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Table 2 Comparison of cell growth and the yield of acetone, butanol and ethanol using different ORP controlling strategies

From: Oxidoreduction potential controlling for increasing the fermentability of enzymatically hydrolyzed steam-exploded corn stover for butanol production

ORP value

Starting time for controlling

Fermentation time (h)

End product formed (g/L)

Final Biomass (g/L)

Sugar consumed (%)

Ethanol

Acetate

Butanol

Butyrate

Acetone

glucose

xylose

cellobiose

Uncontrolled

96 h

4.2

7.2

7.6

4.1

2.4

3.1

94.3

80.2

81.5

− 250

0 h

96 h

1.6

2.7

3.2

2.9

0.9

1.7

40.3

30.6

34.1

− 300

0 h

96 h

2.4

3.7

4.1

2.7

1.4

2.2

74.9

50.3

50.4

− 350

0 h

96 h

2.2

4.1

3.2

3.1

2.6

2.5

84.1

64.3

55.8

− 400

0 h

96 h

0.9

1.9

2.6

1.7

1.1

1.8

31.4

26.4

22.1

− 250

24 h

96 h

3.1

5.0

4.4

4.9

2.8

2.8

87.4

80.7

79.7

− 275

24 h

90 h

5.1

5.4

7.6

3.7

2.6

3.4

96.4

84.4

80.6

− 300

24 h

90 h

5.6

4.2

8.8

3.5

3.1

3.8

97.2

84.2

82.1

− 350

24 h

90 h

5.9

3.9

10.2

2.7

2.0

4.6

98.7

86.5

88.1

− 400

24 h

96 h

1.7

3.1

3.7

2.3

0.4

2.9

86.4

76.4

70.4