2007
DOI: 10.1016/j.jcice.2007.04.005
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On-line estimation of biomass and intracellular protein for recombinant Escherichia coli cultivated in batch and fed-batch modes

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Cited by 9 publications
(5 citation statements)
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“…The state variables defined were biomass concentration X (g L –1 ), substrate concentrations, S b and S f , for the batch and fed-batch phase (g L –1 ), respectively, DO concentration, DO (%), oxygen in the gas phase, O 2 (%), and product concentration, P (g L –1 ). The substrate mass balance for S b was active during the batch phase (0– t b ), and the mass balance for S f was active during the fed-batch phase ( t b – t f ), where S b and S f represent the concentration of the two substrates, glucose and glycerol, in the batch and fed-batch phase, respectively Equations – represent the model equations. where μ b , μ f , q S b , q S f , q O 2,b , q O 2,f , and q P are the specific rates of biomass growth (h –1 ), substrate consumption (g g –1 h –1 ), oxygen consumption (g g –1 h –1 ), and product formation (g g –1 h –1 ), respectively, and the subscripts b and f refer to the batch phase and fed-batch phase, respectively.…”
Section: Modeling and Optimization For E Coli Fermentationmentioning
confidence: 99%
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“…The state variables defined were biomass concentration X (g L –1 ), substrate concentrations, S b and S f , for the batch and fed-batch phase (g L –1 ), respectively, DO concentration, DO (%), oxygen in the gas phase, O 2 (%), and product concentration, P (g L –1 ). The substrate mass balance for S b was active during the batch phase (0– t b ), and the mass balance for S f was active during the fed-batch phase ( t b – t f ), where S b and S f represent the concentration of the two substrates, glucose and glycerol, in the batch and fed-batch phase, respectively Equations – represent the model equations. where μ b , μ f , q S b , q S f , q O 2,b , q O 2,f , and q P are the specific rates of biomass growth (h –1 ), substrate consumption (g g –1 h –1 ), oxygen consumption (g g –1 h –1 ), and product formation (g g –1 h –1 ), respectively, and the subscripts b and f refer to the batch phase and fed-batch phase, respectively.…”
Section: Modeling and Optimization For E Coli Fermentationmentioning
confidence: 99%
“…The highly complex nature of biological processes and dynamic nonlinearity in the responses are the major factors limiting the development of a reliable process model. In spite of its demerits, the model development for a therapeutic protein production process garners much attention owing to its prediction capability and has been attempted by many researchers. Additional challenge includes lack of availability of reliable sensors to measure all the process variables, and a pertinent solution would be the development of soft sensors. ,, In brief, application of advanced monitoring tools and a well-designed process model could significantly enhance consistency in the process and product quality through appropriate real-time control actions. ,, …”
Section: Introductionmentioning
confidence: 99%
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“…Conceptually similar modeling studies addressed the production of amino acids, enzymes, proteins, and other valuable organics in E. coli [58,[521][522][523]. Lall and Mitchell used an S-system model to characterize the reduction of metal in the bacterium Shewanella oneidensis [524].…”
Section: Microbial Studiesmentioning
confidence: 99%
“…Neural networks, which were developed by analogy with the functioning of neurons in living beings (Ko and Wang, 2007;Works, 1989), constitute one other powerful tool for modelling complex systems. The most salient feature of neural networks is their ability to exactly map non-linear behaviour via a series of input (independent variable) and output (dependent variable) data without the need for an exact knowledge of the functional relationships between the two data sets (Emmanouilides and Petyrou, 1997).…”
Section: Introductionmentioning
confidence: 99%