CS257830B1 - A method for preparing immobilized exopolygalacturonase - Google Patents

A method for preparing immobilized exopolygalacturonase Download PDF

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CS257830B1
CS257830B1 CS858992A CS899285A CS257830B1 CS 257830 B1 CS257830 B1 CS 257830B1 CS 858992 A CS858992 A CS 858992A CS 899285 A CS899285 A CS 899285A CS 257830 B1 CS257830 B1 CS 257830B1
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Czechoslovakia
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exopolygalacturonase
immobilized
enzyme
polyethylene terephthalate
preparing immobilized
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CS858992A
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Czech (cs)
Slovak (sk)
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CS899285A1 (en
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Kveta Heinrichova
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Kveta Heinrichova
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  • Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
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Abstract

Očelom riešenia je spósob přípravy imobilizovanej exopolygalakturonázy. Podstata sp6- sobu spočiva v tom, že sa enzým zakotví pri pH 4,2 až 6,4 a teplote medzi 5 až 30 °C na polyetyléntereftalát. Imobilizovaná exopolygalakturonáza má využitie pri úplnej degradácii pektínových látok napr. v konzervárenskom a vinárskom priemysle a pri priprave kyseliny D-galakturónovej.The aim of the solution is a method for preparing immobilized exopolygalacturonase. The essence of the method is that the enzyme is anchored at pH 4.2 to 6.4 and a temperature between 5 and 30 °C on polyethylene terephthalate. Immobilized exopolygalacturonase is used in the complete degradation of pectin substances, e.g. in the canning and winemaking industries and in the preparation of D-galacturonic acid.

Description

257830 2257830 2

Vynález sa týká spósobu přípravy imobil.izovaného pektolytického enzymu exopolygalaktu-ronázy , ktorá specificky katalyzuje postupné stiepenie koncových alfa-1, 4-glykozidickýchvázieb kyseliny pektovej a oligogalakturónových kyselin po monomérnych jednotkách.The present invention relates to a process for preparing an immobilized exopolygalactononase pectolytic enzyme which specifically catalyzes the sequential cleavage of terminal alpha-1,4-glycosidic bonds of pectic acid and oligogalacturonic acids by monomeric units.

Exopolygalakturonázu imobilizovali dosial len kovalentným viazaním na nerozpustný nosična báze polyakrylamidu po jeho aktivácii vodorozpustnými karbodiimidmí (Collection Czech,*Exopolygalacturonase was immobilized only by covalent binding to an insoluble polyacrylamide-based carrier after its activation with water-soluble carbodiimides (Collection Czech, *

Chem. Commun. 50, (1985) v tlaČi). Nevýhodou uvedeného postupu založeného na kovelentnej imobilizácii je operačná zložitost súvisiaca s aktiváciou nosiča, tiez nevýhodné hydrody-namické vlastnosti biogélu, ktoré sa prejavujú pri kolónovej aplikácii imobilizovaného enzýmu.Ďalším nedostatkom je tažká dostupnost a poměrně vysoká cena nosiča i aktivačného činidla.Chem. Commun. 50, (1985) in print). A disadvantage of the above-mentioned process based on cervical immobilization is the operational complexity associated with the activation of the carrier, as well as the disadvantageous hydrodynamic properties of the biogel, which are manifested in the column application of the immobilized enzyme. Another drawback is the severe availability and relatively high cost of both the carrier and the activating agent.

Uvedené nedostatky sa odstraňujú postupom podlá vynálezu, ktorého podstatou je, žesa enzým zakotví pri pH 4,2 až 6,4 a teplote 5 až 30 °C na polyetyléntereftalát, ktorý sapřipraví z etylénglykolu a kyseliny tereftalovej postupom, ktorý zaručuje vysokoprevládajúcuhydrofóbnu adsorbciu enzýmu na nosič {Chem. Prum. 26, 598 (1976). Základný spósob přípravy imobilizovanej exopolygalakturonázy spočívá v operačnej jedno-duchosti postupu a stálého zakotvenia, čo pri dodržiavaní optimálnych podmienok enzýmovejreakcie, umožňuje používat imobilizovaný enzým opakované, alebo v dlhodobých kont.inuálnychprocesoch. ĎalŠou výhodou preparátu připraveného podlá postupu je, že sa spósob jeho účinkuna polymérne substráty oproti účinku volného enzýmu nemení. Východzie reaktanty pre přípravu imobilizovanej exopolygalakturonázy sú lahko dostupné,nakolko exopolygalakturonáza je přítomná v komerčných preparátoch pektináz, vyrábaných prepoužitie v potravinárskom priemysle. Použitý nosič polyetyléntereftalát je čsl. výroby a jecenove přístupný.These drawbacks are solved by the process of the present invention, wherein the enzyme is anchored at a pH of 4.2 to 6.4 and a temperature of 5 to 30 ° C to polyethylene terephthalate, which is prepared from ethylene glycol and terephthalic acid by a process which guarantees the high hydrophobic adsorption of the enzyme to the carrier. {Chem. Prum. 26, 598 (1976). The basic method of preparing immobilized exopolygalacturonase consists in the operational simplicity of the procedure and the permanent anchoring, which allows repeated immobilized enzymes to be used in long-term continuous processes, while maintaining optimal enzyme reaction conditions. Another advantage of the preparation prepared according to the method is that the method of its action does not change the polymer substrates as compared to the effect of the free enzyme. The starting reactants for the preparation of immobilized exopolygalacturonase are readily available because exopolygalacturonase is present in commercial pectinase preparations manufactured by the food industry. The carrier used is polyethylene terephthalate. production and barley accessible.

Rovnako vlastná imobilizácia je velmi jednoduchá, lahko preveditelná a technicky nenáročná.Spočívá v reakcii rozpustného enzýmu s nosičom v prostředí tlmivého roztoku o pH 4,2 až6,4, obvykle sa používá teploty 5 až 30 °C, nižšia teplota nežiadúcim spósobom ovplyvňujerýchlost reakcie, vyššia naopak móže spósobiť deaktiváciu enzýmu. Reakčná doba sa riadipredovŠetkým žiadúcim stupňom konverzie, teplotou a množstvom enzýmu. Obvykle sa pohybujeod 4 do 16 hodin. Po skončení reakcie sa imobilizovaný enzým oddělí od supernatantu dekantáciou,filtráciou cez fritu, alebo odstředěním, premyje tlmívým roztokom a uchovává v suspenzíipri 4 °C.Similarly, the immobilization itself is very simple, easily convertible and technically inexpensive. It consists in reacting the soluble enzyme with the carrier in a buffer solution of pH 4.2-6.4, typically 5-30 ° C, lower temperature adversely affecting the rate of reaction, higher, on the other hand, may cause enzyme inactivation. The reaction time with the predominantly desired conversion rate, temperature and amount of enzyme. Usually it ranges from 4 to 16 hours. Upon completion of the reaction, the immobilized enzyme is separated from the supernatant by decantation, frit filtration, or centrifugation, washed with buffer and stored in suspension at 4 ° C.

Spósob přípravy podlá vynálezu je vysvětlený na nasledujúcich príkladoch. Příklad 1The method of the invention is explained in the following examples. Example 1

Exopolygalakturonáza přítomná v dostupných technických preparátoch pektináz, resp.z nich a vyšších rastlín izolovaná lubovolným postupom napr. gólovou a ionovýmennou chroma-tografiou Biochim. Biophys. Acta 422, 349 (1976); Collection Czech. Chem. Commun 42, 3 214 (1977)Biologia 36, 197 (1981) , bola imobilizovaná na polyetyléntereftalát podlá nasledujúcehopostupu: K 1 g polyetyléntereftalátu premytému 0,1 mol.l octanovým tlmivým roztokomo pH 4,8 suspendovanom v 10 ml toho istého tlmivého toztoku sa přidá 10 mg preparátuexopolygalakturonázy. Po 4 hodinách miešania pri laboratornej teplote sa gél oddělí vhodnýmspósobom. Příklad .2Exopolygalacturonase present in available technical preparations of pectinases, respectively of them and higher plants, isolated by any method, e.g., goal and ion exchange chromatography Biochim. Biophys. Acta 422, 349 (1976); Collection Czech. Chem. Commun 42, 2114 (1977) Biologia 36, 197 (1981), was immobilized on polyethylene terephthalate as follows: To 1 g of polyethylene terephthalate washed with 0.1 mol / L acetate buffer pH 4.8 suspended in 10 ml of the same buffer was 10 mg of the preparation ofexopolygalacturonase is added. After 4 hours of stirring at room temperature, the gel is separated appropriately. Example .2

Polyetyléntereftalát suspendovaný vo vodě, alebo v tlmivých roztokoch o pH 4,2 až 6,4 sa naplní do kolony, cez ktorú sa filtruje roztok obsahujúci exopolygalakturonázu v tlmivom roztoku o pH zodpovedajúcom ekvilibračnému roztoku dovtedy, kým afluent nevykazuje enzýmovú aktivitu. Kolona sa potom premyje tlmivým octanovým roztokom pH 4,8.The polyethylene terephthalate suspended in water or in buffers at pH 4.2-6.4 is charged to the column through which the solution containing the exopolygalacturonase in the pH buffer corresponding to the equilibration solution is filtered until the affluent shows enzyme activity. The column is then washed with pH 4.8 buffer solution.

Claims (1)

PREDMET VYNALEZUOBJECT OF THE INVENTION Spósob přípravy imoblizovanej exopolygalakturonázy vyznačený tým, že sa enzým zakotví pri pH 4,2 až 6,4 a teplote medzi 5 až 30 °C na polyetyléntereftalát.Process for the preparation of an immobilized exopolygalacturonase characterized in that the enzyme is anchored at polyethylene terephthalate at a pH of 4.2 to 6.4 and a temperature of between 5 to 30 ° C.
CS858992A 1985-12-09 1985-12-09 A method for preparing immobilized exopolygalacturonase CS257830B1 (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US12297474B2 (en) 2021-04-29 2025-05-13 Conopco, Inc. Process to produce mono-rhamnolipids
US12371726B2 (en) * 2021-04-29 2025-07-29 Conopco, Inc. Process to produce mono-rhamnolipids

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US12297474B2 (en) 2021-04-29 2025-05-13 Conopco, Inc. Process to produce mono-rhamnolipids
US12371726B2 (en) * 2021-04-29 2025-07-29 Conopco, Inc. Process to produce mono-rhamnolipids

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