Abstract

This paper focuses on an in situ interfacial polymerization modification of polyamide thin film composite membranes with acrylic acid (AA) and zinc oxide (ZnO) nanoparticles. Consequent to this modification, the modified polyamide thin film composite (PA–TFC) membranes exhibited enhanced water permeability and Pb (II) heavy metal rejection. For example, the 0.50:1.50% ZnO/AA modified membranes showed water permeability of 29.85 ± 0.06 L·m−2·h−1·kPa−1 (pH 3), 4.16 ± 0.39 L·m−2·h−1·kPa−1 (pH 7), and 2.80 ± 0.21 L·m−2·h−1·kPa−1 1 (pH 11). This demonstrated enhanced pH responsive properties, and improved water permeability properties against unmodified membranes (2.29 ± 0.59 L·m−2·h−1·kPa−1, 1.79 ± 0.27 L·m−2·h−1·kPa−1, and 0.90 ± 0.21 L·m−2·h−1·kPa−1, respectively). Furthermore, the rejection of Pb (II) ions by the modified PA–TFC membranes was found to be 16.11 ± 0.12% (pH 3), 30.58 ± 0.33% (pH 7), and 96.67 ± 0.09% (pH 11). Additionally, the membranes modified with AA and ZnO/AA demonstrated a significant pH responsiveness compared to membranes modified with only ZnO nanoparticles and unmodified membranes. As such, this demonstrated the swelling behavior due to the inherent “gate effect” of the modified membranes. This was illustrated by the rejection and water permeation behavior, hydrophilic properties, and ion exchange capacity of the modified membranes. The pH responsiveness for the modified membranes was due to the –COOH and –OH functional groups introduced by the AA hydrogel and ZnO nanoparticles.

Highlights

  • Polyamide thin film composite (PA–TFC) membranes have been reported to possess a high capacity for the removal of heavy metals, dissolved salts, and organic solutes from wastewater [1,2,3]

  • For the membranes modified with acrylic acid (AA), two concentrations of 1.00% and 1.50% AA were chosen as constant concentrations

  • The introduction of the zinc oxide (ZnO) nanoparticles demonstrated an increase in hydrophilicity compared to membranes modified with AA hydrogels only

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Summary

Introduction

Polyamide thin film composite (PA–TFC) membranes have been reported to possess a high capacity for the removal of heavy metals, dissolved salts, and organic solutes from wastewater [1,2,3]. TFC membranes are challenged by their low water permeability This is because of the highly crosslinked structure of the PA active thin film layer, and consequent increased fouling [6]. To offset these challenges, extensive efforts are being made to modify the active polyamide thin film of the TFC membranes. Various researchers are modifying the polyamide thin film with suitable additives, such as nanoparticles, to improve the membranes’ hydrophilicity. Such newly incorporated properties can inherently translate into enhanced water permeability and fouling resistance of the modified membranes [7]

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