Please use this identifier to cite or link to this item: http://hdl.handle.net/10603/442410
Title: Study of Arsenic removal from aqueous solution using spiral wound nanofiltration membrane
Researcher: Robin Marlar R
Guide(s): Shailendra Bajpai and Sangeeta Garg
Keywords: Engineering
Engineering and Technology
Engineering Chemical
University: Dr B R Ambedkar National Institute of Technology Jalandhar
Completed Date: 2021
Abstract: newlineArsenic contamination in drinking water is recognized as major health hazard worldwide. In natural water, arsenic is available in two dominant toxic inorganic forms, i.e. arsenic (III) and arsenic (V) and both are toxic in nature. However, arsenic (III) is more toxic than arsenic (V). In this work, arsenic (III) removal was studied using HFN300 Polyethersulfone Nanofiltration membrane in spiral wound configuration at Pilot scale. The influence of various operating parameters such as transmembrane pressure (2.98-8.46 bar), initial feed concentration (10-50 mg/L), feed flowrate (9-17 LPM) and initial solution pH (4-10) on membrane performance were examined. The permeate concentration was analysed using Atomic Absorption Spectrophotometer for arsenic (III) concentration. It was found that rejection was dependent on pressure, feed concentration, and solution pH. Results showed that more than 96.4 % arsenic (III) rejection was achieved for 50 mg L-1 of feed at optimized conditions. The rejection percentage was found to increase from 84 % to 93 %, while increasing initial solution pH from 4 to 10. The effect of co-ion concentration [monovalent (Cl-) and divalent (SO42-)] in feed also studied on membrane performance. The experimental results showed that increasing co-ion concentration (40 200 mg/L) in feed decreases the rejection efficiency of trivalent arsenic. The competitive nature between ions can be attributed to the decrease in rejection efficiency along with electro-migration repulsion of co-ions. Correspondingly, the permeate flux was also decreased with increasing co-ion concentration due to concentration polarization effect. newlineThe membrane performance was modelled over a wide range of solution pHs (4-10). Arsenic (III) is assumed to be in uncharged solute form at below pH 9.2. Therefore, film theory combined Spiegler-Kedem (FTCSK) model which covers the transport mechanism of diffusion and convection was suitably selected to predict the membrane performance at pH 8. Accordingly, membrane parameter
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URI: http://hdl.handle.net/10603/442410
Appears in Departments:Department of Chemical Engineering

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abstract.pdf372.22 kBAdobe PDFView/Open
chapter-1.pdf445.01 kBAdobe PDFView/Open
chapter-3.pdf628.96 kBAdobe PDFView/Open
contents.pdf213.47 kBAdobe PDFView/Open
list of publications.pdf289.86 kBAdobe PDFView/Open
prelim.pdf1.24 MBAdobe PDFView/Open
references.pdf337.7 kBAdobe PDFView/Open
title.pdf156.56 kBAdobe PDFView/Open
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