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A verification experiment using the optimized medium was carried out.
Maximum mycelial biomass yield of 22.50 g/l was achieved in a 15-l fermenter using the optimized medium.
To obtain larger amounts of Mro APO, M. rotula was cultured in 5-L stirred-tank bioreactors using the optimized medium mentioned above.
HBF-3 production obtained by using the optimized medium was 4.52 g/l, which was in close agreement with the predicted value of 4.55 g/l.
Upon using the optimized medium and conditions followed by photocatalytic treatment an increase in decolorization of higher concentrations of the dye was obtained and a reduction in the COD was achieved (Table 4).
Furthermore, the maximum lutein productivity of 3.45 ± 0.07 mg L− 1 d− 1 was obtained upon cultivation of C. minutissima in a 2-L airlift photobioreactor using the optimized medium with appropriate process conditions.
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The yield of exopolysaccharides obtained using the optimized culture medium was 1.89 ± 0.13 g/L 2.3-fold hig/L 2.3-foldat obtained whigheropthanzed culthat medium was used.
Additionally, the submerged cultivation process was explained using the optimized cultivation medium.
The predicted maximal EPS concentration was 5.40 g/l using the optimized culture medium compositions at 23 °C for 5 days.
Using the optimized polymerization medium of 10 wt % HMImCl in TFE and the elevated temperature of 60 °C, well-controlled pSBMA polymers (PDI ≤ 1.17, relative MW up to 25,478) with targeted degrees of polymerizations (DPs) of 50, 100, and 200 were prepared (Table 1, run 3 5; Figure 1c).
The maximum cell density attained using the optimized Freestyle culture medium was 5.4 × 106 cells/mL in batch mode, almost double of that observed using the unsupplemented medium (2.9 × 106 cells/mL).
More suggestions(15)
using the optimized algorithm
using the optimized well
using the optimized transmission
using the optimized cultivation
using the optimized model
using the optimized control
using the optimized carbon
using the optimized condition
using the optimized photoanode
using the electronic medium
using the new medium
using the optimized recipe
using the gaseous medium
using the optimized cos2α
using the physical medium
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