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Table 1 Composition of the process stream fed to the distillation column

From: Simulation of the downstream processing in the ethanol production from lignocellulosic biomass with ASPEN Plus® and IPSEpro

Component

Mass fraction (wt%)

ASPEN Plus® simulation

Formula

Type

Component name

Water

80.35%

H2O

Conv

Water

Ethanol

4.007%

C2H6O

Conv

Ethanol

Acetic acid

0.63%

C2H4O2

Conv

Acetic-acid

Furfural

0.30%

C5H4O2

Conv

Furfural

Glycerol

0.085%

C3H8O3

Conv

Glycerol

CO2

0.078%

CO2

Conv

Carbon-dioxide

Cellulose

0.575%

C6H10O5

Solid

Glucan

Hemi-cellulose

0.27%

C5H8O4

Solid

Xylan

Lignin

4.15%

C x H x O x

Solid

Lignin

C5-monosaccharides

4.66%

C5H10O5

Conv

d-xylose

C6-monosaccharides

0.00%

C6H12O6

Conv

Dextrose

Yeast

0.56%

CH x N x O x S x

Solid

Biomass

Enzymes

0.18%

CH x O x N x

Conv

Zymo

Ash

1.385%

SIO2

Solid

Silicon dioxide

Extractives

1.85%

C18H32O2

Conv

Linoleic acid

Plant protein

0.92%

C5H9NO4

Conv

l-glutamic acid

Sum

100%

H2O

Conv

Water