Treatment of olive mill wastewater by the combination of ultrafiltration and bipolar electrochemical reactor processes

被引:52
作者
Yahiaoui, O. [1 ]
Lounici, H. [1 ]
Abdi, N. [1 ]
Drouiche, N. [1 ,2 ]
Ghaffour, N. [3 ]
Pauss, A. [4 ]
Mameri, N. [4 ]
机构
[1] Ecole Natl Polytechn Alger, Biotechnol Lab BIOGEP, Algiers, Algeria
[2] Silicon Technol Dev Unit UDTS, Algiers 16200, Algeria
[3] King Abdullah Univ Sci & Technol KAUST, Water Desalinat & Reuse Ctr, Jeddah, Saudi Arabia
[4] Univ Technol Compiegne, Dept Chem Engn, F-60205 Compiegne, France
关键词
Electrocoagulation; Iron bipolar electrodes; Olive mill wastewater; Mineral membrane; Ultrafiltration; ELECTROCOAGULATION; REDUCTION; REMOVAL; OME;
D O I
10.1016/j.cep.2010.11.003
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The main purpose of this study was to investigate the removal of the chemical oxygen demand (COD) from olive mill wastewater (OMW) by the combination of ultrafiltration with electrocoagulation process. Ultrafiltration process equipped with CERAVER membrane was used as pre-treatment for electrochemical process. The obtained permeate from the ultrafiltration process allowed COD removal efficiency of about 96% from OMW. Obtained permeate with an average COD of about 1.1 g dm(-3) was treated by electrochemical reactor equipped with a reactor with bipolar iron plate electrodes. The effect of the experimental parameters such as current density, pH, surface electrode/reactor volume ratio and NaCl concentration on COD removal was assessed. The results showed that the optimum COD removal rate was obtained at a current density of 93.3 A m(-2) and pH ranging from 4.5 to 6.5. At the optimum operational parameters for the experiments, electrocoagulation process could reduce COD from 1.1 g dm(-3) to 78 mg dm(-3), allowing direct discharge of the treated OMW as that meets the Algerian wastewater discharge standards (< 125 mg dm(-3)). (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:37 / 41
页数:5
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