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The models used gave the best fit for butanol production, biomass and glucose consumption for both flask scale and bioreactor scale up.
The culture medium was designed at the flask scale, reaching an astaxanthin cellular content of 3.0 mg g−1 cell weight and a volumetric yield of 119 mg L−1 broth.
The experimental data of scale up in 5 L bioreactor and flask scale were fitted to kinetic mathematical models published in the literature to estimate the kinetic parameters of the fermentation.
Further media optimization trials in the shake flask scale followed the temperature comparison.
We demonstrated that the MTP scale assay was predictive of shake flask scale results.
Further optimization of SYN6.4 medium was performed in fed-batch fermentations at the shake flask scale.
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The culture medium for Rhodothermus marinus was optimised on a shake-flask scale by using statistical factorial designs for enhanced production of a highly thermostable α-l-arabinofuranosidase (AFase).
Production of 115.12 g/L was achieved in shake-flask scale, whereas the concentration of LA in a bioreactor was 110 g/L.
Later, Zhou overexpressed dxs and idi genes along with introducing ads (ads encodes the synthase which cyclizes farnesyl diphosphate into amorphadiene) in B. subtilis and got the highest yield of amorphadiene (∼20 mg/L) at shake-flask scale.
Under optimum conditions of the newly developed EDGE process, an ethanol yield of 402 L/MT (dry basis) or 2.17 gallons/bushel of barley was achieved on the shake-flask scale.
In this paper, we report on the development of a shake-flask scale fermentation process for production of ethanol from Thoroughbred, which is an improved version of hulled winter barley with significantly higher starch contents and test weights (lb per bushel) compared to regular feed barley and is available in the USA [ 17].
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