Purification of crude fatty acids using a PDMS-based composite membrane

membrane. During processing crude FA, FA preferentially permeated through the membrane increasing
FA content from 86.5% to 90% while color compounds were substantially reduced (92.8%) improving
the overall purity of FA. Studies with crude FA-used frying oil system showed that a good correlation
existed between reciprocal of viscosity and permeate flux, both total as well as FA fluxes. As expected,
FA flux showed a significant improvement in crude FA–hexane system besides improving the FA content
to the extent of 97% without significantly affecting reduction of color (83–88%). Increase in pressure
as well as hexane dilution improved the FA flux but marginally affected purity and color reduction.
Preferential permeation was observed over a wide of hexane dilution almost throughout the entire range
of X (weight ratio of FA in feed) but to a varying degree and the positive coupling was strong at very
low and high concentrations of hexane and FA. A maximal JFA (FA flux) of 4.4 kg/(m2 h) was obtained at
X = 0.3 demonstrating an improvement of 11 fold achievable with appropriate hexane dilution at 1 MPa. In
both crude FA-used frying oil and crude FA–hexane systems, the mean molar total permeate flux [ln(Jm)]
showed a linear dependency on the mean molar volume [Vm] of permeate, which is in agreement with
solution-diffusion or regular solution model.