Rate expression for enzyme poisoning which are consistent with a Michaelis-Menten main reaction are used to analyze the performance of a fixed bed reactor containing immobilized enzyme. When enzyme deactivation results from the irreversible bonding of a product molecule to an existing substrate-enzyme complex, it is shown that minimum enzyme activity can occur in the interior of the bed, well away from the ends. This suggests that bed sectioning techniques may enable direct evaluation of fundamental poisoning mechanisms
Feeding continuously operated stirred tank reactors with reactants and homogeneous catalysts subject...
Flaschel E, Margot A, Dohmen M, Renken A. Conversion-Space Time Profiles of Stirred-Tank Reactors Co...
The ability to dynamically probe single enzymes allows the experimental investigation of enzyme kine...
We investigate the behaviour of a reaction described by Michaelis-Menten kinetics in an immobilised ...
An approximate analytical solution which describes the deactivation of catalase immobilized on porou...
The reaction rate of starch hydrolysis catalyzed by a glucoamylase covalently bound to chitin partic...
In the presence of a reporter substrate, the progressive inactivation of an enzyme was easily studie...
A general theory is presented in this article for determining the intrinsic rate constants for the m...
Catalyst deactivation in single catalyst pellets and in an isothermal catalytic fixed bed reactor ha...
The balance equations pertaining to the modelling of batch reactors performing an enzyme-catalyzed r...
The transient analysis of immobilized enzyme deactivation in a continuous stirred basket reactor is ...
A general mathematical model was developed for predicting the performance and simulation of a packed...
The stability of ß-galactosidase entrapped in Ca-alginate–K-k-carrageenan gels under operation condi...
The long performance of an isothermal fixed bed reactor undergoing catalyst poisoning is theoretical...
A theoretical analysis of concentration of lactose hydrolysis in a packed bed reactor using immobili...
Feeding continuously operated stirred tank reactors with reactants and homogeneous catalysts subject...
Flaschel E, Margot A, Dohmen M, Renken A. Conversion-Space Time Profiles of Stirred-Tank Reactors Co...
The ability to dynamically probe single enzymes allows the experimental investigation of enzyme kine...
We investigate the behaviour of a reaction described by Michaelis-Menten kinetics in an immobilised ...
An approximate analytical solution which describes the deactivation of catalase immobilized on porou...
The reaction rate of starch hydrolysis catalyzed by a glucoamylase covalently bound to chitin partic...
In the presence of a reporter substrate, the progressive inactivation of an enzyme was easily studie...
A general theory is presented in this article for determining the intrinsic rate constants for the m...
Catalyst deactivation in single catalyst pellets and in an isothermal catalytic fixed bed reactor ha...
The balance equations pertaining to the modelling of batch reactors performing an enzyme-catalyzed r...
The transient analysis of immobilized enzyme deactivation in a continuous stirred basket reactor is ...
A general mathematical model was developed for predicting the performance and simulation of a packed...
The stability of ß-galactosidase entrapped in Ca-alginate–K-k-carrageenan gels under operation condi...
The long performance of an isothermal fixed bed reactor undergoing catalyst poisoning is theoretical...
A theoretical analysis of concentration of lactose hydrolysis in a packed bed reactor using immobili...
Feeding continuously operated stirred tank reactors with reactants and homogeneous catalysts subject...
Flaschel E, Margot A, Dohmen M, Renken A. Conversion-Space Time Profiles of Stirred-Tank Reactors Co...
The ability to dynamically probe single enzymes allows the experimental investigation of enzyme kine...