Polishing Step Purification of High-Strength Wastewaters by Nanofiltration and Reverse Osmosis

This article reports findings on the use of nanofiltration (NF) and reverse osmosis (RO) for secondary treatment of high-strength rendering facility wastewaters following an ultrafiltration step. These wastewaters present significant challenges to classical treatment technologies. Constant-pressure,...

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Main Authors: Jinxiang Zhou, Brian O. Baker, Charles T. Grimsley, Scott M. Husson
Format: Article
Language:English
Published: MDPI AG 2016-03-01
Series:Membranes
Subjects:
Online Access:http://www.mdpi.com/2077-0375/6/1/19
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spelling doaj-f89f8d88564f46b8be0deba2a885a6152020-11-24T22:35:42ZengMDPI AGMembranes2077-03752016-03-01611910.3390/membranes6010019membranes6010019Polishing Step Purification of High-Strength Wastewaters by Nanofiltration and Reverse OsmosisJinxiang Zhou0Brian O. Baker1Charles T. Grimsley2Scott M. Husson3Department of Chemical and Biomolecular Engineering and Animal Co-Products Research and Education Center, Clemson University, Clemson, SC 29634, USADepartment of Chemical and Biomolecular Engineering and Animal Co-Products Research and Education Center, Clemson University, Clemson, SC 29634, USADepartment of Chemical and Biomolecular Engineering and Animal Co-Products Research and Education Center, Clemson University, Clemson, SC 29634, USADepartment of Chemical and Biomolecular Engineering and Animal Co-Products Research and Education Center, Clemson University, Clemson, SC 29634, USAThis article reports findings on the use of nanofiltration (NF) and reverse osmosis (RO) for secondary treatment of high-strength rendering facility wastewaters following an ultrafiltration step. These wastewaters present significant challenges to classical treatment technologies. Constant-pressure, direct-flow membrane filtration experiments were done to screen for flux and effluent water permeate quality of ten commercial NF and RO membranes. All membranes tested were effective in reducing total dissolved salts (TDS) and chemical oxygen demand (COD); however, only two membranes (Koch MPF-34 and Toray 70UB) gave sufficiently stable flux values to warrant longer term cross-flow filtration studies. Cross-flow flux measurements, scanning electron microscopy (SEM), X-ray dispersive spectroscopy (EDS), and attenuated total reflectance-Fourier-transform infrared spectroscopy (ATR-FTIR) indicated that both membranes were eventually fouled by organic and inorganic foulants; however, the Toray 70UB RO membrane yielded a capacity of 1600 L/m2 prior to cleaning. A preliminary economic analysis compared the estimated costs of energy and consumables for a dual-stage UF/RO membrane process and dissolved air floatation (DAF) and found membrane process costs could be less than about 40% of the current DAF process.http://www.mdpi.com/2077-0375/6/1/19impaired watermembrane foulingsustainabilitywater treatment
collection DOAJ
language English
format Article
sources DOAJ
author Jinxiang Zhou
Brian O. Baker
Charles T. Grimsley
Scott M. Husson
spellingShingle Jinxiang Zhou
Brian O. Baker
Charles T. Grimsley
Scott M. Husson
Polishing Step Purification of High-Strength Wastewaters by Nanofiltration and Reverse Osmosis
Membranes
impaired water
membrane fouling
sustainability
water treatment
author_facet Jinxiang Zhou
Brian O. Baker
Charles T. Grimsley
Scott M. Husson
author_sort Jinxiang Zhou
title Polishing Step Purification of High-Strength Wastewaters by Nanofiltration and Reverse Osmosis
title_short Polishing Step Purification of High-Strength Wastewaters by Nanofiltration and Reverse Osmosis
title_full Polishing Step Purification of High-Strength Wastewaters by Nanofiltration and Reverse Osmosis
title_fullStr Polishing Step Purification of High-Strength Wastewaters by Nanofiltration and Reverse Osmosis
title_full_unstemmed Polishing Step Purification of High-Strength Wastewaters by Nanofiltration and Reverse Osmosis
title_sort polishing step purification of high-strength wastewaters by nanofiltration and reverse osmosis
publisher MDPI AG
series Membranes
issn 2077-0375
publishDate 2016-03-01
description This article reports findings on the use of nanofiltration (NF) and reverse osmosis (RO) for secondary treatment of high-strength rendering facility wastewaters following an ultrafiltration step. These wastewaters present significant challenges to classical treatment technologies. Constant-pressure, direct-flow membrane filtration experiments were done to screen for flux and effluent water permeate quality of ten commercial NF and RO membranes. All membranes tested were effective in reducing total dissolved salts (TDS) and chemical oxygen demand (COD); however, only two membranes (Koch MPF-34 and Toray 70UB) gave sufficiently stable flux values to warrant longer term cross-flow filtration studies. Cross-flow flux measurements, scanning electron microscopy (SEM), X-ray dispersive spectroscopy (EDS), and attenuated total reflectance-Fourier-transform infrared spectroscopy (ATR-FTIR) indicated that both membranes were eventually fouled by organic and inorganic foulants; however, the Toray 70UB RO membrane yielded a capacity of 1600 L/m2 prior to cleaning. A preliminary economic analysis compared the estimated costs of energy and consumables for a dual-stage UF/RO membrane process and dissolved air floatation (DAF) and found membrane process costs could be less than about 40% of the current DAF process.
topic impaired water
membrane fouling
sustainability
water treatment
url http://www.mdpi.com/2077-0375/6/1/19
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AT brianobaker polishingsteppurificationofhighstrengthwastewatersbynanofiltrationandreverseosmosis
AT charlestgrimsley polishingsteppurificationofhighstrengthwastewatersbynanofiltrationandreverseosmosis
AT scottmhusson polishingsteppurificationofhighstrengthwastewatersbynanofiltrationandreverseosmosis
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