Abstract

Surface modification of polysulfone ultrafiltration membranes was performed via addition of an anionic polymer flocculant based on acrylamide and sodium acrylate (PASA) to the coagulation bath upon membrane preparation by non-solvent induced phase separation (NIPS). The effect of PASA concentration in the coagulant at different coagulation bath temperatures on membrane formation time, membrane structure, surface roughness, hydrophilic-hydrophobic balance of the skin layer, surface charge, as well as separation and antifouling performance was studied. Scanning electron microscopy (SEM), atomic force microscopy (AFM), Fourier transform infrared (FTIR) spectroscopy, contact angle and zeta potential measurements were utilized for membrane characterization. Membrane barrier and antifouling properties were evaluated in ultrafiltration of model solutions containing human serum albumin and humic acids as well as with real surface water. PASA addition was found to affect the kinetics of phase separation leading to delayed demixing mechanism of phase separation due to the substantial increase of coagulant viscosity, which is proved by a large increase of membrane formation time. Denser and thicker skin layer is formed and formation of macrovoids in membrane matrix is suppressed. FTIR analysis confirms the immobilization of PASA macromolecules into the membrane skin layer, which yields improvement of hydrophilicity and change of zeta potential. Modified membrane demonstrated better separation and antifouling performance in the ultrafiltration of humic acid solution and surface water compared to the reference membrane.

Highlights

  • In recent years, consumption of fresh water has been increased due to the population growth and rapid industry development [1]

  • The surface of the skin layer of A25 and A-0.3-25 membranes was revealed to demonstrate negative charge being higher by absolute value for the modified membrane (Table 3). 0.1 wt % PASA addition to the coagulation bath yields the significant improvement of membrane antifouling performance: Flux recovery ratio (FRR) increases from 87.1% for the reference membrane up to 98% for A-0.3-25 membrane

  • Anionic polymeric flocculant based on acrylamide and sodium acrylate (PASA) produced on commercial scale was used for modification of polysulfone ultrafiltration membranes via addition to the aqueous coagulation bath during membrane preparation by non-solvent induced phase separation (NIPS)

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Summary

Introduction

Consumption of fresh water has been increased due to the population growth and rapid industry development [1]. Membranes 2020, 10, 264 to the increased energy demand, flux decline, deterioration of separation performance and decrease of membrane lifetime [3,4]. This yields a significant increase of operation cost of water treatment and purification. Several strategies have been applied to diminish effect of membrane fouling: feed water pretreatment (pre-coagulation, pre-oxidation) [6,7,8,9], tuning the membrane structure to decrease “membrane-foulant” interactions [10], development of different cleaning protocols (air sparging, backflushing and cleaning-in-place) [1,4]

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