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It is none-the-less worth noting that during the latter stages of batch culture with 70 or 100 g glucose L−1 it was producing lipid at 0.5 g L−1 h−1, indicating that it has more potential than has so far been achieved in batch or fed-batch cultivations.
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A higher C/N ratio was achieved in batch fermentations, which stimulated lipid accumulation.
Whereas the highest biomass concentration was observed during fed-batch fermentation, the maximum resveratrol production was achieved in batch mode.
The design of microfluidic chips can enable either very fast or very slow diffusion and so dictate the speed of crystallisation of precipitation reactions in a way that cannot be achieved in batch reactors.
After seven days, approximately 1 × 10 cells/mL can be achieved in batch cultivation.
We speculate that further improvements or optimization of the fermentation process should let us reach the production levels that were achieved in batch cultures.
High biomass and lipid production were achieved in both batch and fed-batch cultures with glucose as carbon source, and a repeated batch process would be expected to be as efficient as a fed-batch or repeated fed-batch process.
Although high biomass and lipid production were achieved in both batch and fed-batch cultures with glucose as carbon source, for lipid production from mixtures of carbohydrates fed-batch cultivation was preferable.
The mixing of the material in the reactor was significantly better in fed-batch than batch mode, and similarly high or higher ethanol yields were achieved in fed-batch mode compared with batch SSF in some cases.
Production of l-lactic acid was achieved in a batch reactor with the immobilized LDH and this preparation resisted 15 reuses without the loss of activity.
The same molecular weight distribution is always attained for both dead and living polymers when the living polymerization is carried out in a continuously stirred tank reactor, which cannot be achieved in a batch reactor.
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CEO of Professional Science Editing for Scientists @ prosciediting.com