Add to ORKGAbstract A model describing the oxygen dynamics in an E. coli fed-batch cultivation is presented. In a linearised version the parameters are estimated and validated with good results. The model is used to discuss the guidelines for feed controller tuning derived in (Åkesson et al., 2001b). Key words Bio-reactor model, parameter estimation, E. coli fermentation. 1
Fermentation systems are often highly nonlinear, with poorly understood dynamic behaviour of the rea...
Two hypotheses for acetate formation in Escherichia coli are used to obtain relations between glucos...
A new adaptive asymptotic biomass observer for fed-batch E. coli growth on glucose is proposed. The ...
The specific growth rate is one of the most important process variables characterizing the state of ...
The specific growth rate is one of the most important process variables characterizing the state of ...
A study of the feasibility of perturbation-based control methods in industrial fed-batch fermentatio...
In this work, three competing unstructured mathematical models for the biomass growth by recombinant...
International audienceThis work proposes a Generic Model Control (GMC) strategy to regulate biomass ...
International audienceThis work proposes a Generic Model Control (GMC) strategy to regulate biomass ...
In this work, a genetic algorithm was used to estimate both yield and kinetic coefficients of an uns...
Abstract Background Microbial production of biofuels and biochemicals from renewable feedstocks has ...
Model-based fed-batch cultivation approach of non-recombinant Escherichia coli bacteria are presente...
An overall model describing the dynamic behavior of fed-batch E. coli processes for protein producti...
Abstract: A model-based adaptive linearizing control law was derived for the regulation of the aceta...
A new functional state, namely dissolved oxygen limitation state for both bacteria Escherichia coli ...
Fermentation systems are often highly nonlinear, with poorly understood dynamic behaviour of the rea...
Two hypotheses for acetate formation in Escherichia coli are used to obtain relations between glucos...
A new adaptive asymptotic biomass observer for fed-batch E. coli growth on glucose is proposed. The ...
The specific growth rate is one of the most important process variables characterizing the state of ...
The specific growth rate is one of the most important process variables characterizing the state of ...
A study of the feasibility of perturbation-based control methods in industrial fed-batch fermentatio...
In this work, three competing unstructured mathematical models for the biomass growth by recombinant...
International audienceThis work proposes a Generic Model Control (GMC) strategy to regulate biomass ...
International audienceThis work proposes a Generic Model Control (GMC) strategy to regulate biomass ...
In this work, a genetic algorithm was used to estimate both yield and kinetic coefficients of an uns...
Abstract Background Microbial production of biofuels and biochemicals from renewable feedstocks has ...
Model-based fed-batch cultivation approach of non-recombinant Escherichia coli bacteria are presente...
An overall model describing the dynamic behavior of fed-batch E. coli processes for protein producti...
Abstract: A model-based adaptive linearizing control law was derived for the regulation of the aceta...
A new functional state, namely dissolved oxygen limitation state for both bacteria Escherichia coli ...
Fermentation systems are often highly nonlinear, with poorly understood dynamic behaviour of the rea...
Two hypotheses for acetate formation in Escherichia coli are used to obtain relations between glucos...
A new adaptive asymptotic biomass observer for fed-batch E. coli growth on glucose is proposed. The ...