JPS62180787A - Enzyme-containing filter medium and its production and using method thereof - Google Patents

Enzyme-containing filter medium and its production and using method thereof

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Publication number
JPS62180787A
JPS62180787A JP61020927A JP2092786A JPS62180787A JP S62180787 A JPS62180787 A JP S62180787A JP 61020927 A JP61020927 A JP 61020927A JP 2092786 A JP2092786 A JP 2092786A JP S62180787 A JPS62180787 A JP S62180787A
Authority
JP
Japan
Prior art keywords
enzyme
dissolved
polymer
dimensional network
continuous porous
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.)
Pending
Application number
JP61020927A
Other languages
Japanese (ja)
Inventor
Fumihiro Ishimura
文宏 石村
Masayuki Goto
昌幸 後藤
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.)
Toyo Jozo KK
Original Assignee
Toyo Jozo KK
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 Toyo Jozo KK filed Critical Toyo Jozo KK
Priority to JP61020927A priority Critical patent/JPS62180787A/en
Publication of JPS62180787A publication Critical patent/JPS62180787A/en
Pending legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Abstract

PURPOSE:To make the efficient removal of insoluble impurities and removal of dissolved impurities with one stage by using an enzyme-contg. filter medium formed by immobilizing enzyme to a three-dimensional network open-cellular high polymer as a carrier. CONSTITUTION:The enzyme-contg. filter medium is produced by using enzyme such as glucose oxidase, high polymer having a primary amino group such as chitosan gelatin and crosslinking agent such as glutaraldehyde and immobilizing the enzyme to an insoluble polyvinyl formal having the three-dimensional network open-cellular structure as the carrier. This enzyme-contg. filter medium removes the dissolved impurities contained in soln. in a production process of food industry, chemical industry and pharmaceutical industry and is useful to efficiently and inexpensively remove the dissolved materials, for example, the oxygen and hydrogen peroxide to deteriorate the intended material, and glucose, etc., to change flavor in food industry with one stage.

Description

【発明の詳細な説明】 産業上の利用分野 立体網状連続多孔質高分子を担体として酵素を固定化し
てなる酵素含有ろ過材に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to an enzyme-containing filter material in which an enzyme is immobilized using a three-dimensional network continuous porous polymer as a carrier.

さらに詳しくは、食品工業、医薬品工業、化学工業の製
造工程において、処理される溶液中に含μコーヌ等を除
去するための酵素をろ過材に含有させ、もって不溶性不
純物と溶存性不純物の除去を同時に実施できる酵素含有
ろ過材に関する。
More specifically, in the manufacturing process of the food industry, pharmaceutical industry, and chemical industry, enzymes are included in the filter medium to remove μ-containing substances from the solution being processed, thereby removing insoluble impurities and dissolved impurities. This invention relates to an enzyme-containing filter material that can be used simultaneously.

従来の技術 従来、食品工業、医薬品工業、化学工業の製造工程にお
いて、不溶性の不純物の除去は必須の工程である。また
、工程として溶存性の物質の除去が必要な場合がある。
BACKGROUND OF THE INVENTION Conventionally, the removal of insoluble impurities has been an essential step in manufacturing processes in the food industry, pharmaceutical industry, and chemical industry. Additionally, removal of dissolved substances may be necessary as a process.

例えば、食品工業の牛乳の製造において、殺菌に過酸化
水素が用いられることがあるが、滅菌後この過酸化水素
を牛乳中から除去するのに、カルボキンクロリド樹脂に
固定化したカクラーセを用いる方法(USp員、32g
2102 )があり、また従来から牛乳の酸化臭の発生
防止にトリプシンが有効なことが知られていたが、この
酵素を多孔性ガラスに固定化したものを用いる研究も行
なわれている( W 、 F 、 5hipe。
For example, in the production of milk in the food industry, hydrogen peroxide is sometimes used for sterilization, but in order to remove this hydrogen peroxide from milk after sterilization, there is a method that uses caclase immobilized on carboquine chloride resin. (USp member, 32g
Although trypsin has long been known to be effective in preventing the occurrence of oxidized odor in milk, research is also being conducted using this enzyme immobilized on porous glass (W, 2102). F, 5hipe.

et al、 J 、 Dairy Sci、、 3;
!;  乙4t7.(/り72)〕。
et al., J., Dairy Sci., 3;
! ; Otsu 4t7. (/ri72)].

また、ビールを長期間放置しておくと、ビール中に含ま
れているポリフェノール類とポリペプチドが結合して、
いわゆるチル−ハセ(Chill −haze)ができ
て混濁するが、ビールの製造工程においてこれを防止す
る目的で、主としてパパインが使用されているが、この
ようなタンパク賃分解酵素を長期間ビール、中に添加し
ておくと、タンパク質の加水分解が進行しすぎて好まし
くない影響を与えることがある。そのために、このよう
な欠点のないビールの混濁防止法として、固定化パパイ
ンおよび、固定化ポリフェノールオキシダーセの利用が
検討されている( P 、 R、Witt、 et a
l、 Brewers。
In addition, if beer is left for a long time, the polyphenols and polypeptides contained in beer combine,
Papain is mainly used in the beer manufacturing process to prevent so-called chill-haze, which results in turbidity. If it is added to the water, protein hydrolysis may proceed too much and have undesirable effects. Therefore, the use of immobilized papain and immobilized polyphenol oxidase is being considered as a method for preventing beer turbidity without such drawbacks (P, R, Witt, et al.
l, Brewers.

Dig、、 0cLober、 10 (/デフ0)〕
Dig,, 0cLober, 10 (/def0)]
.

また、マヨネーズの分解腐敗の防止のために、グルコー
スオキシダーゼとカフ・ラーゼな作用させグルコースを
除去することにより、5力月間保存しておいても何ら分
解現象がみられず香味の変化も認められないといわれて
いる。(Get、put、 、 / 227ざS5(/
り6乙)〕。 :: また、砂糖きびの圧さく汁の中にデキストランが存在す
ると清澄工程の際tこ種・々の問題を起こすた砕、、こ
れをあらかじめデキス、トラン分解酵素によりて処理し
ようとする試みもある(N、W、H。
In addition, in order to prevent mayonnaise from decomposing and spoiling, glucose is removed by the action of glucose oxidase and cuff rase, and no decomposition phenomenon is observed even after storage for 5 months, and no change in flavor is observed. It is said that there is no. (Get, put, , /227zaS5(/
ri 6 O)]. :: In addition, the presence of dextran in the crushing juice of sugar cane causes various problems during the clarification process, and there have been attempts to treat this in advance with dextran-degrading enzymes. (N, W, H.

CheeLhan eL al、 Carbobydr
ate Res、、  30  タタ (/デフ3 )
〕。
CheeLhan eL al, Carbobydr
ate Res,, 30 Tata (/def3)
].

柑橘類等のソフトドリンクにおいても、香味の変化をも
たらす溶存酸素を除去する試みがなされている( T 
、 Gadfrey、 oL al、 Ir1dust
rial EnrymologyTlre N、LLu
re Press  1129 )。この様に溶存性の
不純物−)除去が必要な工程はたくさんある。しかし目
下、工業的には不溶性の不純物の除去工程であるろ過工
程と、溶存性の不純物の除去工程は別の工程として実施
されている。
Efforts have also been made to remove dissolved oxygen, which causes changes in the flavor of citrus fruit and other soft drinks (T
, Gadfrey, oL al, Ir1dust
real EnrymologyTlre N, LLu
re Press 1129). There are many processes in which it is necessary to remove dissolved impurities. However, currently, industrially, the filtration process, which is a process for removing insoluble impurities, and the process for removing dissolved impurities are carried out as separate processes.

上述のように、従来食品工業において、溶存性の不純物
の酵素的除去が試みられでいるが、効率が悪い、あるい
は新たに高価な設備を必要とする、あるいは単に酵素を
添加することによる処理方法では、添加された酵素が、
不都合な不純物となる等の問題があり、必ずしも満足の
いくものはなく、また不溶不純物のろ過工程を合せ持つ
ものではなかった。不溶不純物のろ過をも合せ持つもの
として、1奴外ろ過膜Vr−酵素を固定化したものも考
えられているが、1哀外ろ過膜は、本来固形物としての
不溶不純物を除去する目的のものではな(、蛋白r等の
溶解した高分子の不純物の除去に使用されるため、堅い
固形物による膜の破損や、目づまり等に起因する効率の
悪さ、及び必要な蛋白質等溶解性の高分子も除去してし
まうため、本質的に本発明の目的をはだすものではない
As mentioned above, attempts have been made to enzymatically remove dissolved impurities in the food industry, but these methods are either inefficient, require new expensive equipment, or simply involve the addition of enzymes. Then, the added enzyme is
There are problems such as the formation of inconvenient impurities, and none of them are necessarily satisfactory, and they also do not include a filtration step for insoluble impurities. A membrane with immobilized enzymes is also considered as a membrane that also has the ability to filter insoluble impurities. Because it is used to remove impurities from dissolved polymers such as protein, there are problems with membrane damage due to hard solids, poor efficiency due to clogging, etc. Since polymers are also removed, this does not essentially defeat the purpose of the present invention.

また、化学工業、医薬品工業の化成品、医薬品の製造工
程において、溶存性の不純物、例えば酸素eこよって化
成品、医薬品の劣化をまねき、収率の低下をもたらす等
、このような溶存性の不純物質の安価で効率のよい除去
が望まれてぎた。
In addition, in the manufacturing process of chemical products and pharmaceutical products in the chemical and pharmaceutical industries, dissolved impurities, such as oxygen, can cause deterioration of chemical products and pharmaceutical products, resulting in a decrease in yield. There has been a desire for inexpensive and efficient removal of impurities.

:問題点を解決するための手段 : 本発明者らは、鋭意検討の結果、立体網状連続多孔
質高分子を担体として酵素を固定化してなる酵素含有ろ
過材が不溶不純物の効率的な除去および溶存性不純物の
除去を7つの工程tことなし得る満足出来るものである
ことを見い出し、本発明を完成したものである。
:Means for Solving the Problems: As a result of intensive studies, the present inventors have found that an enzyme-containing filter material in which enzymes are immobilized using a three-dimensional network continuous porous polymer as a carrier can efficiently remove insoluble impurities and The present invention was completed based on the discovery that the removal of dissolved impurities can be carried out satisfactorily through seven steps.

、すなわち、本発明は、立体網状連続多孔質高分子を担
体として酵素を固定化してなる酵素含有ろ過材及び酵素
を/吸アミノ基を有する高分子と架橋化剤とを用いて、
立体網状連続多孔質高分子を担体として固定化すること
を特徴とする酵素含有ろ過材の製法及び被処理溶液に、
立体網状連続多孔質高分子を担体として酵素を固定化し
てなる酵素含有ろ過材を用いて不溶不純物の除去ととも
Eこ、溶存性不純物を除去することを特徴とする酵素含
有ろ過材の使用方法に関する。
That is, the present invention uses an enzyme-containing filter material in which an enzyme is immobilized using a three-dimensional network continuous porous polymer as a carrier, and an enzyme/a polymer having an absorbing amino group and a crosslinking agent.
A method for producing an enzyme-containing filter material and a solution to be treated, characterized by immobilizing a three-dimensional network continuous porous polymer as a carrier,
A method of using an enzyme-containing filtration material characterized by removing insoluble impurities and also removing dissolved impurities using an enzyme-containing filtration material obtained by immobilizing an enzyme using a three-dimensional network continuous porous polymer as a carrier. Regarding.

本発明で使用する立体網状連続多孔質高分子としては、
たとえば、立体網状連続多孔質構造を有する水不溶性ポ
リビニルホルマール が出来、ろ過材などの用途として市販されており、一般
に平均孔径S〜1000μ、好ましくは平均孔径30〜
100μの範囲の孔径を有する多孔質構造の水不溶性ポ
リビニルアルコール樹脂がj[4いられる。上記多孔質
構造はその組織が樹板状あ完全連続気孔構造であり、且
つ気イし率が高し・ためやご流体抵抗が低い高分子てあ
:る。□水嵩分子は、水中では変質せず、酵素含有菌体
i誉本高分子を担体として固定化する場合には、加熱減
菌温度に耐え得るような性質を有するものが好ましく、
ホルマ〒ル化度約gO%以上のものを使用するのがよい
The three-dimensional network continuous porous polymer used in the present invention includes:
For example, water-insoluble polyvinyl formal having a three-dimensional network continuous porous structure is produced and is commercially available for use as a filter medium, and generally has an average pore diameter of S ~ 1000μ, preferably an average pore diameter of 30~
A water-insoluble polyvinyl alcohol resin with a porous structure having a pore size in the range of 100 μm is used. The above-mentioned porous structure has a dendritic structure with completely continuous pores, and is made of a polymer with high air flow rate and low fluid resistance. □The bulk water molecule is preferably one that does not change in quality in water and can withstand heat sterilization temperatures when immobilizing enzyme-containing bacterial cells i Homamoto polymer as a carrier.
It is preferable to use a material with a degree of formalization of about gO% or more.

水高分子は弱酸、アルカリおよび多くの有機溶媒に対し
て耐薬品性を示すものがよい。市販の立体網状連続多孔
質構造を有する水不溶性ポリビニルホルマール おいて使用する場合をこは、そのままシートの形で、あ
るいは適宜切断した形または粒状で使用され得、あるい
は適宜切断した形または粒状にしたものを加工成形して
も使用され得る。また上記記載の性状を有する高分子で
あれば水不溶性ポリビニルポルマールに限らず、立体網
状連続多孔質溝道を有する高分子であればよい。
The water polymer preferably exhibits chemical resistance to weak acids, alkalis, and many organic solvents. When used as a commercially available water-insoluble polyvinyl formal having a three-dimensional network continuous porous structure, it can be used as it is in the form of a sheet, or in an appropriately cut or granular form, or it can be used in an appropriately cut or granular form. It can also be used even if it is processed and molded. Further, as long as the polymer has the properties described above, it is not limited to water-insoluble polyvinyl polymer, and any polymer having a three-dimensional network of continuous porous channels may be used.

・また本発明で使用される酵素としては被処理溶液に含
まれる溶存性不純物を基質として作用する、ものであれ
ば何んら限定されるものではなく、例工ば、クルコーヌ
jオキシダーセ、カタラーゼ、トリプシン、パパイン、
プロテアーセ、デキスト・う、ン分解酵素、ポリフエノ
ールオキシダーセ等の酵素を、除去したい溶存不純物1
こ従い、上記等の酵素からなる群より選ばれた7種文は
2種以主の酵素を適宜選択しそ用いればiく、□例1え
ば、溶存酸素、溶存グルコーヌを除□頭する場合?、は
、ンルコーヌオキシダーセ、カタラーゼを組芥斗て用い
ればよく、溶存過酸化水素を除シ場合辷は、カタラーゼ
を用いればよく、□溶存デ阜沫箇→ンをi去する場合に
は、デキストラン分―酵素を用い庇ばよい。本発明で使
用される:上記の酵素は、市販の酵素でもよ(、また必
要なi素糾−渠する菌体、及び菌体処理物でもよい。こ
れらの酵素又は酵素含有菌体、及び菌体処理物を拠常知
られた固定化法に従って担体tこ固定化すれば上<、共
有結合法として、ジアゾ法、ペプチド法、アルキル化法
、架橋試薬tこよる担体結蚕法を用い兎こ左が出来る〔
千畑一部編集,固定化酵素り頁厄g5貞講麟社発行,(
/97!;)及びそれeこ記載された文献参116〕。
・Also, the enzyme used in the present invention is not limited in any way as long as it acts on dissolved impurities contained in the solution to be treated as a substrate, and examples include Curcone J oxidase, catalase, trypsin, papain,
Enzymes such as protease, dextrin-degrading enzyme, and polyphenol oxidase are dissolved impurities to be removed 1
Accordingly, the 7 types selected from the group consisting of the enzymes mentioned above can be used by appropriately selecting two or more types of enzymes. □Example 1: For example, when removing dissolved oxygen and dissolved glucone. When removing dissolved hydrogen peroxide, catalase may be used, and when removing dissolved hydrogen peroxide, catalase may be used. can be protected using dextran and enzymes. Used in the present invention: The above-mentioned enzymes may be commercially available enzymes (or may be necessary microbial cells to be strained and drained, and processed microbial cells). If the body-treated product is immobilized on a carrier according to a known immobilization method, the covalent bonding method may be a diazo method, a peptide method, an alkylation method, or a carrier sericulture method using a cross-linking reagent. I can do this [
Partially edited by Chibata, immobilized enzyme page, published by G5 Sadokorinsha, (
/97! ;) and reference 116].

例えば、酵素を、キトサン、セラチン、アミノ化ポリビ
ニルアルコール 有する高分子と、グ/υタルアlレヂヒド等の架橋化剤
とを用いて、立体網状連続多孔質高分子な担体として固
定化すればよく、また酵素をキトサン、ゼラチン、アミ
ン化ポリビニルアルコール等の/級アミノ基ヲ有スる高
分子と、グルタルアルデヒド高分子を担体として固定化
することにおいて、立体網状連続多孔質高分子をあらか
じめ、キトサン、ゼラチン、アミノ化ポリビニルアルコ
ール等の7級アミノ基を有する高分子で被膜し、その後
、アジピン酸、グルタル酸、ピメリン酸等のジカルボン
酸の活性エステル、酸無水物等、グリオキサール、ヌク
シンジアルデヒド、グルタルアルデヒド等のジアルデヒ
ド等の架橋化剤で活性化し、酵素を固定化してもよい。
For example, the enzyme may be immobilized as a three-dimensional network continuous porous polymer carrier using a polymer containing chitosan, seratin, or aminated polyvinyl alcohol, and a crosslinking agent such as g/v taral aldehyde. Furthermore, in immobilizing an enzyme using a polymer having a primary amino group such as chitosan, gelatin, or aminated polyvinyl alcohol, and a glutaraldehyde polymer as a carrier, a three-dimensional network continuous porous polymer is prepared in advance by chitosan, It is coated with a polymer having a seventh amino group such as gelatin or aminated polyvinyl alcohol, and then coated with active esters of dicarboxylic acids such as adipic acid, glutaric acid, and pimelic acid, acid anhydrides, etc., glyoxal, nuxin dialdehyde, and glutaric acid. The enzyme may be immobilized by activation with a crosslinking agent such as a dialdehyde such as an aldehyde.

ここで用いられる担体と酵素量の量的関係としては、不
溶不純物、及び溶存不純物の処理物質に対する割合によ
るが、担体量/ mlに対し酵素量は07〜10OOO
U用いればよく、好ましくは/〜10OOUを用いれば
よい。例えば、溶存過酸化水素の除去を不溶不純物の除
去とともに行なう場合、担体量/ mlに対しカタラー
セ50〜500Uを用いればよく好ましくは、100〜
300U用いればよい。また溶存グルコースの除去を不
溶不純物の除去とともに行なう場合、担体量/ mlに
対シクルコーヌオキシダーゼを/〜10OU1カクラー
セを10〜10OOU用いればよく好ましくは、’ り
/レコースオキシダーセ/〜10U1カタラーゼ100
〜10OOU用いればよい。また溶存デキストランの除
去を不溶不純物の除去ととも1こ行なう場合、担体量/
 mlに対しデキストラン分解酵素10〜10OOU用
いればよく好ましくは、100〜10OOU用いればよ
い。
The quantitative relationship between the carrier used here and the amount of enzyme depends on the ratio of insoluble impurities and dissolved impurities to the treated material, but the amount of enzyme is 0.7 to 10 OOO relative to the amount of carrier/ml.
U may be used, and preferably /~100OU may be used. For example, when removing dissolved hydrogen peroxide as well as removing insoluble impurities, it is sufficient to use 50 to 500 U of catalase per ml of carrier, preferably 100 to 500 U of catalase per ml of carrier.
300U may be used. In addition, when removing dissolved glucose together with removing insoluble impurities, it is sufficient to use 10 to 10 OOU of cyclone oxidase/~10U1 catalase per ml of carrier, preferably 100
~10OOU may be used. In addition, when removing dissolved dextran and removing insoluble impurities, the amount of carrier/
It is sufficient to use 10 to 10 OOU of dextran degrading enzyme per ml, preferably 100 to 10 OOU.

このようにして得られた立体網状連続多孔質高分子を担
体として酵素を固定化したものを、適宜成形加工し、酵
素含有ろ過材とすればよく、/−ト伏の担体に固定化さ
れたものは、使用するろ過器にあわせて切断加工すれば
よい。
The thus obtained three-dimensional network continuous porous polymer is used as a carrier to immobilize the enzyme, and may be appropriately molded to form an enzyme-containing filter material. All you have to do is cut it to fit the filter you are using.

本発明は、上記の如く得られた立体網状連続多孔質高分
子な担体として固定化してなる酵素含有ろ過材を用いて
、不溶不純物の除去とともに、溶存酵素及び/又は溶存
過酸化水素及び/又は溶存デキストラン及び/又は溶存
グイレコース及び又は溶伴゛蛋白質を除去することを用
いて、不溶不純物の除素方法も含み、ろ過流速は、処理
物質の性状にもよるが007〜/ (1) m / b
rで用いればよく好ま、シ<は0/〜.!; m / 
11rで用いればよい。またろ過温度は、処理物質の性
状にもよるが、5〜乙O℃の雫囲で行なえばよく、安定
性の悪いものは、低温竺で行えばよい。例えば不溶歪純
物と溶存デキストランを除去する場合には好ましくは3
0−jOpで行えばよい。しかしながら、処理物質が安
実施例 以下実施例tこより説明するが何ら実施例に限定される
ものではない。
The present invention uses an enzyme-containing filter material immobilized as a three-dimensional network continuous porous polymer carrier obtained as described above to remove insoluble impurities, and remove dissolved enzyme and/or dissolved hydrogen peroxide. It also includes a method for removing insoluble impurities by removing dissolved dextran and/or dissolved gyrecose and/or dissolved protein, and the filtration flow rate is 007~/(1) m/, depending on the properties of the treated substance. b
It is preferable to use it with r, and shi< is 0/~. ! ;m/
11r may be used. Although the filtration temperature depends on the properties of the substance to be treated, it may be carried out at a temperature of 5 to 00C, and if the stability is poor, the filtration may be carried out at a low temperature. For example, when removing insoluble strained substances and dissolved dextran, preferably 3
0-jOp may be used. However, although the processing substance is safe and will be explained in the following examples, it is not limited to these examples in any way.

(実施例/) 多孔性ポリビニルホ)Vマール樹脂シート〔市販のべ!
レイーターEB(A)平均孔径/30μ、気孔率gs%
、/重厚さくカネボウ社)以下多孔性PVFと略す〕を
ハサミでりOxりO重用に裁断し、りO耐×りO重用の
多孔性PVFを得る。得られたりO朋×りQmm角の多
孔性PVF/110枚を7%キトサン液/lに7時間浸
漬させる。7%キトサン液は0. / Nギ酸gOOI
Rtにキトサンとして10fの市販のクリワックヌcp
−乙73(栗田工業)’IbWl解した後、!;N−N
aOHにてpHをII5に調整後、全量が/lになるよ
う蒸留水を加えて調整する。7時間キトサン液(こ浸漬
した多孔性PVFを通風乾燥により乾燥させ、立体的樹
枝網目状連続組織なこキトサンを被膜させた乾燥多孔性
PVFを得る。得られた乾燥多孔性PVFの5枚を、5
%ゲルタールアルデヒド溶R110Omlに力6L棧P
VP 30分憤浸漬した後、49/flfをゲルタールアルデ
ヒド液より取り出し、蒸留水で良く院号する。S%ゲル
タールアルデヒド %グIレタールアルデヒド/Qmlを0. / Mのリ
ン酸バッファ(pH7.5)りQmlと混合させること
により調整する。カタラー−+zの9素液として、市販
ヰ肝Nk由未 ツカ1;l ?−セ( シン−qm. lttsm x
tttigt zzett)を用い、カクラーセ儂度が
/i2U/m1.//Qmlを調整する。前記操作によ
り得られた多孔性PVF/枚を各々の濃度を有するカタ
ラーゼ液/QQmlに攪拌下浸漬する。浸漬を7時間実
施し、カタラーゼ固定化多孔性PVFを得る。得られた
7枚当りの酵素力価は/ /、 2 U 1m1Q度の
カタラーゼ液を用いた場合、1033Uであり、//7
U / ml Q度の場合は1073;Uであり、/2
30U / mlの濃度の場合は/300Uであった。
(Example/) Porous polyvinyl resin sheet (commercially available)
Rater EB (A) Average pore diameter/30μ, porosity gs%
, /Jyuutsuku Kanebo Co., Ltd.) (hereinafter abbreviated as "porous PVF")] was cut with scissors into an Ox-resistance-resistant porous PVF. 110 sheets of porous PVF with a square size of O x Q mm were immersed in a 7% chitosan solution/l for 7 hours. 7% chitosan solution is 0. / N-formic acid gOOI
10f of commercially available Kuriwaknu CP as chitosan to Rt.
- Otsu 73 (Kurita Industries) 'After understanding IbWl! ;N-N
After adjusting the pH to II5 with aOH, add distilled water to adjust the total volume to /l. The porous PVF soaked in chitosan solution for 7 hours is dried by ventilation drying to obtain dry porous PVF coated with chitosan having a three-dimensional dendritic network continuous structure. Five sheets of the obtained dry porous PVF are 5
% gel tar aldehyde solution R 110 Oml to 6L 棧P
VP After soaking for 30 minutes, remove 49/flf from the geltaldehyde solution and rinse well with distilled water. S% Geltaraldehyde% Geltaraldehyde/Qml 0. /M phosphate buffer (pH 7.5) by mixing with Qml. Commercially available as a 9-base solution of Katara-+z. -Se( Shin-qm.lttsm x
tttigt zzett), and the Kaklase degree is /i2U/m1. //Adjust Qml. The porous PVF/sheet obtained by the above operation is immersed in catalase solution/QQml having each concentration under stirring. Soaking is carried out for 7 hours to obtain catalase-immobilized porous PVF. The enzyme titer obtained per 7 pieces is 1033 U when using 2 U 1 ml of catalase solution, //7
U / ml for Q degree 1073; U and /2
For a concentration of 30U/ml, it was /300U.

カタことにより決定した。市販の牛乳/lに過酸化水素
を加えることにより、/(1)ppmの過酸化水素含有
牛乳を調整した、前記固定化操作により得られたカタラ
ーゼ固定化多孔性PVF (107!;U//枚)7枚
を用い、10ppm過酸化水素含有牛乳を加圧ろ過した
。ろ過には35分要した。ろ過された牛乳の過酸化駁素
濃度はO,/ p p m以下であった。
It was decided by Kata. Catalase-immobilized porous PVF (107!; U// Milk containing 10 ppm hydrogen peroxide was filtered under pressure using 7 sheets. Filtration required 35 minutes. The concentration of ferron peroxide in the filtered milk was less than O,/ppm.

(実施例2) /33Uのクルコースオギシタ゛−ゼとZ乙0Ooxi
dase  [アスペルギ!レヌ・ニガー由来)と市販
のカタラーゼ(実施例/と同じ)を用い調整した。得ら
れた酵素p 3 mlと7%キトサン液(実施例/と同
様に調整)3mlと市販の50%グルクールアルデヒド
00乙ゴを良く混合した溶液にり0X90酎の多孔性P
VF(厚さ/酎)7枚を浸漬する。7時間の浸漬の後多
孔性PVFを通風乾燥17枚当りの酵素活性は、グルコ
ースオキシダー上311U、カタラーゼ3SOOUであ
った。/%グルコース液に室温にて攪拌することにより
、廖存酸素濃度3.5 p p mの/%グルコース液
を、前記工程により得られたグルコースオキシダーゼ、
カタラーゼ固定化多孔性PVFを用い加圧ろ過した。ろ
過には25分要した。得られたろ液中の溶存酸素濃度は
O/ppmであった。なお、グルコースオキシダーゼの
酵素力価は、基質としてグルコースを用い、生成するグ
ルコン酸をNaOHIc ”?:中和し、中和tこ必要
なNaOH量として活性を決定した。
(Example 2) /33U crucose oxidase and ZOoxi
dase [Aspergi! (derived from Renu niger) and commercially available catalase (same as in Example). Add 3 ml of the obtained enzyme p, 3 ml of 7% chitosan solution (prepared in the same manner as in Example), and a well-mixed solution of commercially available 50% glucuraldehyde 00 Otogo to the porous P of 0X90 chu.
Soak 7 pieces of VF (thickness/chu). The enzyme activity per 17 sheets of porous PVF dried through ventilation after soaking for 7 hours was 311 U for glucose oxidizer and 3 SOOU for catalase. By stirring the /% glucose solution at room temperature, the /% glucose solution with a residual oxygen concentration of 3.5 ppm is added to the glucose oxidase obtained in the above step,
Pressure filtration was performed using catalase-immobilized porous PVF. Filtration required 25 minutes. The dissolved oxygen concentration in the obtained filtrate was O/ppm. The enzyme titer of glucose oxidase was determined by neutralizing the gluconic acid produced using glucose as a substrate and determining the activity as the amount of NaOH required for neutralization.

(実施例3) 実施例/のカタラーゼ酵素液にデキストランー/ 00
 mlに攪拌下浸漬する。デキストラナーセ液100m
1は、市販のデキストヲナーセ200η(シグマ社、ベ
ニシリニウム由来、23U/’1G)を010Mリン酸
バッファー100m1c PH7,5)に溶解させるこ
とにより得る。デキストラナーセの酵素力価は、デキス
トリンを基質として、デキストランの酵素分解により生
成するイソマルl−−ヌを還元免として定量することに
より決定した。
(Example 3) Add dextran/00 to the catalase enzyme solution of Example/
ml under stirring. Dextranase liquid 100m
1 is obtained by dissolving commercially available Dextoonase 200η (Sigma, derived from benicillinium, 23U/'1G) in 010M phosphate buffer (100ml, pH 7.5). The enzyme titer of dextranase was determined by using dextrin as a substrate and quantifying isomal l--nu produced by enzymatic decomposition of dextran as a reducing enzyme.

シコ 7枚当りの活性は2200Uであった。夢糖10%とデ
キストラン/%を含む溶液/lを調製し、ストランとし
てDextran T 10 (ファルマンア製)を使
用した。ろ液中には還元糖がマルトースとしてq、/を
含まれていた。
The activity per 7 pieces of shiko was 2200U. A solution/l containing 10% dream sugar and dextran/% was prepared, and Dextran T 10 (manufactured by Farmana) was used as the strand. The filtrate contained reducing sugar q,/ as maltose.

発明の効果 本発明の、立体網状連続多孔質高分子を担体として酵素
を固定化した酵素含有ろ過材は、食品工業、化学工業、
薬品工業の製造工程において溶液中に含まれる不溶化不
純物を除去するとともをこ効率よく、しかも安価に、溶
存物質、例えば目的物質の劣化を引きおこす酸素、過酸
化水素あるいは食品工業においては、フレーバーの変化
をもたらすグルコース等を一工程にて除去出来る有用な
ものである。
Effects of the Invention The enzyme-containing filter material of the present invention, in which an enzyme is immobilized using a three-dimensional network continuous porous polymer as a carrier, can be used in the food industry, chemical industry,
In addition to removing insolubilized impurities contained in solutions in the manufacturing process of the pharmaceutical industry, it is possible to efficiently and inexpensively remove dissolved substances such as oxygen, hydrogen peroxide, which cause deterioration of the target substance, or flavor changes in the food industry. This is a useful product that can remove glucose, etc. that cause oxidation in one step.

Claims (1)

【特許請求の範囲】 1)、立体網状連続多孔質高分子を担体として酵素を固
定化してなる酵素含有ろ過材。 2)、立体網状連続多孔質高分子が、立体網状連続多孔
質構造を有する水不溶性ポリビニルホルマールである特
許請求の範囲第1項記載の酵素含有ろ過材。 3)、酵素が、グルコースオキシダーゼ、カタラーゼ、
トリプシン、パパイン、プロテアーゼ、デキストラン分
解酵素、ポリフェノールオキシダーゼからなる群より選
ばれた1種又は2種以上である特許請求の範囲第1項記
載の酵素含有ろ過材。 4)、酵素を1級アミノ基を有する高分子と架橋化剤と
を用いて、立体網状連続多孔質高分子を担体として固定
化することを特徴とする酵素含有ろ過材の製法。 5)、酵素を1級アミノ基を有する高分子と架橋化剤と
を用いて、立体網状連続多孔質高分子を担体として固定
化することにおいて、立体網状連続多孔質高分子をあら
かじめ1級アミノ基を有する高分子で被膜し、その後、
架橋化剤で活性化して固定化することを特徴とする特許
請求の範囲第4項記載の製法。 6)、1級アミノ基を有する高分子が、キトサンゼラチ
ン、アミノ化ポリビニルアルコールからなる群より選ば
れた1種又は2種からなる高分子である特許請求の範囲
第4項または第5項記載の製法。 7)、架橋化剤が、グルタルアルデヒドである特許請求
の範囲第4項、第5項記載の製法。 8)、酵素が、グルコースオキシダーゼ、カタラーゼ、
トリプシン、パパイン、プロテアーゼ、デキストラン分
解酵素、ポリフェノールオキシダーゼからなる群より選
ばれた1種又は2種以上である特許請求の範囲第4項ま
たは第5項記載の製法。 9)、立体網状連続多孔質高分子が立体網状連続多孔質
構造を有する水不溶性ポリビニルホルマールである特許
請求の範囲第4項、第5項記載の製法。 10)、該処理溶液に、立体網状連続多孔質高分子を担
体として酵素を固定化してなる酵素含有ろ過材を用いて
、不溶不純物の除去とともに、溶存性不純物を除去する
ことを特徴とする不純物の除去方法。 11)、溶存性不純物が、溶存酸素、溶存過酸化水素、
溶存デキストラン、溶存グルコースまたは溶存蛋白質で
ある特許請求の範囲第10項記載の不純物の除去方法。
[Claims] 1) An enzyme-containing filtration material in which an enzyme is immobilized using a three-dimensional network continuous porous polymer as a carrier. 2) The enzyme-containing filter material according to claim 1, wherein the three-dimensional network continuous porous polymer is a water-insoluble polyvinyl formal having a three-dimensional network continuous porous structure. 3) The enzyme is glucose oxidase, catalase,
The enzyme-containing filter material according to claim 1, which is one or more selected from the group consisting of trypsin, papain, protease, dextran degrading enzyme, and polyphenol oxidase. 4) A method for producing an enzyme-containing filter medium, which comprises immobilizing an enzyme on a three-dimensional network continuous porous polymer as a carrier using a polymer having a primary amino group and a crosslinking agent. 5) In immobilizing an enzyme as a carrier on a 3D continuous porous polymer using a polymer having a primary amino group and a crosslinking agent, the 3D continuous porous polymer is preliminarily treated with primary amino groups. coated with a polymer having groups, and then
5. The production method according to claim 4, wherein the immobilization is performed by activation with a crosslinking agent. 6) Claim 4 or 5, wherein the polymer having a primary amino group is a polymer consisting of one or two selected from the group consisting of chitosan gelatin and aminated polyvinyl alcohol. manufacturing method. 7) The manufacturing method according to claims 4 and 5, wherein the crosslinking agent is glutaraldehyde. 8) The enzyme is glucose oxidase, catalase,
The production method according to claim 4 or 5, wherein the enzyme is one or more selected from the group consisting of trypsin, papain, protease, dextran degrading enzyme, and polyphenol oxidase. 9) The production method according to claims 4 and 5, wherein the three-dimensional network continuous porous polymer is a water-insoluble polyvinyl formal having a three-dimensional network continuous porous structure. 10) Impurities characterized by removing dissolved impurities as well as insoluble impurities in the treatment solution using an enzyme-containing filter material in which an enzyme is immobilized using a three-dimensional network continuous porous polymer as a carrier. How to remove. 11) The dissolved impurities are dissolved oxygen, dissolved hydrogen peroxide,
11. The method for removing impurities according to claim 10, which is dissolved dextran, dissolved glucose, or dissolved protein.
JP61020927A 1986-01-31 1986-01-31 Enzyme-containing filter medium and its production and using method thereof Pending JPS62180787A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61020927A JPS62180787A (en) 1986-01-31 1986-01-31 Enzyme-containing filter medium and its production and using method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61020927A JPS62180787A (en) 1986-01-31 1986-01-31 Enzyme-containing filter medium and its production and using method thereof

Publications (1)

Publication Number Publication Date
JPS62180787A true JPS62180787A (en) 1987-08-08

Family

ID=12040848

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61020927A Pending JPS62180787A (en) 1986-01-31 1986-01-31 Enzyme-containing filter medium and its production and using method thereof

Country Status (1)

Country Link
JP (1) JPS62180787A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0654483A1 (en) * 1993-11-22 1995-05-24 Roquette Frˬres Process for purifying a hypocaloric soluble glucose polymer and product so obtained
CN105060459A (en) * 2015-08-05 2015-11-18 四川建环科技有限公司 Water treatment enzymatic biological stuffing and preparation method thereof
CN110352179A (en) * 2017-02-15 2019-10-18 法伦生物技术公司 The enzymatic of water purifies

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5311491U (en) * 1976-07-14 1978-01-31
JPS6049795A (en) * 1983-08-31 1985-03-19 Kanai Hiroyuki Sterilizing fiber sheet

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5311491U (en) * 1976-07-14 1978-01-31
JPS6049795A (en) * 1983-08-31 1985-03-19 Kanai Hiroyuki Sterilizing fiber sheet

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0654483A1 (en) * 1993-11-22 1995-05-24 Roquette Frˬres Process for purifying a hypocaloric soluble glucose polymer and product so obtained
FR2712891A1 (en) * 1993-11-22 1995-06-02 Roquette Freres Process for purifying a low-calorie glucose soluble polymer and the product thus obtained
US5573794A (en) * 1993-11-22 1996-11-12 Roquette Freres Process for treating a soluble glucose polymer and product thus obtained
CN105060459A (en) * 2015-08-05 2015-11-18 四川建环科技有限公司 Water treatment enzymatic biological stuffing and preparation method thereof
CN110352179A (en) * 2017-02-15 2019-10-18 法伦生物技术公司 The enzymatic of water purifies

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