JPS609793B2 - Method for producing immobilized glucose isomerase - Google Patents
Method for producing immobilized glucose isomeraseInfo
- Publication number
- JPS609793B2 JPS609793B2 JP7035677A JP7035677A JPS609793B2 JP S609793 B2 JPS609793 B2 JP S609793B2 JP 7035677 A JP7035677 A JP 7035677A JP 7035677 A JP7035677 A JP 7035677A JP S609793 B2 JPS609793 B2 JP S609793B2
- Authority
- JP
- Japan
- Prior art keywords
- glucose isomerase
- glucose
- solution
- immobilized
- immobilized glucose
- 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
Links
- 108700040099 Xylose isomerases Proteins 0.000 title claims description 44
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- 229920001661 Chitosan Polymers 0.000 claims description 18
- 229910019142 PO4 Inorganic materials 0.000 claims description 17
- 230000001580 bacterial effect Effects 0.000 claims description 16
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 13
- 239000010452 phosphate Substances 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 8
- 239000007864 aqueous solution Substances 0.000 claims description 5
- 230000007935 neutral effect Effects 0.000 claims description 5
- 230000004523 agglutinating effect Effects 0.000 claims description 3
- 239000000243 solution Substances 0.000 description 24
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 21
- 239000008103 glucose Substances 0.000 description 21
- 238000006317 isomerization reaction Methods 0.000 description 20
- 235000021317 phosphate Nutrition 0.000 description 16
- 238000006243 chemical reaction Methods 0.000 description 15
- 230000000813 microbial effect Effects 0.000 description 10
- 230000004520 agglutination Effects 0.000 description 8
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- 102000004190 Enzymes Human genes 0.000 description 6
- 108090000790 Enzymes Proteins 0.000 description 6
- MHJAJDCZWVHCPF-UHFFFAOYSA-L dimagnesium phosphate Chemical compound [Mg+2].OP([O-])([O-])=O MHJAJDCZWVHCPF-UHFFFAOYSA-L 0.000 description 6
- 229910000395 dimagnesium phosphate Inorganic materials 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000002253 acid Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 230000002378 acidificating effect Effects 0.000 description 4
- 239000006285 cell suspension Substances 0.000 description 4
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 4
- 230000009257 reactivity Effects 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 239000005715 Fructose Substances 0.000 description 3
- XZTWHWHGBBCSMX-UHFFFAOYSA-J dimagnesium;phosphonato phosphate Chemical compound [Mg+2].[Mg+2].[O-]P([O-])(=O)OP([O-])([O-])=O XZTWHWHGBBCSMX-UHFFFAOYSA-J 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 2
- SRBFZHDQGSBBOR-IOVATXLUSA-N D-xylopyranose Chemical compound O[C@@H]1COC(O)[C@H](O)[C@H]1O SRBFZHDQGSBBOR-IOVATXLUSA-N 0.000 description 2
- 229930091371 Fructose Natural products 0.000 description 2
- RFSUNEUAIZKAJO-ARQDHWQXSA-N Fructose Chemical compound OC[C@H]1O[C@](O)(CO)[C@@H](O)[C@@H]1O RFSUNEUAIZKAJO-ARQDHWQXSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- 241000209094 Oryza Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- JUNWLZAGQLJVLR-UHFFFAOYSA-J calcium diphosphate Chemical compound [Ca+2].[Ca+2].[O-]P([O-])(=O)OP([O-])([O-])=O JUNWLZAGQLJVLR-UHFFFAOYSA-J 0.000 description 2
- ROPDWRCJTIRLTR-UHFFFAOYSA-L calcium metaphosphate Chemical compound [Ca+2].[O-]P(=O)=O.[O-]P(=O)=O ROPDWRCJTIRLTR-UHFFFAOYSA-L 0.000 description 2
- 239000001506 calcium phosphate Substances 0.000 description 2
- 229910000389 calcium phosphate Inorganic materials 0.000 description 2
- 235000011010 calcium phosphates Nutrition 0.000 description 2
- 229940043256 calcium pyrophosphate Drugs 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 235000019821 dicalcium diphosphate Nutrition 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- MTNDZQHUAFNZQY-UHFFFAOYSA-N imidazoline Chemical compound C1CN=CN1 MTNDZQHUAFNZQY-UHFFFAOYSA-N 0.000 description 2
- NOESYZHRGYRDHS-UHFFFAOYSA-N insulin Chemical compound N1C(=O)C(NC(=O)C(CCC(N)=O)NC(=O)C(CCC(O)=O)NC(=O)C(C(C)C)NC(=O)C(NC(=O)CN)C(C)CC)CSSCC(C(NC(CO)C(=O)NC(CC(C)C)C(=O)NC(CC=2C=CC(O)=CC=2)C(=O)NC(CCC(N)=O)C(=O)NC(CC(C)C)C(=O)NC(CCC(O)=O)C(=O)NC(CC(N)=O)C(=O)NC(CC=2C=CC(O)=CC=2)C(=O)NC(CSSCC(NC(=O)C(C(C)C)NC(=O)C(CC(C)C)NC(=O)C(CC=2C=CC(O)=CC=2)NC(=O)C(CC(C)C)NC(=O)C(C)NC(=O)C(CCC(O)=O)NC(=O)C(C(C)C)NC(=O)C(CC(C)C)NC(=O)C(CC=2NC=NC=2)NC(=O)C(CO)NC(=O)CNC2=O)C(=O)NCC(=O)NC(CCC(O)=O)C(=O)NC(CCCNC(N)=N)C(=O)NCC(=O)NC(CC=3C=CC=CC=3)C(=O)NC(CC=3C=CC=CC=3)C(=O)NC(CC=3C=CC(O)=CC=3)C(=O)NC(C(C)O)C(=O)N3C(CCC3)C(=O)NC(CCCCN)C(=O)NC(C)C(O)=O)C(=O)NC(CC(N)=O)C(O)=O)=O)NC(=O)C(C(C)CC)NC(=O)C(CO)NC(=O)C(C(C)O)NC(=O)C1CSSCC2NC(=O)C(CC(C)C)NC(=O)C(NC(=O)C(CCC(N)=O)NC(=O)C(CC(N)=O)NC(=O)C(NC(=O)C(N)CC=1C=CC=CC=1)C(C)C)CC1=CN=CN1 NOESYZHRGYRDHS-UHFFFAOYSA-N 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- GVALZJMUIHGIMD-UHFFFAOYSA-H magnesium phosphate Chemical compound [Mg+2].[Mg+2].[Mg+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O GVALZJMUIHGIMD-UHFFFAOYSA-H 0.000 description 2
- 239000004137 magnesium phosphate Substances 0.000 description 2
- 229910000157 magnesium phosphate Inorganic materials 0.000 description 2
- 229960002261 magnesium phosphate Drugs 0.000 description 2
- 235000010994 magnesium phosphates Nutrition 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000008961 swelling Effects 0.000 description 2
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 description 2
- LWIHDJKSTIGBAC-UHFFFAOYSA-K tripotassium phosphate Chemical compound [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 description 2
- 229920002554 vinyl polymer Polymers 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
- 241000186063 Arthrobacter Species 0.000 description 1
- 241000193830 Bacillus <bacterium> Species 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 241000282693 Cercopithecidae Species 0.000 description 1
- 229920002261 Corn starch Polymers 0.000 description 1
- 108010093096 Immobilized Enzymes Proteins 0.000 description 1
- 102000004877 Insulin Human genes 0.000 description 1
- 108090001061 Insulin Proteins 0.000 description 1
- UEZVMMHDMIWARA-UHFFFAOYSA-N Metaphosphoric acid Chemical compound OP(=O)=O UEZVMMHDMIWARA-UHFFFAOYSA-N 0.000 description 1
- 241000589516 Pseudomonas Species 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 241000187747 Streptomyces Species 0.000 description 1
- 239000003929 acidic solution Substances 0.000 description 1
- 230000004931 aggregating effect Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000003957 anion exchange resin Substances 0.000 description 1
- PYMYPHUHKUWMLA-UHFFFAOYSA-N arabinose Natural products OCC(O)C(O)C(O)C=O PYMYPHUHKUWMLA-UHFFFAOYSA-N 0.000 description 1
- SRBFZHDQGSBBOR-UHFFFAOYSA-N beta-D-Pyranose-Lyxose Natural products OC1COC(O)C(O)C1O SRBFZHDQGSBBOR-UHFFFAOYSA-N 0.000 description 1
- 239000007853 buffer solution Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229960001714 calcium phosphate Drugs 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- GVPFVAHMJGGAJG-UHFFFAOYSA-L cobalt dichloride Chemical compound [Cl-].[Cl-].[Co+2] GVPFVAHMJGGAJG-UHFFFAOYSA-L 0.000 description 1
- 239000008120 corn starch Substances 0.000 description 1
- 229940099112 cornstarch Drugs 0.000 description 1
- 238000012258 culturing Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- ZJIPHXXDPROMEF-UHFFFAOYSA-N dihydroxyphosphanyl dihydrogen phosphite Chemical compound OP(O)OP(O)O ZJIPHXXDPROMEF-UHFFFAOYSA-N 0.000 description 1
- 235000011180 diphosphates Nutrition 0.000 description 1
- XPPKVPWEQAFLFU-UHFFFAOYSA-N diphosphoric acid Chemical compound OP(O)(=O)OP(O)(O)=O XPPKVPWEQAFLFU-UHFFFAOYSA-N 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000005284 excitation Effects 0.000 description 1
- 210000003811 finger Anatomy 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- TVZISJTYELEYPI-UHFFFAOYSA-N hypodiphosphoric acid Chemical compound OP(O)(=O)P(O)(O)=O TVZISJTYELEYPI-UHFFFAOYSA-N 0.000 description 1
- 230000003100 immobilizing effect Effects 0.000 description 1
- 229940125396 insulin Drugs 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 125000005341 metaphosphate group Chemical group 0.000 description 1
- RHJYKEDKMHDZBL-UHFFFAOYSA-L metaphosphoric acid (hpo3), magnesium salt Chemical compound [Mg+2].[O-]P(=O)=O.[O-]P(=O)=O RHJYKEDKMHDZBL-UHFFFAOYSA-L 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- ACVYVLVWPXVTIT-UHFFFAOYSA-N phosphinic acid Chemical compound O[PH2]=O ACVYVLVWPXVTIT-UHFFFAOYSA-N 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229910000160 potassium phosphate Inorganic materials 0.000 description 1
- 235000011009 potassium phosphates Nutrition 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 229940005657 pyrophosphoric acid Drugs 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- ISIJQEHRDSCQIU-UHFFFAOYSA-N tert-butyl 2,7-diazaspiro[4.5]decane-7-carboxylate Chemical compound C1N(C(=O)OC(C)(C)C)CCCC11CNCC1 ISIJQEHRDSCQIU-UHFFFAOYSA-N 0.000 description 1
- 210000003813 thumb Anatomy 0.000 description 1
Landscapes
- Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
- Enzymes And Modification Thereof (AREA)
Description
【発明の詳細な説明】
本発明は固定化グルコースィソメラーゼの製造法に関す
るものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing immobilized glucose isomerase.
近年、グルコースィソメラーゼ活性を有する菌体を担体
に固定化して、この固定化グルコースィソメラーゼを用
いてグルコースを効率よく異性化することが工業的に行
なわれている。In recent years, it has been carried out industrially to immobilize bacterial cells having glucose isomerase activity on a carrier and to efficiently isomerize glucose using the immobilized glucose isomerase.
固定化グルコースィソメラーゼの製法としては例えば菌
体をポリビニルィミダゾリンあるいは陽性アクリルアミ
ド、キトサンなどの可溶性高分子凝集剤で凝集させて固
定化したり、陰イオン交キ製樹脂に吸着させて固定化す
る方法などが知られている。また菌体のグルコースィソ
メラーゼ活性の発現率を高めるために、珪藤土、シリカ
ーアルミナ、活性炭等の多孔性物質を固定化グルコース
ィソメラーゼに含有させることも知られている。しかし
ながら、このようにして得られる固定化グルコースィソ
メラーゼはカラムに充填して連続的にグルコースの異性
化反応を行なわせる場合、異性化反応の初期において異
性化された糠液が酸性に傾いたりあるいは異性化反応の
後期に反応速度が低下するにつれて酸性になる煩向が認
められた。Immobilized glucose isomerase can be produced by, for example, aggregating and immobilizing bacterial cells with polyvinyl imidazoline or a soluble polymer flocculant such as positive acrylamide or chitosan, or by adsorbing them onto an anion exchange resin. There are known methods to do this. It is also known that immobilized glucose isomerase contains porous substances such as silica clay, silica alumina, and activated carbon in order to increase the expression rate of glucose isomerase activity in bacterial cells. However, when the immobilized glucose isomerase obtained in this way is packed into a column and the glucose isomerization reaction is performed continuously, the isomerized bran liquid becomes acidic in the early stage of the isomerization reaction. Alternatively, as the reaction rate decreased in the latter stage of the isomerization reaction, a tendency to become acidic was observed.
このような煩向はグルコースィソメラーゼの至薄pHあ
るいは安定pHから著しく逸脱し、グルコースィソメラ
ーゼの反応性あるいは安定性において充分満足できるも
のとは言い難い。さらに、固定化グルコースィソメラー
ゼをグルコース溶液に投入して、バッチ式に異性化反応
を行なわせる場合も反応が進行するにつれて、異性化さ
れた糠液が酸性になる煩向がある。Such a tendency significantly deviates from the lowest pH or stable pH of glucose isomerase, and it cannot be said that the reactivity or stability of glucose isomerase is fully satisfactory. Furthermore, even when immobilized glucose isomerase is added to a glucose solution and the isomerization reaction is carried out in a batch manner, the isomerized rice bran tends to become acidic as the reaction progresses.
本発明者らは、固定化グルコースィソメラーゼの活性な
らびに物理的強度を低下させることなく、これらの傾向
を解消するために種々鋭意検討したところ、キトサンで
グルコースイソメラーゼ生産菌体を凝集させて固定化グ
ルコースィソメラーゼを製造するに際し、固定化グルコ
ースィソメラーゼに中性あるいはアルカリ性水溶液に難
熔性のリン酸塩を含有させると所期の目的を達成するこ
とを見出し、本発明に到達した。The present inventors conducted various studies to resolve these tendencies without reducing the activity and physical strength of immobilized glucose isomerase, and found that glucose isomerase-producing bacterial cells were aggregated and immobilized with chitosan. The present inventors have discovered that when producing glucose isomerase, the desired objective can be achieved by adding a refractory phosphate to the immobilized glucose isomerase in a neutral or alkaline aqueous solution, and have thus arrived at the present invention. .
すなわち本発明はキトサンでグルコースィソメラーゼ生
産菌体を凝集させて固定化グルコースィソメラーゼを製
造する方法において、任意の段階で固定化グルコースィ
ソメラーゼに中性あるいはアルカリ性水溶液中で難熔性
のリン酸塩を含有させることを特徴とする固定化グルコ
ースィソメラーゼの製造法である。本発明方法による固
定化グルコースィソメラ−ゼは酵素の反応性が著しく増
強され、グルコースの異性化能力が大幅に改善されると
同時にグルコースの異性化力も安定し、操作性にも優れ
る。That is, the present invention provides a method for producing immobilized glucose isomerase by agglutinating glucose isomerase-producing microbial cells with chitosan, and the immobilized glucose isomerase is insoluble in a neutral or alkaline aqueous solution at any stage. This is a method for producing immobilized glucose isomerase, which is characterized in that it contains a phosphate. The immobilized glucose isomerase produced by the method of the present invention has significantly enhanced enzyme reactivity, greatly improved glucose isomerization ability, stable glucose isomerization ability, and excellent operability.
本発明において使用するグルコースィソメラーゼ生産菌
体としては、ストレプトマィセス属「バチルス属、アー
スロバクター属、シュードモナス属等のグルコースィソ
メラーゼを生産する微生物菌体が挙げられる。これらの
菌体は窒素源としてコーンステイープリカー単独または
他の窒素源を添加し「炭素源として澱粉、キシロースな
どの炭水化物類、無機塩としては燐酸カリウムト塩化コ
バルトおよび塩化マグネシウムなどを含んだ培地に培養
して取得する。使用する菌体は培養菌体そのまま「ある
いは加熱処理した菌体のいずれでもよい。またトこの菌
体はpH5〜9も特に5〜7。0の緩衝溶液に分散もし
くは懸濁されていてもよい。この場合、菌体の濃度は通
常0。車〜50重量%、好ましくは0。5〜4の重量%
である。Examples of the glucose-isomerase-producing microbial cells used in the present invention include microbial cells of the genus Streptomyces, Bacillus, Arthrobacter, and Pseudomonas that produce glucose-isomerase. is obtained by culturing it in a medium containing cornstarch liquor alone or other nitrogen sources as a nitrogen source, carbohydrates such as starch and xylose as a carbon source, and potassium phosphate, cobalt chloride, and magnesium chloride as inorganic salts. The microbial cells used may be either cultured microbial cells as they are or heat-treated microbial cells.Furthermore, the microbial cells may be dispersed or suspended in a buffer solution with a pH of 5 to 9, particularly 5 to 7.0. In this case, the concentration of bacterial cells is usually 0.50% by weight, preferably 0.5-4% by weight.
It is.
本発明におけるキトサンはキトサン自体あるいはその溶
液もたとえば酢酸「蟻酸も塩酸等の酸およびこれらの酸
の酸性溶液に溶解して得られる溶液である。この溶液の
濃度は005〜2。増重量%も好ましくは0。1〜1の
重量%である。Chitosan in the present invention is a solution obtained by dissolving chitosan itself or its solution in an acid such as acetic acid, formic acid, hydrochloric acid, or an acidic solution of these acids.The concentration of this solution is 0.005 to 2.0%. Preferably it is 0.1-1% by weight.
本発明におけるキトサンでグルコースィソメラーゼ菌体
を凝集させて固定化グルコースィソメラーゼを製造する
方法はも具体的には菌体を含む液体にキトサンもしくは
その溶液を混合して凝集反応を行なう方法トキトサン溶
液に菌体を添加して混合して凝集反応を行なう方法など
がある。The method of producing immobilized glucose isomerase by agglutinating glucose isomerase cells with chitosan in the present invention is also a method in which chitosan or a solution thereof is mixed with a liquid containing cells to perform an agglutination reaction. There is a method in which bacterial cells are added to a tochitosan solution and mixed to perform an agglutination reaction.
固定化酵素製造の操業性から見てもキトサン溶液に菌体
を添加してよく損拝するかもあるいは猿練りして菌体を
上記キトサン溶液に分散させてから凝集反応を行なうこ
とが好ましい。凝集反応後の菌体は炉過または遠心分離
あるいは圧搾により、水分20〜50%に調節して造粒
機で造粒し、そのまま乾燥するかあるし、は整粒機にか
けて整形した後、乾燥する。From the viewpoint of operability in producing the immobilized enzyme, it is preferable to add the microbial cells to the chitosan solution and mix well or mix it with a monkey to disperse the microbial cells in the chitosan solution before carrying out the agglutination reaction. After the agglutination reaction, the bacterial cells are filtered, centrifuged, or compressed to have a moisture content of 20 to 50%, and then granulated using a granulator and dried as is, or after being shaped using a sizing machine and then dried. do.
本発明において使用する中性あるいはアルカリ性水溶液
中で難溶性であるリン酸塩とはpH6以上において溶解
度が100の9ノd‘以下のリン酸塩である、また本発
明におけるリン酸塩とはリン酸「 メタリン酸「ピロリ
ン酸、次リン酸、亜リン酸「メタ亜リン酸「ピロ亜リン
酸、次亜リン酸を含めた広い概念の酸の金属塩である。The phosphates that are sparingly soluble in neutral or alkaline aqueous solutions used in the present invention are those with a solubility of 9 nod' or less of 100 at pH 6 or higher; Acid "Metaphosphoric acid" is a metal salt of a broad concept of acids, including pyrophosphoric acid, hypophosphoric acid, phosphorous acid, and pyrophosphorous acid and hypophosphorous acid.
具体的にはIJン酸カルシウム、リン酸マグネシウム、
リン酸水素マグネシウムなどのリン酸塩、メタリン酸カ
ルシウム「メタリン酸マグネシウムなどのメタリン酸塩
、ピロリン酸カルシウム、ピロリン酸マグネシウムなど
のピロリン酸塩などが挙げられる。特に好ましくは、リ
ン酸水素マグネシウム「 メタリン酸カルシウム、ピロ
リン酸マグネシウムトピロリン酸カルシウムなどがある
。リン酸塩の添加量は異性化糖液のpH低下を抑制する
量が好ましくトリン酸塩の種類によって異なるがも通常
「原料菌体(乾物)に対して1〜2の重量%であること
が望ましい。Specifically, IJ calcium phosphate, magnesium phosphate,
Examples include phosphates such as magnesium hydrogen phosphate, calcium metaphosphate, metaphosphates such as magnesium metaphosphate, pyrophosphates such as calcium pyrophosphate, and magnesium pyrophosphate. Particularly preferred are magnesium hydrogen phosphate, calcium metaphosphate, Magnesium pyrophosphate, calcium topyrophosphate, etc.The amount of phosphate added is preferably an amount that suppresses the pH drop of the isomerized sugar solution, but it varies depending on the type of phosphate, but it is usually Preferably it is between 1 and 2% by weight.
本発明におけるリン酸塩の使用は任意の段階で行なう。The use of phosphate in the present invention is carried out at any stage.
たとえば菌体懸濁液にリン酸塩を添加した後もキトサン
溶液と混合して凝集反応を行なってもよいしも菌体懸濁
液にキトサン溶液を加えて凝集反応を行なう時にもリン
酸塩の分散液を独立に添加してもよい。またキトサンで
凝集した菌体を成型した後〜乾燥前にリン酸塩またはそ
の分散液と混合してもよい。本発明に用いるリン酸塩に
は中性あるいはアルカリ性水溶液中でもわずかに溶解す
るものがある。For example, even after adding phosphate to the bacterial cell suspension, it is possible to perform the agglutination reaction by mixing it with a chitosan solution, or when adding the chitosan solution to the bacterial cell suspension and performing the agglutination reaction, the phosphate may be added independently. Furthermore, after the microbial cells aggregated with chitosan are molded and before drying, they may be mixed with a phosphate or a dispersion thereof. Some of the phosphates used in the present invention are slightly soluble even in neutral or alkaline aqueous solutions.
このようなリン酸塩はその分散液のpHが中性附近より
外れる場合がある。したがって〜菌体懸濁液あるいはキ
トサン溶液の酸あるいはアルカリの添加量を加減して凝
集反応時のpHを6〜?をこ維持することが望ましい。
本発明によるリン酸塩を含有する固定化グルコースィソ
メラーゼは異性化反応時にリン酸塩が溶鱗しても反応系
のpH低下を防止する。The pH of the dispersion of such phosphates may deviate from around neutrality. Therefore, by adjusting the amount of acid or alkali added to the bacterial cell suspension or chitosan solution, the pH during the aggregation reaction can be adjusted to 6. It is desirable to maintain this.
The immobilized glucose isomerase containing phosphate according to the present invention prevents the pH of the reaction system from decreasing even if the phosphate is dissolved during the isomerization reaction.
したがって異性化糠液のpHが酵素の至適p凡安定pW
こ維持されることから「酵素の安定性〜反応性がきわめ
て良い。また〜固定化グルコースィソメラーゼ内に含有
されているリン酸塩が異性化反応時に生成される酸性物
質を直ちに反応して熔解しトその結果として固定化グル
コースィソメラーゼは多孔性になりもグルコースの拡散
抵抗が減少して反応性が増加する。さらに本発明ではキ
トサンでグルコースィソメラーゼ菌体を凝集させるので
、他のカチオン系凝集剤もたとえばポリビニルィミダゾ
リンあるいは腸性アクリルアミドなどで凝集させる場合
に比しても強度的にきわめて強く〜リン酸塩を含有して
もその圧損が非常に少ない。Therefore, the pH of the isomerized rice bran solution is the optimum pH for the enzyme, which is approximately stable pW.
This maintains the stability and reactivity of the enzyme.Also, the phosphate contained in the immobilized glucose isomerase immediately reacts with the acidic substances produced during the isomerization reaction. As a result of dissolution, the immobilized glucose isomerase becomes porous, but the diffusion resistance of glucose decreases and the reactivity increases.Furthermore, in the present invention, since glucose isomerase cells are aggregated with chitosan, other The cationic coagulant is also extremely strong compared to coagulation with polyvinyl imidazoline or enteric acrylamide, and has very little pressure loss even if it contains phosphate.
したがって、異性化反応時、グルコース溶液の流速が大
きいことは勿論、異性化反応開始時と操作経過後におい
ても、ほとんど流速に変化がみられない。以下、実施例
を用いて本発明を説明する。Therefore, during the isomerization reaction, not only is the flow rate of the glucose solution high, but also there is almost no change in the flow rate between the start of the isomerization reaction and the end of the operation. The present invention will be explained below using examples.
実施例中、単に%とあるのは重量%を示す。酵素蒲性は
国際グルコースィソメラーゼ単位を用い、グルコース溶
液(グルコース濃度2M、0.02MMgS04、0.
001MCoc12、PH6.85)で反応温度60q
0において1分間に1仏モルのグルコースを異性化する
酵素活性を1単位(IGmと略する)とした。In the examples, % simply indicates weight %. For enzyme preparation, the international glucose isomerase unit was used, and glucose solution (glucose concentration 2M, 0.02MMgS04, 0.00%
001MCoc12, PH6.85) and reaction temperature 60q
The enzyme activity that isomerizes 1 French mole of glucose per minute at 0 is defined as 1 unit (abbreviated as IGm).
なお、各測定項副ま下記の方法に従った。The following method was followed for each measurement item.
m 膨潤度
固定化グルコースィソメラーゼ1夕を水に懸濁し、沈降
せしめた時に水中で占める体積(叫)で表わす。m Swelling degree It is expressed as the volume (volume) occupied in water when fixed glucose isomerase is suspended in water and allowed to settle.
【2} 堅さ
粒状の固定化グルコースィソメラーゼを40W/W%ブ
ドウ糖液(pH8.5)で、室温で一夜放置した後ハ次
の方法に従って堅さを検査した。[2} Hardness After the granular immobilized glucose isomerase was left in a 40 W/W% glucose solution (pH 8.5) at room temperature overnight, the hardness was examined according to the following method.
すなわち人差し指と親指でつまみ、3人のパネルで感覚
的に堅さを判定した。工業的使用に耐える堅さは3.5
以上であると考える。In other words, the material was pinched between the index finger and thumb, and a panel of three people visually judged the firmness. Hardness to withstand industrial use is 3.5
I think that's all.
【3; 崩壊性活性測定時の1時間の鷹杵反応中におい
て固定化グルコースィソメラーゼが崩壊する程度を表わ
す。[3; Represents the degree of disintegration of immobilized glucose isomerase during a 1-hour Takapestle reaction when measuring disintegrating activity.
‘4} 沈降性
40W/W%のグルコース溶液中での沈降速度で表わし
た。'4} Sedimentation property It was expressed as the sedimentation rate in a 40W/W% glucose solution.
実施例 1
グルコースィソメラーゼ生産凍結菌体1.5k9(固形
分38%IGIU′夕)を60その水に懸濁し、10の
こ6等分した。Example 1 Glucose Isomerase Production Frozen bacterial cells 1.5k9 (solid content: 38% IGIU') were suspended in 60 liters of water and divided into 6 equal parts.
この懸濁液にリン酸水素マグネシウム、ピロリン酸マグ
ネシウム、リン酸マグネシウム、リン酸カルシウム、ピ
ロリン酸カルシウムを菌体(乾物)当り10%添加し、
次いでpHを7.0に調節した。予め調製した0.2%
キトサンの酢酸溶液(pH6.0)を上記菌体懸濁液に
よく損拝しながら添加し、凝集反応を行なわせた。凝集
した菌体を脱水してキトサン菌体凝集反応物を得た。こ
れを成型したのち70℃の熱風下で乾燥後、節別し30
〜40メッシュの固定化グルコースィソメラーゼを得た
。得られた固定化グルコースィソメラーゼの活性と堅さ
と膨?塵度を第1表に示す。To this suspension, magnesium hydrogen phosphate, magnesium pyrophosphate, magnesium phosphate, calcium phosphate, and calcium pyrophosphate were added at 10% per bacterial cell (dry matter),
The pH was then adjusted to 7.0. 0.2% prepared in advance
An acetic acid solution of chitosan (pH 6.0) was added to the above bacterial cell suspension while stirring carefully to cause an agglutination reaction. The aggregated bacterial cells were dehydrated to obtain a chitosan bacterial cell agglutination reaction product. After molding this and drying it under hot air at 70℃, it was separated for 30 minutes.
~40 mesh of immobilized glucose isomerase was obtained. Activity, firmness and swelling of the obtained immobilized glucose isomerase? The dust level is shown in Table 1.
第1表
これらの固定化グルコースィソメラーゼの異性化反応の
相違を調べるためにグルコースの異性化反応を行ない、
異性化率を測定した。Table 1 In order to investigate the differences in the isomerization reactions of these immobilized glucose isomerases, a glucose isomerization reaction was carried out.
The isomerization rate was measured.
異性化反応はグルコース溶液(グルコース50%、0.
009MMgS04、0.001MCoc12、pH7
.0)20の【に固定化グルコースィソメラーゼ(12
0101U)を加え、60qCで1岬時間反応を行なっ
た。The isomerization reaction was performed using a glucose solution (glucose 50%, 0.
009MMgS04, 0.001MCoc12, pH7
.. 0) Glucose isomerase immobilized on 20 [12
0101U) was added and the reaction was carried out at 60qC for 1 hour.
異性化反応終了後、酵素を回収し、再び同じ組成のグル
コース溶液を加えて異性化反応を繰り返した。フラクト
ース異性化率=グルコース+フラクトース×100反応
終了後、異性化率および異性化糖液のpHを第2表に示
す。After the isomerization reaction was completed, the enzyme was collected, and a glucose solution with the same composition was added again to repeat the isomerization reaction. Fructose isomerization rate=glucose+fructose×100 After the reaction, the isomerization rate and the pH of the high-fructose sugar solution are shown in Table 2.
第 2 表実施例 2
実施例1で得られた30〜40メッシュのリン酸水素マ
グネシウム含有固定化グルコースィソメラーゼ75夕を
カラムに充填し、50%のグルコース溶液を重力下に流
下させ、1時間毎に流速を調べた。Table 2 Example 2 The 30-40 mesh magnesium hydrogen phosphate-containing immobilized glucose isomerase obtained in Example 1 was packed into a column, and a 50% glucose solution was allowed to flow down under gravity. The flow rate was checked every hour.
その結果を第3表に示す。比較のため、同様にして他の
凝集剤、プリマフロツクC−7およびA−10で凝集さ
せ、かつリン酸水素マグネシウム含有した固定化グルコ
ースイン〆う−ゼの場合も第3表に示す。The results are shown in Table 3. For comparison, Table 3 also shows the case of immobilized glucose insulin which was similarly flocculated with other flocculants, Primafloc C-7 and A-10, and contained magnesium hydrogen phosphate.
第3表
第3表から明らかなようにキトサンで凝集させ、かつリ
ン酸水素マグネシウムを含有する固定化グルコースイソ
メラーゼによると「グルコース溶液の流速は全裸作時間
4独特間後もほとんど変化していない。As is clear from Table 3, according to the immobilized glucose isomerase aggregated with chitosan and containing magnesium hydrogen phosphate, the flow rate of the glucose solution remained almost unchanged even after 4 hours of total bare cropping.
実施例 3
実施例1で得た固定化グルコースィソメラーゼ10夕を
二重円筒カラム(2励磁0×18仇肌)に充填し、連続
異性化反応を行なった。Example 3 Ten volumes of the immobilized glucose isomerase obtained in Example 1 were packed into a double cylindrical column (2 excitations, 0 x 18 mm), and a continuous isomerization reaction was carried out.
その結果を第4表に示す。第 4 表
(夫1)異性化率45%を維持して流せるグ’レコース
溶液の最大流速The results are shown in Table 4. Table 4 (Husband 1) Maximum flow rate of glucose solution that can be flowed while maintaining an isomerization rate of 45%
Claims (1)
させて固定化グルコースイソメラーゼを製造する方法に
おいて、任意の段階で固定化グルコースイソメラーゼに
、中性あるいはアルカリ性水溶液中で難溶性のリン酸塩
を含有させることを特徴とする固定化グルコースイソメ
ラーゼの製造法。1. In the method of producing immobilized glucose isomerase by agglutinating glucose isomerase-producing bacterial cells with chitosan, it is possible to add phosphate, which is sparingly soluble in a neutral or alkaline aqueous solution, to the immobilized glucose isomerase at any stage. Characteristic method for producing immobilized glucose isomerase.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7035677A JPS609793B2 (en) | 1977-06-13 | 1977-06-13 | Method for producing immobilized glucose isomerase |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7035677A JPS609793B2 (en) | 1977-06-13 | 1977-06-13 | Method for producing immobilized glucose isomerase |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS545097A JPS545097A (en) | 1979-01-16 |
| JPS609793B2 true JPS609793B2 (en) | 1985-03-13 |
Family
ID=13429061
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7035677A Expired JPS609793B2 (en) | 1977-06-13 | 1977-06-13 | Method for producing immobilized glucose isomerase |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS609793B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS53155073U (en) * | 1977-05-10 | 1978-12-06 | ||
| JPS62287516A (en) * | 1986-06-04 | 1987-12-14 | 日立電線株式会社 | Coaxial core parallel type flat cable |
| JP6088148B2 (en) * | 2012-03-08 | 2017-03-01 | 三菱電線工業株式会社 | Aggregated conductor and method of manufacturing the same |
-
1977
- 1977-06-13 JP JP7035677A patent/JPS609793B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS545097A (en) | 1979-01-16 |
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