JPS637781A - Recovering method for cellulase - Google Patents
Recovering method for cellulaseInfo
- Publication number
- JPS637781A JPS637781A JP61151060A JP15106086A JPS637781A JP S637781 A JPS637781 A JP S637781A JP 61151060 A JP61151060 A JP 61151060A JP 15106086 A JP15106086 A JP 15106086A JP S637781 A JPS637781 A JP S637781A
- Authority
- JP
- Japan
- Prior art keywords
- solution
- cellulases
- saccharification
- solid material
- buffer solution
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 108010059892 Cellulase Proteins 0.000 title claims abstract description 7
- 229940106157 cellulase Drugs 0.000 title claims abstract description 7
- 238000000034 method Methods 0.000 title claims description 23
- 239000000243 solution Substances 0.000 claims abstract description 36
- 239000007853 buffer solution Substances 0.000 claims abstract description 13
- 239000000126 substance Substances 0.000 claims abstract description 11
- 239000007864 aqueous solution Substances 0.000 claims abstract description 10
- 229920001542 oligosaccharide Polymers 0.000 claims abstract description 8
- 150000002482 oligosaccharides Chemical class 0.000 claims abstract description 8
- 239000011343 solid material Substances 0.000 claims abstract description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 6
- 238000007796 conventional method Methods 0.000 claims abstract description 3
- 150000002772 monosaccharides Chemical class 0.000 claims abstract 2
- 108010084185 Cellulases Proteins 0.000 claims description 27
- 102000005575 Cellulases Human genes 0.000 claims description 27
- 239000007787 solid Substances 0.000 claims description 19
- 150000004676 glycans Chemical class 0.000 claims description 7
- 229920001282 polysaccharide Polymers 0.000 claims description 7
- 239000005017 polysaccharide Substances 0.000 claims description 7
- 238000000354 decomposition reaction Methods 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 4
- 239000000284 extract Substances 0.000 claims description 3
- 238000002604 ultrasonography Methods 0.000 claims description 3
- 238000005119 centrifugation Methods 0.000 abstract description 5
- 239000001913 cellulose Substances 0.000 abstract description 4
- 229920002678 cellulose Polymers 0.000 abstract description 4
- 238000000108 ultra-filtration Methods 0.000 abstract description 3
- 230000007062 hydrolysis Effects 0.000 abstract 2
- 238000006460 hydrolysis reaction Methods 0.000 abstract 2
- 102000004190 Enzymes Human genes 0.000 description 20
- 108090000790 Enzymes Proteins 0.000 description 20
- 229940088598 enzyme Drugs 0.000 description 20
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 9
- 239000002023 wood Substances 0.000 description 8
- 238000011084 recovery Methods 0.000 description 6
- 235000013312 flour Nutrition 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 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 4
- 239000008351 acetate buffer Substances 0.000 description 4
- 150000001298 alcohols Chemical class 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000000706 filtrate Substances 0.000 description 4
- 239000008103 glucose Substances 0.000 description 4
- 239000006228 supernatant Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000000123 paper Substances 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 2
- 241000223259 Trichoderma Species 0.000 description 2
- 241000223261 Trichoderma viride Species 0.000 description 2
- 230000001580 bacterial effect Effects 0.000 description 2
- 108010047754 beta-Glucosidase Proteins 0.000 description 2
- 102000006995 beta-Glucosidase Human genes 0.000 description 2
- 239000001768 carboxy methyl cellulose Substances 0.000 description 2
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 2
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000002255 enzymatic effect Effects 0.000 description 2
- 108010002430 hemicellulase Proteins 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 235000000346 sugar Nutrition 0.000 description 2
- 238000009210 therapy by ultrasound Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- LUEWUZLMQUOBSB-FSKGGBMCSA-N (2s,3s,4s,5s,6r)-2-[(2r,3s,4r,5r,6s)-6-[(2r,3s,4r,5s,6s)-4,5-dihydroxy-2-(hydroxymethyl)-6-[(2r,4r,5s,6r)-4,5,6-trihydroxy-2-(hydroxymethyl)oxan-3-yl]oxyoxan-3-yl]oxy-4,5-dihydroxy-2-(hydroxymethyl)oxan-3-yl]oxy-6-(hydroxymethyl)oxane-3,4,5-triol Chemical compound O[C@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)O[C@@H](O[C@@H]2[C@H](O[C@@H](OC3[C@H](O[C@@H](O)[C@@H](O)[C@H]3O)CO)[C@@H](O)[C@H]2O)CO)[C@H](O)[C@H]1O LUEWUZLMQUOBSB-FSKGGBMCSA-N 0.000 description 1
- OHVLMTFVQDZYHP-UHFFFAOYSA-N 1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)-2-[4-[2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidin-5-yl]piperazin-1-yl]ethanone Chemical compound N1N=NC=2CN(CCC=21)C(CN1CCN(CC1)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)=O OHVLMTFVQDZYHP-UHFFFAOYSA-N 0.000 description 1
- IFBHRQDFSNCLOZ-RMPHRYRLSA-N 4-nitrophenyl beta-D-glucoside Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1OC1=CC=C([N+]([O-])=O)C=C1 IFBHRQDFSNCLOZ-RMPHRYRLSA-N 0.000 description 1
- 240000005020 Acaciella glauca Species 0.000 description 1
- 241000609240 Ambelania acida Species 0.000 description 1
- 241000228212 Aspergillus Species 0.000 description 1
- 241000228245 Aspergillus niger Species 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 241000218631 Coniferophyta Species 0.000 description 1
- GUBGYTABKSRVRQ-CUHNMECISA-N D-Cellobiose Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)OC(O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-CUHNMECISA-N 0.000 description 1
- 235000018782 Dacrydium cupressinum Nutrition 0.000 description 1
- 240000000731 Fagus sylvatica Species 0.000 description 1
- 235000010099 Fagus sylvatica Nutrition 0.000 description 1
- 229920002581 Glucomannan Polymers 0.000 description 1
- 102000003886 Glycoproteins Human genes 0.000 description 1
- 108090000288 Glycoproteins Proteins 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- AFCARXCZXQIEQB-UHFFFAOYSA-N N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CCNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 AFCARXCZXQIEQB-UHFFFAOYSA-N 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 235000013697 Pinus resinosa Nutrition 0.000 description 1
- 240000000111 Saccharum officinarum Species 0.000 description 1
- 235000007201 Saccharum officinarum Nutrition 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 239000002154 agricultural waste Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000010905 bagasse Substances 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- -1 cellobiose Chemical compound 0.000 description 1
- 230000001413 cellular effect Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 229940046240 glucomannan Drugs 0.000 description 1
- 239000011121 hardwood Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 150000002771 monosaccharide derivatives Chemical class 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000008055 phosphate buffer solution Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 238000000527 sonication Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
- 150000008163 sugars Chemical class 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Abstract
Description
【発明の詳細な説明】
A、産業上の利用分野
本発明はセルラーゼ類の回収方法に関し、さらに詳しく
は、セルラーゼやヘミセルラーゼなどのセルラーゼ類に
よるセルロース性物質の分解糖化終了液から、残存する
前記のセルラーゼ類を極めて簡便な操作によって高得率
で回収する方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION A. Industrial Field of Application The present invention relates to a method for recovering cellulases, and more specifically, the present invention relates to a method for recovering cellulases, and more specifically, the present invention relates to a method for recovering cellulases, and more specifically, the present invention relates to a method for recovering cellulases. The present invention relates to a method for recovering cellulases with a high yield through extremely simple operations.
B、従来の技術
近年、エネルギー問題、環境汚染、未利用資源の有効利
用などの観点から、セルロース性物質の糖化の研究が盛
んに行われており、なかでも装置や操作が簡単であって
、しかも温和な条件で行うことができ、その上生成した
糖がそれ以上分解することのない酵素糖化法が有効な方
法として注目されている。B. Conventional technology In recent years, research on the saccharification of cellulosic substances has been actively conducted from the viewpoints of energy issues, environmental pollution, and the effective use of unused resources. Moreover, enzymatic saccharification is attracting attention as an effective method because it can be carried out under mild conditions and the produced sugars are not further decomposed.
この酵素糖化法においては、−般に、酵素として用いる
セルラーゼやヘミセルラーゼなどのセルラーゼ類を生産
する費用が全経費の約半分を占めるといわれており、そ
のためこの高価な酵素を回収再利用することが極めて重
要な問題となっている。In this enzymatic saccharification method, it is generally said that the cost of producing cellulases such as cellulases and hemicellulases used as enzymes accounts for about half of the total cost, so it is important to collect and reuse these expensive enzymes. has become an extremely important issue.
しかしながら、従来、セルロース性物質の分解糖化終了
液に遠心分離などを施して分離された溶液中に残存する
セルラーゼ類を回収する方法は種々提案されているもの
の、分離された固形物中に残存するセルラーゼ類を回収
する方法については、まだ報告は少なく、その回収率は
たかだか30%以下である。その中で特に、本発明者の
先の発明(特許第1299068号)(以下、「先願発
明」と記す。)が知られており、それは、セルラーゼ類
によるセルロース性物質の分解糖化終了液から該セルラ
ーゼ類を回収するに当り、まず分解糖化終了液を溶液と
固形物とに分離したのち、該溶液中がら常法に従ってセ
ルラーゼ類を回収するとともに、該固形物中に残存する
セルラーゼ類を水溶性多糖類、オリゴ糖類又はアルコー
ル類の水溶液若しくはpi(緩衝溶液により処理して回
収することを特徴としたものであり、対象とするセルロ
ース性物質の範囲の広さや、操作が室温〜55°Cの温
度でゆるやかにかきまぜるか、あるいは振どうなどを行
って該固形物と溶液を接触させるといった極めて簡便で
あるなどすぐれたものである。しかしながら、回収率は
固形物に残存する量の60り70%であり、さらに回収
率の向上が望ましい。However, although various methods have been proposed in the past for recovering cellulases remaining in the separated solution by centrifuging the solution after decomposition and saccharification of cellulosic substances, There are still few reports on methods for recovering cellulases, and the recovery rate is at most 30% or less. Among these, the present inventor's earlier invention (Patent No. 1299068) (hereinafter referred to as the "prior invention") is particularly well known, and it is a method for decomposing and saccharifying a cellulosic substance by cellulases. To recover the cellulases, first, the solution after decomposition and saccharification is separated into a solution and a solid substance, and then the cellulases are recovered from the solution according to a conventional method, and the cellulases remaining in the solid substance are dissolved in water. It is characterized by being recovered by treating with an aqueous solution or PI (buffer solution) of polysaccharides, oligosaccharides, or alcohols. It is excellent in that it is extremely simple and easy to bring the solid matter into contact with the solution by gently stirring or shaking at a temperature of %, and it is desirable to further improve the recovery rate.
C6発明が解決しようとする問題点
したがって本発明は、固形物に残存する酵素をほぼ完全
に回収し、操作や処理時間をさらに短縮簡便にすること
を目的とするものである。C6 Problems to be Solved by the Invention Therefore, the purpose of the present invention is to recover almost completely the enzyme remaining in the solid material, thereby further shortening and simplifying the operation and processing time.
D0問題点を解決するための手段
上記目的達成のため本発明者らは、各方面から鋭意検討
を重ねた結果、超音波を用いることにより、糖タンパク
質である酵素と未反応固形物との間の水素結合の切断、
及び、未反応固形物の細孔を破壊することにより、酵素
の未反応固形物への化学的結合及び物理的な吸着を減少
させることを見い出した。さらにこの処理を本発明者ら
の先願発明と共に用いることにより、上記化学結合及び
物理吸着の減少は極めて容易に行われることを見い出し
、これらの知見に基づいて本発明を完成するに至った。Means for Solving the D0 Problem In order to achieve the above objective, the present inventors have made intensive studies from various angles and have found that by using ultrasonic waves, the bond between the enzyme, which is a glycoprotein, and unreacted solid matter. breaking of hydrogen bonds,
It has also been found that chemical binding and physical adsorption of enzymes to unreacted solids can be reduced by destroying the pores of unreacted solids. Furthermore, by using this treatment together with the inventors' prior invention, they found that the above chemical bonding and physical adsorption can be extremely easily reduced, and based on these findings, they have completed the present invention.
すなわち、本発明方法においては、分解糖化終了液から
、残存するセルラーゼ類を回収するために、まず該分解
糖化終了液を遠心分離などの手段によって溶液と固形物
とに分離したのち、該溶液中に含まれるセルラーゼ類を
通常用いられている方法、例えば限外ろ過などによって
回収する。この際の回収率は溶液中の残存量に対し90
〜100%である。−方分離された固形物中に残存する
セルラーゼ類は、水溶性多糖類、オリゴ糖類又はアルコ
ール類の水溶液若しくはpH緩衝溶液に含浸し、超音波
を加える。That is, in the method of the present invention, in order to recover the remaining cellulases from the solution after completion of decomposition and saccharification, the solution after completion of decomposition and saccharification is first separated into a solution and solid matter by means such as centrifugation, and then the solution is separated into solid matter. The cellulases contained in the cellulase are recovered by a commonly used method such as ultrafiltration. The recovery rate at this time was 90% of the amount remaining in the solution.
~100%. The cellulases remaining in the separated solid are impregnated with an aqueous solution or pH buffer solution of water-soluble polysaccharides, oligosaccharides, or alcohols, and ultrasonic waves are applied.
温度は5℃から60℃で行われるが、通常室温で行われ
る。超音波処理に要する時間は、未反応固形物の状態に
より多少異なるが、1分以上が必要であり1通常は5分
程度で十分である。The temperature is from 5°C to 60°C, but it is usually performed at room temperature. The time required for the ultrasonic treatment varies somewhat depending on the state of the unreacted solids, but 1 minute or more is required, and usually about 5 minutes is sufficient.
本発明方法において用いるセルロース性物質としては1
例えば針葉樹や広葉樹、南洋材や北洋材などから得られ
る木屑、のこぎり肩、樹皮、廃木材などすべての木質が
挙げられ、さらに農業廃棄物として廃棄するために経費
を必要とする稲ワラやサトウキビ、トウモロコシなどの
廃棄物、あるいは新聞紙、段ボールのような紙類などが
挙げられる。The cellulosic material used in the method of the present invention is 1
Examples include all types of wood such as wood chips, sawnage shoulders, bark, and waste wood obtained from conifers, hardwoods, southern and northern woods, as well as rice straw and sugarcane, which require expense to dispose of as agricultural waste. Examples include waste materials such as corn, and paper materials such as newspaper and cardboard.
また1本発明方法において用いる酵素のセルラーゼ類と
しては、例えばアスペルギルス届の菌体やトリコデルマ
属の菌体などから生産されるセルラーゼ若しくはセルラ
ーゼとへミセルラーゼを含む酵素などが挙げられる。ま
た、本発明においては、これらの酵素はそれぞれ起源の
異なるものを単独で用いてもよいし、あるいは2種以上
同時に用いてもよく、さらに酵素源としてこれらの酵素
を含む菌体抽出液や菌培養液を用いることもできる。Examples of cellulases used in the method of the present invention include cellulases produced from Aspergillus bacteria and Trichoderma bacteria, or enzymes containing cellulases and hemicellulases. In addition, in the present invention, these enzymes may be used singly or two or more of them may be used at the same time, and furthermore, bacterial cell extracts or bacterial cell extracts containing these enzymes may be used as enzyme sources. A culture solution can also be used.
このセルラーゼ類の回収に用いる水溶性多糖類としては
例えばグルコマンナンなどが、オリゴ糖類としては例え
ばセロビオースなどが、アルコール類としては例えばエ
タノールのような1価アルコールやエチレングリコール
のような多価アルコールなどが挙げられる。またグルコ
ースや、p−ニトロフェニル−β−D−グルコシドのよ
うな糖誘導体を用いてもよい。水溶性多糖類やオリゴ糖
類の水溶液若しくはpH緩衝溶液の濃度は0.05〜5
重景%の範囲が好適である。また単糖の誘導体では0.
02重量%から好適な条件となる。Examples of water-soluble polysaccharides used to recover cellulases include glucomannan, oligosaccharides such as cellobiose, and alcohols such as monohydric alcohols such as ethanol and polyhydric alcohols such as ethylene glycol. can be mentioned. Also, glucose and sugar derivatives such as p-nitrophenyl-β-D-glucoside may be used. The concentration of the aqueous solution or pH buffer solution of water-soluble polysaccharides and oligosaccharides is 0.05 to 5.
A range of weighted background % is suitable. In addition, monosaccharide derivatives are 0.
Suitable conditions start from 0.02% by weight.
pH緩衝溶液は、回収後のセルラーゼ類の安定性を増す
ために用いられ、好ましいpHは3.0〜8.0の範囲
である。このpH緩衝溶液としては、通常酢酸緩衝溶液
が好ましく用いられる。A pH buffer solution is used to increase the stability of the cellulases after recovery, and the preferred pH is in the range of 3.0 to 8.0. As this pH buffer solution, an acetic acid buffer solution is usually preferably used.
これらの糖類の水溶液若しくはpH緩衝溶液を用いて得
られたセルラーゼ類を含有する回収液は、そのまま多糖
類やオリゴ糖類の分s′u素源として使用することがで
き、さらにセルロース性物質の分解糖化酵素源として再
使用できる。−方アルコール類の水溶液若しくはpH緩
衝溶液の濃度は1〜30重量%の範囲が好適である。The recovered solution containing cellulases obtained using an aqueous solution of these saccharides or a pH buffer solution can be used as it is as a source for polysaccharides and oligosaccharides, and can also be used to decompose cellulosic substances. Can be reused as a source of saccharifying enzymes. The concentration of the aqueous alcohol solution or pH buffer solution is preferably in the range of 1 to 30% by weight.
E0発明の効果
本発明方法においては、未反応固形物に吸着された酵素
の回収率は、90〜95%であり、従って溶液からの回
収と合わせて高率に使用した酵素を回収することができ
る。またその操作は室温において行われるため、加温の
ためのエネルギーを必要とせず、また操作時間を大幅に
短縮でき、したがって、セルロース性物質の酵素糖化に
本発明方法を適用することにより、その経費を大幅に節
減することができる。E0 Effects of the Invention In the method of the present invention, the recovery rate of the enzyme adsorbed on unreacted solids is 90 to 95%, and therefore, in addition to recovery from the solution, it is possible to recover the enzyme used at a high rate. can. Moreover, since the operation is carried out at room temperature, no energy is required for heating, and the operation time can be significantly shortened. can save significantly.
F、実施例 次に実施例によって本発明をさらに詳細に説明する。F. Example Next, the present invention will be explained in more detail with reference to Examples.
実施例−1
pH4,5酢酸塩緩衝溶液50mQにボールミル粉砕を
行ったアカマツ木粉2gを加え、さらに市販のアスペル
ギルス、ニゲル起源のセルロジンAPとトリコデルマ・
ビリデ起源のセルラーゼオノヅカR−10の l:1混
合物200 m gを加えて48時間40℃で振とうし
、反応終了液をろ過し、溶液と固形物780mgとに分
離した。Example-1 2 g of ball-milled red pine wood flour was added to 50 mQ of pH 4,5 acetate buffer solution, and commercially available cellulosin AP originating from Aspergillus niger and Trichoderma.
200 mg of a 1:1 mixture of cellulase Onodzuka R-10 derived from viride was added and shaken at 40° C. for 48 hours, and the reaction-completed liquid was filtered to separate the solution and 780 mg of solid matter.
木粉の61%が分解した。溶液中には、当初加えた酵素
の60%が残存した。 固形物を50mQ共栓フラスコ
に入れ、1%カルボキシメチルセルロースのpH4,5
酢酸塩緩衝溶液25maを加えて室温で5分間超音波処
理を行い、遠心分離を行って上澄液を得た。上澄液に含
まれる酵素は当初用いた酵素の36%であった。上澄液
にさらにボールミル粉砕を行ったセルロース1gを加え
そのまま40℃で振とうした。48時間後生成したグル
コースをNelson−5omogyi法で定量を行っ
たところ、940 m gであった。61% of the wood flour was decomposed. 60% of the originally added enzyme remained in the solution. Place the solid in a 50mQ stoppered flask and add 1% carboxymethyl cellulose to pH 4.5.
A 25 mA acetate buffer solution was added, sonication was performed at room temperature for 5 minutes, and a supernatant was obtained by centrifugation. The enzyme contained in the supernatant was 36% of the enzyme originally used. 1 g of ball milled cellulose was added to the supernatant, and the mixture was shaken at 40°C. Glucose produced after 48 hours was quantified by the Nelson-5omogyi method and found to be 940 mg.
実施例−2
500cc容のフラスコに炭素源として適量のセルロー
ス粉末を加えた水溶性栄養培地100mmを入れて滅菌
したのち、これにトリコデルマ・ビリデQM414を接
種し、30℃の温度で好気条件下に6日間培養した。培
養液のPHは常に5.4に調節した。Example-2 A 500 cc flask was filled with 100 mm of an aqueous nutrient medium containing an appropriate amount of cellulose powder as a carbon source and sterilized. Trichoderma viride QM414 was inoculated into the flask, and the medium was incubated at a temperature of 30°C under aerobic conditions. The cells were cultured for 6 days. The pH of the culture solution was always adjusted to 5.4.
別のroomQ容フラスコにボールミル粉砕を行ったブ
ナ木粉2gを入れ、これに前記の培養液50 m m
(酵素含有量120mg)を加え、40℃にて48時間
分解を行って木粉のの56%を分解したのち1反応終了
液を遠心分離により溶液と固形物とに分離した。 溶液
には50mgの酵素が残存しており、限外ろ過により酵
素42 m gを回収した。−方固形物を0.8%カル
ボキシメチルセルロース水溶液20m(lに含浸し、1
0分間室温で超音波を加えた。固形物をろ別したろ液に
は65mgの酵素が含まれていた。ろ液にpH4,8の
リン酸塩緩衝溶液を加え全容を25mQとし、1gの過
酸化水素−アルカリ蒸解によりバガスがら作製された紙
を細片(1cmX1cm)にしたものを加え、40’C
で振とうした。8時間後には紙は完全に溶解し、Nel
son−5omogyi法によるグルコースの生成量は
1200mgであった。Put 2 g of ball milled beech wood flour into another room Q flask, and add 50 m m of the above culture solution to this.
(Enzyme content: 120 mg) was added and decomposed at 40° C. for 48 hours to decompose 56% of the wood flour. After one reaction was completed, the liquid was separated into a solution and a solid by centrifugation. 50 mg of enzyme remained in the solution, and 42 mg of enzyme was recovered by ultrafiltration. - The solid material was impregnated with 20 ml (l) of 0.8% carboxymethyl cellulose aqueous solution,
Ultrasound was applied for 0 minutes at room temperature. The filtrate from which the solid matter was filtered contained 65 mg of enzyme. Add a phosphate buffer solution of pH 4.8 to the filtrate to bring the total volume to 25 mQ, add 1 g of hydrogen peroxide-alkali cooking to make paper made from bagasse into strips (1 cm x 1 cm), and heat at 40'C.
It was shaken with After 8 hours, the paper was completely dissolved and Nel
The amount of glucose produced by the son-5omogyi method was 1200 mg.
実施例−3
新聞紙を乾燥し、−辺3mの正方形片として2gを50
mMの水に悲濁し、これにセルラーゼーオノヅカR−1
0,100mgを加えて40℃で24時間分解を行った
のち1反応終了液を遠心分離により溶液と固形物1.4
gとに分離した。溶液には35mgのセルラーゼが残存
していた。Example 3 Dry newspaper and weigh 2 g of 50 square pieces with sides of 3 m.
Cellular Zee Onozuka R-1
After adding 0.100 mg of the solution and decomposing it at 40°C for 24 hours, the solution after one reaction was centrifuged to separate the solution and solid matter.
It was separated into g. 35 mg of cellulase remained in the solution.
前記で得られた固形物1.4gに15重量%エチレング
リコール水溶液40mMを加えて。Add 40 mM of a 15% by weight ethylene glycol aqueous solution to 1.4 g of the solid obtained above.
室温で10分間超音波を加えた。エチレングリコール水
溶液中には62mgの酵素が含まれていた。Ultrasound was applied for 10 minutes at room temperature. The ethylene glycol aqueous solution contained 62 mg of enzyme.
実施例−4
ボールミル粉砕したイエローラワン木粉2gをl OO
m m容の三角フラスコにはかり込み。Example-4 2 g of ball milled yellow lauan wood flour
Pour into a m Erlenmeyer flask.
45mMのPH5,0酢酸塩緩衝溶液を加えて45℃で
加温した。セルロジンAPとトリコデルマ・ビリデ起源
のメイセラーゼ 1:l 混合物6% 5mMを加え、
そのまま48時間振とうした後、ろ別した。ろ液には、
グルコースに換算して1160mgが検出された。ま
たろ液のβ−グルコシダーゼ活性は当初加えた量の80
%が検出された。未反応固形物40mgを0.03%P
−ニトロフェニルーβ−D−グルコシドPH4,5酢酸
塩緩衝溶液に加え5分間超音波処理を行い、遠心分離後
上澄液を40℃で10分間浸漬して溶出したβ−グルコ
シダーゼ活性を測定した。固形物に吸着された量に対し
て94%が溶出した。A 45mM PH5.0 acetate buffer solution was added and the mixture was heated at 45°C. Add 6% 5mM of cellulosin AP and meicelase of Trichoderma viride origin in a 1:l mixture;
After shaking for 48 hours, the mixture was filtered. In the filtrate,
1160 mg was detected in terms of glucose. In addition, the β-glucosidase activity of the filtrate was 80% of the initially added amount.
% was detected. 0.03% P for 40 mg of unreacted solids
-Nitrophenyl-β-D-glucoside was added to PH4,5 acetate buffer solution and subjected to ultrasonic treatment for 5 minutes, and after centrifugation, the supernatant was immersed at 40°C for 10 minutes to measure the eluted β-glucosidase activity. . 94% of the amount adsorbed on the solid material was eluted.
特許出願人 工業技術院長 飯 塚 幸 三指定代理人
工業技術院大阪工業技術試験所長速水諒三Patent applicant Kozo Iizuka, Director of the Agency of Industrial Science and Technology Designated agent: Ryozo Hayami, Director of the Osaka Institute of Industrial Science and Technology, Agency of Industrial Science and Technology
Claims (4)
終了液から該セルラーゼ類を回収するに当り、まず分解
糖化終了液を溶液と固形物とに分離した後、該溶液中か
ら常法に従ってセルラーゼ類を回収するとともに、該固
形物中に残存するセルラーゼ類を水溶性の多糖類、オリ
ゴ糖類、及び単糖類との誘導体の水溶液若しくは上記の
pH緩衝溶液、若しくはアルコール溶液に含浸し、超音
波で処理して回収することを特徴とするセルラーゼ類の
回収方法。(1) Decomposition of cellulosic substances by cellulases In recovering the cellulases from the saccharification-completed liquid, first separate the decomposition-saccharification-completed liquid into a solution and solid matter, and then extract the cellulases from the solution according to a conventional method. At the same time, the cellulase remaining in the solid material is impregnated with an aqueous solution of a derivative of water-soluble polysaccharides, oligosaccharides, and monosaccharides, the above pH buffer solution, or an alcohol solution, and treated with ultrasound. 1. A method for recovering cellulases, the method comprising recovering cellulases.
H緩衝溶液の濃度が0.5〜5重量%である特許請求の
範囲第1項記載の方法。(2) Water-soluble polysaccharide or oligosaccharide aqueous solution or p
2. A method according to claim 1, wherein the concentration of the H buffer solution is 0.5 to 5% by weight.
度が1〜30重量%である特許請求の範囲第1項記載の
方法。(3) The method according to claim 1, wherein the concentration of the aqueous alcohol solution or pH buffer solution is 1 to 30% by weight.
請求の範囲第1項記載の方法。(4) The method according to claim 1, wherein the pH of the pH buffer solution is 3.0 to 8.0.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61151060A JPS637781A (en) | 1986-06-26 | 1986-06-26 | Recovering method for cellulase |
CA000533184A CA1277621C (en) | 1986-06-26 | 1987-03-27 | Process for producing immobilized beta-glucosidase |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61151060A JPS637781A (en) | 1986-06-26 | 1986-06-26 | Recovering method for cellulase |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS637781A true JPS637781A (en) | 1988-01-13 |
Family
ID=15510422
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61151060A Pending JPS637781A (en) | 1986-06-26 | 1986-06-26 | Recovering method for cellulase |
Country Status (2)
Country | Link |
---|---|
JP (1) | JPS637781A (en) |
CA (1) | CA1277621C (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998045418A1 (en) * | 1997-04-07 | 1998-10-15 | University Of Florida Research Foundation, Inc. | Improvement of ethanol production from lignocellulose |
WO2011007574A1 (en) * | 2009-07-17 | 2011-01-20 | 日揮株式会社 | Saccharified solution preparation method and saccharification reaction device |
WO2011065449A1 (en) | 2009-11-27 | 2011-06-03 | 三井化学株式会社 | Process for production of monosaccharide |
CN108715842A (en) * | 2018-06-04 | 2018-10-30 | 浙江工业大学 | A kind of preparation method of high activity beta-glucosidase |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113151241B (en) * | 2021-04-09 | 2024-02-09 | 东南大学 | Method for immobilizing cellulase by two-dimensional nanosheets |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6024713A (en) * | 1983-07-19 | 1985-02-07 | Matsushita Electric Ind Co Ltd | Pre-amplifier |
-
1986
- 1986-06-26 JP JP61151060A patent/JPS637781A/en active Pending
-
1987
- 1987-03-27 CA CA000533184A patent/CA1277621C/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6024713A (en) * | 1983-07-19 | 1985-02-07 | Matsushita Electric Ind Co Ltd | Pre-amplifier |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998045418A1 (en) * | 1997-04-07 | 1998-10-15 | University Of Florida Research Foundation, Inc. | Improvement of ethanol production from lignocellulose |
WO2011007574A1 (en) * | 2009-07-17 | 2011-01-20 | 日揮株式会社 | Saccharified solution preparation method and saccharification reaction device |
WO2011065449A1 (en) | 2009-11-27 | 2011-06-03 | 三井化学株式会社 | Process for production of monosaccharide |
JP5431499B2 (en) * | 2009-11-27 | 2014-03-05 | 三井化学株式会社 | Monosaccharide production method |
CN108715842A (en) * | 2018-06-04 | 2018-10-30 | 浙江工业大学 | A kind of preparation method of high activity beta-glucosidase |
Also Published As
Publication number | Publication date |
---|---|
CA1277621C (en) | 1990-12-11 |
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