JP2657886B2 - Immobilized enzyme and transesterification method using the same - Google Patents
Immobilized enzyme and transesterification method using the sameInfo
- Publication number
- JP2657886B2 JP2657886B2 JP5121650A JP12165093A JP2657886B2 JP 2657886 B2 JP2657886 B2 JP 2657886B2 JP 5121650 A JP5121650 A JP 5121650A JP 12165093 A JP12165093 A JP 12165093A JP 2657886 B2 JP2657886 B2 JP 2657886B2
- Authority
- JP
- Japan
- Prior art keywords
- enzyme
- immobilized enzyme
- group
- immobilized
- resin
- 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
Links
- 108010093096 Immobilized Enzymes Proteins 0.000 title claims description 31
- 238000005809 transesterification reaction Methods 0.000 title claims description 20
- 238000000034 method Methods 0.000 title claims description 16
- 239000003921 oil Substances 0.000 claims description 24
- 235000019198 oils Nutrition 0.000 claims description 24
- 239000011347 resin Substances 0.000 claims description 24
- 229920005989 resin Polymers 0.000 claims description 24
- 108090001060 Lipase Proteins 0.000 claims description 22
- 102000004882 Lipase Human genes 0.000 claims description 22
- 239000004367 Lipase Substances 0.000 claims description 22
- 235000019421 lipase Nutrition 0.000 claims description 22
- 108090000790 Enzymes Proteins 0.000 claims description 20
- 102000004190 Enzymes Human genes 0.000 claims description 20
- 239000003925 fat Substances 0.000 claims description 19
- 235000019482 Palm oil Nutrition 0.000 claims description 15
- 239000002540 palm oil Substances 0.000 claims description 15
- 125000000524 functional group Chemical group 0.000 claims description 14
- 238000005349 anion exchange Methods 0.000 claims description 11
- 239000007864 aqueous solution Substances 0.000 claims description 6
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 6
- 125000003700 epoxy group Chemical group 0.000 claims description 6
- 239000000194 fatty acid Substances 0.000 claims description 6
- 229930195729 fatty acid Natural products 0.000 claims description 6
- 150000004665 fatty acids Chemical class 0.000 claims description 5
- 125000001302 tertiary amino group Chemical group 0.000 claims description 5
- 230000000694 effects Effects 0.000 description 12
- 238000006243 chemical reaction Methods 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 239000000126 substance Substances 0.000 description 6
- 239000007788 liquid Substances 0.000 description 5
- 239000000203 mixture Substances 0.000 description 4
- 239000011148 porous material Substances 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 235000019197 fats Nutrition 0.000 description 3
- -1 fatty acid esters Chemical class 0.000 description 3
- 230000002209 hydrophobic effect Effects 0.000 description 3
- 230000003100 immobilizing effect Effects 0.000 description 3
- BFSVOASYOCHEOV-UHFFFAOYSA-N 2-diethylaminoethanol Chemical group CCN(CC)CCO BFSVOASYOCHEOV-UHFFFAOYSA-N 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 2
- CERQOIWHTDAKMF-UHFFFAOYSA-M Methacrylate Chemical compound CC(=C)C([O-])=O CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 description 2
- 241000235395 Mucor Species 0.000 description 2
- 235000019484 Rapeseed oil Nutrition 0.000 description 2
- 241000235527 Rhizopus Species 0.000 description 2
- 125000003172 aldehyde group Chemical group 0.000 description 2
- 239000003957 anion exchange resin Substances 0.000 description 2
- 239000007853 buffer solution Substances 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- MYRTYDVEIRVNKP-UHFFFAOYSA-N divinylbenzene Substances C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 150000004676 glycans Chemical class 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 2
- 239000008363 phosphate buffer Substances 0.000 description 2
- 229920001282 polysaccharide Polymers 0.000 description 2
- 239000005017 polysaccharide Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 125000000467 secondary amino group Chemical group [H]N([*:1])[*:2] 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- QKNYBSVHEMOAJP-UHFFFAOYSA-N 2-amino-2-(hydroxymethyl)propane-1,3-diol;hydron;chloride Chemical compound Cl.OCC(N)(CO)CO QKNYBSVHEMOAJP-UHFFFAOYSA-N 0.000 description 1
- TWJNQYPJQDRXPH-UHFFFAOYSA-N 2-cyanobenzohydrazide Chemical compound NNC(=O)C1=CC=CC=C1C#N TWJNQYPJQDRXPH-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 1
- 241000251468 Actinopterygii Species 0.000 description 1
- 241000588986 Alcaligenes Species 0.000 description 1
- 241000228212 Aspergillus Species 0.000 description 1
- 241000222120 Candida <Saccharomycetales> Species 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229920001661 Chitosan Polymers 0.000 description 1
- 241000588881 Chromobacterium Species 0.000 description 1
- 241000146387 Chromobacterium viscosum Species 0.000 description 1
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical group N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- SXRSQZLOMIGNAQ-UHFFFAOYSA-N Glutaraldehyde Chemical compound O=CCCCC=O SXRSQZLOMIGNAQ-UHFFFAOYSA-N 0.000 description 1
- 108010048733 Lipozyme Proteins 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- 235000021360 Myristic acid Nutrition 0.000 description 1
- TUNFSRHWOTWDNC-UHFFFAOYSA-N Myristic acid Natural products CCCCCCCCCCCCCC(O)=O TUNFSRHWOTWDNC-UHFFFAOYSA-N 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 241000228143 Penicillium Species 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 241000589516 Pseudomonas Species 0.000 description 1
- 241000952054 Rhizopus sp. Species 0.000 description 1
- 229920002125 Sokalan® Polymers 0.000 description 1
- 239000004164 Wax ester Substances 0.000 description 1
- 239000008351 acetate buffer Substances 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 239000010775 animal oil Substances 0.000 description 1
- 210000000988 bone and bone Anatomy 0.000 description 1
- 239000000872 buffer Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000003729 cation exchange resin Substances 0.000 description 1
- 239000013522 chelant Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 125000002147 dimethylamino group Chemical group [H]C([H])([H])N(*)C([H])([H])[H] 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000002255 enzymatic effect Effects 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 235000019688 fish Nutrition 0.000 description 1
- VOZRXNHHFUQHIL-UHFFFAOYSA-N glycidyl methacrylate Chemical compound CC(=C)C(=O)OCC1CO1 VOZRXNHHFUQHIL-UHFFFAOYSA-N 0.000 description 1
- 239000012051 hydrophobic carrier Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 235000019626 lipase activity Nutrition 0.000 description 1
- FCCDDURTIIUXBY-UHFFFAOYSA-N lipoamide Chemical compound NC(=O)CCCCC1CCSS1 FCCDDURTIIUXBY-UHFFFAOYSA-N 0.000 description 1
- 230000002366 lipolytic effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 125000000962 organic group Chemical group 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 125000004430 oxygen atom Chemical group O* 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 125000002924 primary amino group Chemical class [H]N([H])* 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 235000015170 shellfish Nutrition 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 150000003431 steroids Chemical class 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 125000004306 triazinyl group Chemical group 0.000 description 1
- 125000005457 triglyceride group Chemical group 0.000 description 1
- PHYFQTYBJUILEZ-IUPFWZBJSA-N triolein Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OCC(OC(=O)CCCCCCC\C=C/CCCCCCCC)COC(=O)CCCCCCC\C=C/CCCCCCCC PHYFQTYBJUILEZ-IUPFWZBJSA-N 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- 235000019386 wax ester Nutrition 0.000 description 1
Landscapes
- Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Description
【0001】[0001]
【技術分野】本発明は、特に油脂のエステル交換に適し
た固定化酵素、及びこれを用いるパーム油を含む油脂類
のエステル交換法に関する。TECHNICAL FIELD The present invention relates to an immobilized enzyme particularly suitable for transesterification of fats and oils, and a method for transesterifying fats and oils including palm oil using the same.
【0002】[0002]
【従来技術】エステル交換反応は、ワックスエステル、
各種脂肪酸エステル、糖エステルやステロイド等の製造
法、あるいは植物油、動物油の改質法として重要な技術
である。このエステル交換反応の触媒として、脂質分解
酵素の一種であるリパーゼを用いると温和な条件下でエ
ステル交換反応を行うことが可能となり、また、その基
質特異性や位置特異性により目的物を効率よく生産する
ことができる。又、系内の水分をできる限り少なくし、
かつ酵素の活性が発現するに充分な量のリパーゼを存在
させてエステル交換反応を行うことが提案されている。
ところが、リパーゼは水溶性であり、微水系(油系)で
は均一に分散することが困難である。このような問題を
解決するためにリパーゼを不溶性担体に担持させた固定
化リパーゼが用いられている。そして、固定化リパーゼ
を採用することによって、さらに、生産物の分離が容易
となり、リパーゼの繰り返し利用が可能となり、反応系
の連続化が容易になるなどの利点が得られている。2. Description of the Related Art Transesterification reactions include wax esters,
This is an important technique as a method for producing various fatty acid esters, sugar esters, steroids, etc., or a method for modifying vegetable oils and animal oils. When lipase, a kind of lipolytic enzyme, is used as a catalyst for this transesterification reaction, transesterification can be performed under mild conditions, and the target product can be efficiently produced by its substrate specificity and positional specificity. Can be produced. Also, make the water in the system as small as possible,
In addition, it has been proposed to carry out a transesterification reaction in the presence of a lipase in an amount sufficient to express the activity of the enzyme.
However, lipase is water-soluble, and it is difficult to uniformly disperse it in a slightly water-based (oil-based) system. In order to solve such a problem, an immobilized lipase in which a lipase is carried on an insoluble carrier has been used. The use of the immobilized lipase has further obtained advantages such as easy separation of the product, repeated use of the lipase, and continuity of the reaction system.
【0003】しかし、このような利点を有しているにも
係わらず、実用化に耐えうる固定化リパーゼは得られて
いない。固定化リパーゼの調製方法としては、多孔性の
キトサン成型物(特開昭59−213390)、マクロ
ポーラス型陰イオン交換樹脂(特開昭60−9898
4)、マクロポーラス型フェノール系吸着樹脂(特開昭
61−20268)、獣骨(特開昭64−8028
6)、発泡性フェノール樹脂の焼成物(特開平2−10
0678)、50nm以上の細孔径を持つ疎水性担体
(特開平2−138986)、陽イオン交換樹脂(特開
平3−64185)、マクロポーラス型アクリル系吸着
樹脂(特開平3−501922)を担体として用いるも
のが提案されている。しかしながら、これらの担体を使
用したのでは、十分なリパーゼ活性が得られない。又、
特開昭60−137290では多糖類の水酸基を酸化し
たアルデヒド基を用いて酵素を多糖類担体に固定化する
方法が示されている。しかし、担体が親水性のため微水
系での反応には適していない。また、特開平1−262
795にはキレート樹脂に酵素を固定化する方法が示さ
れているが、実用に耐える活性を得るには至っていな
い。[0003] However, despite having such advantages, an immobilized lipase that can withstand practical use has not been obtained. The method for preparing the immobilized lipase includes a porous chitosan molded product (JP-A-59-213390) and a macroporous anion exchange resin (JP-A-60-9898).
4), macroporous phenolic adsorption resin (JP-A-61-20268), animal bone (JP-A-64-8028)
6), a fired product of a foamable phenol resin (Japanese Patent Laid-Open No.
0678), a hydrophobic carrier having a pore diameter of 50 nm or more (JP-A-2-138986), a cation exchange resin (JP-A-3-64185), and a macroporous acrylic adsorption resin (JP-A-3-501922). Use has been proposed. However, when these carriers are used, sufficient lipase activity cannot be obtained. or,
JP-A-60-137290 discloses a method of immobilizing an enzyme on a polysaccharide carrier using an aldehyde group obtained by oxidizing a hydroxyl group of a polysaccharide. However, since the carrier is hydrophilic, it is not suitable for a reaction in a fine water system. Also, Japanese Patent Application Laid-Open No. 1-262
No. 795 discloses a method of immobilizing an enzyme on a chelate resin, but does not achieve a practically usable activity.
【0004】[0004]
【発明が解決しようとする課題】本発明は、担体に固定
化したリパーゼであって、これらの酵素活性の発現に優
れ、微水系でエステル交換反応を行うのに特に適してお
り、かつ寿命が長い固定化酵素を提供することを目的と
する。本発明は、また、該固定化リパーゼを用いるパー
ム油を含む油脂類のエステル交換法を提供することを目
的とする。DISCLOSURE OF THE INVENTION The present invention relates to a lipase immobilized on a carrier, which is excellent in the expression of these enzymatic activities, is particularly suitable for performing transesterification in a microaqueous system, and has a long life. It is intended to provide a long immobilized enzyme. Another object of the present invention is to provide a method for transesterifying fats and oils including palm oil using the immobilized lipase.
【0005】[0005]
【課題を解決するための手段】本発明は、疎水性の母材
でかつその表面に酵素と水溶液中で共有結合を形成する
官能基と陰イオン交換基とを併せ持つ、マクロポーラス
型の樹脂で形成された特定の担体に、目的酵素を固定化
することにより、高活性で寿命の長い固定化酵素を得る
ことができるとの知見に基づいてなされたのである。す
なわち、本発明は、酵素と水溶液中で共有結合を形成す
る官能基と弱塩基性陰イオン交換基とを有する樹脂担体
にリパーゼを固定化したことを特徴とする固定化酵素を
提供する。本発明は、また、パーム油を含む油脂および
脂肪酸、あるいはパーム油を含む2種以上の油脂を上記
固定化酵素の存在下でエステル交換することを特徴とす
るエステル交換法を提供する。SUMMARY OF THE INVENTION The present invention is directed to a macroporous resin which is a hydrophobic base material and has on its surface both a functional group capable of forming a covalent bond with an enzyme in an aqueous solution and an anion exchange group. It has been made based on the finding that by immobilizing the target enzyme on the formed specific carrier, an immobilized enzyme having high activity and long life can be obtained. That is, the present invention provides an immobilized enzyme, wherein lipase is immobilized on a resin carrier having a functional group capable of forming a covalent bond with an enzyme in an aqueous solution and a weakly basic anion exchange group. The present invention also provides a transesterification method comprising transesterifying fats and oils and fatty acids containing palm oil, or two or more fats and oils containing palm oil in the presence of the immobilized enzyme.
【0006】本発明において、担体を形成する不溶性有
機高分子としては、ジビニルベンゼン(DVB)系共重
合体、メタクリル酸エステル、アクリル酸エステル、ポ
リプロピレン、ナイロン、フェノールなどを母材とする
ものが用いられるが、特にジビニルベンゼン系共重合体
が好ましく用いられる。また、樹脂の細孔径は5nm〜
1000nm、好ましくは10nm〜1000nmのも
のが適当である。上記樹脂が有する、酵素と水溶液中で
共有結合を形成する官能基としては、エポキシ基、シア
ニド基、アルデヒド基、トリアジニル基などがあげられ
る。このうち、エポキシ基が好ましく、特に隣り合った
炭素に酸素原子が付加した1,2エポキシ基が好まし
い。又、上記樹脂が有する陰イオン交換基としては、1
級アミノ基、2級アミノ基、3級アミノ基などがあげら
れるが、弱塩基性の3級アミノ基であるジエチルアミノ
エチル基(DEAE基)やジメチルアミノ基が好まし
い。In the present invention, as the insoluble organic polymer forming the carrier, those based on divinylbenzene (DVB) copolymer, methacrylate, acrylate, polypropylene, nylon, phenol or the like are used. In particular, a divinylbenzene copolymer is preferably used. Further, the pore diameter of the resin is from 5 nm to
Thicknesses of 1000 nm, preferably 10 nm to 1000 nm are suitable. Examples of the functional group of the resin that forms a covalent bond with an enzyme in an aqueous solution include an epoxy group, a cyanide group, an aldehyde group, and a triazinyl group. Of these, an epoxy group is preferable, and a 1,2 epoxy group in which an oxygen atom is added to adjacent carbon is particularly preferable. Further, as the anion exchange group possessed by the resin, 1
Examples include a tertiary amino group, a secondary amino group, and a tertiary amino group, and a weakly basic tertiary amino group such as a diethylaminoethyl group (DEAE group) and a dimethylamino group are preferable.
【0007】本発明においては、樹脂担体中の上記官能
基及び陰イオン交換基の割合は任意とすることができる
が、共重合する共有結合を形成する官能基を0.2〜5.0
mol/Kg含有するのが好ましく、特に好ましくは0.5〜2.
0mol/Kgである。また陰イオン交換基を0.2〜5.0mol/
Kg含有するのが好ましく、特に好ましくは0.5〜2.0mo
l/Kgである。これら官能基や陰イオン交換基は常法によ
り上記樹脂に導入することができる。例えば、これらの
官能基や陰イオン交換基を有するモノマーを上記樹脂の
重合時に共存させて共重合させて導入すること、上記の
樹脂やこれを前処理して反応性の官能基を生成させたも
のに、エステル結合等の一般の化学結合法で導入するこ
となどがあげられる。このような方法により上記特定の
官能基と陰イオン交換基とを導入した樹脂は、例えば、
バイエル社のレバチットR260Kが入手でき、また後
述する参考例/あるいは実施例3のように調製してもよ
い。尚、レバチットR260Kは、エポキシ基と2級ア
ミノ基を有するが、エポキシ基と3級アミノ基を有する
参考例1に記載のものが一層好ましい担体樹脂である。In the present invention, the ratio of the above-mentioned functional group and anion exchange group in the resin carrier can be arbitrarily set, but the functional group forming a covalent bond to be copolymerized is 0.2 to 5.0.
mol / Kg, preferably 0.5 to 2.
It is 0 mol / Kg. In addition, 0.2 to 5.0 mol /
Kg is preferably contained, particularly preferably 0.5 to 2.0mo.
l / Kg. These functional groups and anion exchange groups can be introduced into the resin by a conventional method. For example, monomers having these functional groups or anion exchange groups were introduced by co-existing and copolymerizing during the polymerization of the resin, and the above-mentioned resin or a pre-treatment of the resin to form a reactive functional group. For example, it can be introduced by a general chemical bonding method such as an ester bond. The resin into which the specific functional group and the anion exchange group are introduced by such a method, for example,
Bayer's Levatit R260K is available and may be prepared as in Reference Example / or Example 3 below. In addition, Levatit R260K has an epoxy group and a secondary amino group, but the one described in Reference Example 1 having an epoxy group and a tertiary amino group is a more preferable carrier resin.
【0008】本発明では、担体として任意の粒径のもの
を使用することができるが、一般に担体の粒子径の90
%以上が50〜1,000μmのものを使用するのが好ま
しいが、特に平均粒径が300〜600μmのものを使
用するのが好ましい。上記担体に固定されるリパーゼと
しては、ムコール属、リゾプス属、アスペルギルス属、
アルカリゲネス属、ジオトリクム属、キャンディダ属、
シュードモナス属、ペニシリウム属、クロモバクテリウ
ム属等の微生物由来のリパーゼがあげられる。このう
ち、特に、ムコール属やリゾプス属のリパーゼを用いる
のが好ましい。In the present invention, a carrier having an arbitrary particle size can be used.
% Or more is preferably used in a range of 50 to 1,000 μm, and particularly preferably one having an average particle size of 300 to 600 μm. As the lipase immobilized on the carrier, Mucor, Rhizopus, Aspergillus,
Alcaligenes, Geotricum, Candida,
Lipases derived from microorganisms such as Pseudomonas, Penicillium, Chromobacterium and the like can be mentioned. Among them, it is particularly preferable to use a lipase of the genus Mucor or Rhizopus.
【0009】本発明の固定化酵素は、例えば、多孔質の
不溶性担体である樹脂に酵素液を接触させることにより
担体にリパーゼを担持させて製造することができる。こ
こで、酵素液としては用いるリパーゼによって決まる
が、例えば、酵素を0.05〜10重量%含む水溶液を担
体(乾燥重量)1重量部当たり1〜200重量部使用す
るのが好ましい。この際緩やかに撹拌することが好まし
い。固定化に要する時間は10分から40時間で、好ま
しくは1時間から24時間である。固定化時の温度は4
℃から50℃、好ましくは5℃から25℃である。ま
た、必要に応じて酵素液を緩衝液で調製することもでき
る。この場合、調整pHは酵素の至適pH付近が好まし
く、遊離酵素の状態で測定した加水分解活性の至適p
H、例えばpH5〜9に調整するのが好ましい。緩衝液
の種類は特に規定されないが、酢酸緩衝液、リン酸緩衝
液を用いることができる。酵素を担持した担体は濾過等
により残液を除き、必要に応じてイオン交換水等で洗浄
する。この際、洗浄液にトリス塩酸緩衝液等のアミノ基
を有する物質を含んだ水溶液を用いることにより、担体
に残存する、未反応の共有結合を形成する官能基をブロ
ックすることも可能である。除液した固定化酵素は減圧
乾燥法等により乾燥するのが好ましく、乾燥後の水分が
0.5重量%〜30重量%、好ましくは5重量%〜10重
量%となるようにするのがよい。乾燥後の水分が0.5重
量%未満の場合、十分にエステル交換活性が発現され
ず、また30重量%を超える場合、失活の原因になると
ともに副反応である加水分解が無視できなくなる。固定
化操作において使用する担体と酵素の割合は、担体1g
(乾燥重量)に対し、酵素中のタンパク質が0.1gから
10g、好ましくは0.2gから5gであるが、特にこれ
に限定されるものではない。[0009] The immobilized enzyme of the present invention can be produced, for example, by bringing a resin, which is a porous insoluble carrier, into contact with an enzyme solution to allow the carrier to carry lipase. Here, the enzyme solution is determined by the lipase to be used. For example, it is preferable to use 1 to 200 parts by weight of an aqueous solution containing 0.05 to 10% by weight of the enzyme per 1 part by weight of the carrier (dry weight). At this time, it is preferable to stir gently. The time required for immobilization is from 10 minutes to 40 hours, preferably from 1 hour to 24 hours. Temperature at the time of immobilization is 4
C. to 50.degree. C., preferably 5 to 25.degree. Further, if necessary, the enzyme solution can be prepared with a buffer solution. In this case, the adjusted pH is preferably around the optimum pH of the enzyme, and the optimum pH of the hydrolysis activity measured in the state of the free enzyme is adjusted.
It is preferable to adjust H, for example, to pH 5 to 9. The type of the buffer is not particularly limited, but an acetate buffer or a phosphate buffer can be used. The carrier carrying the enzyme is removed of residual liquid by filtration or the like, and washed with ion-exchanged water or the like as necessary. At this time, by using an aqueous solution containing a substance having an amino group such as a Tris-HCl buffer solution as the washing solution, it is possible to block the functional groups that form unreacted covalent bonds remaining on the carrier. It is preferable to dry the removed immobilized enzyme by a vacuum drying method or the like.
The content should be 0.5% to 30% by weight, preferably 5% to 10% by weight. When the water content after drying is less than 0.5% by weight, transesterification activity is not sufficiently exhibited, and when it exceeds 30% by weight, it causes deactivation and hydrolysis as a side reaction cannot be ignored. The ratio of the carrier and the enzyme used in the immobilization operation is 1 g of the carrier.
The protein in the enzyme is from 0.1 g to 10 g, preferably from 0.2 g to 5 g, based on (dry weight), but is not particularly limited to this.
【0010】本発明の固定化酵素を用いて、パーム油を
含む油脂のエステル交換を効率的に行うことができる。
特に、反応系中の水分含有量を50〜2000ppm、
好ましくは100〜1000ppmに低下させた微水系
でエステル交換反応を行うのに適している。本発明にお
いて、好適なエステル交換反応としては、温度30〜7
0℃であり、必要に応じて有機溶媒を用いることもでき
る。用いる有機溶媒としては固定化酵素の活性を低下さ
せないものが選ばれ、例えばn−ヘキサンや石油エーテ
ルがあげられる。又、対象となる油脂類としては、パー
ム油を含む油脂および脂肪酸、またはパーム油を含む2
種以上の油脂であり、エステル交換反応の原料として少
なくとも1種以上がパーム油を含む油脂であることを必
須とする。ここでパーム油を含む油脂としてはパーム
油、その分別油、水添油等の加工油脂等のほか、これを
混合した各種油脂を例示できる。一方、かかるパーム油
を含む油脂と組み合わせる原料としては植物由来の油脂
および脂肪酸が好適であるが、この他に動物油脂、魚貝
類油脂およびそれらの脂肪酸を対象とすることもでき
る。By using the immobilized enzyme of the present invention, transesterification of fats and oils including palm oil can be efficiently performed.
In particular, the water content in the reaction system is 50 to 2000 ppm,
It is suitable for carrying out the transesterification reaction in a slightly water system preferably reduced to 100 to 1000 ppm. In the present invention, a suitable transesterification reaction includes a temperature of 30 to 7
The temperature is 0 ° C., and an organic solvent can be used if necessary. The organic solvent to be used is selected from those which do not decrease the activity of the immobilized enzyme, and examples thereof include n-hexane and petroleum ether. The target fats and oils are fats and oils containing palm oil and fatty acids, or 2
It is essential that at least one or more kinds of fats and oils contain palm oil as raw materials for the transesterification reaction. Here, examples of fats and oils containing palm oil include palm oil, fractionated oil thereof, processed fats and oils such as hydrogenated oil and the like, and various fats and oils obtained by mixing them. On the other hand, as a raw material to be combined with such fats and oils containing palm oil, plant-derived fats and oils and fatty acids are suitable, but in addition, animal fats and oils, fish and shellfish fats and fatty acids can also be used.
【0011】[0011]
【発明の効果】本発明によれば、物理的強度と化学的強
度に優れ、高活性でかつ担持された酵素の活性発現状態
が安定で寿命の長い固定化酵素を提供することができ
る。従って、本発明の固定化酵素は工業的に極めて重要
である。またこれを用いて、パーム油を含む油脂類のエ
ステル交換反応を効率的に行なわしめることができる。
次に実施例により本発明を説明する。According to the present invention, it is possible to provide an immobilized enzyme which has excellent physical strength and chemical strength, is highly active, has a stable activity expression state of the carried enzyme, and has a long life. Therefore, the immobilized enzyme of the present invention is extremely important industrially. In addition, the transesterification of fats and oils including palm oil can be efficiently carried out by using this.
Next, the present invention will be described with reference to examples.
【0012】[0012]
参考例1 ジビニルベンゼン(DVB)70%とメタクリル酸グリ
シジル15%とDEAEメタクレート15%を通常の方
法で共重合し、樹脂担体を得た。この樹脂担体の平均細
孔径は12.3nmで細孔容積は0.5cm3 /gであった。 実施例1 参考例1で得た樹脂担体100gにRhizopus sp.由来の
リパーゼFAP−15(天野製薬(株)製150,000
u/g)の2%水溶液1000mlを加え、4時間25℃
で攪拌しながら固定化を行った。濾過、洗浄後真空乾燥
器で3時間乾燥した。得られた固定化酵素は50gで水
分は5%であった。 実施例2 実施例1でリパーゼをChromobacterium Viscosum由来の
リパーゼLP(東洋醸造(株)製100,000u/
g)、Pseudomonus sp. 由来のリパーゼCES(天野製
薬(株)製20,000u/g)に替えて固定化酵素を調
製し、そのエステル交換活性を測定した。Reference Example 1 70% of divinylbenzene (DVB), 15% of glycidyl methacrylate and 15% of DEAE methacrylate were copolymerized by a usual method to obtain a resin carrier. This resin carrier had an average pore diameter of 12.3 nm and a pore volume of 0.5 cm 3 / g. Example 1 Lipase FAP-15 derived from Rhizopus sp. (150,000, manufactured by Amano Pharmaceutical Co., Ltd.) was added to 100 g of the resin carrier obtained in Reference Example 1.
u / g) at 1000C for 4 hours.
The mixture was immobilized while stirring. After filtration and washing, it was dried in a vacuum dryer for 3 hours. The obtained immobilized enzyme was 50 g and the water content was 5%. Example 2 In Example 1, the lipase was replaced with lipase LP derived from Chromobacterium Viscosum (100,000 u / Toyo Brewing Co., Ltd.).
g), an immobilized enzyme was prepared in place of Pseudomonus sp.-derived lipase CES (20,000 u / g, manufactured by Amano Pharmaceutical Co., Ltd.), and its transesterification activity was measured.
【0013】実施例3 予め、メタクリル酸を母材とし1級アミンを含む多孔性
樹脂であるFE4612(オルガノ社製)100gに1
重量%グルタルアルデヒド(0.05Mリン酸緩衝液中)
200mlを加え、室温で1時間緩やかに攪拌し、水洗し
た後ろ過により水をきった樹脂担体を用いた以外は実施
例1と同様にして固定化酵素を調製した。 比較例1 参考例1で担体を官能基として共有結合基も陰イオン交
換基もない疎水性の樹脂であるDuolite S861を用い実施
例1と同様に調整した。 比較例2 固定化酵素として市販されている陰イオン交換樹脂を担
体としたリポザイム(ノボ・ノルディスク・バイオイン
ダストリー社製)を使用した。 比較例3 参考例1で担体を官能基として陰イオン交換基がない疎
水性の樹脂であるLewatit R259K を用い実施例1と同様
に調製した。Example 3 One hundred grams of FE4612 (manufactured by Organo), which is a porous resin containing methacrylic acid as a base material and containing a primary amine, was previously added to 100 g.
Wt% glutaraldehyde (in 0.05M phosphate buffer)
200 ml was added, and the mixture was gently stirred at room temperature for 1 hour, washed with water, and then filtered to remove water, to thereby prepare an immobilized enzyme in the same manner as in Example 1. Comparative Example 1 Preparation was performed in the same manner as in Example 1 using Duolite S861, which is a hydrophobic resin having a carrier as a functional group and having neither a covalent bond group nor an anion exchange group. Comparative Example 2 Lipozyme (manufactured by Novo Nordisk Bioindustry) using a commercially available anion exchange resin as a carrier was used as the immobilized enzyme. Comparative Example 3 The procedure of Example 1 was repeated, except that Lewatit R259K, a hydrophobic resin having a functional group as a carrier and no anion exchange group, was used.
【0014】実施例4 上記実施例及び比較例で得られた固定化酵素のエステル
交換活性と寿命を次のようにして測定した。固定化酵素のエステル交換活性 エステル交換活性は50℃でのパームオレインへのミリ
スチン酸の取り込み速度(μmol/min/g 固定化酵素)で
測定し、固定化酵素の単位容量に換算した(単位:unit
/ml 固定化酵素)。固定化酵素の寿命 固定化酵素をカラムに詰め、パーム油とナタネ油の混合
物をSV(空間速度)=1(リットル/リットルカラム
・hr)で流し、構成脂肪酸の炭素数の合計が50および
52のトリグリセリドの組成の変化から反応率を出し、
70%の反応率を維持できる間の通油可能量を固定化酵
素の寿命とした。結果を表−1に示す。Example 4 The transesterification activity and life of the immobilized enzymes obtained in the above Examples and Comparative Examples were measured as follows. Transesterification activity of immobilized enzyme The transesterification activity was measured by the rate of incorporation of myristic acid into palm olein at 50 ° C. (μmol / min / g immobilized enzyme) and was converted to the unit volume of immobilized enzyme (unit: unit
/ ml immobilized enzyme). Lifetime of immobilized enzyme The immobilized enzyme was packed in a column, and a mixture of palm oil and rapeseed oil was allowed to flow at SV (space velocity) = 1 (liter / liter column · hr). From the change in the composition of the triglyceride of the reaction rate,
The amount of oil that can pass while maintaining a reaction rate of 70% was defined as the life of the immobilized enzyme. The results are shown in Table 1.
【0015】[0015]
【表1】 表−1 固定化 エステル交換活性 寿命 酵素の例 (unit/ml固定化酵素) (1原料油/1固定化酵素) 実施例1 93 1000 実施例2 68 800 65 800 実施例3 90 900 比較例1 85 400 比較例2 48 250比較例3 83 500 [Table 1] Table-1 Example of immobilized transesterification activity long-lived enzyme (unit / ml immobilized enzyme) (1 feed oil / 1 immobilized enzyme) Example 1 93 1000 Example 2 68 800 65 800 Example 3 90 900 Comparative Example 1 85 400 Comparison Example 2 48 250 Comparative Example 3 83 500
【0016】実施例5 実施例1で得た固定化酵素を容量100mlのカラムにつ
め、パーム油:ナタネ油=1:1の混合油を50℃にて
SV=1で流した。750時間後に約1Kgをサンプリン
グし、反応率を測定した。また、このエステル交換油脂
を5℃にてウインタリングし、得られた液体部の収率を
測定した。 比較例4 比較例3で得た固定化酵素を容量100mlのカラムにつ
め、実施例5と同様に反応、サンプリングを行い反応率
およびウインタリング時の液体部の収率を測定した。上
記実施例5および比較例4で得られた反応率ならびにウ
インタリング時の液体部収率を表−2に示した。Example 5 The immobilized enzyme obtained in Example 1 was packed in a column having a capacity of 100 ml, and a mixed oil of palm oil: rapeseed oil = 1: 1 was flowed at 50 ° C. and SV = 1. After 750 hours, about 1 kg was sampled and the reaction rate was measured. Further, this transesterified fat was wintered at 5 ° C., and the yield of the obtained liquid part was measured. Comparative Example 4 The immobilized enzyme obtained in Comparative Example 3 was packed in a column having a capacity of 100 ml, and the reaction and sampling were performed in the same manner as in Example 5 to measure the reaction rate and the yield of the liquid part during wintering. Table 2 shows the reaction rates obtained in Example 5 and Comparative Example 4 and the yield of the liquid part during wintering.
【0017】[0017]
【表2】 表−2 ────────────────────────────────── 反応率 ウインタリング時液体部収率 (%) (%) ────────────────────────────────── 実施例5 80 71 比較例4 23 46 ──────────────────────────────────Table 2 ────────────────────────────────── Reaction rate Liquid part yield at wintering (%) (%) 例 Example 5 80 71 Comparative Example 4 23 46 ──────────────────────────────────
───────────────────────────────────────────────────── フロントページの続き (72)発明者 安藤 登 神奈川県横浜市神奈川区守屋町3丁目13 番地 千代田化工建設株式会社 千代田 リサーチパーク内 (72)発明者 浅岡 佐知夫 神奈川県横浜市神奈川区守屋町3丁目13 番地 千代田化工建設株式会社 千代田 リサーチパーク内 (72)発明者 小林 治人 神奈川県横浜市神奈川区守屋町3丁目13 番地 千代田化工建設株式会社 千代田 リサーチパーク内 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Noboru Ando 3--13 Moriyacho, Kanagawa-ku, Yokohama-shi, Kanagawa Prefecture Chiyoda Chemical Construction Co., Ltd. Chiyoda Research Park (72) Inventor Sachio Asaoka Moriyacho, Kanagawa-ku, Yokohama-shi, Kanagawa 3-13-13 Chiyoda Chemical Construction Co., Ltd. Chiyoda Research Park (72) Inventor Haruto Kobayashi 3-13 Moriyacho, Kanagawa-ku, Yokohama-shi, Kanagawa Chiyoda Chemical Construction Co., Ltd. Chiyoda Research Park
Claims (3)
能基と弱塩基性陰イオン交換基とを有する樹脂担体にリ
パーゼを固定化したことを特徴とする固定化酵素。1. An immobilized enzyme comprising lipase immobilized on a resin carrier having a functional group capable of forming a covalent bond with the enzyme in an aqueous solution and a weakly basic anion exchange group.
基、共有結合を形成する官能基がエポキシ基であり、か
つ樹脂担体が多孔性である請求項1記載の固定化酵素。2. The method according to claim 1, wherein the weakly basic anion exchange group is a tertiary amino acid.
2. The immobilized enzyme according to claim 1, wherein the functional group forming the group and the covalent bond is an epoxy group, and the resin carrier is porous.
ーム油を含む2種以上の油脂を請求項1または2記載の
固定化酵素の存在下でエステル交換することを特徴とす
るエステル交換法。3. A transesterification method comprising transesterifying an oil containing palm oil and a fatty acid or two or more fats and oils containing palm oil in the presence of the immobilized enzyme according to claim 1 or 2.
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