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Separation of dilute aqueous butanol and acetone solutions by pervaporation through liquid membranes
Author(s) -
Matsumura Masatoshi,
Kataoka Hiroshi
Publication year - 1987
Publication title -
biotechnology and bioengineering
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 1.136
H-Index - 189
eISSN - 1097-0290
pISSN - 0006-3592
DOI - 10.1002/bit.260300712
Subject(s) - pervaporation , oleyl alcohol , membrane , acetone , butanol , chemistry , chromatography , aqueous solution , extraction (chemistry) , selectivity , surface tension , chemical engineering , stripping (fiber) , alcohol , ethanol , permeation , organic chemistry , materials science , catalysis , biochemistry , physics , quantum mechanics , engineering , composite material
A simultaneous extraction‐stripping process is proposed for separating volatile products from fermentation broths, it is based on pervaporation through a liquid membrane supported with a hydrophobic porous membrane. The liquid membrane prepared with oleyl alcohol was selected as the most suitable for separating volatile products resulting from acetone‐butanol fermentation. The separation performance and stability of the oleyl alcohol liquid membrane were investigated by using dilute aqueous butanol and acetone solutions. The oleyl alcohol liquid membrane was found to be superior by far in both selectivity and permeability of butanol to the better known silicone rubber membrane in its high selectivity for alcohols. Using the oleyl alcohol liquid membrane, the dilute aqueous butanol solutions of around 4 g/L obtained in acetone‐butanol fermentation could be concentrated up to 100 times. The stability of this liquid membrane was also quite good as long as the surface tension of the feed solution was less than the critical surface tension of the support membrane. No change in the separation performance was found after the continuous usage in a long period of 100 h.