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Table 5 Effect of different treating steps on the concentration of PHL components

From: A process for purifying xylosugars of pre-hydrolysis liquor from kraft-based dissolving pulp production process

PHL

Lignin (g/L)

Acetic acid (g/L)

HMF (g/L)

Xylose (g/L)

Xylan (g/L)

Xylosugars (g/L)

Origin PHL

9.7 ± 0.49

6.2 ± 0.26

1.9 ± 0.1

12.3 ± 0.68

23.3 ± 0.79

35.6 ± 1.47

PHL-1st

5.7 ± 0.29

11.7 ± 0.59

1.0 ± 0.04

12.1 ± 0.56

23.1 ± 0.99

35.2 ± 1.55

PHL-2nd

2.6 ± 0.17

11.2 ± 0.34

0.1

11.8 ± 0.47

21.3 ± 0.89

33.1 ± 1.36

PHL-4th

0.9 ± 0.07

12.7 ± 0.55

0

11.6 ± 0.52

20.5 ± 0.98

32.1 ± 1.5

Removal (%)

90.7

100

5.7

12.0

9.9