CS265540B1 - A method of isolating alpha-amylase from biological materials - Google Patents
A method of isolating alpha-amylase from biological materials Download PDFInfo
- Publication number
- CS265540B1 CS265540B1 CS876574A CS657487A CS265540B1 CS 265540 B1 CS265540 B1 CS 265540B1 CS 876574 A CS876574 A CS 876574A CS 657487 A CS657487 A CS 657487A CS 265540 B1 CS265540 B1 CS 265540B1
- Authority
- CS
- Czechoslovakia
- Prior art keywords
- amylase
- solution
- alpha
- biological materials
- enzyme
- Prior art date
Links
Landscapes
- Enzymes And Modification Thereof (AREA)
- Peptides Or Proteins (AREA)
Abstract
Riešenie sa týká nového spósobu izolácie a čistenia alfa - amylázy v priemyselnej výrobě z biologických materiálov. Je založené na využívaní existencie izoelektrického bodu tohoto enzýmu, kde sa autofokusáciou pósobením jednosměrného prúdu pri napatí 200 až 1 000 V vyděluje, zo zmesi enzýmov a bielkovín v roztoku o vodivosti 100 až 800 pS.cnT1 pri pH 5,82 až 6,12. Táto frakcia sa podrobí deliacej technike využívajúcej rozdielne molekulové hmotnosti, s výhodou gélovej chromatografií. Opakováním alebo zamieňaním oboch technik možno dosiahnut superčistý enzým potřebný hlavně v priemyselnej výrobě.The solution concerns a new method of isolation and purification of alpha-amylase in industrial production from biological materials. It is based on the use of the existence of an isoelectric point of this enzyme, where it is separated by autofocusing under the action of a direct current at a voltage of 200 to 1,000 V, from a mixture of enzymes and proteins in a solution with a conductivity of 100 to 800 pS.cnT1 at a pH of 5.82 to 6.12. This fraction is subjected to a separation technique using different molecular weights, preferably gel chromatography. By repeating or interchanging both techniques, it is possible to achieve a superpure enzyme needed mainly in industrial production.
Description
265540 2265540 2
Vynález sa týká spósobu izolácie a čistenia enzýmu alfa - amylázy (EC 3.2.1.1.) v prie-myselnej výrobě, ktorý využiv# existenciu izoelektrického bodu tohoto enzýmu ako kritériajeho čistoty.The invention relates to a process for the isolation and purification of the alpha-amylase enzyme (EC 3.2.1.1.) In industrial production, which utilizes the isoelectric point of this enzyme as a purity criterion.
Podlá doterajších postupov sa alfa - amyláza vyrábala niekolkými pochodmi, zahrnujúcimizrážanie síranom amonným, etanolom,acetónom, dalej róznymi systémami gélovej a iontomeničovejchromatografie či elektroforézou v rozličných usporiadaniach. Ich spoločnou nevýhodou bolaprácnosť, náročnost na technické vybavenie pričom dosiahnutiu vyššej čistoty bránila tá skutočnost, že v konečnom stádiu izolácie bola zmes bielkovín přibližné rovnakej molekulovéj hmotnosti, kde podstatná část tvořil enzým, ale obsah příměsí bol + 5 až 10 %. Tieto balastné bielko-viny znižujú mernú aktivitu a spósobujá aj iné vedlajšie efekty, ako postupná degradáciuizolátu. V našich vynálezoch CS AO 211 856 a 234 801 sa chráni principiálně nový spósob samo-činného izoelektrického fokusovania pósobením jednosměrného prádu v rovnorodom roztoku delenejlátky, ktorý je mechanicky stabilizovaný, ako aj jednoduché zariadenie na uskutočňovaniespósobu.According to the prior art, alpha-amylase has been produced by several processes including precipitation with ammonium sulfate, ethanol, acetone, other gel and ion exchange systems, or electrophoresis in a variety of configurations. Their common disadvantage was the difficulty in the technical equipment, while the higher purity was hampered by the fact that at the final stage of isolation the protein mixture was approximately the same molecular weight, where a substantial part was the enzyme but the impurity content was + 5 to 10%. These ballast proteins reduce specific activity and cause other side effects, such as gradual degradation of the isolate. In our inventions CS-A-211 856 and 234 801, in principle, a new method of self-acting isoelectric focusing is protected by the action of unidirectional laundry in a uniform solution of the diluent, which is mechanically stabilized, as well as a simple apparatus for carrying out the process.
Vyššie opísané nedostatky izolácie a čistenia enzýmu v podstatnej miere odstraňuje vyná-lez, ktorého podstata spočívá v tom, že dialýzou, alebo ultrafiltráciou sa upraví vodivostroztoku biologického materiálu obsahujáceho alfa - amylázová aktivitu na hodnoty 100 až800 pS.cm 1 a obsah bielkovín sa upraví na 1 až 30 g.l \ roztok sa autofokusuje jednosměrnýmelektrickým prádom pri napatí 200 až 1 000 V, roztok tvoriaci frakciu s najvyššou enzymatic-kou aktivitou, s výhodou pri pH 5,82 až 6,18 sa izoluje a podrobí deliacej technike využíva-jácej rozdielnu molekulová hmotnost dělených látok, s výhodou gélová chromatografiu, pričomv závislosti na požadovanej čistotě sa jedna alebo obe deliace techniky opakujá aspoň jeden-krát.The above described drawbacks of isolation and purification of the enzyme are substantially eliminated by the invention, wherein dialysis or ultrafiltration adjusts the conductivity of the alpha-amylase-containing biological material to 100 to 800 pS.cm 1 and adjusts the protein content to 1 to 30 g of solution is autofocused with unidirectional electrical underwear at a tension of 200 to 1000 volts, a solution forming a fraction with the highest enzymatic activity, preferably at a pH of 5.82 to 6.18, is isolated and subjected to a different molecular technique the weight of the divided substances, preferably gel chromatography, depending on the purity required, one or both separation techniques are repeated at least once.
Vynález je vhodný pre získavanie superčistej alfa - amylázy v technologickom meradlepri výrobě tohoto enzýmu pre potřeby viacerých odvětví priemyslu. PřikladlThe invention is suitable for obtaining super-pure alpha-amylase in the process of manufacturing this enzyme for the needs of multiple industries. Přikladl
Bakteriálna kultura kmeňa Bacill.us subtilis sa odstředí a získaný supernatant sa zahustívo vákuovej odparke. Vodivost zahuštěného supernatantu sa dialýzou alebo ultrafiltráciouupraví na 100 až 800 p.S.cm za pridávania Mcllvariovho tlmivého roztoku 0,01 mol.l pH 6,0s obsahom citrátových iontov, ktoré stabilizujá alfa - amylázová aktivitu. Obsah bielkovínsa upraví na 10 až 30 g.l 1 riedením tlmivým roztokom. Takto upraveným roztokom sa naplníautofokusačná aparatára s počtom komórok 20 a po uzatvorení sa aplikuje jednosměrný elektrickýregulovaný prád o napStí 200 až 1 000 V regulovanom tak, aby sáčin prádu a napátia nepřekročil3 W. Autofokusácia prebieha pri chlade do +4 °C. Proces autofokusácie je ukončený, keS prinapatí 1 000 V klesne prád na nulu. Delená zmes si samočinné vytvára vzostupný gradient pH,pozdlž ktorého sa jednotlivé frakcie bielkovín formujá do vrcholov podlá svojich izoelektric-kých bodov. Alfa - amyláza sa nachádza vo frakciách s najvyššou enzymatickou aktivitou, hlavněv komórkach s pH medzi 5,82 až 6,18 pričom enzymatická aktivita sa stanovuje na základenarastajácej"Oxidačnej aktivity enzýmom štiepeného škrobu. Bielkoviny z tohoto rozmedzia sazjednotia a nanesá na kolonu rozmerov 80x50 cm naplněná molekulárnym sitom Spheron P-40,ekvilibrovaná Mcllvainovým tlmivým roztokom. Chromatografia prebieha pri 4 °C pri prietoku120 ml/h a zhromaždujá sa frakcie po 30 ml. Po ukončení gélovej filtrácie sa vo všetkýchfrakciách stanoví obsah bielkovín podlá Lawryho a alfa - amylázová aktivita ako bolo opísanévyššie. Gólovou filtráciou sa autofokusaciou izolované bielkoviny rozdelia do štyroch vrcholovkde čistá alfa -- amyláza sa nachádza v treť.om vrchole od počiatku zhromaždovania frakcií.Jednotlivé kroky možno opakovat podlá potřebného stupňa čistoty, ktorá je definovaná jednakelektroforeticky prítomnosťou jedinej linie ale tiež měrnou aktivitou, ktorá má dosiahnuťaspoň 3 U.mg podlá medzinárodného hodnotenia. Tak sa dosahuje až 99,99 %-nej čistoty enzýmu.The bacterial culture of Bacillus subtilis strain is centrifuged and the supernatant obtained is concentrated by vacuum evaporation. The conductivity of the thickened supernatant is adjusted to 100 to 800 p.S.cm by dialysis or ultrafiltration with the addition of Mcllvari buffer 0.01 mol pH 6.0 containing citrate ions which stabilize the alpha-amylase activity. The protein content is adjusted to 10-30 g / l by dilution with buffer. The treated solution is filled with autofocusing apparatus with a number of chambers 20 and unidirectional electrical-controlled laundry is applied after closing to a temperature of 200 to 1000 V regulated so that the laundry linen and the tension do not exceed 3 W. Autofocusing takes place under a cold to +4 ° C. The autofocusing process is over when 1000 V drops to zero. The split mixture self-generates an upward pH gradient over which individual protein fractions are formed into peaks according to their isoelectric points. The alpha-amylase is found in the fractions with the highest enzymatic activity, mainly in the chambers with a pH between 5.82 and 6.18, while the enzymatic activity is determined on the basis of the "oxidative activity of the cleaved starch enzyme. Proteins from this range are unified and applied to a column of 80x50 cm filled with Spheron P-40 molecular sieve, equilibrated with Clclvain buffer, and chromatographed at 4 ° C at a flow rate of 120 ml / h and 30 ml fractions were collected, and the protein content of Lawry and alpha-amylase activity was determined in all fractions after all gel filtration. Goal filtration by autofocusing of the isolated protein is divided into four vertically pure alpha-amylases located in the third peak from the beginning of fraction collection. The individual steps can be repeated according to the degree of purity required, which is defined by the single electrophoresis of the only one. but it is also not a specific activity to be achieved by at least 3 U.mg according to international evaluation. Thus, up to 99.99% purity of the enzyme is obtained.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS876574A CS265540B1 (en) | 1987-09-10 | 1987-09-10 | A method of isolating alpha-amylase from biological materials |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS876574A CS265540B1 (en) | 1987-09-10 | 1987-09-10 | A method of isolating alpha-amylase from biological materials |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CS657487A1 CS657487A1 (en) | 1989-02-10 |
| CS265540B1 true CS265540B1 (en) | 1989-10-13 |
Family
ID=5413138
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CS876574A CS265540B1 (en) | 1987-09-10 | 1987-09-10 | A method of isolating alpha-amylase from biological materials |
Country Status (1)
| Country | Link |
|---|---|
| CS (1) | CS265540B1 (en) |
-
1987
- 1987-09-10 CS CS876574A patent/CS265540B1/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| CS657487A1 (en) | 1989-02-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| DE69119216T2 (en) | Enzymatic process for the production of 7-aminocephalosporic acid and derivatives | |
| US3389133A (en) | Process for isolating and purifying soluble ribonucleic acid | |
| EP0599159A2 (en) | Alpha-L-rhamnosidase for obtaining rhamnose, process for the preparation and use | |
| US4426323A (en) | Selected recovery of proteins from fermentation broths | |
| AU1176197A (en) | Thermolabile uracil-DNA-glycosylase, process for its production and use for removing uracil from DNA | |
| IE54643B1 (en) | Process for the preparation of isomaltulose (6-0-alpha-d-glucopyranosido-d-fructose) by the use of immobilized bacterial cells | |
| CA1334948C (en) | Enzymatic purification process | |
| US4591563A (en) | Process for the purification of dextran-sucrase | |
| CS265540B1 (en) | A method of isolating alpha-amylase from biological materials | |
| BE899661A (en) | PROCESS FOR INCREASING THE PRODUCTION OF ANTIBIOTICS BY GENETIC RECOMBINATION IN VIVO. | |
| WO2003046199A3 (en) | Process for the production of alginate having a high mannuronic acid-content | |
| ZA9610233B (en) | Process of preparing an organic acid | |
| US4543330A (en) | Process for the production of a fermentation starting material | |
| Richards et al. | Studies on dextranases: Part I. Isolation of extracellular, bacterial dextranases | |
| JPH11113592A (en) | Production of d-amino acid | |
| WO2000068395A3 (en) | Sulfohydrolases, corresponding amino acid and nucleotide sequences, sulfohydrolase preparations, processes, and products thereof | |
| DE3689181T2 (en) | Thermostable tryptophanase, process for its preparation and thermostable tryptophanase-producing microorganism. | |
| JPH03160995A (en) | Production of trehalose | |
| JPH0646951B2 (en) | Method for producing palatinose and trehalulose by microorganism | |
| WO2000056768A3 (en) | Chromatographic albumin process | |
| ONODERA et al. | Purification and crystallization of invertases from Fusarium oxysporum | |
| BG102357A (en) | Continuous method for the production of tartaric acid and fodder yeast from wine sludge (cloud) | |
| KR100253423B1 (en) | How to purify erythritol | |
| CS277433B6 (en) | A method of isolating lysozyme enzyme from biological materials | |
| JP3835000B2 (en) | Method for purifying L-ribose |