Ultrafiltration (UF) of desizing wastewater containing PVA (MW=10 000-70 00
0), which is a synthetic and nonbiodegradable sizing agent, was investigate
d to develop the technology for size recovery from textile effluents. Using
bench-scale UF system with polysulfone hollow fiber membranes (MWCO= 10 00
0 and 30 000), membrane performance, i.e. permeate flux and rejection rate,
was examined with the variation of operating parameters such as PVA concen
tration, transmembrane pressure, temperature, pH, cross-flow velocity, and
prefilter sizes. From the experimental results, it was confirmed that the u
ltrafiltration of desizing wastewater through polysulfone membranes is cont
rolled by the well-known phenomena of concentration polarization caused by
gel-layer formation. The permeate flux exhibited asymptotic behavior beyond
a certain transmembrane pressure, 2.0 kg cm(-2), and the rejection rate wa
s over 99 %. However, the flux at high concentration ranges (> 3.0 wt % of
PVA) did not satisfy a linear semi-logarithmic relationship predicted by th
e gel-layer model, that is, upward limiting flux was observed. Prefilter tr
eatment before UF process considerably reduced the suspended solids in the
feed (about 70-80 %), and it appears to better control the ultrafiltration
of desizing wastewater. In basic conditions (pH=9-10), the permeate flux wa
s increased almost two times at the expense of a slight decrease of rejecti
on rate. With respect to membrane MWCO, there was distinct difference in pe
rmeate flux between MWCO=10 000 and 30 000.