Abstract: In the most cases of the practical fermentation processes with filamentous microorganisms, direct monitoring of the cell morphology and biomass distribution in the culture medium is not easily possible. Use of a mathematical model is a suitable way to describe the substrate uptake and cell growth behavior of these microorganisms. Penicillium brevicompactum is one of the morphologically complex filamentous fungi with different structural forms. In this work, nutrient uptake and cell growth kinetics were investigated using Monod and Moser models through batch submerged fermentation in a bench-scale stirred tank bioreactor. The experimental data were fitted with both the Monod and the Moser kinetic with a regression value of 0.87. Th...
This research covers the modeling of the velocity profile of a bioreactor with recycle; the concept ...
A microbroth kinetic model based on turbidity measurements was developed in order to analyze the gro...
This objective of this study is to predict cell masses and substrate consumption in a fed-batch syst...
Fed-batch fermenters are generally operated with the addition of small doses of nutrients, therefore...
Beauvericin (BEA) is a cyclic hexadepsipeptide mycotoxin with notable phytotoxic and insecticidal ac...
A mathematical growth model for the batch solid-state fermentation process for fungal tannase produc...
ABSTRACT The chapter focuses on the growth kinetics and modelling of recombinant Escherichia coli...
A comparative study of kinetic models to describe the dynamics of the fermentation process of cultur...
The kinetics of cell growth, substrate utilization and biosurfactant production by Bacillus lichenif...
In this paper, we propose multi-scale models for a batch bioreactor, which are developed by expandin...
The development and implementation of control strategies for bioreactor systems require improved pre...
In this study, we have conducted kinetics and modelling studies ofCentella asiatica cell growth and ...
This study presents a mathematical model of a batch fermentation of lactose oxidation from a natural...
The aim of this work was to describe growth dynamics, substrate depletion and polygalacturonases pro...
Abstract- In practical situations where direct observation of the morphology and biomass distributio...
This research covers the modeling of the velocity profile of a bioreactor with recycle; the concept ...
A microbroth kinetic model based on turbidity measurements was developed in order to analyze the gro...
This objective of this study is to predict cell masses and substrate consumption in a fed-batch syst...
Fed-batch fermenters are generally operated with the addition of small doses of nutrients, therefore...
Beauvericin (BEA) is a cyclic hexadepsipeptide mycotoxin with notable phytotoxic and insecticidal ac...
A mathematical growth model for the batch solid-state fermentation process for fungal tannase produc...
ABSTRACT The chapter focuses on the growth kinetics and modelling of recombinant Escherichia coli...
A comparative study of kinetic models to describe the dynamics of the fermentation process of cultur...
The kinetics of cell growth, substrate utilization and biosurfactant production by Bacillus lichenif...
In this paper, we propose multi-scale models for a batch bioreactor, which are developed by expandin...
The development and implementation of control strategies for bioreactor systems require improved pre...
In this study, we have conducted kinetics and modelling studies ofCentella asiatica cell growth and ...
This study presents a mathematical model of a batch fermentation of lactose oxidation from a natural...
The aim of this work was to describe growth dynamics, substrate depletion and polygalacturonases pro...
Abstract- In practical situations where direct observation of the morphology and biomass distributio...
This research covers the modeling of the velocity profile of a bioreactor with recycle; the concept ...
A microbroth kinetic model based on turbidity measurements was developed in order to analyze the gro...
This objective of this study is to predict cell masses and substrate consumption in a fed-batch syst...