.
なお文中部またはチとあるのは重量基準である。Note that the text in the middle of the sentence or ``chi'' is based on weight.
実施例1
エビの甲殻よシ単離したキチンを42重量−の苛性ソー
ダ水溶液中で100’Cで2時間処理してキトサンとし
た。該キトサンの粘度は0.5%の濃度で20℃□にお
いて20センチボイズであった。Example 1 Chitin isolated from shrimp shells was treated in a 42 wt. caustic soda aqueous solution at 100'C for 2 hours to obtain chitosan. The viscosity of the chitosan was 20 centivoise at 20° C. at a concentration of 0.5%.
該キトサン20部を20%の酢酸水溶液に加え3日間放
置して濃度20%の高粘度のキトサン溶液を得た。該溶
液を脱泡処理し、孔径0.4鯖の紡糸ノズルから15K
g/−の紡糸圧力で” 00 mm/ n+1n。20 parts of the chitosan was added to a 20% aqueous acetic acid solution and left to stand for 3 days to obtain a highly viscous chitosan solution with a concentration of 20%. The solution was degassed and passed through a spinning nozzle with a pore size of 0.4 at 15K.
00 mm/n+1n at a spinning pressure of g/-.
の吐出速度で空気中に押出し、次いでアンモニアガスに
さらしプこ後水洗してキトサン系を得た。このキトサン
糸の乾強度は2 t / aでありその伸度は11チで
あり、またヤング率は100 y / dであった。ま
た、湿強度は0.8 t / aであり、その伸度は3
2膏であった。The mixture was extruded into air at a discharge rate of , and then exposed to ammonia gas and washed with water to obtain a chitosan system. This chitosan yarn had a dry strength of 2 t/a, an elongation of 11 inches, and a Young's modulus of 100 y/d. In addition, the wet strength is 0.8 t/a, and the elongation is 3
It was 2 plasters.
実施例2
実施例1におけるキトサンに代えて0.5%濃度で20
℃における粘度が200センチボイズであるキトサン1
0部を5チ酢酸水溶液に溶解しキ]・サンの10%水溶
液を得た。該水溶液を使用し、実施例1と同一条件でキ
トサン糸を得た。このキトサン系の乾強度は3,5r/
aであり、その伸度は12チであり、ヤング率は100
t/aであった。Example 2 Chitosan in Example 1 was replaced with 20 at a concentration of 0.5%.
Chitosan 1 with a viscosity of 200 centiboise at °C
0 part was dissolved in an aqueous solution of 5-thiacetic acid to obtain a 10% aqueous solution of Ki].san. Using this aqueous solution, chitosan threads were obtained under the same conditions as in Example 1. The dry strength of this chitosan type is 3.5r/
a, its elongation is 12 inches, and its Young's modulus is 100
It was t/a.
才だ湿強度は1.1f/dでありその伸度は40係であ
った。The wet strength was 1.1 f/d and the elongation was 40.
Claims (3)
製し、該水性溶液を加圧下に押出成形することを特徴と
するキトサン成形物の製造方法。(1) A method for producing a chitosan molded article, which comprises preparing an aqueous solution containing chitosan of 10 weight φ or more, and extruding the aqueous solution under pressure.
(iアンモニアガス雰囲気中に押出成形する特許請求の
範囲第(1)項に記載の製造方法。(2) Chitosan aqueous solution in nitrogen atmosphere, inert gas or l
(i) The manufacturing method according to claim (1), which involves extrusion molding in an ammonia gas atmosphere.
特許請求の範囲第(1)頂に記載の製造方法。(3) The manufacturing method according to claim 1, wherein the chitosan concentration is 151 q6 to 40 wt.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58148742A JPS6040224A (en) | 1983-08-16 | 1983-08-16 | Manufacture of formed article of chitosan |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58148742A JPS6040224A (en) | 1983-08-16 | 1983-08-16 | Manufacture of formed article of chitosan |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6040224A true JPS6040224A (en) | 1985-03-02 |
JPS638208B2 JPS638208B2 (en) | 1988-02-22 |
Family
ID=15459604
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58148742A Granted JPS6040224A (en) | 1983-08-16 | 1983-08-16 | Manufacture of formed article of chitosan |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6040224A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5622666A (en) * | 1992-09-30 | 1997-04-22 | Novasso Oy | Modified viscose fibres and method for their manufacture |
KR100451112B1 (en) * | 1999-05-15 | 2004-10-02 | 기 수 한 | Kitosan staple fibers, chemically modified kitosan fibers, and a process for preparation thereof |
FR2860007A1 (en) * | 2003-09-18 | 2005-03-25 | Europlak | Spinning chitosan to produce chitosan yarn, e.g. for medical, cosmetic or agricultural applications, comprises subjecting a chitosan solution to the coagulating action of a gas |
WO2011140860A1 (en) * | 2010-05-10 | 2011-11-17 | 山东华兴海慈新材料有限公司 | Spinning solution for industrially producing pure chitosan fiber and preparation method thereof |
JP2016536481A (en) * | 2013-09-02 | 2016-11-24 | 海斯摩爾生物科技有限公司 | High-viscosity pure chitosan spinning solution combined air bubble removal method |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0248322A (en) * | 1988-08-09 | 1990-02-19 | Myotoku Kk | Parallel shift device |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56106901A (en) * | 1980-01-30 | 1981-08-25 | Mitsubishi Rayon Co Ltd | Production of formed product of chitosan |
JPS5777310A (en) * | 1980-10-29 | 1982-05-14 | Unitika Ltd | Chitin fiber and its production |
-
1983
- 1983-08-16 JP JP58148742A patent/JPS6040224A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56106901A (en) * | 1980-01-30 | 1981-08-25 | Mitsubishi Rayon Co Ltd | Production of formed product of chitosan |
JPS5777310A (en) * | 1980-10-29 | 1982-05-14 | Unitika Ltd | Chitin fiber and its production |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5622666A (en) * | 1992-09-30 | 1997-04-22 | Novasso Oy | Modified viscose fibres and method for their manufacture |
KR100451112B1 (en) * | 1999-05-15 | 2004-10-02 | 기 수 한 | Kitosan staple fibers, chemically modified kitosan fibers, and a process for preparation thereof |
FR2860007A1 (en) * | 2003-09-18 | 2005-03-25 | Europlak | Spinning chitosan to produce chitosan yarn, e.g. for medical, cosmetic or agricultural applications, comprises subjecting a chitosan solution to the coagulating action of a gas |
WO2005025520A3 (en) * | 2003-09-18 | 2005-05-19 | Europlak | Chitosan spinning method, device therefor, and resulting chitosan yarn, and uses thereof |
WO2011140860A1 (en) * | 2010-05-10 | 2011-11-17 | 山东华兴海慈新材料有限公司 | Spinning solution for industrially producing pure chitosan fiber and preparation method thereof |
GB2494793A (en) * | 2010-05-10 | 2013-03-20 | Shangdong Huaxing Haici New Materials Co Ltd | Spinning solution for industrially producing pure chitosan fiber and preparation method thereof |
US9017469B2 (en) | 2010-05-10 | 2015-04-28 | Shandong Huaxing Haici New Materials Co., Ltd | Spinning solution for industrial production of pure chitosan fiber and the method for fabricating the same |
GB2494793B (en) * | 2010-05-10 | 2016-12-21 | Shangdong Huaxing Haici New Mat Co Ltd | A method for fabricating a spinning solution for industrial production of pure chitosan fibre. |
JP2016536481A (en) * | 2013-09-02 | 2016-11-24 | 海斯摩爾生物科技有限公司 | High-viscosity pure chitosan spinning solution combined air bubble removal method |
Also Published As
Publication number | Publication date |
---|---|
JPS638208B2 (en) | 1988-02-22 |
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