JPH02200810A - Production of pulpy chitosan fiber and production apparatus therefor - Google Patents
Production of pulpy chitosan fiber and production apparatus thereforInfo
- Publication number
- JPH02200810A JPH02200810A JP2226789A JP2226789A JPH02200810A JP H02200810 A JPH02200810 A JP H02200810A JP 2226789 A JP2226789 A JP 2226789A JP 2226789 A JP2226789 A JP 2226789A JP H02200810 A JPH02200810 A JP H02200810A
- Authority
- JP
- Japan
- Prior art keywords
- chitosan
- fibers
- pulp
- laminar flows
- contact zone
- 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
- 229920001661 Chitosan Polymers 0.000 title claims abstract description 90
- 239000000835 fiber Substances 0.000 title claims abstract description 49
- 238000004519 manufacturing process Methods 0.000 title claims description 18
- 230000001112 coagulating effect Effects 0.000 claims abstract description 12
- 239000007788 liquid Substances 0.000 claims description 14
- 238000005345 coagulation Methods 0.000 claims description 9
- 230000015271 coagulation Effects 0.000 claims description 9
- 229920002678 cellulose Polymers 0.000 abstract description 14
- 239000001913 cellulose Substances 0.000 abstract description 14
- 239000012530 fluid Substances 0.000 abstract 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 18
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 18
- 238000000034 method Methods 0.000 description 17
- 239000000243 solution Substances 0.000 description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 239000002253 acid Substances 0.000 description 8
- 239000007864 aqueous solution Substances 0.000 description 8
- 229920002101 Chitin Polymers 0.000 description 5
- 239000011230 binding agent Substances 0.000 description 5
- 230000006196 deacetylation Effects 0.000 description 4
- 238000003381 deacetylation reaction Methods 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- 241000238557 Decapoda Species 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 150000007513 acids Chemical class 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
- 239000011707 mineral Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 230000001580 bacterial effect Effects 0.000 description 2
- 210000004027 cell Anatomy 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- 241000254173 Coleoptera Species 0.000 description 1
- 241000238424 Crustacea Species 0.000 description 1
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- 241000238631 Hexapoda Species 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- 241000269821 Scombridae Species 0.000 description 1
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 210000002421 cell wall Anatomy 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000000850 deacetylating effect Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 230000003100 immobilizing effect Effects 0.000 description 1
- 239000012784 inorganic fiber Substances 0.000 description 1
- 235000020640 mackerel Nutrition 0.000 description 1
- 239000012567 medical material Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Artificial Filaments (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、分離膜、医療用材料、食品包装紙等の特殊紙
の原料としてのキトサン繊維の新規な製造法及び製造装
置に関する。さらに詳しくいえば、叩解したセルロース
パルプ状のキトサン繊維の簡便な製造法及びその製造装
置に関する。このパルプ状キトサン繊維はセルロースパ
ルプ、合成繊維及び無機繊維等のバインダーとして、ま
た、酵素あるいは酵母等の菌体の固定に利用することも
可能である。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a novel method and apparatus for producing chitosan fibers as a raw material for special papers such as separation membranes, medical materials, and food wrapping paper. More specifically, the present invention relates to a simple method for producing chitosan fibers in the form of beaten cellulose pulp and an apparatus for producing the same. This pulpy chitosan fiber can be used as a binder for cellulose pulp, synthetic fibers, inorganic fibers, etc., and also for immobilizing enzymes or bacterial cells such as yeast.
従来の技術
キチンは海老、蟹等の甲殻類、かぶと虫などの昆虫類、
菌類の細胞壁等に存在し、自然界ではセルロースに次い
で広くかつ多量に生産されており、その化学構造はポリ
〔β(1−4)−2−アセトアミド−2−デオキシグル
カン〕で表わされる多糖類である。しかしながら、キチ
ンはセルロースが広く各分野で利用されているのに比べ
てほとんど利用されるに至っていない。Conventional technology chitin can be found in crustaceans such as shrimp and crabs, insects such as beetles,
It exists in the cell walls of fungi, etc., and is widely produced in nature in large quantities, second only to cellulose. Its chemical structure is a polysaccharide represented by poly[β(1-4)-2-acetamido-2-deoxyglucan]. be. However, compared to cellulose, which is widely used in various fields, chitin has hardly been used.
キチンを濃厚な水酸化ナトリウム液で加水分解すると、
脱アセチル化が起り、キトサンが生成する。脱アセチル
化度70%以上のものは一般的にキトサンと呼ばれてい
る。キトサンはアルカリや通常のを機溶剤には溶解しな
いが、希酸には溶解する。そのキトサンを原料とするキ
トサン繊維の製造法としてはキトサンを酢酸水溶液に溶
解して、細孔より凝固液中に押出し延伸してキトサン繊
維を製造する方法が提案されている(特開昭56−26
049号公報)。しかし、この方法で得られるキトサン
繊維は単独で紙にすると強度は小さく、多量のバインダ
ーを加える必要がある等の欠点を有している。When chitin is hydrolyzed with concentrated sodium hydroxide solution,
Deacetylation occurs and chitosan is produced. Those with a degree of deacetylation of 70% or more are generally called chitosan. Chitosan does not dissolve in alkalis or ordinary organic solvents, but it does dissolve in dilute acids. As a method for producing chitosan fibers using chitosan as a raw material, a method has been proposed in which chitosan is dissolved in an acetic acid aqueous solution, extruded through pores into a coagulating liquid, and stretched to produce chitosan fibers (Japanese Patent Application Laid-Open No. 1983-1999-1). 26
Publication No. 049). However, chitosan fibers obtained by this method have drawbacks such as low strength when made into paper alone and the need to add a large amount of binder.
また、粉末状のキトサンを水に分散させ、高圧用均質化
装置を通過させて、キトサン懸濁液を製造し、次いでキ
トサン懸濁液を抄紙する方法も提案されている(特開昭
59−84938号公報)。しかしながら、この方法は
高圧用均質化装置という特殊な装置を必要とするため、
その製造コストが高くなる上、高温下での高剪断力を加
える等の苛酷な条件のため、キトサンのグルコシド結合
の切断を伴うという難点がある。In addition, a method has also been proposed in which powdered chitosan is dispersed in water and passed through a high-pressure homogenizer to produce a chitosan suspension, and then the chitosan suspension is made into paper (Japanese Patent Laid-Open No. 1983-1982-1). 84938). However, this method requires special equipment called a high-pressure homogenizer, so
In addition to the high manufacturing cost, the harsh conditions such as applying high shear force at high temperatures lead to the cleavage of glucosidic bonds in chitosan.
キトサンの希酸水溶液に撹拌下アルカリ金属水酸化物を
添加してキトサン懸濁液を調整し、次いでこれを抄造す
るキトサン系抄造体の製造方法が提案された(特開昭6
3−59499号公報)。しかしながら、この方法は家
庭用ミキサー等で撹拌する!こめ、キトサンはコロイド
状となり、抄紙する際に微細物による金網が目詰りし、
脱水が困難となる等の問題があった。A method for producing a chitosan-based paper product was proposed in which a chitosan suspension was prepared by adding an alkali metal hydroxide to a dilute acid aqueous solution of chitosan under stirring, and then papermaking was made from this suspension (Japanese Patent Application Laid-Open No. 1989-1993).
3-59499). However, this method requires stirring with a household mixer! Rice and chitosan become colloidal, and the fine particles clog the wire mesh during paper making.
There were problems such as difficulty in dehydration.
このようにキトサン繊維の紙の原料として使用するため
には、繊維の構造に問題があり、紙の強度は小さく多量
のバインダーを加える必要がある等の欠点を有している
。As described above, in order to use chitosan fibers as a raw material for paper, there are problems with the structure of the fibers, the strength of the paper is low, and it is necessary to add a large amount of binder.
発明が解決しようとする課題
本発明は、叩解したセルロースパルプのような枝分れし
た保水性のあるキトサン繊維を製造することによって、
前記の欠点を解消することを見出したものである。本発
明は公知のセルロースバルブのような繊維を簡便な方法
で製造するための方法及び装置を提供することを目的と
するものである。Problems to be Solved by the Invention The present invention solves the following problems by producing branched water-retentive chitosan fibers such as beaten cellulose pulp.
It has been discovered that the above-mentioned drawbacks can be overcome. An object of the present invention is to provide a method and apparatus for producing fibers such as known cellulose bulbs in a simple manner.
課題を解決するための手段
本発明者らは、従来のキトサン繊維の製造法に代わる新
規な製造方法の工業的に有利な製造法について鋭意検討
した結果、キトサンの水分散液に酢酸などの酸を添加し
てキトサンを溶解させ、次にたがいに対向する2方向か
ら2つの連続層流として流れている凝固液の中間に、こ
のキトサン溶液を連続的又は断続的に加えると、意外に
も叩解したセルロースパルプのように、枝分れした繊維
長11II+以上のパルプ状キトサンが生成し、これを
通常の方法で抄紙すると、良好な地合いと優れた強度特
性を有し、しかも密度の高いキトサン系抄造体が容易に
得られることを発見し、本発明を完成するに至っt;。Means for Solving the Problems As a result of intensive study on a new manufacturing method that is industrially advantageous as an alternative to the conventional manufacturing method for chitosan fibers, the present inventors found that an acid such as acetic acid was added to the chitosan aqueous dispersion. When this chitosan solution is added continuously or intermittently to the middle of the coagulating liquid flowing as two continuous laminar flows from two opposing directions, surprisingly, the refining Like cellulose pulp, pulpy chitosan with a branched fiber length of 11II+ or more is produced, and when this is made into paper by a normal method, it has good texture and excellent strength properties, and is a high-density chitosan-based paper. It was discovered that paper products can be easily obtained, leading to the completion of the present invention.
すなわち、本発明は、所定の接触帯域において、キトサ
ン溶液と凝固液とを接触させてキトサン繊維を製造する
に当り、該接触帯域に凝固液をたがいに対向する2方向
から2つの連続層流として導入し、該接触帯域において
それぞれの層流をほぼ直角方向に方向転換させながら排
出させると共に、該接触帯域にキトサン溶液を連続的又
は断続的に導入し、凝固と同時に繊維状化することによ
ってパルプ状キトサン繊維を製造する方法及び凝固液を
満たした上方開放容器、容器中にほぼ等間隔で2列2行
に直立して配置した4本の回転ローラ、隣接する各ロー
ラをそれぞれ逆方向に回転させるための駆動機構及び4
本の回転ローラのほぼ中央位置に向けて開口したキトサ
ン溶液導入管から成るパルプ状キトサン繊維の製造装置
を提供するものである。That is, in producing chitosan fibers by bringing a chitosan solution and a coagulating liquid into contact in a predetermined contact zone, the present invention applies the coagulating liquid to the contact zone as two continuous laminar flows from two opposing directions. The chitosan solution is continuously or intermittently introduced into the contact zone, and the chitosan solution is simultaneously coagulated and fibrous, thereby producing pulp. A method for producing chitosan fibers, an upwardly open container filled with a coagulation liquid, four rotating rollers arranged vertically in two rows and two rows at approximately equal intervals in the container, and each adjacent roller rotates in the opposite direction. a drive mechanism for causing the
The present invention provides an apparatus for producing pulp-like chitosan fibers, which comprises a chitosan solution introduction tube that opens toward the approximate center of a rotating roller of a book.
以下、本発明の詳細な説明する。The present invention will be explained in detail below.
本発明において使用するキトサンとしては、市販されて
いるキチン又は海老殻や蟹殻等から採取したキチンを常
法により脱アセチル化した脱アセチル化度70%以上の
キトサンを挙げることができる。また、これらのキトサ
ンに鉱酸又は酸化剤を作用させて得られる低分子化キト
サンも挙げることができる。また、キトサンを溶解させ
る溶剤としでは、ギ酸、酢酸等の有機酸及び塩酸等の鉱
酸の水溶液が挙げられる。また、凝固液としては水酸化
ナトリウム、水酸化カルシウムやエチレンジアミン等の
アミン類のアルカリ水溶液又はアルカリメタノール溶液
が用いられる。Examples of the chitosan used in the present invention include commercially available chitin or chitosan with a deacetylation degree of 70% or more obtained by deacetylating chitin collected from shrimp shells, crab shells, etc. by a conventional method. Also included are low-molecular-weight chitosans obtained by treating these chitosans with mineral acids or oxidizing agents. Examples of solvents for dissolving chitosan include aqueous solutions of organic acids such as formic acid and acetic acid, and mineral acids such as hydrochloric acid. Further, as the coagulating liquid, an alkaline aqueous solution or alkaline methanol solution of amines such as sodium hydroxide, calcium hydroxide, and ethylenediamine is used.
次に添付図面に従って、本発明の製造装置を説明する。Next, the manufacturing apparatus of the present invention will be explained according to the accompanying drawings.
第1図は本発明装置の要部を示す斜視図であり、また第
2図は平面図であって、本発明装置は、箱状の凝固浴槽
2中にほぼ等間隔に2列2行に配置した4本のロール1
.1,1.1から構成され、これらのロールは所要の駆
動機構、例えばモータ(図示せず)によりそれぞれ隣接
するものがたがいに逆方向に回転するように、すなわち
各矢印方向に回転するように構成されている。この回転
速度は例えば0〜1500rpn+の範囲で調整しうる
ようになっている。このようにしてロール1.1.1.
lを回転させると凝固液は第2図のA、Aの方向から凝
固槽2の中心部3に向って内方へ移動し、この地点から
B、B方向に向きを変え、外方へ移動する。このように
して乱流のない層流が形成される。FIG. 1 is a perspective view showing the main parts of the apparatus of the present invention, and FIG. 2 is a plan view. 4 rolls placed 1
.. 1 and 1.1, and these rolls are driven by a required drive mechanism, e.g. a motor (not shown), so that the adjacent rolls rotate in opposite directions, i.e. in the directions of the respective arrows. It is configured. This rotational speed can be adjusted, for example, in the range of 0 to 1500 rpm+. In this way Roll 1.1.1.
When rotating l, the coagulating liquid moves inward from the direction A and A in Figure 2 toward the center 3 of the coagulation tank 2, and from this point changes direction in the direction B and B and moves outward. do. In this way, a laminar flow without turbulence is created.
そして、この中心部3に対し導入管4を介してキトサン
溶液を連続的又は断続的に滴下すると、キトサン溶液は
左右に延伸されるとともに凝固し、枝分れした繊維長1
i+m以上のキトサン繊維が得られる。このパルプ状キ
トサン繊維を200メツシユの金網で受は十分に水洗を
行う。最適な条件下で製造したパルプ状キトサン繊維で
は、200メツシユの金網を通過する微細物はほとんど
なく繊維状物のみが得られる。When a chitosan solution is continuously or intermittently dropped into this central part 3 through an introduction tube 4, the chitosan solution is stretched from side to side and solidified, resulting in branched fiber lengths 1
Chitosan fibers of i+m or more are obtained. This pulp-like chitosan fiber is thoroughly washed with water using a 200-mesh wire mesh. In pulp-like chitosan fibers produced under optimal conditions, only fibrous materials are obtained with almost no fine particles passing through the 200-mesh wire gauze.
本発明におけるパルプ状キトサン繊維の調製は、例えば
以下のような方法で行うことができるが、これらの具体
例に限定されるものではない。Pulp-like chitosan fibers in the present invention can be prepared, for example, by the following methods, but are not limited to these specific examples.
まず、キトサン濃度が0.1−10%、望ましくはlO
〜2000cpになるようにキトサンの希酸水溶液を作
成する。次にパルプ状キトサン製造装置の凝固浴槽に水
酸化ナトリウム水溶液など凝固液を入れ、ロールを回転
させる。4本のロールの中心点付近にキトサンの希酸水
溶液を連続的あるいは断続的に滴下する。キトサンの濃
度によって異なるが、ロールの回転速度が遅いとビーズ
状あるいはまが玉状となり、回転速度が速すぎるとコロ
イド状となる傾向がある。しかし、500〜1300r
pmの回転速度では、枝分れしたパルプ状の繊維が得ら
れる。最適な回転速度において、キトサンの濃度の影響
を調べると、低濃度では微細な鱗状となり、高濃度では
ビーズ状となるが、最適な濃度ではパルプ状のキトサン
繊維が得られる。低分子化したキトサンでは、最適濃度
を高めることも可能である。凝固液としては、5%の水
酸化ナトリウムが適していた。First, the chitosan concentration is 0.1-10%, preferably lO
A dilute acid aqueous solution of chitosan is prepared to have a concentration of ~2000 cp. Next, a coagulating liquid such as an aqueous sodium hydroxide solution is placed in the coagulating bath of the pulp chitosan manufacturing apparatus, and the rolls are rotated. A dilute aqueous chitosan acid solution is dropped continuously or intermittently near the center of the four rolls. Although it varies depending on the concentration of chitosan, if the rotation speed of the roll is slow, it tends to become bead-like or bead-like, and if the rotation speed is too fast, it tends to become colloidal. However, 500~1300r
At rotation speeds of pm, branched pulpy fibers are obtained. Examining the effect of chitosan concentration at the optimal rotation speed, we found that at low concentrations, the fibers become fine scales, at high concentrations they become bead-like, but at the optimal concentration, pulp-like chitosan fibers are obtained. It is also possible to increase the optimum concentration of low-molecular chitosan. 5% sodium hydroxide was suitable as the coagulation liquid.
このような方法で得られる本発明のパルプ状キトサン繊
維は叩解したパルプと同様に保水性が高く1、水に対す
る分散性も優れている。水洗後、このパルプ状キトサン
繊維紙粁を単独又はセルロースと混合し、JISP 8
209法に準じて抄紙することができる。The pulp-like chitosan fibers of the present invention obtained by such a method have high water retention properties1 like beaten pulp, and also have excellent dispersibility in water. After washing with water, this pulp-like chitosan fiber paper mackerel is used alone or mixed with cellulose, and JISP 8
Paper can be made according to the 209 method.
本発明によるパルプ状キトサン繊維は通常の抄紙法によ
り抄紙することができ、得られた紙は高密度でかつ耐水
性の高い紙様を呈した。また、セルロースバルブとの混
抄においても、簡単に抄紙することができ、耐水性の高
い紙を製造することができる。The pulp-like chitosan fibers according to the present invention can be made into paper using a conventional paper-making method, and the paper obtained has a paper-like appearance with high density and high water resistance. In addition, even in mixed papermaking with cellulose bulbs, paper can be easily made and paper with high water resistance can be produced.
発明の効果
本発明方法によるパルプ状キトサン繊維の製法は簡便で
繊維の切断を伴うこともなく製造できる優れた方法であ
る。Effects of the Invention The method for producing pulp-like chitosan fibers according to the method of the present invention is an excellent method that is simple and can be produced without cutting the fibers.
この方法で調製したパルプ状キトサン繊維は叩解したセ
ルロースバルブのように枝分れした繊維からなり、保水
性が高く、水分散性もよく、セルロースバルブと同様の
用途に広く利用することができる等であって、新しいタ
イプのキトサン繊維として期待できるものである。また
、セルロースバルブがアニオン性を示すのに比べて、本
発明のパルプ状キトサン繊維はカチオン性を示すことを
利用してセルロースバルブ等との混抄やバインダーとし
ても使用でき、さらに酵素や菌体の固定化担体、分離性
シート等に利用できる等の応用範囲も広く大いに期待で
・きる。Pulp-like chitosan fibers prepared by this method are composed of branched fibers similar to beaten cellulose bulbs, have high water retention and good water dispersibility, and can be widely used in the same applications as cellulose bulbs. Therefore, it can be expected as a new type of chitosan fiber. In addition, compared to cellulose bulbs which exhibit anionic properties, the pulp-like chitosan fibers of the present invention exhibit cationic properties and can be used as a binder or mixed with cellulose bulbs, etc., and can also be used as a binder for enzymes and bacterial cells. It has great potential for a wide range of applications, including use as immobilization carriers, separable sheets, etc.
実施例 次に本発明を実施例によって詳細に説明する。Example Next, the present invention will be explained in detail by way of examples.
実施例1
脱アセチル化度が100%のキトサン(0,5%キトサ
7−0.5%酢酸水溶液の粘度は385cp/ 20°
C)15gに水1243gを入れ、キトサンの分散液と
し、これに1%の酢酸水溶液1243gを添加し、2時
間撹拌して、0.6%濃度のキトサン溶液を調製した。Example 1 Chitosan with a degree of deacetylation of 100% (viscosity of 0.5% chitosa 7-0.5% acetic acid aqueous solution is 385 cp/20°
C) 1243 g of water was added to 15 g to prepare a chitosan dispersion, and 1243 g of a 1% acetic acid aqueous solution was added thereto and stirred for 2 hours to prepare a 0.6% chitosan solution.
このキトサン溶液の粘度は419cp/ 20℃であっ
た。この溶液をろ過脱泡後、内径lamのノズルをつけ
た分液漏斗に入れた。The viscosity of this chitosan solution was 419 cp/20°C. This solution was filtered and degassed, and then placed in a separatory funnel equipped with a nozzle having an inner diameter of lam.
次に、バルブ状キトサン繊維製造装置の凝固浴槽に5%
の水酸化ナトリウムの水溶液を入れ、4本のロールを8
00rpmで回転させた。その中央部に分液漏斗からキ
トサン溶液を断続的に滴下し、平均繊維長1111以上
のパルプ状キトサン繊維を製造した。この繊維を200
メツシユのふるいに入れ、十分に水洗し、JIS法に準
じ抄紙した。なお、水洗中にふるいを通過するコロイド
物質は皆無であった。得られた紙は厚み0.06mm、
密度0−92g/crm3であり、裂断長は1.54k
mであっt;。Next, 5%
Add an aqueous solution of sodium hydroxide and place 4 rolls into 8
It was rotated at 00 rpm. A chitosan solution was intermittently dropped into the center from a separatory funnel to produce pulp-like chitosan fibers with an average fiber length of 1111 or more. 200% of this fiber
The mixture was placed in a mesh sieve, thoroughly washed with water, and paper was made according to the JIS method. Note that no colloidal substances passed through the sieve during washing with water. The obtained paper has a thickness of 0.06 mm,
Density 0-92g/crm3, breaking length 1.54k
It's m;.
実施例2
実施例Iで用いたキトサンを使用して、キトサン濃度と
パルプ状キトサン繊維の製造条件を調べた。その結果を
第1表に示す。Example 2 Using the chitosan used in Example I, the chitosan concentration and the manufacturing conditions of pulp-like chitosan fibers were investigated. The results are shown in Table 1.
第 1 表
第1表から明らかなように、キトサンの濃度が低いと溶
解又はコロイド状となり、また濃度が高いとビーズ状に
なることが判明した。最適な条件下で、凝固浴濃度の影
響を調べると、水酸化ナトリウムの濃度は1%以上必要
であり、5%濃度が最適であった。Table 1 As is clear from Table 1, when the concentration of chitosan is low, it becomes dissolved or colloidal, and when the concentration is high, it becomes bead-like. When examining the influence of coagulation bath concentration under optimal conditions, it was found that the concentration of sodium hydroxide should be 1% or more, and 5% concentration was optimal.
実施例3
実施例1で使用したキトサンを鉱酸で加水分解を行い、
キトサンを低分子化した。0.5%の酢酸に帆5%にな
るよう1こ溶解した時の粘度(20°C)は92(A)
及び14(B)cpであった。この低分子化したキトサ
ンを用い、パルプ状キトサン繊維の製造条件を調べた結
果を第2表に示す。Example 3 The chitosan used in Example 1 was hydrolyzed with mineral acid,
Chitosan has been reduced to a lower molecular weight. When dissolved in 0.5% acetic acid to give a concentration of 5%, the viscosity (at 20°C) is 92 (A).
and 14(B) cp. Table 2 shows the results of examining the manufacturing conditions for pulp-like chitosan fibers using this low-molecular-weight chitosan.
第 2 表
により、キトサン溶液を高濃度にしてパルプ状キトサン
繊維が容易に得られることを認めた。From Table 2, it was confirmed that pulpy chitosan fibers could be easily obtained by increasing the concentration of the chitosan solution.
実施例4
実施例1で得られたパルプ状キトサン繊維とNBKPと
の混抄を行った。パルプ状キトサン繊維の増加とともに
得られた紙の密度は高くなり、まt;、抄紙排水である
白水中のコロイド物質は著しく減少することが判明した
。Example 4 The pulp-like chitosan fiber obtained in Example 1 and NBKP were mixed into paper. It was found that as the pulpy chitosan fibers increased, the density of the paper obtained increased, and the colloidal substances in the white water, which is wastewater from papermaking, decreased significantly.
第1図は本発明の方法を実施するのに適用されたパルプ
状キトサン繊維の製造装置の概略図、第2図はバルブ状
キトサン繊維製造装置中のロールを回転させた際の凝固
液の流れを示す。
図中符号lはロール、2は凝固浴槽、3は中心部、4は
キトサン溶液導入管であり、A、Bは凝固液の流れ方向
である。Figure 1 is a schematic diagram of a pulp chitosan fiber manufacturing apparatus applied to carry out the method of the present invention, and Figure 2 is a flow of coagulation liquid when the rolls in the bulb-shaped chitosan fiber manufacturing apparatus are rotated. shows. In the figure, numeral 1 is a roll, 2 is a coagulation bath, 3 is a center part, 4 is a chitosan solution introduction tube, and A and B are the flow direction of the coagulation liquid.
Claims (1)
を接触させてキトサン繊維を製造するに当り、該接触帯
域に凝固液をたがいに対向する2方向から2つの連続層
流として導入し、該接触帯域においてそれぞれの層流を
ほぼ直角方向に方向転換させながら排出させると共に、
該接触帯域にキトサン溶液を連続的又は断続的に導入し
、凝固と同時に繊維状化することを特徴とするパルプ状
キトサン繊維の製造方法。 2 凝固液を満たした上方開放容器、容器中にほぼ等間
隔で2列2行に直立して配置した4本の回転ローラ、隣
接する各ローラをそれぞれ逆方向に回転させるための駆
動機構及び4本の回転ローラのほぼ中央位置に向けて開
口したキトサン溶液導入管から成るパルプ状キトサン繊
維の製造装置。[Claims] 1. When producing chitosan fibers by bringing a chitosan solution into contact with a coagulation liquid in a predetermined contact zone, the coagulation liquid is introduced into the contact zone in two continuous laminar flows from two opposing directions. and discharge the respective laminar flows in the contact zone while changing direction approximately at right angles, and
A method for producing pulp-like chitosan fibers, characterized in that a chitosan solution is continuously or intermittently introduced into the contact zone, and simultaneously coagulated and turned into fibers. 2. An upwardly open container filled with a coagulating liquid, 4 rotating rollers arranged vertically in 2 rows and 2 rows at approximately equal intervals in the container, a drive mechanism for rotating each adjacent roller in the opposite direction, and 4. This is a pulp chitosan fiber manufacturing device consisting of a chitosan solution introduction tube that opens toward the center of a rotating book roller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2226789A JPH02200810A (en) | 1989-01-30 | 1989-01-30 | Production of pulpy chitosan fiber and production apparatus therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2226789A JPH02200810A (en) | 1989-01-30 | 1989-01-30 | Production of pulpy chitosan fiber and production apparatus therefor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02200810A true JPH02200810A (en) | 1990-08-09 |
| JPH0450405B2 JPH0450405B2 (en) | 1992-08-14 |
Family
ID=12077996
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2226789A Granted JPH02200810A (en) | 1989-01-30 | 1989-01-30 | Production of pulpy chitosan fiber and production apparatus therefor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02200810A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2014065747A1 (en) * | 2012-10-22 | 2014-05-01 | Innventia Ab | Method of spinning fibres or extrusion, and the products obtained |
| CN112981721A (en) * | 2021-03-09 | 2021-06-18 | 维尼健康(深圳)股份有限公司 | Method for manufacturing natural-color degradable dispersible non-woven fabric |
-
1989
- 1989-01-30 JP JP2226789A patent/JPH02200810A/en active Granted
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2014065747A1 (en) * | 2012-10-22 | 2014-05-01 | Innventia Ab | Method of spinning fibres or extrusion, and the products obtained |
| US10132005B2 (en) | 2012-10-22 | 2018-11-20 | Rise Innventia Ab | Method of spinning fibres or extrusion, and the products obtained |
| CN112981721A (en) * | 2021-03-09 | 2021-06-18 | 维尼健康(深圳)股份有限公司 | Method for manufacturing natural-color degradable dispersible non-woven fabric |
| CN112981721B (en) * | 2021-03-09 | 2022-01-14 | 维尼健康(深圳)股份有限公司 | Method for manufacturing natural-color degradable dispersible non-woven fabric |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0450405B2 (en) | 1992-08-14 |
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