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Korean Journal of Chemical Engineering

, Volume 13, Issue 6, pp 612–619 | Cite as

Mathematical modeling of fed-batch butanol fermentation with simultaneous pervaporation

  • Chang-Ho Park
  • Charles Q. Geng
Article

Abstract

A mathematical model was developed to describe a fed-batch acetone-butanol-ethanol (ABE) fermentation with simultaneous pervaporation. The model predicted satisfactorily batch or fed-batch fermentation with or without pervaporalion by introducing a parameter reflecting cell activity loss during fed-batch fermentation with pervaporation. The model also predicted the effect of membrane area, membrane thickness, and sweep air flow rate on glucose consumption rate and residual butanol concentration in the fermentation broth. Glucose consumption rate increased by 30% by either doubling the membrane area or decreasing membrane thickness by half.

Key words

Mathematical Model Butanol Fermentation Prevaporation Membrane Area and Thickness Sweep Air Flow Rate 

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Copyright information

© Korean Institute of Chemical Engineering 1996

Authors and Affiliations

  • Chang-Ho Park
    • 2
    • 1
  • Charles Q. Geng
    • 2
  1. 1.Department of Chemical EngineeringThe Institute of Material Science and Technology,Kyung Hee UniversityYongin-SiKorea
  2. 2.The Pillsbury Technology Center330 Univ. Ave. S.E.MinneapolisUSA

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