DE3937892A1 - Enzyme membrane reactor with ultrafiltration membrane - with surfaces of thermoplastic polymer free from Gps. interfering with protein structure of enzyme - Google Patents

Enzyme membrane reactor with ultrafiltration membrane - with surfaces of thermoplastic polymer free from Gps. interfering with protein structure of enzyme

Info

Publication number
DE3937892A1
DE3937892A1 DE3937892A DE3937892A DE3937892A1 DE 3937892 A1 DE3937892 A1 DE 3937892A1 DE 3937892 A DE3937892 A DE 3937892A DE 3937892 A DE3937892 A DE 3937892A DE 3937892 A1 DE3937892 A1 DE 3937892A1
Authority
DE
Germany
Prior art keywords
enzyme
membrane
reactor
gps
ultrafiltration membrane
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.)
Granted
Application number
DE3937892A
Other languages
German (de)
Other versions
DE3937892C2 (en
Inventor
Udo Kragl
Joerg Peters
Christian Prof Wandrey
Maria-Regina Prof Kula
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Forschungszentrum Juelich GmbH
Original Assignee
Forschungszentrum Juelich GmbH
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Forschungszentrum Juelich GmbH filed Critical Forschungszentrum Juelich GmbH
Priority to DE3937892A priority Critical patent/DE3937892A1/en
Priority to CH3518/90A priority patent/CH679676A5/de
Publication of DE3937892A1 publication Critical patent/DE3937892A1/en
Application granted granted Critical
Publication of DE3937892C2 publication Critical patent/DE3937892C2/de
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M21/00Bioreactors or fermenters specially adapted for specific uses
    • C12M21/18Apparatus specially designed for the use of free, immobilized or carrier-bound enzymes
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M25/00Means for supporting, enclosing or fixing the microorganisms, e.g. immunocoatings
    • C12M25/02Membranes; Filters

Abstract

In an enzyme membrane reactor with a cell closed by an ultrafiltration membrane which retains enzymes, over which the reactor effluent passes, surfaces, apart from the ultrafiltration membrane, coming into contact with reaction medium contg. enzymes, are of a thermoplastic polymer free from -C-S or -C-O gps. The polymer is formed of vinyl gps. of formula H2C=CHR. R = H, Me, Cl or Ph. ADVANTAGE - The synthetic is free from components which interfere with the protein structure of the enzymes, and the deactivation rate of enzymes, esp. of aldolases, is low.

Description

Die Erfindung bezieht sich auf einen Enzymmembran­ reaktor mit einer Reaktionszelle, die von einer Ultrafiltrationsmembran mit Rückhaltevermögen für Enzyme abgeschlossen ist, über die der Reaktorab­ lauf erfolgt.The invention relates to an enzyme membrane reactor with a reaction cell from a Ultrafiltration membrane with retention capacity for Enzymes through which the reactor is shut off run takes place.

Enzymmembranreaktoren sind für die kontinuierliche Durchführung enzymkatalysierter Umsetzungen von großem Interesse. Die Verhaltensweise solcher Bio­ katalysatoren ist je nach Eigenart unterschiedlich und wird empfindlich durch die umgebenden Medien beeinflußt.Enzyme membrane reactors are for continuous Implementation of enzyme-catalyzed reactions of great interest. The behavior of such bio Catalysts vary depending on their particularity and becomes sensitive to the surrounding media influenced.

Es hat sich nun gezeigt, daß nicht nur das umgeben­ de Medium selbst, sondern auch das Wandmaterial des Reaktors eine Rolle bei der Desaktivierung der im Reaktor enthaltenen Enzyme spielt.It has now been shown that not only that surrounds de medium itself, but also the wall material of the Reactor plays a role in the deactivation of the Reactor contained enzymes plays.

Üblicherweise werden solche Enzymmembranreaktoren aus Stahl, insbesondere Edelstahl, gefertigt. Für Demonstrationszwecke wurden jedoch auch bereits Zellen aus durchsichtigen Kunststoff (insbesondere Plexiglas) gezeigt.Such enzyme membrane reactors are usually used made of steel, especially stainless steel. For However, demonstration purposes have also been used Clear plastic cells (especially Plexiglass).

Es wurde nun gefunden, daß die Desaktivierungsge­ schwindigkeit insbesondere von Aldolasen besonders gering ist, wenn der Reaktor aus einem Kunststoff mit glatter hydrophober Oberfläche besteht, dessen chemische Zusammensetzung möglichst frei von Kompo­ nenten ist, die zu Störungen in der Proteinstruktur des Enzyms führen können.It has now been found that the deactivation gene speed especially of aldolases in particular is low if the reactor is made of a plastic  with a smooth hydrophobic surface, whose chemical composition as free of compo as possible is leading to disturbances in the protein structure of the enzyme can lead.

Der daraufhin entwickelte erfindungsgemäße Enzymmem­ branreaktor der eingangs genannten Art ist dadurch gekennzeichnet, daß die mit enzymhaltigem Reaktions­ medium in Kontakt kommenden Flächen - abgesehen von der Ultrafiltrationsmembran - aus einem thermopla­ stischen Polymerisat bestehen, das frei von -C-S- oder -C-O-Gruppen ist.The enzyme membrane according to the invention then developed branch reactor of the type mentioned is characterized in that with enzyme-containing reaction medium coming into contact - apart from the ultrafiltration membrane - from a thermopla consist polymeric that is free of -C-S- or -C-O groups.

Vorzugsweise ist dabei das Polymerisat aus vinyli­ schem Monomeren der FormelThe polymer is preferably vinyli cal monomers of the formula

gebildet, bei denen R für H, CH3, Cl oder C6H5 steht.formed in which R is H, CH 3 , Cl or C 6 H 5 .

Die beigefügten Zeichnungen dienen zur weiteren Ver­ anschaulichung der Erfindung; es zeigen:The accompanying drawings serve for further ver illustration of the invention; show it:

Fig. 1 schematisch den Aufbau eines EMR im Schnitt; Figure 1 schematically shows the structure of an EMR in section.

Fig. 2 eine gebaute EMR-Zelle in Explosions­ darstellung; Figure 2 is a built EMR cell in an exploded view.

Fig. 3 den Aktivitätsverlauf einer Aldolase in Abhängigkeit von der Zeit bei Anwe­ senheit unterschiedlicher Materialien. Fig. 3 shows the activity profile of an aldolase as a function of time when different materials are present.

Gemäß Fig. 1 umfaßt ein EMR 1 eine durch eine Ul­ trafiltrationsmembran 2 abgeschlossene Reaktionszel­ le 3, in die über ein oder mehrere Zuläufe 4 Sub­ strate eingespeist werden, während über 5 der Reak­ torablauf abgeht. In der Zelle 3 befindet sich die Reaktionsflüssigkeit mit darin löslichem Enzym 6, die mittels eines Magnetrührers 7 bewegt wird.Referring to FIG. 1, an EMR 1 comprises a trafiltrationsmembran by a Ul 2 completed Reaktionszel le 3, in which via one or more feed streams are fed 4 sub strate, while 5 of the reac torablauf going on. In the cell 3 there is the reaction liquid with the enzyme 6 soluble therein, which is moved by means of a magnetic stirrer 7 .

Eine praktische Ausführungsart nit Flachmembran ist in Fig. 2 dargestellt, gemäß der die Zelle zwischen Endflanschen 8, 8′ gebildet wird, zwischen denen die Seitenwand sowie die Membran samt Dichtringen eingespannt wird.A practical embodiment nit flat membrane is shown in Fig. 2, according to which the cell is formed between end flanges 8 , 8 ', between which the side wall and the membrane together with sealing rings is clamped.

Fig. 3 zeigt deutlich, daß je nach Material, das mit der enzymhaltigen Reaktionsflüssigkeit in Kon­ takt komnt, deutlich unterschiedliche Desakti­ vierungsraten erhalten werden. Fig. 3 clearly shows that depending on the material that comes into contact with the enzyme-containing reaction liquid in Kon, significantly different deactivation rates are obtained.

Claims (2)

1. Enzymmembranreaktor nit einer Reaktionszelle, die von einer Ultrafiltrationsmembran mit Rückhaltever­ mögen für Enzyme abgeschlossen ist, über die der Reaktorablauf erfolgt, dadurch gekennzeichnet, daß die mit enzymhaltigem Reaktionsmedium in Kon­ takt kommenden Flächen - abgesehen von der Ultrafil­ trationsmembran - aus einem thermoplastischen Poly­ merisat bestehen, das frei von -C-S- oder -C-O-Grup­ pen ist.1. Enzyme membrane reactor with a reaction cell, which is completed by an ultrafiltration membrane with retention properties for enzymes via which the reactor outlet takes place, characterized in that the surfaces coming into contact with the enzyme-containing reaction medium come into contact - apart from the ultrafiltration membrane - from a thermoplastic polymer exist that is free of -CS- or -CO groups. 2. Reaktor nach Anspruch 1, dadurch gekennzeichnet, daß das Polymerisat aus Vinylgruppen gebildet ist, bei denen R für H, CH3, Cl odar C6H5 steht.2. Reactor according to claim 1, characterized in that the polymer from vinyl groups is formed in which R is H, CH 3 , Cl or C 6 H 5 .
DE3937892A 1989-11-15 1989-11-15 Enzyme membrane reactor with ultrafiltration membrane - with surfaces of thermoplastic polymer free from Gps. interfering with protein structure of enzyme Granted DE3937892A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
DE3937892A DE3937892A1 (en) 1989-11-15 1989-11-15 Enzyme membrane reactor with ultrafiltration membrane - with surfaces of thermoplastic polymer free from Gps. interfering with protein structure of enzyme
CH3518/90A CH679676A5 (en) 1989-11-15 1990-11-05

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE3937892A DE3937892A1 (en) 1989-11-15 1989-11-15 Enzyme membrane reactor with ultrafiltration membrane - with surfaces of thermoplastic polymer free from Gps. interfering with protein structure of enzyme

Publications (2)

Publication Number Publication Date
DE3937892A1 true DE3937892A1 (en) 1991-05-16
DE3937892C2 DE3937892C2 (en) 1991-09-12

Family

ID=6393521

Family Applications (1)

Application Number Title Priority Date Filing Date
DE3937892A Granted DE3937892A1 (en) 1989-11-15 1989-11-15 Enzyme membrane reactor with ultrafiltration membrane - with surfaces of thermoplastic polymer free from Gps. interfering with protein structure of enzyme

Country Status (2)

Country Link
CH (1) CH679676A5 (en)
DE (1) DE3937892A1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998033894A1 (en) * 1997-01-29 1998-08-06 Forschungszentrum Jülich GmbH Method for the production of ndp-sugar
WO2004007058A1 (en) * 2002-07-11 2004-01-22 Co2 Solution Inc. Triphasic bioreactor and process for gas effluent treatment
US7176017B2 (en) 2001-07-13 2007-02-13 Co2 Solution Inc. Triphasic bioreactor and process for gas effluent treatment

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
NICHTS ERMITTELT *

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998033894A1 (en) * 1997-01-29 1998-08-06 Forschungszentrum Jülich GmbH Method for the production of ndp-sugar
US7176017B2 (en) 2001-07-13 2007-02-13 Co2 Solution Inc. Triphasic bioreactor and process for gas effluent treatment
US7579185B2 (en) 2001-07-13 2009-08-25 Co2 Solution Inc. Triphasic process for gas effluent treatment
US7820432B2 (en) 2001-07-13 2010-10-26 Co2 Solution Inc. Triphasic bioreactor and process for gas effluent treatment
WO2004007058A1 (en) * 2002-07-11 2004-01-22 Co2 Solution Inc. Triphasic bioreactor and process for gas effluent treatment

Also Published As

Publication number Publication date
DE3937892C2 (en) 1991-09-12
CH679676A5 (en) 1992-03-31

Similar Documents

Publication Publication Date Title
DE3617875A1 (en) METHOD FOR IMMOBILIZING MICROORGANISMS
DE3011334C2 (en) Laminar flow reactor for reactions with enzyme or cofactors, in which the enzyme or the cofactor is immobilized on a matrix with a flat surface
WO1987003615A1 (en) Process for supplying oxygen from fermentation plant and device for implementation of the process
Saunders et al. Effect of mean-cell residence time on organic composition of activated sludge effluents
EP0205790A2 (en) Support for the cultivation of human or animal cells in a fermenter
DE2835979A1 (en) METHOD OF PERFORMING ENZYMATIC CONVERSIONS
DE3937892C2 (en)
DE60315992T2 (en) MONITORING OF CELLS
WO2006119867A1 (en) Fermentation method and apparatus for its implementation
EP0531955A2 (en) Method and apparatus for the determination of nitrification activity in a waste water stream or basin and its application
EP0263371A3 (en) Process and apparatus for animal cell culture
DE19945162A1 (en) Process for culturing cells, membrane module, use of a membrane module and reaction system for culturing cells
EP2171036B1 (en) Method and apparatus for cultivating living cells
DE3245312A1 (en) METHOD FOR CARRYING OUT (BIO-) CHEMICAL REACTIONS
WO1999048823A1 (en) Growth bodies for immobilizing microorganisms
DE3822451C2 (en)
EP1207960B1 (en) Needle, method for transferring liquids and method for producing said needle
DE19917955C2 (en) Method and device for the short-term determination of the biological oxygen demand
DE102005061629A1 (en) Apparatus and method for transporting and forming compartments
DE3530440A1 (en) Arrangement for the three-dimensional growth of animal and human cells
DE3502272A1 (en) Packed reactor
CH667641A5 (en) METHOD FOR AUTOTROPHIC DENITRIFICATION OF WATER.
DE102004025224B4 (en) Quantitative dermination of hydrogen sulfide in gases, e.g. for monitoring waste gases, using flow system with biosensor comprising sulfur-oxidizing bacteria immobilized on oxygen sensor and/or pH sensor
AT346285B (en) METHOD FOR DETERMINING THE ACTIVITY OF AN ENZYME AND DEVICE FOR CARRYING OUT THIS PROCEDURE
Horn et al. Simulation of substrate conversion and mass transport in biofilm systems

Legal Events

Date Code Title Description
OP8 Request for examination as to paragraph 44 patent law
D2 Grant after examination
8364 No opposition during term of opposition
8339 Ceased/non-payment of the annual fee