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,...
Main Authors: | , , , |
---|---|
Format: | Article |
Language: | English |
Published: |
MDPI AG
2016-03-01
|
Series: | Membranes |
Subjects: | |
Online Access: | http://www.mdpi.com/2077-0375/6/1/19 |
id |
doaj-f89f8d88564f46b8be0deba2a885a615 |
---|---|
record_format |
Article |
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 |
work_keys_str_mv |
AT jinxiangzhou polishingsteppurificationofhighstrengthwastewatersbynanofiltrationandreverseosmosis AT brianobaker polishingsteppurificationofhighstrengthwastewatersbynanofiltrationandreverseosmosis AT charlestgrimsley polishingsteppurificationofhighstrengthwastewatersbynanofiltrationandreverseosmosis AT scottmhusson polishingsteppurificationofhighstrengthwastewatersbynanofiltrationandreverseosmosis |
_version_ |
1725723093036433408 |