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Table 2 Growth comparison of Acetobacter sp. CIP 58.66 with glycerol as substrate, at different initial pH

From: Efficient 3-hydroxypropionic acid production by Acetobacter sp. CIP 58.66 through a feeding strategy based on pH control

 

Shake flask culturesa

Biocatalyst productionb

Initial pH

4.0

4.5

5.0

6.5

5.0

DW (gDW L−1)

0.14 ± 0.01

0.33 ± 0.04

1.14 ± 0.04

0.43 ± 0.02

0.88 ± 0.05

Glycerol consumption (%)c

1.0 ± 0.8

4.6 ± 1.9

16.9 ± 0.7

5.8 ± 0.6

18.6 ± 1.7

Biomass yield (\({\text{g}}_{\text{DW}}\, {\text{g}}_{\text{glycerol}}^{-1}\))

NDd

0.83 ± 0.28

0.69 ± 0.05

0.76 ± 0.06

0.40 ± 0.05

Final pH

4.10 ± 0.02

4.58 ± 0.08

5.38 ± 0.03

6.55 ± 0.03

6.94 ± 0.13

µmax,1 (h−1)

0.10 ± 0.01

0.15 ± 0.004

0.18 ± 0.004

0.11 ± 0.004

0.24 ± 0.02

R2

0.94

0.98

0.99

0.98

0.88

µmax,2 (h−1)

0.03 ± 0.002

0.06 ± 0.002

0.09 ± 0.002

0.07 ± 0.001

0.18 ± 0.01

R2

0.92

0.97

0.99

0.99

0.96

  1. aComparison at 30.5 h of culture
  2. bValues at 31 h of culture in bioreactor
  3. cCalculated as the percentage of glycerol initially supplied
  4. dCould not be calculated because no significant glycerol consumption occurred