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Table 3 The results of enzymatic hydrolysis on various lignocellulosic materials at high solids loadings using different hydrolysis modes

From: Fed-batch enzymatic hydrolysis of alkaline organosolv-pretreated corn stover facilitating high concentrations and yields of fermentable sugars for microbial lipid production

Entry

Hydrolysis mode

Lignocellulosic materials

Pretreatment methods

Solids loading

Hydrolysis time (h)

Sugar concentration (g/L)

 

Conversion rate

References

Glucose

Xylose

Cello-oligosaccharides

Xylo-oligosaccharides

TRS

1

Fed-batch

Corncob

Irradiation pretreatment

40% (w/v)

120

235

16

_

_

251

_

[20]

2

Fed-batch

Corn stover

Steam explosion and alkaline hydrogen-peroxide pretreatment

30% (w/v)

144

175

22

20

 

220

Total conversion rate of 60%

[28]

3

Batch with mechanical stirring

Corn stover

NaOH pretreatment and mechanical refining

28% (w/w), equals to 38.9% (w/v)

120

135.2

99.4

7.3

_

270

Monomeric sugar yield of 87%

[12]

4

Fed-batch

Sugarcane bagasse

Alkali pretreatment

33% (w/v)

120

129.5

56.0

9.4

_

200

Glucan conversion of 59.9%

[16]

5

Fed-batch

Corn stover

SMs pretreatment

40% (w/v)

120

146.7

58.7

15.6

25.9

251.8

Glucan and xylan conversions of 89.5% and 88.5%, respectively

This work