Amenaghawon, N. A.
Department of Chemical Engineering Faculty of Engineering University of Benin, PMB 1154, Benin City, Nigeria
Osayuki-Aguebor, W.
Department of Chemical Engineering Faculty of Engineering University of Benin, PMB 1154, Benin City, Nigeria
Ebewele, O. E.
Department of Chemical Engineering Faculty of Engineering University of Benin, PMB 1154, Benin City, Nigeria
ABSTRACT
Ethanol
fermentation becomes inhibitory to microbial growth at elevated ethanol
concentrations. This problem could be alleviated by continuous removal of
ethanol from the broth during fermentation and this could increase productivity
and potentially reduce the cost of ethanol recovery during distillation. The
use of in situ gas stripping as a means of recovering ethanol from fermentation
broth was analysed using a batch fermentation model. The Hinshelwood specific
growth rate model and the Luedeking-Piret production model were used to
formulate and simulate the fermentation model. The model was simulated to
investigate the effect of stripping gas flow rate on the fermentation process. Results of gas stripping
analysis showed that increasing the stripping gas flow rate enhanced the
stripping of ethanol from the fermentation broth thereby keeping its
concentration below inhibitory levels. This ensured that the fermentation could
be continued for long periods. Almost 50% ethanol recovery was achieved when a
stripping gas flow rate of 80 L/h was used. The maximum water fraction in the
gas phase was 1% which was not enough to dilute the gas phase.These results
show the possibility of recovering ethanol from fermentation broth by gas
stripping.
Keywords: Bioethanol, Fermentation, Luedeking-Piret model, Geobacillus thermoglucosidasius, Gas stripping
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Published
Friday, December 18, 2015
Issue
Vol. 1 No. 2, DEC 2015
Article Section
GENERAL
The contents of the articles are the sole opinion of the author(s) and not of UJET.
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