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The ethanol yields obtained from all tested glycerol concentrations were approaching theoretical yield when the batch fermentation was performed at optimized conditions.
Batch fermentation was performed at 30 °C, in a 50 mL stirred tank bioreactor with controlled heating and stirring, built in the laboratory of UNL (Argentina).
Batch fermentation was performed in a 10 l bioreactor (B-Braun).
Anaerobic batch fermentation was performed in either 3 l Biostat Bio Reactors (B.
Batch fermentation was performed using sugarcane juice as the carbon source.
a Batch fermentation was performed in 5 L fermentor containing 3 L medium and cultivated at 55°C controlling pH as 6.5 with 5 M of sodium hydroxide.
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Batch fermentation was perform with 200 g/l glucose concentration.
After validation of the model in flasks, assays of batch fermentation were performed in a 7 l Infors HT fermenter (Infors AG, Rittergasse 27, 4013 Bottmingen, Switzerland) with a working volume of 3.5 l under the optimized culture conditions.
In order to optimize the fermentation outcomes, fed-batch fermentation was performed with hydrolyzed molasses in PFB, giving 91.89 ± 4.59 g l 1 of propionic acid at 254 h.
Finally, a fed-batch fermentation was performed to evaluate the FFAs production in a scaleable process.
To improve 2,3-butanediol production from sugarcane molasses, a fed-batch fermentation was performed with EMY-70S.
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batch fermentation was found
batch reactor was performed
batch normalization was performed
batch purification was performed
batch alignment was performed
batch phase was performed
batch adjustment was performed
batch fermentation was chosen
batch fermentation was run
batch fermentation was revealed
batch cultivation was performed
batch hydrolysis was performed
batch fermentation was carried
batch acidogenesis was performed
batch fermentation was prepared
batch fermentation was adopted
batch culturing was performed
batch fermentation was started
batch analysis was performed
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