Abstract

This work was focused on the study of hypochlorite treatment on the pore size distribution of membranes. To this end, ultrafiltration membranes from a polysulfone/polyvinylpyrrolidone blend with a sponge-like structure were fabricated and exposed to hypochlorite solutions with different active chlorine concentrations for 4 h at ambient temperature. Liquid–liquid displacement and scanning electron microscopy were employed to study the limiting and surface pores, respectively. After treatment with 50 ppm hypochlorite solution at pH = 7.2, a five-fold increase in water permeance up to 1400 L/(m2·h·bar) was observed, accompanied by a 40% increase in the limiting pore sizes and almost a three-fold increase in the porosity. After 5000 ppm treatment at pH = 11.5, a 40% rise in the maximum limiting pore size and almost a two-fold increase in the porosity and permeance was observed, whereas the mean pore size was constant. Apparently, changes in the membrane structure at pH = 11.5 were connected with polyvinylpyrrolidone (PVP) degradation and wash-out, whereas at lower pH and despite lower active chlorine concentration, this process was coupled with polysulfone (PSf) destruction and removal.

Highlights

  • Polysulfone (PSf) is a widely applied material to produce polymeric membranes for different applications [1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18]

  • The aim of this study was the evaluation of the effect of sodium hypochlorite treatment on the porous structure and transport characteristics of ultrafiltration membranes made of a polysulfone/polyvinylpyrrolidone blend

  • Employment of liquid–liquid displacement porosimetry and scanning electron microscopy allowed for simultaneous investigations of limiting and surface pores, respectively

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Summary

Introduction

Polysulfone (PSf) is a widely applied material to produce polymeric membranes for different applications [1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18] In water treatment, these membranes are commonly modified by the addition of polyvinylpyrrolidone (PVP) to increase hydrophilicity and water permeance [9,19,20,21,22,23]. Depending on the characteristics of the treated water, membrane elements may be subjected to NaOCl solutions with active chlorine concentrations up to 20 ppm for up to 5 min for backwashing processes and with concentrations up to 400 ppm for up to 4 h for chemical cleaning processes [28]

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