JP2007006717A - Method for producing immobilized enzyme - Google Patents

Method for producing immobilized enzyme Download PDF

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JP2007006717A
JP2007006717A JP2005188230A JP2005188230A JP2007006717A JP 2007006717 A JP2007006717 A JP 2007006717A JP 2005188230 A JP2005188230 A JP 2005188230A JP 2005188230 A JP2005188230 A JP 2005188230A JP 2007006717 A JP2007006717 A JP 2007006717A
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enzyme
carrier
immobilized
immobilization
solution
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Tatsunori Iguma
立規 猪熊
Haruyuki Iefuji
治幸 家藤
Kazuo Masaki
和夫 正木
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DIC Corp
National Research Institute of Brewing
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National Research Institute of Brewing
Dainippon Ink and Chemicals Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for immobilizing an enzyme in an enzyme solution on a carrier with high efficiency according to a physical adsorption method using the enzyme solution containing a contaminant such as a microorganism cultured product. <P>SOLUTION: The method for producing an immobilized enzyme comprises carrying out an enzyme immobilizing step of bringing the enzyme solution containing the contaminant into contact with a carrier for immobilizing the enzyme according to the physical adsorption a plurality of times and thereby immobilizing the enzyme in the enzyme solution on the carrier. The method for producing the immobilized enzyme has a carrier washing step of washing the carrier at least once with a water-soluble organic solvent or an aqueous solution thereof during the enzyme immobilizing step at a plurality of times. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、微生物培養物等、夾雑物を含有した酵素溶液中の酵素を担体に固定化する固定化酵素の製造方法に関する。   The present invention relates to a method for producing an immobilized enzyme in which an enzyme in an enzyme solution containing impurities such as a microorganism culture is immobilized on a carrier.

生体触媒である酵素を利用した反応は、酵素の高い基質特異性を利用した反応であることから目的物を効率よく製造でき、コスト低減に有利である。また、温和な条件下での反応であるため、消費するエネルギーが少なく、環境負荷を低くすることができるなど優れた方法である。
そのため、酵素反応は、工業的に多くの分野でその利用法が研究されているが、酵素と基質を溶液中で撹拌して反応させる方法では、酵素と反応生成物とを分離することが困難であり、酵素を効率的に回収することができないため、特に、高価な酵素を用いる場合は、酵素反応の工業化は経済的に困難であった。
Since the reaction using the enzyme which is a biocatalyst is a reaction using the high substrate specificity of the enzyme, the target product can be produced efficiently, which is advantageous for cost reduction. In addition, since the reaction is performed under mild conditions, it is an excellent method such that less energy is consumed and the environmental load can be reduced.
Therefore, the use of enzyme reaction has been studied industrially in many fields, but it is difficult to separate the enzyme and the reaction product by the method in which the enzyme and substrate are stirred and reacted in a solution. Since the enzyme cannot be efficiently recovered, it is economically difficult to industrialize the enzyme reaction particularly when an expensive enzyme is used.

このため、酵素を共有結合、イオン結合、物理的吸着、生化学的親和力等により、不溶性の担体に固定化した、担体結合法による固定化酵素の作製法が永年に亘り研究されている。   Therefore, a method for producing an immobilized enzyme by a carrier binding method in which an enzyme is immobilized on an insoluble carrier by covalent bond, ionic bond, physical adsorption, biochemical affinity, etc. has been studied for many years.

なかでも、物理的吸着法による酵素の固定化は、酵素を修飾することなしに担体に固定化できるため、固定化酵素作製にあたって、その作製工程が簡便で低コストであり、また酵素が失活する可能性が低い。したがって、工業的利用に大きな利点を持つものである
(例えば、非特許文献1参照)。
In particular, immobilization of an enzyme by physical adsorption can be immobilized on a carrier without modifying the enzyme, so the production process is simple and low-cost in the production of the immobilized enzyme, and the enzyme is deactivated. Is less likely to do. Therefore, it has a big advantage for industrial use (for example, refer nonpatent literature 1).

物理的吸着法による酵素の固定化法として、例えば、有機溶剤を含有したタンパク質溶液を用いて担体に固定化し、その固定化担体を有機溶剤が含まれないか又はタンパク質を変性させない程度の低濃度有機溶剤を含む緩衝液等で洗浄する方法が知られている(特許文献1参照)。しかしながら、該固定化法は、例えば、クチナーゼ等の疎水性酵素のように、酵素の種類によっては固定化工程で溶媒中に有機溶剤が含まれていると酵素が溶解したままの状態となり、酵素の固定化量が落ちてしまうことがあった。
バイオリアクターの世界−実践者のためのその基礎と応用−、pp25−pp61、1992 特開平11−174055号公報
As an enzyme immobilization method by physical adsorption, for example, a protein solution containing an organic solvent is immobilized on a carrier, and the immobilized carrier does not contain an organic solvent or does not denature proteins. A method of washing with a buffer solution containing an organic solvent is known (see Patent Document 1). However, the immobilization method, for example, depending on the type of enzyme, such as a hydrophobic enzyme such as cutinase, when the organic solvent is contained in the solvent in the immobilization step, the enzyme remains dissolved, and the enzyme In some cases, the amount of immobilization dropped.
The world of bioreactors-its basics and applications for practitioners, pp25-pp61, 1992 Japanese Patent Laid-Open No. 11-174055

また、物理的吸着力による酵素の固定化は、一般的に酵素と担体間の結合が弱いため、固定化酵素の作製において、固定化温度や固定化時の共存物質などの影響を考慮する必要がある。
特に、微生物培養物等は、種々のタンパク質あるいは多糖類等の多くの微生物由来の夾雑物を含んでおり、このような培養物を固定化用の酵素試料として用いる場合、含まれる夾雑物による固定化阻害により、一層酵素の固定化量が低下してしまう。そのため、用いる酵素試料は、可能な限り高純度なものとする必要があるが、このような高純度の酵素の作製には、複雑で多くの精製工程を経なければならず、コスト的にも不利であるいう問題点があった。
In addition, enzyme immobilization by physical adsorption force generally has a weak bond between the enzyme and the carrier, so it is necessary to consider the effects of immobilization temperature and coexisting substances during immobilization in the production of the immobilized enzyme. There is.
In particular, microbial cultures and the like contain many microorganism-derived contaminants such as various proteins or polysaccharides, and when such cultures are used as enzyme samples for immobilization, fixation with the contained contaminants is required. The amount of enzyme immobilized further decreases due to the inhibition of crystallization. For this reason, the enzyme sample to be used must be as pure as possible. However, the production of such a high-purity enzyme requires complicated and many purification steps, and is also costly. There was a problem that it was disadvantageous.

そこで本発明の目的は、微生物培養物等、夾雑物を含んだ酵素溶液を用いて、物理的吸着法により、該酵素溶液中の酵素を高い効率で担体に固定化する方法を提供することにある。   Accordingly, an object of the present invention is to provide a method for immobilizing an enzyme in an enzyme solution on a carrier with high efficiency by a physical adsorption method using an enzyme solution containing impurities such as a microorganism culture. is there.

本発明者らは、鋭意検討の結果、夾雑物を含んだ酵素溶液と、物理的吸着法によって酵素を固定化可能な固定化用担体を用いて、これらを接触させて、前記酵素溶液中の酵素を担体に固定化する工程中で、水溶性有機溶剤またはその水溶液で、この固定化担体を洗浄することにより、酵素の担体への固定化量を向上できることを見出し、本発明を完成させるに至った。   As a result of intensive studies, the present inventors contacted an enzyme solution containing impurities and an immobilization carrier that can immobilize the enzyme by a physical adsorption method, and brought them into contact with each other in the enzyme solution. In the process of immobilizing an enzyme on a carrier, the amount of the enzyme immobilized on the carrier can be improved by washing the immobilized carrier with a water-soluble organic solvent or an aqueous solution thereof, thereby completing the present invention. It came.

すなわち、本発明は、夾雑物を含んだ酵素溶液と、物理的吸着により酵素を固定化する担体とを接触させる酵素固定化工程を複数回行うことにより、酵素溶液中の酵素を担体に固定化する固定化酵素の製造方法であって、複数回の酵素固定化工程の間に、水溶性有機溶剤またはその水溶液で、少なくとも1回担体を洗浄する担体洗浄工程を有することを特徴とする固定化酵素の製造方法である。   That is, the present invention immobilizes an enzyme in an enzyme solution on a carrier by performing an enzyme immobilization step in which an enzyme solution containing impurities and a carrier on which the enzyme is immobilized by physical adsorption are contacted multiple times. A method for producing an immobilized enzyme, comprising: a carrier washing step of washing the carrier at least once with a water-soluble organic solvent or an aqueous solution thereof between a plurality of enzyme immobilization steps. It is a manufacturing method of an enzyme.

本発明によれば、微生物培養物等の夾雑物を含有した酵素溶液を用いて、該溶液中の酵素を高い効率で担体に固定化した、固定化酵素を提供できる。   According to the present invention, it is possible to provide an immobilized enzyme in which an enzyme solution containing impurities such as a microorganism culture is immobilized on a carrier with high efficiency.

以下、本発明について詳しく説明する。
(酵素)
本発明において、担体への固定化に用いる酵素としては、特に制限はないが、リパーゼ,エステラーゼ及びクチナーゼを好ましい例として挙げることができる。なかでも、リパーゼおよびクチナーゼが特に好ましい。
通常、酵素試料は、それを生産する微生物を培養することで入手できる。しかし、微生物培養においては、目的とする酵素以外にも夾雑物として糖や他のタンパク質も同時に生産される。これら夾雑物は、微生物が生育する時に細胞内で生産された後、細胞外に分泌されたものであり、このような夾雑物としては、例えば、糖であれば、グルコース、ガラクトース等の単糖が結合して高分子量化した多糖類等が挙げられ、他のタンパク質であれば、微生物の増殖に必要な各種の酵素類等が挙げられ、その他にも、前記糖が脂質やタンパク質等と複合体を形成したもの等、多数のものが挙げられる。
The present invention will be described in detail below.
(enzyme)
In the present invention, the enzyme used for immobilization on the carrier is not particularly limited, but preferred examples include lipase, esterase and cutinase. Of these, lipase and cutinase are particularly preferred.
Usually, an enzyme sample can be obtained by culturing a microorganism that produces it. However, in microbial culture, sugars and other proteins are simultaneously produced as impurities in addition to the target enzyme. These contaminants are produced intracellularly when the microorganism grows and then secreted outside the cell. Examples of such contaminants include monosaccharides such as glucose and galactose in the case of sugar. Examples of other proteins include various enzymes necessary for the growth of microorganisms. In addition, the sugars are complexed with lipids and proteins. There are many things such as those forming a body.

本発明で用いる、夾雑物を多く含有した酵素溶液として、例えば、酵母の一種であるクリプトコッカス エスピー エス−2(Cryptococcus sp S−2;FERM P−15155、以下、クリプトコッカス エスピー エス−2と略記)が生産するクチナーゼを含んだ培養液を、好ましいものとして挙げることができる。
クチナーゼは、例えば、以下の方法により入手できる。すなわち、クチナーゼを生産する酵母の一種であるクリプトコッカス エスピー エス−2を、常法に従って生育に最適な培養条件にて培養した後、その培養液から遠心分離法にて菌体を分離し、クチナーゼを含む培養上清液を得る。この上清液を、例えば、限外濾過膜を用いて濾過し、クチナーゼ酵素液を得る。このクチナーゼ酵素液は、その酵素活性を長期に亘り維持するため、凍結乾燥処理により乾燥粉末としたクチナーゼ酵素乾燥粉末とすることが好ましいが、乾燥粉末を得るための上記操作を省略し、微生物培養液をそのまま、担体への固定化に供することもできる。
通常、酵素を担体に固定化する場合は、固定化効率を上げるために、複雑で多くの精製工程を経た高純度の酵素試料を用いる必要があるが、種々の夾雑物を含むこれら微生物培養液あるいは凍結乾燥粉末等に対して、本発明は特に有効であり、前記のような複雑で多くの精製を行うことなく、高い効率で目的とする酵素を担体に固定化することができる。
As an enzyme solution containing a large amount of impurities used in the present invention, for example, Cryptococcus sp S-2 (FERM P-15155, hereinafter abbreviated as Cryptococcus sp S-2), which is a kind of yeast, is used. A culture solution containing the cutinase to be produced can be mentioned as a preferable one.
Cutinase can be obtained, for example, by the following method. That is, after culturing Cryptococcus sp-2, which is a kind of yeast that produces cutinase, under culture conditions that are optimal for growth according to conventional methods, the cells are separated from the culture solution by centrifugation, and cutinase is obtained. A culture supernatant containing is obtained. The supernatant is filtered using, for example, an ultrafiltration membrane to obtain a cutinase enzyme solution. This cutinase enzyme solution is preferably a cutinase enzyme dry powder obtained by freeze-drying to maintain the enzyme activity for a long period of time, but the above operation for obtaining the dry powder is omitted, and the microorganism culture is performed. The solution can be used for immobilization on a carrier as it is.
Usually, when an enzyme is immobilized on a carrier, it is necessary to use a high-purity enzyme sample that has undergone many purification steps in order to increase the immobilization efficiency, but these microorganism culture solutions containing various contaminants Alternatively, the present invention is particularly effective for freeze-dried powders and the like, and the target enzyme can be immobilized on a carrier with high efficiency without performing the above complicated and many purifications.

(担体)
本発明で用いる酵素固定化用担体は、物理的吸着法で酵素を固定化できる担体であり、材質に関しては、有機質、無機質のいずれでも良く、担体に固定化した酵素の活性が失われず、取り扱い上、物理的および化学的に安定であれば、特に制限されない。
無機質の固定化用担体としては、例えば、セライト、ケイソウ土、カオリナイト、モレキュラーシーブ、多孔質ガラス、セラミック等を挙げることができ、有機質の固定化用担体としては、例えば、アクリル樹脂、ポリエステル樹脂、イオン交換樹脂、セルロースパウダー等を挙げることができる。
(Carrier)
The enzyme immobilization carrier used in the present invention is a carrier capable of immobilizing an enzyme by a physical adsorption method, and the material may be either organic or inorganic, and the activity of the enzyme immobilized on the carrier is not lost and is handled. In addition, there is no particular limitation as long as it is physically and chemically stable.
Examples of the inorganic immobilization carrier include celite, diatomaceous earth, kaolinite, molecular sieve, porous glass, ceramic and the like. Examples of the organic immobilization carrier include acrylic resin and polyester resin. , Ion exchange resin, cellulose powder and the like.

本発明においては、前記のような材質からなり、酵素分子と近似のサイズである細孔を有する酵素固定化用担体を用いることが望ましく、固定化する酵素の種類に応じて、適宜選定すれば良い。
また、ここで言う物理的吸着とは、ファンデルワールス力、疎水結合等、分子間引力によって、酵素が担体に固定化されることを指す。
In the present invention, it is desirable to use an enzyme immobilization carrier made of the material as described above and having pores that are approximately the same size as the enzyme molecule, and can be selected appropriately according to the type of enzyme to be immobilized. good.
The physical adsorption referred to here means that the enzyme is immobilized on the carrier by intermolecular attractive force such as van der Waals force or hydrophobic bond.

例えば、固定化する酵素が、酵母の一種であるクリプトコッカス エスピー エス−2が生産するクチナーゼである場合は、クチナーゼの分子サイズが3〜5nmと推定されるため、好ましく用いることができる固定化用担体として、レバチット VP OC 1600(バイエル社製、平均細孔径15nm)、レバチット VP OC 1064MD(バイエル社製、平均細孔径5〜10nm)、レバチット VP OC 1163(バイエル社製、平均細孔径0.5〜10nm)デュオライトA−568(ローム・アンド・ハース社製、細孔径15〜25nm)、デュオライトA−7(ローム・アンド・ハース社製、細孔径15〜30nm)等を挙げることができる。なかでも、レバチット VP OC 1600を用いることが特に好ましい。   For example, when the enzyme to be immobilized is a cutinase produced by Cryptococcus sp. S-2, which is a kind of yeast, the molecular size of cutinase is estimated to be 3 to 5 nm. Lebatit VP OC 1600 (manufactured by Bayer, average pore diameter 15 nm), Lebatit VP OC 1064MD (manufactured by Bayer, average pore diameter 5-10 nm), Lebatit VP OC 1163 (manufactured by Bayer, average pore diameter 0.5- 10 nm) Duolite A-568 (Rohm and Haas, pore size 15 to 25 nm), Duolite A-7 (Rohm and Haas, pore size 15 to 30 nm), and the like. Among these, it is particularly preferable to use Levacit VP OC 1600.

(水溶性有機溶剤)
本発明で用いる水溶性有機溶剤としては、メタノール,エタノール,n−プロパノール、イソプロパノールなど、水に可溶な低級アルコールが好ましく、なかでも、メタノールが特に好ましい。これらの水溶性有機溶剤は、水と混合することなく用いることもできるが、水との混合溶媒として用いることが好ましい。また、水溶性有機溶剤は、1種のみを用いても良いし、2種以上を併用しても良い。
(Water-soluble organic solvent)
As the water-soluble organic solvent used in the present invention, water-soluble lower alcohols such as methanol, ethanol, n-propanol, and isopropanol are preferable, and methanol is particularly preferable. These water-soluble organic solvents can be used without being mixed with water, but are preferably used as a mixed solvent with water. Moreover, only 1 type may be used for a water-soluble organic solvent, and 2 or more types may be used together.

上記の溶剤は、固定化した酵素を担体から脱離させにくく、他の夾雑物等を酵素固定化担体から脱離させることができるため、複数ある酵素固定化工程の間に、これらの溶剤を用いて担体を洗浄することにより、酵素を高い効率で担体に固定化でき、酵素の固定化量を向上できると考えられる。
しかしながら、固定化する酵素によっては、その酵素活性を失活させる作用を有する水溶性有機溶剤もあるので、酵素の種類に応じて酵素活性を損なうことがない水溶性有機溶剤を選択することが重要である。
Since the above-mentioned solvent is difficult to desorb the immobilized enzyme from the carrier and other impurities can be desorbed from the enzyme-immobilized carrier, these solvents can be removed during a plurality of enzyme immobilization steps. It is considered that the enzyme can be immobilized on the carrier with high efficiency and the amount of immobilized enzyme can be improved by washing the carrier using the carrier.
However, depending on the enzyme to be immobilized, some water-soluble organic solvents have the effect of deactivating the enzyme activity, so it is important to select a water-soluble organic solvent that does not impair the enzyme activity depending on the type of enzyme. It is.

また、本発明において、水溶性有機溶剤を水との混合溶媒として用いる場合には、水溶性有機溶剤と水との混合比率は特に重要である。混合比率は特定の濃度域に限定されるものではなく、目的の酵素の性状に応じて混合比率を設定する必要がある。固定化担体の洗浄に用いる水溶性有機溶剤は、使用する有機溶剤と酵素の組み合わせによって、その酵素活性を失活させる有機溶剤の濃度が異なる為、目的の酵素に応じて酵素活性を損なうことがない濃度を、予備実験等を行いその結果をもとに決定することが重要である。   In the present invention, when a water-soluble organic solvent is used as a mixed solvent with water, the mixing ratio of the water-soluble organic solvent and water is particularly important. The mixing ratio is not limited to a specific concentration range, and it is necessary to set the mixing ratio according to the properties of the target enzyme. The water-soluble organic solvent used for washing the immobilization carrier differs in the concentration of the organic solvent that deactivates the enzyme activity depending on the combination of the organic solvent and the enzyme used, so that the enzyme activity may be impaired depending on the target enzyme. It is important to determine a non-concentration based on the results of preliminary experiments.

例えば、固定化に用いる酵素溶液中で、クチナーゼあるいはリパーゼは、疎水性タンパク質として存在しており、水に溶解しにくい。一方、共存する多糖類や夾雑タンパク質は多種に渡る。目的とする酵素以外の夾雑タンパク質あるいは多糖類のうち、親水性を有するものや担体の細孔径よりも大きな分子サイズのものは、水による洗浄工程で除去できる。しかしながら、疎水的な夾雑タンパク質等は、水だけによる洗浄工程だけでは必ずしも効率的に除去できない。そこで、水よりも疎水的な有機溶剤の水溶液を、担体に固定化した酵素が溶解しない溶剤濃度域に調製してこれを用いて洗浄することで、疎水的な夾雑タンパク質を除去できる。例えば、クチナーゼあるいはリパーゼを固定化した担体を洗浄する場合には、1〜50%メタノール水溶液が好ましく、10〜30%メタノール水溶液が特に好ましい。このような濃度のメタノール水溶液による洗浄で、効果的にこれら酵素を失活させることなく、かつ担体から脱離させることなく、他の夾雑物等を固定化担体から脱離させることができる。これにより、クチナーゼあるいはリパーゼを高い効率で固定化した固定化酵素を作製できる。   For example, in an enzyme solution used for immobilization, cutinase or lipase exists as a hydrophobic protein and is difficult to dissolve in water. On the other hand, there are many types of polysaccharides and contaminating proteins that coexist. Among contaminating proteins or polysaccharides other than the target enzyme, those having hydrophilicity and those having a molecular size larger than the pore diameter of the carrier can be removed by a washing step with water. However, hydrophobic contaminant proteins and the like cannot always be efficiently removed only by a washing step with water alone. Therefore, hydrophobic contaminating proteins can be removed by preparing an aqueous solution of an organic solvent that is more hydrophobic than water in a solvent concentration range in which the enzyme immobilized on the carrier does not dissolve, and using this to wash. For example, when washing a carrier on which cutinase or lipase is immobilized, a 1-50% aqueous methanol solution is preferred, and a 10-30% aqueous methanol solution is particularly preferred. By washing with an aqueous methanol solution having such a concentration, other impurities and the like can be detached from the immobilized carrier without effectively deactivating these enzymes and without detaching them from the carrier. Thereby, an immobilized enzyme in which cutinase or lipase is immobilized with high efficiency can be produced.

(固定化方法)
以下に本発明の酵素固定化の方法を説明する。
(酵素溶液)
本発明においては、酵素溶液として、多糖類あるいは該酵素以外の夾雑タンパク質等が多く含まれたものを、固定化酵素の製造に好適に用いることができる。
酵素溶液は、酵素の長期安定性を考慮して、酵素乾燥粉末を緩衝液に溶解したものを用いることが好ましいが、微生物培養液をそのまま用いることもできる。また、酵素溶液中の酵素濃度は、固定化を高い効率で行うために、酵素の溶解度以下でかつ高めの濃度とすることが好ましい。
さらに、酵素溶液中には水溶性有機溶媒を含まないか、水溶性有機溶媒を含むとしても、後の洗浄工程で用いる水溶性有機溶媒の濃度よりも低濃度の水溶性有機溶媒とすることが重要である。例えば、固定化に用いる酵素溶液中で、クチナーゼあるいはリパーゼは、有機溶媒に溶解しやすいため、固定化工程では有機溶媒が存在すると酵素が溶解した状態となり固定化量が低下するためである。
(Immobilization method)
The enzyme immobilization method of the present invention will be described below.
(Enzyme solution)
In the present invention, an enzyme solution containing a large amount of polysaccharides or contaminating proteins other than the enzyme can be suitably used for producing an immobilized enzyme.
In consideration of the long-term stability of the enzyme, it is preferable to use an enzyme solution obtained by dissolving an enzyme dry powder in a buffer solution, but a microorganism culture solution can also be used as it is. In addition, the enzyme concentration in the enzyme solution is preferably set to a concentration lower than or equal to the solubility of the enzyme in order to perform immobilization with high efficiency.
Furthermore, even if the enzyme solution does not contain a water-soluble organic solvent or contains a water-soluble organic solvent, the enzyme solution may be a water-soluble organic solvent having a lower concentration than the concentration of the water-soluble organic solvent used in the subsequent washing step. is important. For example, in the enzyme solution used for immobilization, cutinase or lipase is easily dissolved in an organic solvent, so that in the immobilization step, the presence of the organic solvent results in the enzyme being dissolved and the amount of immobilization being reduced.

また、酵素乾燥粉末を溶解する緩衝液は、特に限定されないが、酵素固定化時に酵素活性を失わせることがないよう、pHや濃度を酵素の特性にあわせて選択すればよい。例えば、クチナーゼあるいはリパーゼ溶液を調製する場合には、pHを6〜7に、濃度を5〜500mMに調製した緩衝液を用いることが好ましく、なかでも10〜100mM リン酸緩衝液(pH6.0)が特に好ましい。   The buffer solution for dissolving the enzyme dry powder is not particularly limited, but the pH and concentration may be selected according to the enzyme characteristics so that the enzyme activity is not lost during enzyme immobilization. For example, when preparing a cutinase or lipase solution, it is preferable to use a buffer solution having a pH of 6 to 7 and a concentration of 5 to 500 mM, and in particular, a 10 to 100 mM phosphate buffer solution (pH 6.0). Is particularly preferred.

(固定化工程)
酵素溶液と酵素固定化用担体を接触させる酵素固定化方法は、特に限定されず、常法に従って行うことができる。
例えば、酵素溶液と担体をプラスチックやガラス製の容器内で撹拌させるバッチ方式や、担体をカラムに詰めて酵素溶液を流す連続方式でも良いが、酵素分子と酵素固定化担体が頻繁に接触でき、担体が破損されることがないよう、酵素・担体混合溶液を撹拌や振とう,流動させることが重要である。
(Immobilization process)
The enzyme immobilization method in which the enzyme solution and the enzyme immobilization carrier are brought into contact with each other is not particularly limited, and can be performed according to a conventional method.
For example, the batch method in which the enzyme solution and the carrier are stirred in a plastic or glass container, or the continuous method in which the carrier is packed in a column and the enzyme solution is allowed to flow, may be frequently contacted with the enzyme molecule and the enzyme-immobilized carrier. It is important to stir, shake or flow the enzyme / carrier mixed solution so that the carrier is not damaged.

酵素の固定化を行う温度は、酵素が熱により失活を起こさない温度条件であれば特に限定されないが、例えば、クチナーゼあるいはリパーゼの場合、5〜30℃が好ましい。
また、1回の固定化を行う時間は、特に限定されないが、酵素の固定化反応が平衡状態に達するまでの時間をかけて行うことが好ましく、例えば、クチナーゼあるいはリパーゼの固定化の場合は、5〜40時間かけて行うことが好ましく、10〜24時間かけて行うことがより好ましい。
一方、本発明において、酵素固定化は複数回、好ましくは3回以上行うが、用いる酵素、担体、夾雑物の種類や量により適正回数は種々異なるため、各工程後の固定化酵素量を測定し、固定化酵素量が飽和に達する回数を適宜選択することがより好ましい。
The temperature at which the enzyme is immobilized is not particularly limited as long as the enzyme does not inactivate due to heat. For example, in the case of cutinase or lipase, 5 to 30 ° C. is preferable.
In addition, the time for performing the immobilization once is not particularly limited, but it is preferable to perform the time until the enzyme immobilization reaction reaches an equilibrium state. For example, in the case of immobilization of cutinase or lipase, It is preferable to carry out over 5 to 40 hours, and it is more preferable to carry out over 10 to 24 hours.
On the other hand, in the present invention, the enzyme immobilization is performed a plurality of times, preferably three times or more, but the appropriate number of times varies depending on the type and amount of the enzyme, carrier, and contaminants used, so the amount of immobilized enzyme after each step is measured. It is more preferable to appropriately select the number of times that the amount of the immobilized enzyme reaches saturation.

(洗浄工程)
本発明においては、複数回ある酵素固定化工程の間で、水溶性有機溶剤またはその水溶液で、少なくとも1回担体を洗浄するが、夾雑物を効率よく除去するためには、水溶性有機溶剤またはその水溶液で毎回洗浄することが好ましい。また、各洗浄工程は、水溶性有機溶剤またはその水溶液による1回の洗浄でもよいが、水(蒸留水)による洗浄と水溶性有機溶剤またはその水溶液による洗浄とを、複数回組み合わせて一つの洗浄工程としてもよく、用いる酵素溶液あるいは担体の種類を考慮して、適宜最適な方法を選択すれば良い。
また、前記水溶性有機溶剤またはその水溶液は、25%メタノール水溶液であることが好ましい。
(Washing process)
In the present invention, the carrier is washed at least once with a water-soluble organic solvent or an aqueous solution thereof during a plurality of enzyme immobilization steps. In order to efficiently remove impurities, the water-soluble organic solvent or It is preferable to wash each time with the aqueous solution. In addition, each cleaning step may be performed once with a water-soluble organic solvent or an aqueous solution thereof. However, one cleaning is performed by combining a cleaning with water (distilled water) and a water-soluble organic solvent or an aqueous solution thereof multiple times. It may be a process, and an optimal method may be selected as appropriate in consideration of the type of enzyme solution or carrier used.
The water-soluble organic solvent or an aqueous solution thereof is preferably a 25% methanol aqueous solution.

また、洗浄方法は、特に限定されないが、担体が破損することなく、十分な洗浄効果を得るために、洗浄液を反転、撹拌、振とう、流動等させる方法を用いると良い。
この時の洗浄温度は、酵素が熱により失活を起こさない温度であれば特に限定されないが、クチナーゼあるいはリパーゼの場合は、5〜30℃であることが好ましい。
一方、洗浄時間は、酵素を担体から脱離させることなく、他の夾雑物等を固定化担体から脱離させる十分な効果があれば特に限定されないが、例えばクチナーゼあるいはリパーゼの場合は、水溶性有機溶剤またはその水溶液による洗浄は、1〜24時間であることが好ましく、3〜12時間であることがより好ましい。
The cleaning method is not particularly limited, but in order to obtain a sufficient cleaning effect without damaging the carrier, it is preferable to use a method in which the cleaning liquid is inverted, stirred, shaken, fluidized, or the like.
The washing temperature at this time is not particularly limited as long as the enzyme is not deactivated by heat, but in the case of cutinase or lipase, it is preferably 5 to 30 ° C.
On the other hand, the washing time is not particularly limited as long as it has a sufficient effect of detaching other impurities from the immobilized carrier without detaching the enzyme from the carrier. For example, in the case of cutinase or lipase, Washing with an organic solvent or an aqueous solution thereof is preferably 1 to 24 hours, and more preferably 3 to 12 hours.

(後処理工程)
酵素を固定化させた担体は、洗浄工程を経た後、該固定化担体の使用目的に応じて、後処理を行うと良く、例えば、酵素活性を損なわない乾燥方法により乾燥することが好ましい。そのような乾燥法として、例えば、30℃以下の冷風乾燥や減圧乾燥等を挙げることができる。
(Post-processing process)
The carrier on which the enzyme is immobilized may be subjected to a post-treatment according to the purpose of use of the immobilized carrier after the washing step. For example, the carrier is preferably dried by a drying method that does not impair the enzyme activity. Examples of such a drying method include cold air drying at 30 ° C. or lower, drying under reduced pressure, and the like.

以下に実施例を挙げて、さらに本説明を詳細に説明する。ただし、本発明は、下記実施例の内容に何ら限定されるものではない。
(実施例1)
◎酵素溶液の調製
酵母の一種であるクリプトコッカス エスピー エス−2を培養して得られる、本酵母が生産するクチナーゼと、該酵母由来の多糖類を含有したクチナーゼ凍結乾燥試料を作製した。
この酵素凍結乾燥試料を50mMリン酸緩衝液(pH6.0)にて試料濃度100mg/mLとなるように溶解して、固定化用の酵素溶液を調製した。
Hereinafter, the present invention will be described in detail with reference to examples. However, the present invention is not limited to the contents of the following examples.
Example 1
Preparation of enzyme solution A cutinase lyophilized sample containing a cutinase produced by the yeast and a polysaccharide derived from the yeast, which was obtained by culturing Cryptococcus sp-2, a kind of yeast, was prepared.
This enzyme lyophilized sample was dissolved in 50 mM phosphate buffer (pH 6.0) to a sample concentration of 100 mg / mL to prepare an enzyme solution for immobilization.

◎第1回酵素固定化工程
クチナーゼの分子サイズと近似のサイズである細孔を有する担体として、レバチット VP OC 1600(バイエル社製)約134mgと、先に調製したクチナーゼ酵素溶液 500μLを、2mL容量の蓋付プラスチックチューブ内にて混ぜ合わせ、15℃で一昼夜撹拌して酵素を担体に固定化した。固定化終了後、遠心分離処理することで、酵素固定化担体と固定化に供した酵素溶液とを分離した。
◎ 1st enzyme immobilization step As a carrier having pores having a size approximate to the molecular size of cutinase, about 134 mg of Lebatit VP OC 1600 (manufactured by Bayer) and 500 μL of the previously prepared cutinase enzyme solution in a volume of 2 mL Were mixed in a plastic tube with a lid and stirred at 15 ° C. all day and night to immobilize the enzyme on a carrier. After completion of the immobilization, the enzyme immobilization carrier and the enzyme solution subjected to the immobilization were separated by centrifugation.

◎第1回洗浄工程;水/メタノール水溶液/水
次に、酵素固定化担体を、蒸留水500μLで室温にて反転・撹拌法により5回洗浄し、25%メタノール水溶液500μLを加え、15℃で12時間撹拌した。撹拌後、1500rpmで5分間遠心分離処理することで、洗浄に供した25%メタノール水溶液の遠心上清を除去した。さらに、分離した酵素固定化担体を、蒸留水500μLで室温にて反転・撹拌法により5回洗浄した。
◎ First washing step; water / methanol aqueous solution / water Next, the enzyme-immobilized carrier was washed five times with 500 μL of distilled water at room temperature by inversion and stirring, added with 500 μL of 25% methanol aqueous solution, and at 15 ° C. Stir for 12 hours. After stirring, the centrifugal supernatant of 25% aqueous methanol solution used for washing was removed by centrifuging at 1500 rpm for 5 minutes. Further, the separated enzyme-immobilized carrier was washed five times with 500 μL of distilled water at room temperature by the inversion / stirring method.

◎第2回酵素固定化工程
蒸留水による酵素固定化担体の洗浄後、先に調製した酵素溶液を再度加え、前記酵素固定化担体と酵素溶液とを接触させる酵素固定化工程を、15℃で一昼夜撹拌することにより行った。
最後に、蒸留水500μLで室温にて反転・撹拌法により、酵素固定化担体を5回洗浄した後、15℃で乾燥させ、固定化酵素を得た。固定化された酵素の量を、下記の方法により測定した(以下同様)結果、担体1gあたり21.1mgであった。結果を表1に示す。
◎ The second enzyme immobilization step After washing the enzyme immobilization carrier with distilled water, the enzyme immobilization step in which the previously prepared enzyme solution is added again and the enzyme immobilization carrier and the enzyme solution are brought into contact with each other at 15 ° C. This was done by stirring overnight.
Finally, the enzyme-immobilized carrier was washed 5 times with 500 μL of distilled water at room temperature by inversion and stirring, and then dried at 15 ° C. to obtain an immobilized enzyme. The amount of the immobilized enzyme was measured by the following method (hereinafter the same), and as a result, it was 21.1 mg / g carrier. The results are shown in Table 1.

固定化されたクチナーゼの量の測定:
酵素固定化前後の酵素溶液を採取し、各酵素溶液中に含まれるタンパク質量を、バイオラッド社製プロテインアッセイキットにて測定した。得られた測定値より、以下の式から固定化酵素量(mg)を算出した。
固定化酵素量(mg)=(酵素固定化前の溶液中のタンパク質量)−(酵素固定化後の溶液中のタンパク質量)
Determination of the amount of immobilized cutinase:
Enzyme solutions before and after enzyme immobilization were collected, and the amount of protein contained in each enzyme solution was measured with a protein assay kit manufactured by Bio-Rad. From the obtained measured value, the amount (mg) of immobilized enzyme was calculated from the following formula.
Amount of immobilized enzyme (mg) = (Amount of protein in solution before enzyme immobilization) − (Amount of protein in solution after enzyme immobilization)

(実施例2)
◎第2回洗浄工程;水/メタノール水溶液/水
実施例1と同様の方法で2回酵素の固定化を行った担体を、さらに、下記のように洗浄した。
すなわち、酵素固定化担体を、蒸留水500μLで室温にて反転・撹拌法により5回洗浄し、25%メタノール水溶液 500μLを加え15℃にて7時間撹拌した。撹拌後、1500rpmで5分間遠心分離処理することで、酵素固定化担体から25%メタノール水溶液を除去し、さらに、得られた酵素固定化担体を蒸留水500μLで室温にて反転・撹拌法により5回洗浄した。
(Example 2)
Second washing step: Water / aqueous methanol solution / water The carrier on which the enzyme was immobilized twice in the same manner as in Example 1 was further washed as follows.
That is, the enzyme-immobilized carrier was washed five times with 500 μL of distilled water at room temperature by inversion and stirring, added with 500 μL of 25% aqueous methanol solution, and stirred at 15 ° C. for 7 hours. After stirring, the 25% methanol aqueous solution is removed from the enzyme-immobilized support by centrifuging at 1500 rpm for 5 minutes. Further, the obtained enzyme-immobilized support is mixed with 500 μL of distilled water at room temperature by inversion and stirring. Washed twice.

◎第3回酵素固定化工程
蒸留水による酵素固定化担体の洗浄後、先に調製した酵素溶液を再度加え、酵素固定化を2回行った前記酵素固定化担体と酵素溶液を接触させる酵素固定化工程を、15℃で一昼夜撹拌することにより行った。
最後に、蒸留水500μLで室温にて反転・撹拌法により酵素固定化担体を5回洗浄した後、15℃で乾燥させ、固定化酵素を得た。固定化された酵素の量を測定した結果、担体1gあたり30.6mgであった。結果を表1に示す。
◎ The third enzyme immobilization step After washing the enzyme immobilization carrier with distilled water, the enzyme solution prepared above is added again, and the enzyme immobilization carrier is brought into contact with the enzyme immobilization carrier that has been immobilized twice. The crystallization step was performed by stirring at 15 ° C. all day and night.
Finally, the enzyme-immobilized carrier was washed 5 times with 500 μL of distilled water at room temperature by inversion and stirring, and then dried at 15 ° C. to obtain an immobilized enzyme. As a result of measuring the amount of the immobilized enzyme, it was 30.6 mg per 1 g of the carrier. The results are shown in Table 1.

(比較例1)
◎1回酵素固定化
実施例1と同じ手順で、クチナーゼ凍結乾燥試料を作製した。この酵素凍結乾燥試料を、試料濃度100mg/mLとなるように、50mMリン酸緩衝液(pH6.0)に溶解して、固定化用の酵素溶液を調製した。
(Comparative Example 1)
◎ Single-time enzyme immobilization A cutinase lyophilized sample was prepared in the same procedure as in Example 1. This enzyme freeze-dried sample was dissolved in 50 mM phosphate buffer (pH 6.0) so as to have a sample concentration of 100 mg / mL to prepare an enzyme solution for immobilization.

酵素固定化用樹脂であるレバチット VP OC 1600(バイエル社製)約135mgと、先に調製したクチナーゼ酵素溶液 500μLを、2mL容量の蓋付プラスチックチューブ内にて混ぜ合わせ、酵素と固定化用担体を接触させる酵素固定化工程を、15℃で一昼夜撹拌することにより1回行った。   About 135 mg of Levacit VP OC 1600 (Bayer), which is an enzyme immobilization resin, and 500 μL of the previously prepared cutinase enzyme solution are mixed in a 2 mL-capacity plastic tube with a lid, and the enzyme and immobilization carrier are mixed. The enzyme immobilization step to be contacted was performed once by stirring at 15 ° C. all day and night.

固定化終了後、遠心分離処理により、酵素固定化担体から、固定化に供した酵素溶液を分離除去した。
次に、酵素固定化担体を、蒸留水500μLで室温にて反転・撹拌法により5回洗浄した後、15℃で乾燥させ、固定化酵素を得た。固定化された酵素の量を測定した結果、担体1gあたり10.7mgであった。結果を表1に示す。
After completion of the immobilization, the enzyme solution subjected to the immobilization was separated and removed from the enzyme immobilization carrier by centrifugation.
Next, the enzyme-immobilized carrier was washed 5 times with 500 μL of distilled water at room temperature by inversion and stirring, and then dried at 15 ° C. to obtain an immobilized enzyme. As a result of measuring the amount of the immobilized enzyme, it was 10.7 mg per 1 g of the carrier. The results are shown in Table 1.

(比較例2)
◎洗浄なし、3回酵素固定化
蒸留水/25%メタノール水溶液による洗浄工程を挿入しない以外は、実施例2と同様の方法で3回の酵素固定化工程を行った。
最後に、酵素固定化担体を、蒸留水500μLで室温にて反転・撹拌法により5回洗浄した後、15℃で乾燥させ、固定化酵素を得た。固定化された酵素の量を測定した結果、担体1gあたり27.4mgであった。結果を表1に示す。
(Comparative Example 2)
◎ No washing, enzyme immobilization three times The enzyme immobilization step was performed three times in the same manner as in Example 2 except that no washing step with distilled water / 25% aqueous methanol was inserted.
Finally, the enzyme-immobilized carrier was washed 5 times with 500 μL of distilled water at room temperature by inversion and stirring, and then dried at 15 ° C. to obtain an immobilized enzyme. As a result of measuring the amount of the immobilized enzyme, it was 27.4 mg per 1 g of the carrier. The results are shown in Table 1.

(比較例3)
◎水洗浄、3回酵素固定化
酵素固定化工程間における洗浄を、25%メタノール水溶液ではなく、蒸留水500μLで行った以外は、実施例2と同様の方法で3回酵素固定化工程を行った。
最後に、酵素固定化担体を、蒸留水500μLで室温にて反転・撹拌法により5回洗浄した後、15℃で乾燥させ、固定化酵素を得た。固定化された酵素の量を測定した結果、担体1gあたり25.6mgであった。結果を表1に示す。
(Comparative Example 3)
◎ Water washing, enzyme immobilization three times The enzyme immobilization step was performed three times in the same manner as in Example 2 except that washing between enzyme immobilization steps was performed with 500 μL of distilled water instead of 25% methanol aqueous solution. It was.
Finally, the enzyme-immobilized carrier was washed 5 times with 500 μL of distilled water at room temperature by inversion and stirring, and then dried at 15 ° C. to obtain an immobilized enzyme. As a result of measuring the amount of the immobilized enzyme, it was 25.6 mg per 1 g of the carrier. The results are shown in Table 1.

Figure 2007006717
Figure 2007006717

表1に示すように、夾雑物を含んだ酵素溶液と担体を用い、複数回酵素を担体に固定化するに際して、酵素固定化工程間で、25%メタノール水溶液による担体の洗浄を行うことにより、酵素固定化が1回の場合よりも多くの酵素を担体に固定化できること、さらに、酵素固定化工程を2回、3回と繰り返すことにより、その回数に比例して、より多くの量の酵素を担体に固定化できることが確認された。   As shown in Table 1, by using an enzyme solution and a carrier containing impurities and immobilizing the enzyme to the carrier a plurality of times, by washing the carrier with a 25% aqueous methanol solution between the enzyme immobilization steps, More enzyme can be immobilized on the carrier than when the enzyme is immobilized once, and the enzyme immobilization process is repeated twice or three times to increase the amount of enzyme in proportion to the number of times. It was confirmed that can be immobilized on a carrier.

一方、比較例2のように洗浄工程を挿入しない場合や、比較例3のように洗浄工程が水による洗浄だけの場合には、酵素の固定化量が、25%メタノール水溶液洗浄を行った場合と比較して、大きく下がることが確認された。   On the other hand, when the washing process is not inserted as in Comparative Example 2, or when the washing process is only washing with water as in Comparative Example 3, the immobilized enzyme amount is 25% methanol aqueous solution washing. It was confirmed that it was significantly lower than

以上、本発明の固定化酵素の製造方法により、固定化に用いる酵素試料として、多糖類あるいは固定化する酵素以外のタンパク質等、多くの微生物由来の夾雑物を含む培養液を用いても、酵素の担体への固定化量を向上できることが確認された。
また、本発明は、前記のように、酵素試料として微生物培養物等を用いることができるため、酵素の精製等、複雑かつ多くの工程を省略でき、簡便な製造工程で多くの固定化酵素を提供できるため、コスト的にも優れたものである。
As described above, according to the method for producing an immobilized enzyme of the present invention, as an enzyme sample used for immobilization, a culture solution containing many microorganism-derived contaminants such as polysaccharides or proteins other than the enzyme to be immobilized can be used. It was confirmed that the amount immobilized on the carrier can be improved.
In addition, as described above, since the present invention can use a microorganism culture or the like as an enzyme sample, complicated and many steps such as enzyme purification can be omitted, and many immobilized enzymes can be obtained by a simple production process. Since it can be provided, it is excellent in terms of cost.

本発明の製造方法により得られた固定化酵素は、工業的な各種酵素反応に供することができる。また、担体への酵素固定化量が多いため、基質の反応点近傍の酵素濃度が高く、さらに容易に生成物と分離、回収、再利用をすることができるので、酵素反応を経済的かつ工業的に利用することができる。
The immobilized enzyme obtained by the production method of the present invention can be subjected to various industrial enzyme reactions. In addition, since the amount of enzyme immobilized on the carrier is large, the enzyme concentration in the vicinity of the reaction point of the substrate is high, and the product can be easily separated, recovered, and reused. Can be used.

Claims (5)

夾雑物を含んだ酵素溶液と、物理的吸着により酵素を固定化する担体とを接触させる酵素固定化工程を複数回行うことにより、酵素溶液中の酵素を担体に固定化する固定化酵素の製造方法であって、
複数回の酵素固定化工程の間に、水溶性有機溶剤またはその水溶液で、少なくとも1回担体を洗浄する担体洗浄工程を有することを特徴とする固定化酵素の製造方法。
Manufacture of an immobilized enzyme that immobilizes the enzyme in the enzyme solution on the carrier by performing the enzyme immobilization step that contacts the enzyme solution containing impurities and the carrier that immobilizes the enzyme by physical adsorption multiple times. A method,
A method for producing an immobilized enzyme, comprising a carrier washing step of washing a carrier at least once with a water-soluble organic solvent or an aqueous solution thereof between a plurality of enzyme immobilization steps.
前記夾雑物が、多糖である請求項1に記載の固定化酵素の製造方法。   The method for producing an immobilized enzyme according to claim 1, wherein the contaminant is a polysaccharide. 前記水溶性有機溶剤が、アルコールである請求項1または2に記載の固定化酵素の製造方法。   The method for producing an immobilized enzyme according to claim 1 or 2, wherein the water-soluble organic solvent is alcohol. 前記アルコールが、メタノールである請求項3に記載の固定化酵素の製造方法。   The method for producing an immobilized enzyme according to claim 3, wherein the alcohol is methanol. 前記酵素が、リパーゼまたはクチナーゼである請求項1〜4のいずれか一項に記載の固定化酵素の製造方法。

The method for producing an immobilized enzyme according to any one of claims 1 to 4, wherein the enzyme is lipase or cutinase.

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Cited By (1)

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Publication number Priority date Publication date Assignee Title
JP2010243342A (en) * 2009-04-07 2010-10-28 Peptide Door Co Ltd Method for analyzing lipopolysaccharide or lipid a

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010243342A (en) * 2009-04-07 2010-10-28 Peptide Door Co Ltd Method for analyzing lipopolysaccharide or lipid a

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