The recovery of phenol from aqueous solutions with CYANEX (R) 923 was studi
ed. Classical dispersive extraction and three membrane extraction-stripping
systems (bulk liquid membranes, three-phase hollow fiber contactor and two
hollow fiber modules set-up) were used. It was found that CYANEX (R) 923 w
as a convenient carrier for recovery of phenol from aqueous streams in extr
action-stripping membrane processes. The problem of emulsion formation, so
important in dispersive extraction, was avoided. Both mass transfer experim
ents in different membrane systems and measurement of the dynamic interfaci
al tension demonstrated importance of the interfacial phenomena occurring i
n the stripping stage. A blocking of this interface was observed that resul
ted in a decrease of phenol mass transfer.