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JPH054139B2 - - Google Patents
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JPH054139B2 - - Google Patents

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Publication number
JPH054139B2
JPH054139B2 JP60175265A JP17526585A JPH054139B2 JP H054139 B2 JPH054139 B2 JP H054139B2 JP 60175265 A JP60175265 A JP 60175265A JP 17526585 A JP17526585 A JP 17526585A JP H054139 B2 JPH054139 B2 JP H054139B2
Authority
JP
Japan
Prior art keywords
chitosan
anion exchanger
solution
water
diisocyanate
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.)
Expired - Fee Related
Application number
JP60175265A
Other languages
Japanese (ja)
Other versions
JPS6238246A (en
Inventor
Yoshihide Kawamura
Hiroaki Yabe
Itsuo Kurahashi
Eiji Hirose
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.)
Fujibo Holdings Inc
Original Assignee
Fuji Spinning Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Fuji Spinning Co Ltd filed Critical Fuji Spinning Co Ltd
Priority to JP60175265A priority Critical patent/JPS6238246A/en
Publication of JPS6238246A publication Critical patent/JPS6238246A/en
Publication of JPH054139B2 publication Critical patent/JPH054139B2/ja
Granted legal-status Critical Current

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  • Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
  • Polysaccharides And Polysaccharide Derivatives (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

〔産業上の利用分野〕 本発明は、粒状多孔質のキトサンを担体とした
陰イオン交換体の製造方法に関し、本発明による
陰イオン交換体は、クロマトグラフイ用充填剤、
生体触媒固定化用担体、及び細胞培養用担体等多
くの用途に好適なものである。 〔従来技術〕 近年、酵素・細胞利用工業に於いて、触媒的作
用を応用した反応工程の連続自動化が進んでい
る。このような工程においては、各種のイオン交
換体が用いられるが、担体を塔又は槽内に充填し
て使用している間に目詰りを生じたり、担体自体
が破壊したりして反応液の流通が順調に行なわれ
なくなる欠点があり、これを解除するために担体
の改善が検討されているが、未だ充分でない状態
にある。 キチン、キトサンを担体として陰イオン交換体
を製造する方法としては、例えば特公昭55−
35180号による提案がなされている。当該公報に
開示されている方法は、キチン又はキトサンその
ものを原料としてアリカリ水溶液に接触させた
後、置換、もしくは非置換アミノ基又は置換第四
アンモニウム基を有する有機ハライドを結合させ
て陰イオン交換体を製造する方法であり、得られ
た陰イオン交換体のイオン交換能は、実施例等か
ら明らかな如く、0.8meq/g程度にとどまって
居り、酵素固定化用担体として用いた場合に、酵
素の吸着量が極めて低く、触媒効率が劣つている
欠点があり、又、細胞培養用担体として使用する
場合には、その用いられる細胞によつては電荷の
制御が必要となるが、この方法によつて得られた
陰イオン交換体は、その処理時に酸又はアリカリ
により膨潤ないしは溶解してしまうという欠点が
ある。 〔発明が解決しようとする問題点〕 本発明は、上述した従来の欠点を解決したキト
サン系陰イオン交換体の製造方法を提供すること
を目的とする。本発明は、低分子量キトサンを用
いることにより粒度の揃った、しかも球表面、割
断面に均一な微細孔を具備する粒状多孔質キトサ
ンを得、更にこれを極性溶媒中で有機ジイソシア
ネート化合物と接触架橋させた材料を用いること
により、従来の方法で得られたキトサン系陰イオ
ン交換体に比較して、イオン交換能を著しく向上
させると共にその能力を自由に調整可能であり、
充分な物理的強度を有し、酸及びアリカリ性溶液
中での膨潤乃至は溶解の生じない、広範囲のイオ
ン交換能域で使用可能なキトサン系陰イオン交換
体を製造し、上記した従来の欠点を解決したもの
である。 〔問題点を解決するための手段〕 本発明は、低分子量キトサンを酸性水溶液に溶
解し、該溶解液を塩基性溶液中に落下せしめて得
た粒状多孔質キトサンを、極性溶媒中で有機ジイ
ソシアネート化合物と接触架橋させ、その後塩基
性溶液と接触させた後、置換もしくは非置換アミ
ノ基又は置換第四アンモニウム基を有する有機ハ
ライドと反応させることを特徴とする陰イオン交
換体を製造する方法にかかわる。 本発明においては、平均分子量が10000〜
230000の低分子量キトサンが用いられる。フレー
ク状の高分子量キトサンは過硼酸ソーダ水溶液中
で加温処理することによつて所望の分子量を有す
る良質なキトサンが得られる。低分子量キトサン
は、酢酸、ジクロル酢酸、蟻酸の単独、若しくは
混合物の水溶液に溶解し、キトサン酸性溶液とす
るが、その濃度は取扱いの容易な範囲、即ち2〜
20%の範囲で自由に選択できる。該酸性溶液を例
えば孔径0.1〜0.25m/mより圧力下で次の塩基
性凝固浴中に一定量ずつ落下させ、粒状多孔質キ
トサンを得る。凝固浴の塩基性物質としては、水
酸化ナトリウム、水酸化カリウム、炭酸ナトリウ
ム、炭酸カリウム、アンモニア、エチレンジアミ
ン等のアルカリ性物質が用いられ、塩基性溶液に
は、水、又はメタノール、エタノール等の極性を
有するアルコール類又は水とアルコールとの混合
物に前記塩基性物質を加えて使用する。粒状多孔
性キトサンは、凝固液中を粒状で沈降しながら脱
溶媒反応の進行と共に微細組織を形成する。沈降
した粒状凝固物を取り出し、中性になる迄水洗
し、粒状多孔質キトサンを得る。 次いで、極性溶媒を用いて水洗に用いた水を粒
状多孔質キトサンから置換除去する。水置換に用
いた極性溶媒と同一又は異る極性溶媒中に有機ジ
イソシアネート化合物を溶解した液中で、キトサ
ンの球状凝固物の架橋処理を行い、充分架橋処理
が行われた後で、未反応の有機ジイソシアネート
化合物を反応に用いた極性溶媒によつて充分に洗
浄除去した後、更に水で充分洗浄し、架橋処理を
した粒状多孔質キトサンを得る。 本発明で用いる極性溶媒としては、メタノー
ル、エタノール、イソプロピルアルコール等のア
ルコール類、アセトン、メチルエチルケトン等の
ケトン類、ジメチルホルムアミド、ジメチルアセ
トアミド等のアミド類が用いられ、1種又は2種
以上混合して使用してもよい。 有機ジイソシアネートとしては、4,4′−ジフ
エルメタンジイソシアネート、2,4−トリレン
ジイソシアネート、ナフタレンジイソシアネー
ト、1,4−ジクロヘキサンジイソシアネート、
4,4′−ジシクロヘキシルメタンジイソシアネー
ト、キシリレンジイソシアネート、イソフオロン
ジイソシアネート、ヘキサメチレンジイソシアネ
ート等が挙げられる。有機ジイソシアネートはキ
トサンのグルコサミン残基1モルに対し0.5〜1
モルを添加し、30〜60℃で0.5〜4時間の反応条
件で接触架橋させればよい。 尚、有機ジイソシアネートと接触させない多孔
性粒状キトサンを用いて、下記のように有機ハラ
イドと反応させて陰イオン交換体を製造すると、
得られた陰イオン交換体は1N−NClで完全に溶
解してしまう。また、有機ジイソシアネートと接
触させない多孔性粒状キトサンを無水酢酸で部分
的にキチン化した場合は、陰イオン交換体粒は脆
く、強度的欠点がある。 上記のようにして架橋処理をされた粒状多孔質
キトサンは、塩基性水溶液として苛性ソーダ、苛
性カリ等の50%水溶液に浸漬接触させる。接触条
件は40℃、24時間程度でよい。この処理により、
多孔性粒状キトサン分子中のOH基は−ONa基、
又は−OK基等に変換される。更に陰イオン交換
能を具備する置換、若しくは非置換アミノ基又は
置換第四アンモニウム基を有する有機ハライド試
薬を所望のイオン交換能を発現すべき量だけ作用
させる。有機ハライドとしては、塩酸β−ジエチ
ルアミノエチルクロライド、塩酸β−クロルエチ
ルアミン等が一般的である。 有機ハライド試薬と作用させる時には、−ONa
基又は−OK基が−OH基に容易に変換されてし
まうと好ましくないので、塩基性水溶液で処理さ
れたキトサン多孔性粒状体を減圧吸引して充分に
余分の塩基性水溶液を除去しておくことが重要で
あり、更にイソプロピルアルコール等の有機極性
溶媒中で有機ハライド試薬と作用させる必要があ
る。しかる後に、更にイソプロピルアルコール等
の有機極性溶媒で充分洗浄:水洗、湯洗等をして
塩基性水溶液で脱イオン後、脱イオン水で充分水
洗してキトサン系陰イオン交換体を得る。 〔実施例〕 以下、本発明を実施例により更に詳細に説明す
るが、本願発明は実施例記載の範囲に限定される
ものではない。 Γ乾燥重量単位当りの総イオン交換容量(CTW)
の測定法は1N−NaOHにて洗浄後、脱イオン
水で水洗した湿潤状態にある試料約100mlを採
取し、水分平衡調整し、素早く約30gづつ秤量
し次の操作を算出する。 (1) 正確な重量W2(g)を乾燥し、乾重量W3
(g)を求める。 (2) 正確な重量W1(g)をとりN/5−HCl
500ml中に入れ、時々撹拌し12時間以上放置
する。この液を10ml取り、N/10−NaOH
にてフエノールフタレンを指示薬として中和
滴定し次式で総イオン交換容量(CTW)を
求める。(meq/g) (3) CTW=(b−a)×NaOH×1/10×500/10
×100/W1×(100−水分含有率)(meq/g) 但し:b:サンプルのN/10−NaOH消費量 a:ブランクのN/10−NaOH消費量 NaOH:N/10−NaOHの力価 水分含有率=W2−W3/W3×100(%) Γ 膨潤度は 膨潤度(%)=Y−X/X×100 Y:試料をIN−HCl又は4N−NaOH中で膨潤
させた後、減圧脱水して水分平衡調整した湿
重量 X:試料を減圧脱水して水分平衡調整した湿重
量 Γ比表面積は比表面積測定装置を用いてBET法
で測定した。 実施例 1 脱アセチル化度80%、平均分子量43000のキト
サン60gを酢酸30gを含む水910gに溶解させ、
粘度2700cpのキトサン溶液を得た。これを0.25
m/m孔径ノズルから10%苛性ソーダ、30%メタ
ノール、60%水からなる塩基性溶液中に落下せし
め、凝固析出させた後、水で中性になる迄充分洗
浄して0.8m/m径の比表面積78.6m2/gの粒状
多孔質キトサンを得た。これを50mlとり減圧吸引
して含まれる水分を除去した後、100ml中のアセ
トン有機極性溶媒中に入れ充分に水分を極性溶媒
と置換した。 これを100mlのアセトン中グルコサミン残基1
モルに対し1モルの4,4′−ジフエニルメタンジ
イソシアネート(MDI)を入れて30℃で30分反
応させ、未反応のMDIをアセトンで充分洗浄後、
更に水で充分洗浄して有機ジイソシアネートと接
触させた粒状多孔質キトサンを得た。 この粒状多孔質キトサンに47%苛性ソーダ200
ml注入後、40℃で24時間撹拌反応させ、しかる後
減圧吸引し、付着している苛性ソーダ水溶液を除
去し、イソプロピルアルコールを100ml注入し、
有機ハライド試薬として試料番号1〜5について
は塩酸β−ジエチルアミノエチルクロライドを、
試料番号6〜10については塩酸β−クロルエチル
アミンを夫々多孔性粒状キトサン100mlに対して
夫々0.5g、1g、2g、5g、10g添加し、90
℃で4時間反応させた。しかる後、イソプロピル
アルコールを更に100ml注入することを3回繰返
した後、水洗、湯洗してキトサン系陰イオン交換
体を得た。これらの比面積、CTW、1N−HCl及
び4N−NaOHにおける膨潤度を測定し、第1表
の結果を得た。
[Industrial Application Field] The present invention relates to a method for producing an anion exchanger using granular porous chitosan as a carrier.
It is suitable for many uses such as a carrier for immobilizing a biocatalyst and a carrier for cell culture. [Prior Art] In recent years, continuous automation of reaction processes using catalytic action has been progressing in the enzyme/cell utilization industry. In such processes, various ion exchangers are used, but while the carrier is packed in a column or tank and used, clogging occurs or the carrier itself is destroyed, causing the reaction solution to deteriorate. There is a drawback that distribution cannot be carried out smoothly, and improvements to the carrier are being considered to overcome this problem, but the situation is still insufficient. As a method for producing an anion exchanger using chitin or chitosan as a carrier, for example,
Proposal No. 35180 has been made. The method disclosed in this publication involves using chitin or chitosan itself as a raw material and contacting it with an aqueous alkali solution, and then bonding it with an organic halide having a substituted or unsubstituted amino group or a substituted quaternary ammonium group to form an anion exchanger. As is clear from Examples, the ion exchange capacity of the anion exchanger obtained is only about 0.8 meq/g, and when used as a carrier for enzyme immobilization, the ion exchange capacity of the anion exchanger obtained is This method has the drawbacks of extremely low adsorption amount and poor catalytic efficiency, and when used as a cell culture carrier, charge control is required depending on the cells used. The anion exchanger thus obtained has the disadvantage that it swells or dissolves due to acid or alkali during treatment. [Problems to be Solved by the Invention] An object of the present invention is to provide a method for producing a chitosan-based anion exchanger that solves the above-mentioned conventional drawbacks. The present invention uses low molecular weight chitosan to obtain granular porous chitosan with uniform particle size and uniform micropores on the spherical surface and cut surface, and further cross-links this by contact with an organic diisocyanate compound in a polar solvent. By using this material, the ion exchange ability can be significantly improved compared to chitosan-based anion exchangers obtained by conventional methods, and the ability can be freely adjusted.
A chitosan-based anion exchanger that has sufficient physical strength, does not swell or dissolve in acidic and alkaline solutions, and can be used in a wide range of ion exchange capacities is produced, thereby solving the above-mentioned conventional drawbacks. This is the solution. [Means for Solving the Problems] The present invention involves dissolving low molecular weight chitosan in an acidic aqueous solution and dropping the dissolved solution into a basic solution. Relates to a method for producing an anion exchanger characterized by contacting and crosslinking with a compound, then contacting with a basic solution, and then reacting with an organic halide having a substituted or unsubstituted amino group or a substituted quaternary ammonium group. . In the present invention, the average molecular weight is from 10,000 to
230,000 low molecular weight chitosan is used. High-quality chitosan having a desired molecular weight can be obtained by heating flaky high-molecular-weight chitosan in an aqueous solution of sodium perborate. Low-molecular-weight chitosan is dissolved in an aqueous solution of acetic acid, dichloroacetic acid, or formic acid alone or in a mixture to form an acidic chitosan solution, and the concentration is within an easy-to-handle range, that is, 2 to 2.
You can freely choose within a range of 20%. A fixed amount of the acidic solution is dropped into the next basic coagulation bath under pressure from, for example, a pore size of 0.1 to 0.25 m/m to obtain granular porous chitosan. As the basic substance in the coagulation bath, alkaline substances such as sodium hydroxide, potassium hydroxide, sodium carbonate, potassium carbonate, ammonia, and ethylenediamine are used.The basic solution is water, or polar substances such as methanol and ethanol. The basic substance is added to an alcohol or a mixture of water and alcohol. The granular porous chitosan forms a fine structure as the desolvation reaction progresses while settling in the coagulation liquid in granular form. The precipitated granular coagulum is taken out and washed with water until it becomes neutral to obtain granular porous chitosan. Next, the water used for washing is removed by displacement from the granular porous chitosan using a polar solvent. Crosslinking of chitosan spherical coagulates is carried out in a solution in which an organic diisocyanate compound is dissolved in a polar solvent that is the same as or different from the polar solvent used for water displacement. After sufficient crosslinking, unreacted After the organic diisocyanate compound is thoroughly washed away with the polar solvent used in the reaction, the mixture is further washed thoroughly with water to obtain crosslinked granular porous chitosan. The polar solvent used in the present invention includes alcohols such as methanol, ethanol, and isopropyl alcohol, ketones such as acetone and methyl ethyl ketone, and amides such as dimethylformamide and dimethylacetamide. May be used. Examples of the organic diisocyanate include 4,4'-diphermethane diisocyanate, 2,4-tolylene diisocyanate, naphthalene diisocyanate, 1,4-diclohexane diisocyanate,
Examples include 4,4'-dicyclohexylmethane diisocyanate, xylylene diisocyanate, isophorone diisocyanate, hexamethylene diisocyanate, and the like. The amount of organic diisocyanate is 0.5 to 1 per mole of glucosamine residue in chitosan.
mol, and catalytic crosslinking is carried out under reaction conditions of 30 to 60°C for 0.5 to 4 hours. In addition, when an anion exchanger is produced by reacting with an organic halide as described below using porous granular chitosan that is not brought into contact with an organic diisocyanate,
The obtained anion exchanger is completely dissolved in 1N-NCl. Furthermore, when porous granular chitosan that is not brought into contact with an organic diisocyanate is partially chitinized with acetic anhydride, the anion exchanger particles are brittle and have a strength disadvantage. The granular porous chitosan crosslinked as described above is brought into contact with a 50% aqueous solution of caustic soda, caustic potash, etc. as a basic aqueous solution by immersion. The contact conditions may be 40°C for about 24 hours. With this process,
The OH group in the porous granular chitosan molecule is -ONa group,
Or converted to -OK group, etc. Further, an organic halide reagent having a substituted or unsubstituted amino group or a substituted quaternary ammonium group having anion exchange ability is applied in an amount necessary to develop the desired ion exchange ability. As the organic halide, β-diethylaminoethyl chloride hydrochloride, β-chloroethylamine hydrochloride, etc. are generally used. When reacting with an organic halide reagent, −ONa
Since it is undesirable if the group or -OK group is easily converted to -OH group, the chitosan porous granules treated with the basic aqueous solution are suctioned under reduced pressure to sufficiently remove the excess basic aqueous solution. Furthermore, it is necessary to react with an organic halide reagent in an organic polar solvent such as isopropyl alcohol. Thereafter, the product is further thoroughly washed with an organic polar solvent such as isopropyl alcohol, such as with water or hot water, deionized with a basic aqueous solution, and then thoroughly washed with deionized water to obtain a chitosan-based anion exchanger. [Examples] Hereinafter, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited to the scope described in the Examples. ΓTotal ion exchange capacity (CTW) per dry weight unit
The measurement method involves taking approximately 100 ml of a wet sample that has been washed with 1N NaOH and deionized water, adjusting the water balance, and quickly weighing approximately 30 g each to calculate the next operation. (1) Dry the exact weight W 2 (g), dry weight W 3
Find (g). (2) Take the exact weight W 1 (g) and add N/5-HCl
Pour into 500 ml of water, stir occasionally and leave for 12 hours or more. Take 10ml of this solution and add N/10-NaOH
Perform neutralization titration using phenolphthalene as an indicator, and calculate the total ion exchange capacity (CTW) using the following formula. (meq/g) (3) CTW=(ba-a)×NaOH×1/10×500/10
×100/W 1 × (100-moisture content) (meq/g) However: b: N/10-NaOH consumption of sample a: N/10-NaOH consumption of blank NaOH: N/10-NaOH consumption Titer water content = W 2 - W 3 / W 3 × 100 (%) Γ Swelling degree is Swelling degree (%) = Y-X/X × 100 Y: Swell the sample in IN-HCl or 4N-NaOH After that, the sample was dehydrated under reduced pressure to adjust the water balance. X: Wet weight after the sample was dehydrated under reduced pressure to adjust the water balance. Example 1 60 g of chitosan with a degree of deacetylation of 80% and an average molecular weight of 43,000 was dissolved in 910 g of water containing 30 g of acetic acid,
A chitosan solution with a viscosity of 2700 cp was obtained. This is 0.25
After dropping into a basic solution consisting of 10% caustic soda, 30% methanol, and 60% water through a m/m hole diameter nozzle and allowing it to solidify and precipitate, it was thoroughly washed with water until it became neutral, and a diameter of 0.8 m/m was formed. Granular porous chitosan with a specific surface area of 78.6 m 2 /g was obtained. After 50 ml of this was taken and suctioned under reduced pressure to remove the water contained therein, it was placed in 100 ml of acetone organic polar solvent to sufficiently replace the water with the polar solvent. Add this to 1 glucosamine residue in 100 ml of acetone.
Add 1 mol of 4,4'-diphenylmethane diisocyanate (MDI) per mole, react at 30°C for 30 minutes, and wash unreacted MDI thoroughly with acetone.
Further, granular porous chitosan was obtained by thoroughly washing with water and contacting with an organic diisocyanate. 47% caustic soda 200% in this granular porous chitosan
After injecting ml, stir the reaction at 40℃ for 24 hours, then vacuum the solution to remove the attached caustic soda aqueous solution, and inject 100ml of isopropyl alcohol.
For sample numbers 1 to 5, hydrochloric acid β-diethylaminoethyl chloride was used as the organic halide reagent,
For sample numbers 6 to 10, 0.5 g, 1 g, 2 g, 5 g, and 10 g of β-chloroethylamine hydrochloride were added to 100 ml of porous granular chitosan, respectively.
The reaction was carried out at ℃ for 4 hours. After that, an additional 100 ml of isopropyl alcohol was injected three times, followed by washing with water and hot water to obtain a chitosan-based anion exchanger. The specific area, CTW, degree of swelling in 1N-HCl and 4N-NaOH were measured, and the results shown in Table 1 were obtained.

【表】 実施例 2 実施例1と同様に得られたキトサン多孔性粒状
物を100mlのジメチルホルムアミド中にグルコサ
ミン残基1モルに対し0.5モルのヘキサメチレン
ジイソシアネート(HDI)を入れて60℃で4時
間反応させ、未反応のHDIをジメチルホルムア
ミド中で充分洗浄後、更に水で充分洗浄して粒状
多孔質キトサンを得た。このキトサンを実施例1
と同様にして、有機ハライドとして塩酸β−クロ
ルエチルアミンを用いて5g、2g、1gを加え
てキトサン陰イオン交換体を得た。これらの比表
面積CTW、1N−HCl及び4N−NaOHの膨潤度
を測定した第2表の結果を得た。
[Table] Example 2 Chitosan porous granules obtained in the same manner as in Example 1 were mixed with 0.5 mol of hexamethylene diisocyanate (HDI) per 1 mol of glucosamine residue in 100 ml of dimethylformamide at 60°C. After reacting for a time, unreacted HDI was thoroughly washed in dimethylformamide, and then thoroughly washed with water to obtain granular porous chitosan. This chitosan was used in Example 1.
In the same manner as above, using β-chloroethylamine hydrochloride as the organic halide, 5 g, 2 g, and 1 g were added to obtain a chitosan anion exchanger. The specific surface area CTW, swelling degree of 1N-HCl and 4N-NaOH were measured, and the results shown in Table 2 were obtained.

【表】 実施例 3 脱アセチル化度80%、平均分子量47000のキト
サン60gを用いて実施例1と同様な操作を行って
比表面積80.6m2/g、粒径1.0m/mの多孔性キ
トサンを得、アセトン有機溶媒中でキトサン中の
グルコサミン残基1モルに対し、キシリレンジイ
ソシアネート(XDI)又はトリレンジイソシアネ
ート(TDI)を夫々1モルを30℃、1時間反応さ
せ、実施例1と同様にイソプロピルアルコール中
で有機ハライドとして塩酸β−ジエチルアミノエ
チルクロライドを10g、5g2gとそれぞれ反応
させ、キトサン系陰イオン交換体を得た。これら
の比表面積、CTW、1N−HCl、4N−NaOHに
おける膨潤度を測定した結果を第3表に示す。
[Table] Example 3 Using 60 g of chitosan with a degree of deacetylation of 80% and an average molecular weight of 47,000, the same operation as in Example 1 was performed to obtain porous chitosan with a specific surface area of 80.6 m 2 /g and a particle size of 1.0 m/m. 1 mole of glucosamine residue in chitosan was reacted with 1 mole each of xylylene diisocyanate (XDI) or tolylene diisocyanate (TDI) at 30°C for 1 hour in the same manner as in Example 1. Then, 10 g and 5 g of 2 g of β-diethylaminoethyl chloride hydrochloride as an organic halide were reacted in isopropyl alcohol to obtain a chitosan-based anion exchanger. Table 3 shows the results of measuring the specific surface area and degree of swelling in CTW, 1N-HCl, and 4N-NaOH.

〔発明の効果〕〔Effect of the invention〕

上記実施例に記載したように、本発明によつて
得られたキトサン系陰イオン交換体は、従来のも
のに比べて8〜6倍強の総イオン交換容量を有す
るものであつて、しかも、条件を選択することに
より総イオン交換容量を自由に制御することがで
きる。また、酸、アルカリに対する耐膨潤度にお
いても優れたものであるので、広範囲のイオン交
換能域での使用が可能である。 また、本発明によつて得られるキトサン系陰イ
オン交換体は、粒状体の割断面及び表面上に均一
な微細孔を有し、比表面積が大きいにもかかわら
ず強度も高いものであるので、カラム等に充填し
て使用する場合にも、変形が生じることなく、通
液抵抗が増加することがない。
As described in the above examples, the chitosan-based anion exchanger obtained by the present invention has a total ion exchange capacity 8 to 6 times stronger than that of the conventional one, and moreover, The total ion exchange capacity can be freely controlled by selecting conditions. Furthermore, since it has excellent swelling resistance against acids and alkalis, it can be used in a wide range of ion exchange capacities. In addition, the chitosan-based anion exchanger obtained by the present invention has uniform micropores on the fractured surface and surface of the granules, and has high strength despite having a large specific surface area. Even when used by filling a column etc., there is no deformation and no increase in liquid flow resistance.

Claims (1)

【特許請求の範囲】[Claims] 1 低分子量キトサンを酸性水溶液に溶解し、該
溶解液を塩基性溶液中に落下せしめて得た粒状多
孔質キトサンを、極性溶媒中で有機ジイソシアネ
ート化合物と接触架橋させ、その後塩基性溶液と
接触させて、置換、若しくは非置換アミノ基又は
置換第四アンモニウム基を有する有機ハライドと
反応させることを特徴とする陰イオン交換体の製
造方法。
1. Particulate porous chitosan obtained by dissolving low molecular weight chitosan in an acidic aqueous solution and dropping the solution into a basic solution is contacted and crosslinked with an organic diisocyanate compound in a polar solvent, and then brought into contact with a basic solution. A method for producing an anion exchanger, which comprises reacting the anion exchanger with an organic halide having a substituted or unsubstituted amino group or a substituted quaternary ammonium group.
JP60175265A 1985-08-09 1985-08-09 Preparation of chitosan anion exchange body Granted JPS6238246A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60175265A JPS6238246A (en) 1985-08-09 1985-08-09 Preparation of chitosan anion exchange body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60175265A JPS6238246A (en) 1985-08-09 1985-08-09 Preparation of chitosan anion exchange body

Publications (2)

Publication Number Publication Date
JPS6238246A JPS6238246A (en) 1987-02-19
JPH054139B2 true JPH054139B2 (en) 1993-01-19

Family

ID=15993127

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60175265A Granted JPS6238246A (en) 1985-08-09 1985-08-09 Preparation of chitosan anion exchange body

Country Status (1)

Country Link
JP (1) JPS6238246A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106436313B (en) * 2016-09-23 2018-10-12 泉州亚林新材料科技有限公司 Chitosan quaternary ammonium salt antibacterial fiber, fabric, hygiene product and its preparation process

Also Published As

Publication number Publication date
JPS6238246A (en) 1987-02-19

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