Comparison of tertiary treatment by nanofiltration and reverse osmosis for water reuse in denim textile industry

被引:85
|
作者
Ben Amar, Nihel [1 ,2 ]
Kechaou, Noura [3 ]
Palmeri, John [4 ]
Deratani, Andre [5 ]
Sghaier, Ali [6 ]
机构
[1] Inst Natl Sci Appl & Technol, Tunis 1080, Tunisia
[2] ENIT, Lab Modelisat Math & Numer Sci Ingenieur, Tunis 1002, Tunisia
[3] INRA, Unite Ecol & Physiol Syst Digestif, F-78352 Jouy En Josas, France
[4] Univ Toulouse 3, Phys Theor Lab, CNRS, UMR5152,IRSAMC, F-31062 Toulouse 4, France
[5] Univ Montpellier 2, CNRS, ENSCM, Inst Europeen Membranes,UMR5635, F-34095 Montpellier 5, France
[6] Soc Ind Text, Ksar Hellal 5070, Tunisia
关键词
Textile wastewater; Water recycling; Nanofiltration; Membrane configuration; Reverse osmosis; WASTE-WATER; MASS-TRANSFER; MEMBRANE; EFFLUENTS; COLOR; ULTRAFILTRATION; TECHNOLOGIES; PRETREATMENT; TRANSPORT; CHANNELS;
D O I
10.1016/j.jhazmat.2009.04.130
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The wastewaters resulting from different baths of a dyeing factory specialized in denim fabric are collected and treated by an activated sludge plant. This study investigated the coupling of activated sludge treatment with either nanofiltration (NF) or reverse osmosis (RO) to recycle water and reuse it in the process. We first conducted NF experiments with a HL membrane in different configurations: dead end and cross-flow for flat sheets and also in spiral wound form. Results on water permeation and salt rejection show that performances are configuration dependent. Then, for the study of the NF/RO textile wastewater treatment, experiments were conducted with spiral wound membranes in order to be closest to the industrial configuration. After analyzing the removal efficiencies of suspended solids and chemical oxygen demand (COD) of the treatment plant, we conducted NF experiments using an HL2514TF spiral wound membrane preceded by ultrafiltration (UF) treatment. We used as well an RO membrane (AG2514TF) to compare performances in water yield and quality for the same pumping costs. The results show that NF allows higher yield, while respecting the Tunisian standard of water reuse (COD < 90 mg L-1). Above 9 bar, the TDS rejection reaches 60% and the hardness is lower than the factory constraint (100 mg L-1 CaCOA allowing the reuse of the water in the process. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:111 / 117
页数:7
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