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Digestion processes were performed in batch and semicontinuous reactors.
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The reactor was operated in both batch and semicontinuous modes.
Using said device, batch and semicontinuous cultures of P. lutheri were maintained at maximum growth rates and biomass productivities – hence avoiding photoinhibition, and consequent waste of radiant energy.
A solvent screening criterion was developed based on the maximum product concentration attainable for the assessment of batch and semicontinuous multicomponent extractive fermentations.
Cationic latexes based on styrene and butyl acrylate using cetyl trimethyl ammonium bromide (CTAB) as surfactant were carried out using both batch and semicontinuous emulsion polymerization.
Its application to batch and flow reactors is discussed.
We found that strains' product yields are similar in both batch and fedbatch reactors.
The reactions in batch and fed-batch reactors are discussed.
In batch and semi-batch reactors, the heat of reaction ˙QR is normally estimated using calorimetry.
This work deals with modelling of emulsion polymerization processes using batch and semi-batch reactors.
The biofilms were cultivated with lactate and sulfate in a continuously fed biofilm reactor, and compared to both batch and reactor planktonic populations.
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