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Table 3 Comparison of heating demand, cooling demand, and integrated heat for the different process configurations

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

 

Unit

Five-stage evaporation

Biogas production

Two-column distillation

Three-column distillation

Two-column distillation

Three-column distillation

Heating demand

MW

64.0

60.3

38.3

35.2

Cooling demand

MW

64.8

59.1

39.9

33.7

Heat integration

MW

91.9

125.9

69.5

103.4

Pinch point

°C

116.4

116.6

116.4

142.9

Minimum energy consumption per kilogram of ethanol

MJ/kgEtOH

18.4

17.2

11.1

10

Process configuration

 

A

B

C

D