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Table 4 Comparison between microwave-assisted batch and fast heating rate flow-through reaction systems: effect of processing time on the product concentrations

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

Reaction conditions

Monomer conc.

Oligomer/polymer conc.

Degradation product conc.

Exp.

T (°C)

t (min)

Ï„ (min)

Q (mL/min)

Mb/Vw (g/L)

Log (KSFS)

Log (KSFL)

Glu (g/L)

Xyl (g/L)

Arab (g/L)

ASL (g/L)

Olig (Cell) (g/L)

Olig (Hemi) (g/L)

Acet (g/L)

Lev (g/L)

HMF (g/L)

F (g/L)

FA (g/L)

2FT

200

20

4.3

7.0

50

4.25

3.58

0.2

1.8

0.4

3.8

0.6

9.3

0.2

0.0

0.0

0.0

0.0

3FT

200

40

8.6

3.5

50

4.55

3.88

1.3

4.5

0.4

3.1

1.6

4.5

2.3

0.0

0.3

0.4

0.8

4FT

200

20

8.6

3.5

100

4.25

3.88

0.5

6.7

0.8

3.7

1.2

13.5

1.5

0.0

0.0

0.6

0.6

2MW

200

20

–

–

50

4.25

4.25

0.9

4.8

1.6

2.2

1.1

2.3

0.2

0.7

<0.1

0.0

0.0

3MW

200

40

–

–

50

4.55

4.55

1.9

3.9

0.0

4.1

0.0

0.0

0.0

3.0

0.2

0.5

0.0

4MW

200

20

–

–

100

4.25

4.25

1.5

8.8

1.3

3.1

1.4

1.3

0.0

2.6

0.0

0.7

0.0

  1. Ï„ 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, 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