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Table 2 Glucan and xylan recovery of the dry pretreatment in the helically agitated reactor

From: Helically agitated mixing in dry dilute acid pretreatment enhances the bioconversion of corn stover into ethanol

Pretreatment conditions

Cellulose content before pretreatment (%)

Xylan content before pretreatment (%)

Glucan recovery (%)

Xylan recovery (%)

Raw corn stover

37.15 ± 0.22

19.86 ± 0.56

-

-

Changing temperature

    

165°C , 2.5%, 3 minutes

38.04 ± 2.04

8.57 ± 2.26

100.09

94.24

175°C , 2.5%, 3 minutes

37.23 ± 0.75

5.28 ± 0.02

96.69

79.32

185°C , 2.5%, 3 minutes

40.93 ± 0.06

2.93 ± 0.16

96.50

62.00

Changing acid usage

    

185°C, 1.5%, 3 minutes

37.71 ± 1.07

6.48 ± 0.18

92.05

78.89

185°C, 2.0%, 3 minutes

37.41 ± 0.06

4.16 ± 0.08

96.63

74.91

185°C, 2.5%, 3 minutes

40.93 ± 0.06

2.93 ± 0.16

96.50

62.00

185°C, 3.0%, 3 minutes

38.48 ± 0.40

2.52 ± 0.17

73.97

43.18

185°C, 3.5%, 3 minutes

36.85 ± 1.25

1.79 ± 0.21

75.12

36.37

185°C, 4.0%, 3 minutes

35.98 ± 1.10

1.05 ± 0.10

65.53

29.75

Changing residue time

    

185°C, 2.5%, 1 minute

41.52 ± 5.88

4.06 ± 0.41

92.71

64.08

185°C, 2.5%, 3 minutes

40.93 ± 0.06

2.93 ± 0.16

96.50

62.00

185°C, 2.5%, 5 minutes

38.54 ± 1.88

2.93 ± 0.08

82.78

57.29

185°C, 2.5%, 10 minutes

39.29 ± 0.75

2.21 ± 0.22

76.44

42.96

Changing agitation rate

    

185°C, 2.5%, 3 minutes, 10 rpm

40.23 ± 2.59

3.00 ± 0.19

84.81

54.03

185°C, 2.5%, 3 minutes, 30 rpm

38.41 ± 0.58

2.86 ± 0.87

93.20

64.19

185°C, 2.5%, 3 minutes, 50 rpm

40.93 ± 0.06

2.93 ± 0.16

96.50

62.00