JPH0585158B2 - - Google Patents
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- Publication number
- JPH0585158B2 JPH0585158B2 JP2112838A JP11283890A JPH0585158B2 JP H0585158 B2 JPH0585158 B2 JP H0585158B2 JP 2112838 A JP2112838 A JP 2112838A JP 11283890 A JP11283890 A JP 11283890A JP H0585158 B2 JPH0585158 B2 JP H0585158B2
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- JP
- Japan
- Prior art keywords
- acetic acid
- chitosan
- acid bacteria
- porous
- 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.)
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- Polysaccharides And Polysaccharide Derivatives (AREA)
- Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
Description
〓産業上の利用分野〓
本発明は、酢酸菌の固定化に優れた機能を発揮
する固定化用担体とその製造法に関し、本発明に
係る酢酸菌固定化用担体は、酢酸菌を利用した酢
酸の連続醗酵、物質の変換等に使用される各種の
反応器中等での酢酸菌の固定化に優れた性能を有
するものである。
〓従来の技術〓
従来、多孔質キトサン成形物を酢酸菌固定化用
担体として利用出来ることは、本発明者等が特願
平1−45781号の応用例で開示し、該発明におい
て、多孔質キトサン粒状体を酸溶液で処理し、架
橋処理を行つている。
〓発明が解決しようとする課題〓
酢酸菌を固定するためには、担体との親和性を
高めることが重要で、これによつて担体中の酢酸
菌量を増加させることが可能となり、酢酸菌を利
用した物質の変換を行うための反応器中での使用
に優れた性能を示す。
本発明者等が先に開示した多孔質キトサン成形
物を酸処理し、夫々についてヘキサメチレンビス
−2(2,3−エポキシプロピルジメチルアンモ
ニウムクロライド)、ヘキサメチレンジイソシア
ネート及び4,4′−ジフエニルメタンジイソシア
ネートを架橋した多孔質キトサン成形物では未だ
酢酸菌との親和性が低く、従つて吸着菌数も低い
欠点があつた。
本発明は、多孔質キトサン粒状体に対し、酢酸
菌について高い固定化能を具備させることを目的
とするものである。
〓課題を解決するための手段〓
本発明は、多孔質粒状体のキトサンを構成する
ピラノース環100構造単位当りフエニル基導入量
が4〜45で、該多孔質粒状体の細孔径が3〜
10μmである酢酸菌固定化用担体に関するもので
あり、このような酢酸菌固定化用担体は、低分子
量キトサンの酸性水溶液を塩基性水溶液中で凝固
析出させて多孔質キトサン粒状体を得、次いで酸
溶液で処理し、更にフエニルイソシアネートを反
応させることによつて得られる。
本発明においては、キトサンとして平均分子量
が10000〜230000の低分子量キトサンが用いられ、
これを酢酸、ジクロル酢酸、蟻酸等の単独又は混
合水溶液に溶解させ、キトサン酸性水溶液とす
る。キトサン酸性水溶液のキトサンの濃度は2〜
20%(重量)の範囲で自由に選択することができ
る。この際、キトサン酸性水溶液中に、細孔調節
剤として水溶性高分子物質であるポリビニルアル
コール、ポリエチレングリコール等を単独又は組
合せて添加してもよい。該キトサン酸性水溶液か
らキトサンを再生して多孔質キトサン粒状体を得
るためには、例えば孔径0.1〜0.25mmφのノズル
より、圧力下で塩基性水溶液中に該キトサン酸性
水溶液を一定量ずつ落下させることにより多孔質
キトサン粒状体が得られる。
塩基性凝固浴中に加える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
とするには、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
ル類の混合物に上述の塩基性物質を加えて使用す
る。得られた水を含む多孔質キトサン粒状体はメ
タノール、エタノール、イソプロピルアルコール
等のアルコール類やアクリロニトリル等の極性溶
媒を用いて水を置換する。次いで酸水溶液で該多
孔質キトサン粒状体の表面処理をするが、この際
用いられる酸としては、酢酸、蟻酸、プロピオン
酸等の有機酸、又は塩酸、硝酸等の鉱酸が挙げら
れ、多孔質キトサン粒状体の表面を酸水溶液で短
時間処理し、次いで酸を充分水洗する。この時粒
状体に水が含まれていれば酸の水溶液を、極性溶
媒が含まれている場合には該極性溶媒と酸の混合
物を用いることが好ましい。酸の濃度としては、
0.5〜5.0%(重量)のものが使用され、酸処理は
25℃で10秒〜5分間行う。しかし、処理条件はキ
トサン酸性水溶液の濃度、塩基性凝固浴濃度、処
理に用いる酸の種類と濃度によつて粒状体内部の
大きな気孔を表面に具備させるように自由に選択
出来る。
上記の酸処理によつて得られた多孔質キトサン
粒状体は、表面及びその近傍にある、内部より、
より直径の小さい細孔径気孔部分が除去されるの
で、表面から内部に向つて大きな直径の気孔を有
するものとなる。
得られた多孔質キトサン粒状体を、メタノー
ル、エタノール、ジメチルホルムアミド、ジオキ
サン等の有機溶媒で水を完全に置換する。次い
で、フエニルイソシアネートを多孔質キトサン粒
状体中のアミノ基と室温で1〜10時間架橋反応さ
せ、反応終了後、再び前述の有機溶媒で未反応の
フエニルイソシアネートを除去し、完全に水洗す
る。この際のフエニルイソシアネートは多孔質キ
トサン粒状体の乾燥重量1gに対し0.04〜3.5g
添加される。
上記のように、本発明においてはフエニルイソ
シアネートを導入して酢酸菌の固定化用担体を得
るのであるが、フエニルイソシアネートが用いら
れる理由は、イソシアネート基がキトサンの骨格
構造中のアミノ基との反応性が高く、しかもフエ
ニル基以外の直鎖状のアルキルに結合しているイ
ソシアネート基を有する化合物に比べて反応性が
著しく高い。そして疎水基の導入により担体の疎
水性も高まり、酢酸菌との親和性を高める効果が
あるからである。原料であるキトサンはグルコサ
ミンのみでなく、N−アセチルグルコサミンとの
共重合体であることが多く、その比率(脱アセチ
ル化度)は50〜100%である。
フエニル基の導入量は、多孔質粒状体のキトサ
ンを構成するピラノース環100構造単位当り4〜
45である時に全PH域で安定であり、酢酸菌を固定
化して食酢を製造する際にも何らの変化を受ける
ことがない。そして疎水基が導入されているので
酢酸菌と担体の親和性が著しく向上し、固定化操
作時の酢酸菌吸着数を顕著に向上させることがで
き、増殖菌体を担体表面及び内部で増殖させると
きも菌の保持性に優れた性能を具備する。フエニ
ル基を導入した多孔質キトサン粒状体を酢酸菌固
定化用担体として使用するには、細孔径が3〜
10μmの範囲にあると酢酸菌の吸着量が高く、し
かも圧縮弾性率の優れたものが得られる。尚、フ
エニル基導入量は下記の実施例に詳述した方法に
よつて求めることができる。
〓実施例〓
以下、本発明を、実施例を上げて詳述するが、
本発明はこの範囲に限定されるものではない。
実施例において記載のフエニル基導入量、細孔
径、圧縮弾性率及び酢酸菌吸着数は次の方法によ
り測定した。
フエニル基導入量
フエニルイソシアネートを反応させて得た多
孔質キトサン粒状体50ml(湿容積)をメスシリ
ンダーで正確に採取し、エタノールで4回置換
する。
更にエーテルを用いて4回置換する。
エーテルを抜き取り、真空デシケーター中で
エーテル臭がなくなるまで乾燥させ、その重量
を測定する(Ag)
別に、フエニルイソシアネートを反応させな
い多孔質キトサン粒状体50ml(湿容積)を、上
記〜の操作を行つて乾燥重量を測定する
(Bg)。
ピラノース環100構造単位当りのフエニル基
導入量を次式で求めた。
フエニル基導入量={M×(A−B)/(119×
B)}×100
但し、
M:ピラノース環換算の分子量で次式より求め
た。
M=〔(161×DAC/100)+{203×(100−DAC)/100
}〕
DAC:脱アセチル化度(%)
119:フエニルイソシアネートの分子量
161:DAC100%時のピラノース環換算分子量
203:DAC0%時のピラノース環換算分子量
細孔径
試料を液体窒素中で急冷し、−50℃、10-7トー
ルの真空度下で凍結乾燥後、走査型電子顕微鏡で
測定した。
圧縮弾性率
レオメーターNRM−2010J−CW(不動工業(株)
製)を用いて直径6.0mmφ、深さ10mmのサンプル
アダプターに試料を詰め、直径5.5mmφの棒で2
cm/minの速さで4mm押し込んだときの圧縮弾性
率を測定した。
酢酸菌吸着数
グリコース、ポリペプトン、酵母エキスから
なるPGY倍地にエタノールを2%となるよう
に加えた培地30mlにアセトバクターアセチ
(Acetobacter aceti,IFO−3823)を植菌し、
30℃で24時間振盪培養を行う。
この培養懸濁液4mlを、予め滅菌しておいた
試料に加え、4℃で1時間振盪し吸着させる。
吸着終了後、上清を100ml取り、4000倍希釈
し、そのうちの100mlを取つて予め用意してお
いた平板培地に塗抹して48時間培養後、出現し
たコロニー数をカウントする。吸着前の培養懸
濁液については、8000倍希釈して同様の操作で
コロニー数をカウントしておく。
吸着前後の細胞数の差から吸着数を算出す
る。
実施例 1
脱アセチル化度76%、平均分子量51000のキト
サン60gとポリエチレングリコール(分子量
20000、和光純薬工業(株)製)100gを6%酢酸に溶
解し、総量が1000mlとなるようにした。該酸性水
溶液を、5.5%水酸化ナトリウム、20%エタノー
ル、74.5%水よりなる混合液中に孔径0.25mmφの
ノズルから一定量ずつ落下させ凝固再生した後、
中性になるまで充分水洗して平均粒径約1.2mmφ、
細孔径0.2μm、圧縮弾性率2.5×106dyn/cm2の多
孔質キトサン粒状体950mlを得た。該多孔質キト
サン粒状体の付着水を吸引濾過で除去後、0.5%
酢酸水溶液1中に25℃で30秒間浸漬処理を行つ
た。これの細孔径は5μm、圧縮弾性率は1.3×106
dyn/cm2であつた。
該粒状体100ml(湿容積)を秤量し乾燥後、乾
燥重量を測定したところ7.3gであつた。次いで
夫々100ml(湿容積)を5本採取し夫々について
ジメチルホルムアミドで水分を置換し、フエニル
イソシアネート0.47g、2.37g、4.73g、9.46g
及び23.65gを添加し30分間反応させた。反応後、
未反応のフエニルイソシアネートをジメチルホル
ムアミドで完全に除去、置換し、その後水洗し酢
酸菌固定化用担体5種類(試料1〜5)を得た。
試料1〜5のフエニル基導入量、圧縮弾性率、
細孔径を測定し、その結果を第1表に示した。
又、酢酸菌IFO−3823をグリコース、ポリペプト
ン、酵母エキスを含むPGY培地30mlに植菌後、
30℃、24時間、120回転/分で振盪培養した培養
懸濁液4mlに対し、試料1〜5を夫々各2ml加
え、50℃で1時間酢酸菌を吸着させて吸着菌数を
測定し第1表に示した。
〓Field of Industrial Application〓 The present invention relates to an immobilization carrier that exhibits an excellent function in immobilizing acetic acid bacteria and a method for producing the same. It has excellent performance in immobilizing acetic acid bacteria in various reactors used for continuous fermentation of acetic acid, conversion of substances, etc. 〓Prior art〓 Conventionally, the present inventors disclosed in the application example of Japanese Patent Application No. 1-45781 that a porous chitosan molded product can be used as a carrier for immobilizing acetic acid bacteria. Chitosan granules are treated with an acid solution to perform crosslinking treatment. 〓Problem to be solved by the invention〓 In order to immobilize acetic acid bacteria, it is important to increase the affinity with the carrier.This makes it possible to increase the amount of acetic acid bacteria in the carrier, and It exhibits excellent performance when used in reactors for the conversion of substances using The porous chitosan molded article previously disclosed by the present inventors was treated with an acid, and hexamethylene bis-2 (2,3-epoxypropyldimethylammonium chloride), hexamethylene diisocyanate, and 4,4'-diphenylmethane were respectively treated. Porous chitosan molded products crosslinked with diisocyanate still have a low affinity for acetic acid bacteria, and therefore have the disadvantage of a low number of adsorbed bacteria. The object of the present invention is to provide porous chitosan particles with a high ability to immobilize acetic acid bacteria. <Means for Solving the Problems> The present invention is characterized in that the amount of phenyl groups introduced per 100 structural units of pyranose rings constituting the chitosan of the porous granules is 4 to 45, and the pore diameter of the porous granules is 3 to 45.
This relates to a carrier for immobilizing acetic acid bacteria having a diameter of 10 μm, and such a carrier for immobilizing acetic acid bacteria is prepared by coagulating and precipitating an acidic aqueous solution of low molecular weight chitosan in a basic aqueous solution to obtain porous chitosan particles, and then It is obtained by treatment with an acid solution and further reaction with phenyl isocyanate. In the present invention, low molecular weight chitosan with an average molecular weight of 10,000 to 230,000 is used as chitosan,
This is dissolved in an aqueous solution of acetic acid, dichloroacetic acid, formic acid, etc. alone or in combination to obtain an acidic chitosan aqueous solution. The concentration of chitosan in the chitosan acidic aqueous solution is 2~
It can be freely selected within a range of 20% (weight). At this time, polyvinyl alcohol, polyethylene glycol, etc., which are water-soluble polymer substances, may be added alone or in combination as a pore control agent to the chitosan acidic aqueous solution. In order to regenerate chitosan from the chitosan acidic aqueous solution and obtain porous chitosan granules, the chitosan acidic aqueous solution is dropped in a constant amount into the basic aqueous solution under pressure, for example, from a nozzle with a pore diameter of 0.1 to 0.25 mmφ. Porous chitosan granules are obtained. Basic substances added to the basic coagulation bath include:
Alkaline substances such as sodium hydroxide, potassium hydroxide, sodium carbonate, potassium carbonate, ammonia, and ethylenediamine are used. To make a basic solution, water, polar alcohols such as methanol and ethanol, or water are used. The above-mentioned basic substance is added to a mixture of alcohols for use. The water in the obtained porous chitosan particles containing water is replaced using an alcohol such as methanol, ethanol, isopropyl alcohol, or a polar solvent such as acrylonitrile. Next, the surface of the porous chitosan particles is treated with an acid aqueous solution. Examples of acids used at this time include organic acids such as acetic acid, formic acid, and propionic acid, and mineral acids such as hydrochloric acid and nitric acid. The surface of the chitosan particles is treated with an aqueous acid solution for a short time, and then the acid is thoroughly washed away with water. At this time, if the granules contain water, it is preferable to use an aqueous acid solution, and if the granules contain a polar solvent, it is preferable to use a mixture of the polar solvent and the acid. The concentration of acid is
0.5-5.0% (by weight) is used, and acid treatment is
Perform at 25°C for 10 seconds to 5 minutes. However, the treatment conditions can be freely selected depending on the concentration of the chitosan acidic aqueous solution, the concentration of the basic coagulation bath, and the type and concentration of the acid used in the treatment so as to form large pores inside the granules on the surface. The porous chitosan particles obtained by the above acid treatment have the following properties:
Since the pore portion with a smaller diameter is removed, the pores have a larger diameter from the surface toward the inside. The water in the obtained porous chitosan particles is completely replaced with an organic solvent such as methanol, ethanol, dimethylformamide, dioxane, etc. Next, phenyl isocyanate is cross-linked with the amino groups in the porous chitosan particles at room temperature for 1 to 10 hours, and after the reaction is completed, unreacted phenyl isocyanate is removed again with the above-mentioned organic solvent and thoroughly washed with water. . At this time, the amount of phenyl isocyanate is 0.04 to 3.5 g per 1 g of dry weight of porous chitosan granules.
added. As mentioned above, in the present invention, phenyl isocyanate is introduced to obtain a carrier for immobilizing acetic acid bacteria. The reactivity is high, and the reactivity is significantly higher than that of compounds having an isocyanate group bonded to a linear alkyl group other than a phenyl group. This is because introduction of a hydrophobic group increases the hydrophobicity of the carrier, which has the effect of increasing affinity with acetic acid bacteria. Chitosan, which is a raw material, is often a copolymer of not only glucosamine but also N-acetylglucosamine, and its ratio (degree of deacetylation) is 50 to 100%. The amount of phenyl groups introduced is 4 to 100 structural units of pyranose rings constituting the porous granular chitosan.
45, it is stable in the entire pH range, and does not undergo any changes even when vinegar is produced by immobilizing acetic acid bacteria. Since a hydrophobic group is introduced, the affinity between the acetic acid bacteria and the carrier is significantly improved, and the number of acetic acid bacteria adsorbed during the immobilization operation can be significantly increased, allowing proliferative bacteria to proliferate on the surface and inside of the carrier. It also has excellent performance in retaining bacteria. In order to use porous chitosan particles into which phenyl groups have been introduced as a carrier for immobilizing acetic acid bacteria, the pore size must be between 3 and 3.
When the thickness is in the range of 10 μm, the amount of acetic acid bacteria adsorbed is high and the compressive elastic modulus is excellent. The amount of phenyl group introduced can be determined by the method detailed in the Examples below. 〓Example〓 Hereinafter, the present invention will be described in detail with reference to Examples.
The present invention is not limited to this range. The amount of phenyl group introduced, pore diameter, compressive elastic modulus, and number of acetic acid bacteria adsorbed described in Examples were measured by the following methods. Amount of phenyl group introduced: Accurately collect 50 ml (wet volume) of porous chitosan particles obtained by reacting phenyl isocyanate with a graduated cylinder, and replace with ethanol four times. Four more substitutions are made with ether. Remove the ether, dry it in a vacuum dessicator until the ether odor disappears, and measure its weight (Ag).Separately, 50 ml (wet volume) of porous chitosan granules that are not reacted with phenyl isocyanate are subjected to the above steps. and measure the dry weight (Bg). The amount of phenyl group introduced per 100 structural units of the pyranose ring was determined using the following formula. Amount of phenyl group introduced = {M×(AB)/(119×
B)}×100 However, M: Molecular weight in terms of pyranose ring, calculated from the following formula. M=[(161×DAC/100)+{203×(100−DAC)/100
} ] DAC: Degree of deacetylation (%) 119: Molecular weight of phenyl isocyanate 161: Molecular weight in terms of pyranose rings at 100% DAC 203: Molecular weight in terms of pyranose rings at 0% DAC Pore diameter The sample was rapidly cooled in liquid nitrogen, and - After freeze-drying at 50°C under a vacuum of 10 -7 Torr, measurements were taken using a scanning electron microscope. Compressive modulus Rheometer NRM-2010J-CW (Fudou Kogyo Co., Ltd.)
Pack the sample into a sample adapter with a diameter of 6.0 mmφ and a depth of 10 mm using a
The compressive elastic modulus was measured when the material was pushed in 4 mm at a speed of cm/min. Number of acetic acid bacteria adsorbed Acetobacter aceti (IFO-3823) was inoculated into 30 ml of PGY medium consisting of glycose, polypeptone, and yeast extract with 2% ethanol added.
Perform shaking culture at 30°C for 24 hours. Add 4 ml of this culture suspension to the previously sterilized sample and shake for 1 hour at 4°C to allow adsorption. After the adsorption is completed, take 100 ml of the supernatant, dilute it 4000 times, take 100 ml of the supernatant, spread it on a prepared plate medium, and after culturing for 48 hours, count the number of colonies that have appeared. For the culture suspension before adsorption, dilute it 8000 times and count the number of colonies using the same procedure. The number of adsorbed cells is calculated from the difference in the number of cells before and after adsorption. Example 1 60 g of chitosan with a degree of deacetylation of 76% and an average molecular weight of 51000 and polyethylene glycol (molecular weight
20000, manufactured by Wako Pure Chemical Industries, Ltd.) was dissolved in 6% acetic acid so that the total volume was 1000 ml. After solidifying and regenerating the acidic aqueous solution by dropping it into a mixed solution of 5.5% sodium hydroxide, 20% ethanol, and 74.5% water through a nozzle with a hole diameter of 0.25 mm,
Wash thoroughly with water until neutral, and the average particle size is approximately 1.2mmφ.
950 ml of porous chitosan granules with a pore diameter of 0.2 μm and a compressive modulus of 2.5×10 6 dyn/cm 2 were obtained. After removing the water adhering to the porous chitosan granules by suction filtration, 0.5%
A immersion treatment was performed in acetic acid aqueous solution 1 at 25° C. for 30 seconds. The pore diameter of this is 5 μm and the compressive modulus is 1.3×10 6
It was dyn/ cm2 . After weighing and drying 100 ml (wet volume) of the granules, the dry weight was determined to be 7.3 g. Next, 5 tubes of 100 ml (wet volume) were collected from each tube, and the water was replaced with dimethylformamide to obtain 0.47 g, 2.37 g, 4.73 g, and 9.46 g of phenyl isocyanate.
and 23.65 g were added and reacted for 30 minutes. After the reaction,
Unreacted phenyl isocyanate was completely removed and replaced with dimethylformamide, and then washed with water to obtain five types of carriers for immobilizing acetic acid bacteria (samples 1 to 5). Amount of phenyl group introduced in samples 1 to 5, compressive elastic modulus,
The pore diameter was measured and the results are shown in Table 1.
In addition, after inoculating acetic acid bacteria IFO-3823 into 30 ml of PGY medium containing glycose, polypeptone, and yeast extract,
Add 2 ml of each of samples 1 to 5 to 4 ml of the culture suspension cultured at 30°C for 24 hours with shaking at 120 rotations/min, let the acetic acid bacteria adsorb at 50°C for 1 hour, and measure the number of adsorbed bacteria. It is shown in Table 1.
【表】
第1表の結果より、フエニル基の導入量に応じ
て酢酸菌の吸着数が増加する一方、細孔径はフエ
ニル基の導入による変化はないが、フエニル基導
入により圧縮弾性率がかなり向上し、酢酸菌固定
化用担体として優れたものであることが明らかで
ある。
実施例 2
脱アセチル化度80%、平均分子量52000のキト
サン130gにポリエチレングリコール(平均分子
量20000、和光純薬工業(株)製)200gを添加し、総
量が2000mlになるようにして6%酢酸水溶液に溶
解した。該酸性水溶液を、5%水酸化ナトリウ
ム、30%エタノール、65%水よりなる混合溶液中
に孔径0.25mmφのノズルより一定量ずつ落下させ
凝固再生させた後、中性になるまで充分水洗し、
平均粒径約1.0mmφの多孔質キトサン粒状体1960
mlを得た。次いで得られた多孔質キトサン粒状体
各400ml(湿容積)を3本採取し、夫々付着水を
吸引濾過除去し、酢酸水溶液の各0.1,0.25及び
0.5%溶液500ml中で25℃、30秒間処理し中性にな
るまで水洗した。水洗後の多孔質キトサン粒状体
の湿容積は夫々396ml、268ml、244mlであつた。
得られた粒状体100mlの乾燥重量を測定したとこ
ろ夫々7.6g、7.0g、6.9gであつた。次に夫々粒
状体100ml(湿容積)についてジメチルホルムア
ミドで水を置換し夫々にフエニルイソシアネート
6.5g、4.5g、4.0gを添加し、室温で1時間反応
させ試料6〜8を得た。得られた試料6〜8につ
いて実施例1と同様にフエニル基導入量、圧縮弾
性率、細孔径を測定し、その結果を第2表に示し
た。又、実施例1と同様に酢酸菌を吸着させて、
その酢酸菌の吸着数を測定し、その結果を第2表
に示した。[Table] From the results in Table 1, the number of adsorbed acetic acid bacteria increases depending on the amount of phenyl groups introduced, while the pore diameter does not change due to the introduction of phenyl groups, but the compressive elastic modulus increases considerably due to the introduction of phenyl groups. It is clear that the carrier is excellent as a carrier for immobilizing acetic acid bacteria. Example 2 200 g of polyethylene glycol (average molecular weight 20,000, manufactured by Wako Pure Chemical Industries, Ltd.) was added to 130 g of chitosan with a deacetylation degree of 80% and an average molecular weight of 52,000, and a 6% acetic acid aqueous solution was added so that the total amount was 2,000 ml. dissolved in A certain amount of the acidic aqueous solution is dropped into a mixed solution consisting of 5% sodium hydroxide, 30% ethanol, and 65% water through a nozzle with a hole diameter of 0.25 mmφ to solidify and regenerate, and then thoroughly washed with water until it becomes neutral.
Porous chitosan granules 1960 with an average particle diameter of approximately 1.0 mmφ
Got ml. Next, three 400 ml (wet volume) each of the obtained porous chitosan granules were collected, the adhering water was removed by suction filtration, and each of 0.1, 0.25 and 0.25 ml of acetic acid aqueous solution was collected.
It was treated in 500 ml of 0.5% solution at 25°C for 30 seconds and washed with water until it became neutral. The wet volumes of the porous chitosan granules after washing with water were 396 ml, 268 ml, and 244 ml, respectively.
When the dry weights of 100 ml of the obtained granules were measured, they were 7.6 g, 7.0 g, and 6.9 g, respectively. Next, water was replaced with dimethylformamide for 100 ml (wet volume) of each granule, and phenyl isocyanate was added to each granule.
6.5 g, 4.5 g, and 4.0 g were added and reacted at room temperature for 1 hour to obtain samples 6 to 8. The amount of phenyl group introduced, compressive elastic modulus, and pore diameter of the obtained Samples 6 to 8 were measured in the same manner as in Example 1, and the results are shown in Table 2. Also, as in Example 1, acetic acid bacteria were adsorbed,
The number of adsorbed acetic acid bacteria was measured, and the results are shown in Table 2.
【表】
第2表から明らかな如く、細孔径が3μm以下で
あるとフエニル基導入量がほぼ同一であつても酢
酸菌の吸着数が著しく低いことが明らかである。
実施例 3
脱アセチル化度78%、平均分子量50000のキト
サン120gにポリエチレングリコール(平均分子
量20000、和光純薬工業(株)製)200gを6%酢酸に
溶解し総量が2000mlとなるようにした。該酸性水
溶液を5.5%水酸化ナトリウム、30%エタノール、
64.5%水よりなる混合液中に孔径0.25mmφのノズ
ルより一定量ずつ落下させ凝固再生させた後、中
性になるまで充分水洗して平均粒径1.0mmφの多
孔質キトサン粒状体1920ml(湿容積)を得た。次
いで得られた多孔質キトサン粒状体を夫々400ml
(湿容積)を3本採取し、付着している水分を吸
引濾過除去後、酢酸水溶液の各0.5,1.0,5.0%水
溶液500ml中で25℃、30秒間処理し中性になるま
で水洗したところ、夫々の湿容積は260ml、242
ml、210mlであつた。得られた粒状体から夫々100
mlを採取し乾燥重量を測定したところ、夫々7.5
g、7.2g、6.8gであつた。次に得られた粒状体
より夫々100ml(湿容積)を採取し、ジメチルホ
ルムアミドで水を置換し、にフエニルイソシアネ
ートを夫々4.5g、4.0g、4.0gを添加し、室温で
1時間反応させた後、未反応のフエニルイソシア
ネートをジメチルホルムアミドで置換し、その後
充分水洗し、試料9〜11を得た。得られた試料に
ついて実施例1と同様にフエニル基導入量、圧縮
弾性率、細孔径を測定し、その結果を第3表に示
した。又、実施例1と同様に酢酸菌を吸着させて
その酢酸菌の吸着数を測定し、その結果を第3表
に示した。[Table] As is clear from Table 2, it is clear that when the pore diameter is 3 μm or less, the number of acetic acid bacteria adsorbed is significantly lower even if the amount of phenyl groups introduced is almost the same. Example 3 In 120 g of chitosan with a deacetylation degree of 78% and an average molecular weight of 50,000, 200 g of polyethylene glycol (average molecular weight 20,000, manufactured by Wako Pure Chemical Industries, Ltd.) was dissolved in 6% acetic acid so that the total amount was 2,000 ml. The acidic aqueous solution was mixed with 5.5% sodium hydroxide, 30% ethanol,
After solidifying and regenerating a fixed amount of chitosan particles by dropping them into a mixed solution consisting of 64.5% water through a nozzle with a pore size of 0.25 mmφ, the porous chitosan particles with an average particle size of 1.0 mmφ were washed thoroughly with water until they became neutral. ) was obtained. Next, 400 ml of each of the obtained porous chitosan granules
Three bottles (wet volume) were collected, and after removing the adhering moisture by suction filtration, they were treated with 500 ml of each 0.5, 1.0, and 5.0% aqueous acetic acid solution at 25°C for 30 seconds, and washed with water until they became neutral. , each wet volume is 260ml, 242
ml, 210ml. 100 each from the obtained granules
When I collected ml and measured the dry weight, it was 7.5
g, 7.2 g, and 6.8 g. Next, 100 ml (wet volume) of each of the obtained granules was collected, the water was replaced with dimethylformamide, 4.5 g, 4.0 g, and 4.0 g of phenyl isocyanate were added thereto, and the mixture was allowed to react at room temperature for 1 hour. After that, unreacted phenyl isocyanate was replaced with dimethylformamide, and then thoroughly washed with water to obtain Samples 9 to 11. The amount of phenyl group introduced, compressive elastic modulus, and pore diameter of the obtained sample were measured in the same manner as in Example 1, and the results are shown in Table 3. Further, in the same manner as in Example 1, acetic acid bacteria were adsorbed and the number of adsorbed acetic acid bacteria was measured, and the results are shown in Table 3.
【表】
第3表から明らかなように細孔径が15μmを超
えるとフエニル基を導入しても圧縮弾性率の著し
い低下が認められる。
〓発明の効果〓
本発明は、低分子量キトサンの酸性水溶液を塩
基性水溶液中で成型し、これを酸溶液で処理し、
更にフエニルイソシアネートを反応させることに
より、多孔質粒状体のキトサンを構成するピラノ
ース環100構造単位当りのフエニル基導入量を4
〜45とすると共に、多孔質粒状体の孔径を3〜
10μmの特定範囲とすることにより、担体に要求
される圧縮弾性率を高めると共に、酢酸菌の吸着
量を従来の担体(特願平1−45781号記載)より
も数倍増加せしめることが可能となつたものであ
り、本発明によれば優れた酢酸菌固定化用担体を
得ることができる。[Table] As is clear from Table 3, when the pore diameter exceeds 15 μm, a significant decrease in the compressive elastic modulus is observed even when phenyl groups are introduced. Effects of the Invention The present invention involves molding an acidic aqueous solution of low molecular weight chitosan in a basic aqueous solution, treating it with the acid solution,
Furthermore, by reacting with phenyl isocyanate, the amount of phenyl groups introduced per 100 structural units of pyranose rings constituting the porous granular chitosan was reduced to 4.
〜45, and the pore size of the porous granules is 3〜45.
By setting the specific range of 10 μm, it is possible to increase the compressive elastic modulus required of the carrier and increase the amount of acetic acid bacteria adsorbed several times compared to conventional carriers (described in Japanese Patent Application No. 1-45781). According to the present invention, an excellent carrier for immobilizing acetic acid bacteria can be obtained.
Claims (1)
ス環100構造単位当りのフエニル基導入量が4〜
45で、該多孔質粒状体の細孔径が3〜10μmであ
ることを特徴とする酢酸菌固定化用担体。 2 低分子量キトサンの酸性水溶液を塩基性水溶
液中で凝固析出させて多孔質キトサン粒状体を
得、次いで酸溶液で処理し、更にフエニルイソシ
アネートを反応させることを特徴とする酢酸菌固
定化用担体の製造法。[Scope of Claims] 1. The amount of phenyl groups introduced per 100 structural units of pyranose rings constituting the chitosan of the porous granules is 4 to 4.
45, the carrier for immobilizing acetic acid bacteria, wherein the porous granules have a pore diameter of 3 to 10 μm. 2. A carrier for immobilizing acetic acid bacteria, characterized in that porous chitosan particles are obtained by coagulating and precipitating an acidic aqueous solution of low molecular weight chitosan in a basic aqueous solution, then treated with an acid solution, and further reacted with phenyl isocyanate. manufacturing method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11283890A JPH0411888A (en) | 1990-04-27 | 1990-04-27 | Carrier for immobilizing acetic acid bacteria and its manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11283890A JPH0411888A (en) | 1990-04-27 | 1990-04-27 | Carrier for immobilizing acetic acid bacteria and its manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0411888A JPH0411888A (en) | 1992-01-16 |
| JPH0585158B2 true JPH0585158B2 (en) | 1993-12-06 |
Family
ID=14596799
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11283890A Granted JPH0411888A (en) | 1990-04-27 | 1990-04-27 | Carrier for immobilizing acetic acid bacteria and its manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0411888A (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6176504A (en) * | 1984-09-21 | 1986-04-19 | Fuji Boseki Kk | Production method of granular porous chitosan |
| JPS6229978A (en) * | 1985-07-30 | 1987-02-07 | Fuji Boseki Kk | Carrier for immobilizing physiologically active substance |
-
1990
- 1990-04-27 JP JP11283890A patent/JPH0411888A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0411888A (en) | 1992-01-16 |
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