Butanol recovery from model solution/fermentation broth by pervaporation: evaluation of membrane performance

Citation
N. Qureshi et Hp. Blaschek, Butanol recovery from model solution/fermentation broth by pervaporation: evaluation of membrane performance, BIO BIOENER, 17(2), 1999, pp. 175-184
Citations number
21
Categorie Soggetti
Environment/Ecology
Journal title
BIOMASS & BIOENERGY
ISSN journal
09619534 → ACNP
Volume
17
Issue
2
Year of publication
1999
Pages
175 - 184
Database
ISI
SICI code
0961-9534(1999)17:2<175:BRFMSB>2.0.ZU;2-H
Abstract
This is an overview of butanol separation from model solutions and fermenta tion broth by pervaporation. It is difficult to compare different authors' work on butanol separation because of the number of variables involved. The se variables include type of membrane, membrane thickness, feed temperature , condensation temperature, vacuum or sweep gas, feed butanol concentration , etc. For comparison we have calculated the butanol concentration in the p ermeate and butanol flux from the data given by various authors. Polytetraf luoroethylene (PTFE) membrane and polypropylene (PP) membrane pass a large amount of water through the membrane. Fermentation broth was found to decre ase flux and selectivity of a liquid membrane. A silicalite membrane offers high butanol flux and high butanol concentration when using fermentation b roth. A thin polydimethylsiloxane (PDMS) membrane offers high flux and low selectivity, while a thick membrane offers high selectivity and low flux. ( C) 1999 Elsevier Science Ltd. All rights reserved.