A morphologically structured model is proposed to describe penicillin production in fed-batch cultivations. The model accounts for the effects of dissolved oxygen on cell growth and penicillin production and variations in volume fractions of abiotic and biotic phases due to biomass formation. Penicillin production is considered to occur in the subapical hyphal cell compartment and to be affected by availability of glucose and oxygen. As it stands, the model provides a wide range of applicability in terms of operating conditions. The model has been tested for various conditions and has given satisfactory results. A series of glucose feeding profiles have been considered to demonstrate the capabilities of the proposed model. It is concluded t...
The mathematical model for the penicillin G fed-batch fermentation proposed by Heijnen et al. (1979)...
In large-scale production reactors the combination of high broth viscosity and large broth volume le...
In large-scale bioreactors, there is often insufficient mixing and as a consequence, cells experienc...
The development and implementation of control strategies for bioreactor systems require improved pre...
A systematic and practical approach is developed for the optimization of the fed-batch production of...
In this paper, an updated unstructured mathematical model for the penicillin G fed-batch fermentatio...
In this paper, an updated unstructured mathematical model for the penicillin G fed-batch fermentatio...
This study focuses on the metabolic impacts of simultaneous glucose and oxygen concentration gradien...
In this paper, an updated unstructured mathematical model for the penicillin G fed-batch fermentatio...
This paper proposes a cell age model forPenicillium chrysogenum fed-batch cultivation to supply a qu...
This paper proposes a cell age model forPenicillium chrysogenum fed-batch cultivation to supply a qu...
This work presents a deterministic non-structured model of the penicillin production process. For th...
In large-scale production reactors the combination of high broth viscosity and large broth volume le...
In large scale fermentors the cultivated cells are exposed to dynamic changes in the nutrient concen...
The mathematical model for the penicillin G fed-batch fermentation proposed by Heijnen et al. (1979)...
The mathematical model for the penicillin G fed-batch fermentation proposed by Heijnen et al. (1979)...
In large-scale production reactors the combination of high broth viscosity and large broth volume le...
In large-scale bioreactors, there is often insufficient mixing and as a consequence, cells experienc...
The development and implementation of control strategies for bioreactor systems require improved pre...
A systematic and practical approach is developed for the optimization of the fed-batch production of...
In this paper, an updated unstructured mathematical model for the penicillin G fed-batch fermentatio...
In this paper, an updated unstructured mathematical model for the penicillin G fed-batch fermentatio...
This study focuses on the metabolic impacts of simultaneous glucose and oxygen concentration gradien...
In this paper, an updated unstructured mathematical model for the penicillin G fed-batch fermentatio...
This paper proposes a cell age model forPenicillium chrysogenum fed-batch cultivation to supply a qu...
This paper proposes a cell age model forPenicillium chrysogenum fed-batch cultivation to supply a qu...
This work presents a deterministic non-structured model of the penicillin production process. For th...
In large-scale production reactors the combination of high broth viscosity and large broth volume le...
In large scale fermentors the cultivated cells are exposed to dynamic changes in the nutrient concen...
The mathematical model for the penicillin G fed-batch fermentation proposed by Heijnen et al. (1979)...
The mathematical model for the penicillin G fed-batch fermentation proposed by Heijnen et al. (1979)...
In large-scale production reactors the combination of high broth viscosity and large broth volume le...
In large-scale bioreactors, there is often insufficient mixing and as a consequence, cells experienc...