Applied Biochemistry and Biotechnology

, Volume 20, Issue 1, pp 621–633

Computer simulation of the dartmouth process for separation of dilute Ethanol/Water mixtures

Authors

  • José L. Torres
    • Thayer School of EngineeringDartmouth College
  • Hans E. Grethlein
    • Thayer School of EngineeringDartmouth College
  • Lee R. Lynd
    • Thayer School of EngineeringDartmouth College
Session 3 Bioengineering research

DOI: 10.1007/BF02936513

Cite this article as:
Torres, J.L., Grethlein, H.E. & Lynd, L.R. Appl Biochem Biotechnol (1989) 20: 621. doi:10.1007/BF02936513

Abstract

High energy costs are associated with the recovery of ethanol from fermentation broths. This paper discusses a computer simulation of the Dartmouth Process, which aims to reduce these costs by the use of IHOSR distillation, extensive heat integration, and extractive distillation using a salt.

To resolve the uncertainty in modeling alcohol-water-salt vapor-liquid equilibrium, a new and more accurate activity coefficient model was used. An Aspen™ model was used to generate capital and energy costs for a range of ethanol concentrations in the feed. Simulation results show that the Dartmouth Process offers substantial economic advantages over benzene azeotropic distillation, particularly at low feed concentrations.

Index Entries

Ethanol separation activity coefficients computer simulation

Copyright information

© Humana Press Inc. 1989