Skip to main content

Table 2 Comparison between microwave-assisted batch and fast heating rate flow-through reaction systems: effect of operative temperature on the product yields (% w/w)

From: Autohydrolysis pretreatment of Arundo donax: a comparison between microwave-assisted batch and fast heating rate flow-through reaction systems

Reaction conditions

Xtot (%)

Monomer yield

Oligomer/polymer yield

Degradation product yield

Exp.

T (°C)

t (min)

Ï„ (min)

Q (mL/min)

Mb/Vw (g/L)

Log (KSFS)

Log (KSFL)

YGlu (%)

YXyl (%)

YArab (%)

YASL (%)

Yolig(Cell) (%)

Yolig(Hemi) (%)

YAcet (%)

YLev (%)

YHMF (%)

YF (%)

YFA (%)

1FT

180

20

4.3

7.0

50

3.66

2.99

28.5

0.2

0.6

0.6

7.7

1.3

15.2

0.4

0.0

0.0

0.0

0.1

2FT

200

20

4.3

7.0

50

4.25

3.58

40.3

0.4

4.6

0.9

9.7

1.7

24.0

0.6

0.0

0.0

0.2

0.0

1MW

180

20

–

–

50

3.66

3.66

29.0

0.7

2.2

1.7

4.4

4.8

9.8

0.0

0.4

0.0

0.0

0.0

2MW

200

20

–

–

50

4.25

4.25

34.0

1.8

9.8

3.2

4.5

2.3

4.5

0.5

1.4

0.0

0.0

0.0

  1. τ average residence time, Q water flow rate, M b /V w biomass to water ratio (w/vol), KSF S kinetic severity factor for the solid phase, KSF L kinetic severity factor for the liquid phase, X tot total solubilized fraction of the initial biomass calculated by Eq. 8, Glu glucose, Xyl xylose, Arab arabinose, ASL acid-soluble lignin, Cell cellulose, Hemi hemicellulose, Acet acetic acid, Lev levulinic acid, HMF hydroxymethilfurfural, F furfural, FA formic acid