Defluoridation of drinking water using a new flow column-electrocoagulation reactor (FCER) - Experimental, statistical, and economic approach

JOURNAL OF ENVIRONMENTAL MANAGEMENT

卷:197

Article

Hashim, Khalid S.^1,2  Shaw, Andy¹  Al Khaddar, Rafid¹  Pedrola, Montserrat Ortoneda¹  Phipps, David¹ 

[1] Liverpool John Moores Univ, Dept Civil Engn, Liverpool, Merseyside, England

[2] Babylon Univ, Dept Environm Engn, Babylon, Iraq

关键词: Fluoride;    Electrocoagulation;    Perforated electrodes;    Modelling;    SEM;    Operating cost;   

DOI  :  10.1016/j.jenvman.2017.03.048

来源: Elsevier

【 摘 要 】

A new batch, flow column electrocoagulation reactor (FCER) that utilises a perforated plate flow column as a mixer has been used to remove fluoride from drinking water. A comprehensive study has been carried out to assess its performance. The efficiency of fluoride removal (R%) as a function of key operational parameters such as initial pH, detention time (t), current density (CD), inter-electrode distance (ID) and initial concentration (Co) has been examined and an empirical model has been developed. A scanning electron microscopy (SEM) investigation of the influence of the EC process on morphology of the surface of the aluminium electrodes, showed the erosion caused by aluminium loss. A preliminary estimation of the reactor's operating cost is suggested, allowing for the energy from recycling of hydrogen gas hydrogen gas produced amount. The results obtained showed that 98% of fluoride was removed within 25 min of electrolysis at pH of 6, ID of 5 mm, and CD of 2 mA/cm(2). The general relationship between fluoride removal and operating parameters could be described by a linear model with R-2 of 0.823. The contribution of the operating parameters to the suggested model followed the order: t > CD > Co > ID > pH. The SEM images obtained showed that, after the EC process, the surface of the anodes, became non-uniform with a large number of irregularities due to the generation of aluminium hydroxides. It is suggested that these do not materially affect the performance. A provisional estimate of the operating cost was 0.379 US $/m(3). Additionally, it has been found that 0.6 kW/m(3) is potentially recoverable from the H-2 gas. Crown Copyright (C) 2017 Published by Elsevier Ltd. All rights reserved.

【 授权许可】

Free