Journal of Water Process Engineering 4 (2014) 25–30
Contents lists available at ScienceDirect
Journal of Water Process Engineering
journal h om epage: www.elsevier.com/locate/jwpe
An electrocoagulation column (ECC) for groundwater purification
Shaima S. Hamdan, Muftah H. El-Naas
∗
Chemical and Petroleum Engineering Department, UAE University, P.O. Box 15551, Al-Ain, United Arab Emirates
a r t i c l e i n f o
Article history:
Received 7 May 2014
Received in revised form 7 August 2014
Accepted 16 August 2014
Keywords:
Electrocoagulation column
Chromium (VI)
Brackish groundwater
Heavy metals
a b s t r a c t
A novel electrocoagulation column (ECC) has been evaluated for the treatment of brackish groundwater
to reduce the concentrations of Cr(VI) and other ions to be within drinking water limits. The ECC was
fabricated from Plexiglas and had a rod anode and helical cathode; both electrodes were made from iron.
The effect of influent flow rate, applied current density, initial concentration, pH and air mixing were
studied at a temperature of 25
◦
C. The results showed that Cr(VI) removal rate was inversely proportional
to the inlet flow rate and directly proportional to applied current density, reaching 100% chromium
removal for initial chromium concentration of 5 mg/L at inlet flow rate of 30 mL/min with lowest energy
consumption of 0.75 kWh/m
3
and dissolved iron of 0.185 mg/L with an electrical cost of 0.03 US $/m
3
of
treated groundwater. The EC column could also reduce other contaminants and metals ions such as Mg, Zn
and Sr. Overall, the study affirmed that electrocoagulation is a reliable and environmentally compatible
technique for the purification of groundwater.
© 2014 Elsevier Ltd. All rights reserved.
1. Introduction
Nowadays, there is a growing environmental concern for the
quality of re-used water sources in irrigation, agricultures or even
industrial purposes. These concerns are attributed to the presence
of pollutants, such as carcinogenic chemicals, organic matter, dyes
and oils, which have adverse impacts once the contaminated water
is discharged into the environment. Chromium compounds that
have harmful effects on all living forms are extensively used in
chrome plating, leather tanning, wood preserving, and manufac-
turing of cement, dye and paper [1–3]. Chromium occurs primarily
in two states: hexavalent Cr(VI) and trivalent Cr(III); hexavalent
chromium is certainly more harmful to humans and animals. It has
severe risks in terms of toxicity, including skin irritation, kidney
failure, and gastric damage, in addition to the carcinogenic effect
[4].
Researchers have been striving to develop advanced technolo-
gies for the removal of toxic chromium species from wastewater.
Various methods have been proposed and applied toward the
attainment of this goal, including chemical precipitations [5,6],
adsorption [7–9], biological reduction via bacteria [10], reverse
osmoses [11], ion-exchange [12], electrodialysis [13] and photo-
catalysis [14]. As a non-conventional technique, electrocoagulation
(EC) presents important advantages over others including low
∗
Corresponding author. Tel.: +971 3 713 5188.
E-mail address: Muftah@uaeu.ac.ae (M.H. El-Naas).
operating cost, low occurrence of secondary pollution, and low
sludge generation [15].
In wastewater treatment, electrocoagulation (EC) process works
through destabilizing suspended or dissolved contaminants in an
aqueous medium by introducing a current into the medium and
generating coagulant in situ by electrolytic oxidation of an appro-
priate anode material [16]. The EC technique used in the this work
focuses on the removal of chromium from groundwater, while
simultaneously converting Cr(VI) to Cr(III), which is less toxic and
soluble in aqueous media; the aim is to reduce the chromium con-
centration to be within the maximum allowable drinking water
limit of 0.05 mg/L. The reactions taking place in an electrochemi-
cal cell when iron metal (Fe) used as “sacrificial electrode” can be
described by the following equations:
Anode reaction: Fe
(s)
→ Fe
2+
(aq)
+ 2e
-
(1)
Cathode reactions: Cr
2
O
2-
7
+ 6e
-
+ 7H
2
O → 2Cr
3+
(aq)
+ 14OH
-
(2)
Cr
2
O
2-
7
+ 6Fe
2+
+ 7H
2
O → 2Cr
3+
(aq)
+ 6Fe
3+
+ 14OH
-
(3)
In site reactions:
Cr
3+
(aq)
+ 3OH
-
(aq)
→ Cr(OH)
3(s)
(4)
Fe
3+
(aq)
+ 3OH
-
(aq)
→ Fe(OH)
3(s)
(5)
During the past few years, considerable amount of research
has been focused on the development of new and more efficient
continuous EC processes. Recently the performance of vertical
http://dx.doi.org/10.1016/j.jwpe.2014.08.004
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