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Table 2 Comparison between free cell and immobilized cell batch fermentation for butyric acid production with differential operating modes

From: Enhanced production of butyric acid through immobilization of Clostridium tyrobutyricum in a novel inner disc-shaped matrix bioreactor

Fermentation parameter

Free-cell fermentation mode

Immobilized cell fermentation mode

Batch

Fed-batch

Batch

Fed-batch

Fermentation time (h)

30 ± 2

107 ± 2

24 ± 2

85 ± 2

Fermentable sugar utilized (g/L)

43.55 ± 2.17

153.47 ± 2.42

47.52 ± 2.13

150.68 ± 2.51

Fermentable sugar utilization rate (g/L·h)

1.45 ± 0.03

1.43 ± 0.04

1.98 ± 0.03

1.77 ± 0.03

Butyrate concentrations (g/L)

18.48 ± 0.92

58.32 ± 3.01

21.47 ± 1.07

61.87 ± 2.37

Butyrate yield (g/g)

0.42 ± 0.01

0.38 ± 0.01

0.45 ± 0.01

0.42 ± 0.01

Butyrate productivity (g/L·h)

0.62 ± 0.02

0.55 ± 0.02

0.85 ± 0.03

0.73 ± 0.01

Acetate concentration (g/L)

3.46 ± 0.16

5.46 ± 0.21

2.49 ± 0.17

4.23 ± 0.18

Butyrate/acetate ratio (g/g)

5.34 ± 0.23

10.68 ± 0.46

8.62 ± 0.38

14.61 ± 0.57

  1. Data are presented as the mean ± SD (n = 3)