posted on 2009-08-07, 12:26authored byJ.P. Robinson, Steve Tarleton, C.R. Millington, Arian Nijmeijer
A dense polydimethylsiloxane (PDMS) membrane was used to assess the flux and separation
performance of a range of solutes (e.g. poly-nuclear aromatics and organometallics) and organic
solvents (e.g. heptane and xylene). Solvent flux was modelled with the Hagen-Poiseuille equation
and found to fit the model well, with the degree of swelling influencing the effective pore size and
porosity of the membrane.
The rejection mechanism for low-polarity solutes was found to be predominantly size exclusion.
The rejection varied with solvent type and rejections were higher in poorer-swelling solvents. For
instance, the rejection of 9,10 Diphenylanthracene was 2% in a pure heptane solvent compared
with 15% in xylene. It is postulated that dense PDMS membranes exhibit the characteristics of a
porous structure when swollen with solvent, and that the degree of swelling impacts on the
separation performance of the membrane. A comparison between the Hildebrand solubility
parameters for the PDMS membrane and the challenge solvent was found to be a good indicator
of flux/rejection performance.
History
School
Aeronautical, Automotive, Chemical and Materials Engineering
Department
Chemical Engineering
Citation
ROBINSON, J.P. ... et al, 2004. Evidence for swelling-induced pore structure in dense PDMS nanofiltration membranes. Filtration, 4 (1), pp. 50-56.