Investigation of ultrafiltration (UF) performance for the purpose of removi
ng the colour of three different effluents coming from the dyeing cycle of
a tannery industry was carried out using four polyethersulphone (PES) membr
anes with molecular weight cut-offs (MWCO) of 40, 10, 5 and 3 kDa. A closed
-loop recycle (CLR) and batch (B) modes of operation were used. For the fir
st mode of operation, the evolution of permeate flux and colour rejection v
s. time of operation was evaluated. For the batch concentration experiments
, attention was focused upon the evolution of the rejection and/or concentr
ation of colour with the volume reduction factor (VRF) and on the decrease
of the permeate flux as a function of VRF for all the membranes under study
. All experiments showed the occurrence of concentration polarization and a
dsorptive fouling with a pronounced effect for the membranes with higher MW
CO. Due to that, the 40 and 10 kDa membranes did not offer a significant re
gaining of permeate productivity. High-colour and low-solids rejections wer
e observed for all the experiments, showing a marked dependence on the type
of effluent used.