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Table 1 The comparison of integrated process and typical anaerobic fermentation for BA production

From: A techno-practical method for overcoming the biotoxicity and volatility obstacles of butanol and butyric acid during whole-cell catalysis by Gluconobacter oxydans

Strain

Substrate

Time (h)

Production (g/L)

Productivity (g/L/h)

Yield (%)

Comparison (%)

References

C. tyrobutyricum

Glucose

74

44.0

0.6

38

Zhang et al. [26]

C. tyrobutyricum

Glucose

120

43.0

0.4

47

39.3

Liu et al. [13]

C. tyrobutyricum

Sugarcane molasses

34.6

0.6

− 1.6

Jiang et al. [27]

C. tyrobutyricum

Flour hydrolysate

50

62.8

1.3

45

+ 111.9

Fayolle et al. [28]

C. butyricum

Whey

42

18.6

0.4

39

− 25.4

Vandak et al. [29]

C. butyricum

Saccharose

30

7.3

0.2

24

− 59.3

Zigova et al. [30]

G. oxydans (AS-BR)

Butanol

24

30.7

1.3

35

+ 116.9

G. oxydans (SOS-BR)

Butanol

24

33.2

1.4

96

+ 133.9

G. oxydans (Integrated process)

Butanol

60

135.3

2.3

95

+ 283.1

  1. Where time represents bioreactor tank operation time and the productivity is calculated based on 1-L fermentation broth. During comparison, the productivity of BA production from glucose by C. tyrobutyricum is set as 1