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Environmental Research
journal homepage: www.elsevier.com/locate/envres
Aluminosilicate-catalyzed electrochemical removal of ammonium cation
from water –kinetics and selectivity.
Ahmed Enmili
a
, Frédéric Monette
a
, Chakib Yahiat
a
, Makram Amor
a
, Ali Hedhli
b
,
Abdelkrim Azzouz
a,b,*
a
École de Technologie Supérieure, Montréal, Québec, H3C 1K3, Canada
b
University of Quebec at Montreal, Department of Chemistry, Montréal, Québec, H3C 3P8, Canada
ARTICLE INFO
Keywords:
Ammonium-rich wastewaters
Electrochemical treatment
Zeolites
Clinoptilolite
Electro-catalysis
Aluminosilicates
ABSTRACT
Aluminosilicate-catalyzed electrochemical decomposition of ammonium cation (NH
4
+
) in water was in-
vestigated using NH
4
+
-saturated clinoptilolite and copper-nickel electrodes in the presence of different salts and
acidic species. The results showed beneficial roles of chloride anion and moderately acidic media. NH
4
+
ad-
sorbed by the zeolites was converted with a 98% selectivity into nitrogen. The process was found to obey zero-
order kinetics in the presence of clinoptilolite and a first order process when NaCl is added. Beneficial buffering
effects of the zeolite and acidic species were registered. Clinoptilolite turned out to act as both catalyst and NH
4
+
reservoir. These results allow envisaging effective and waste-free technology in treating NH
4
+
-rich aqueous
effluents through total electroconversion into nitrogen using low cost aluminosilicates. Clay minerals, soils,
sludges and natural water turbidity are potential catalysts for this purpose.
1. Introduction
The presence of high amounts of nitrogen-containing compounds
(N-compounds) in aqueous effluents is known to produce eutrophica-
tion of aquatic media. This leads to excessive growth of aquatic plants
and decay in oxygen content with negative impacts on biodiversity. One
of these N-compounds is ammonium cation. The latter originates from
wide variety of sources such as natural and artificial fertilizers, in-
dustrial and urban nitrogen-rich wastewaters (Erisman et al., 2007; Liu
et al., 2005; Lord et al., 2002; Schröder et al., 2004). This also causes a
major environmental issue that resides in the pollution of aquatic
media.
More or less satisfactory attempts to remove ammonia from do-
mestic and industrial wastewaters have been made through biological
processes and others (Peng and Zhu, 2006; Langwaldt, 2008; Leyva-
Ramos et al., 2010; Mook et al., 2012). Almost total removal of am-
monia can be achieved by materials exhibiting cation exchange capa-
city (CEC) (Widiastuti et al., 2011). The most commonly used are or-
ganic resins and aluminosilicates. On aluminosilicates (AS), the CEC is
strongly depending on the particle size and accessible specific surface
area, which determine the contribution of the permanent charges
arising from the Al atoms and that of the temporary charges resulting
from silanol protonation-deprotonation. The temporary charges, in
turn, are narrowly dependent on the pH level, ammonium concentra-
tion and possible presence of competing cations (Widiastuti et al.,
2011).
Zeolites are expanded AS structures displaying appreciable CEC, and
the SiO
2
/Al
2
O
3
ratio, framework type and pore size play key-roles in
this regard (Ribeiro et al., 2013). These features are key criteria for
using specific zeolite structure according to the targeted application
(Maia, 2002). Among the wide variety of zeolites tested so far, chaba-
zite and clinoptilolite have shown interesting performances for this
purpose (Langwaldt, 2008; Leyva-Ramos et al., 2010; Widiastuti et al.,
2011; Rahmani et al., 2004; Lahav and Green, 1998; Qiu et al., 2010;
Wang et al., 2016; Malovanyy et al., 2013). However, clinoptilolite is
the most abundant of more than 40 types of natural zeolites that turned
out to be of great interest for environmental purposes (Ming and
Boettinger, 2001; Ming and Dixon, 1987).
Ion exchange imposes a regeneration of the adsorbents, which are
usually treated with aqueous NaCl or NaOH solutions (Langwaldt,
2008; Leyva-Ramos et al., 2010; Widiastuti et al., 2011; Rahmani et al.,
2004; Lahav and Green, 1998; Wang et al., 2016). However, re-
generation requires operating time, reagents, energy consumption and
often leads to a secondary pollution. Biological regeneration could be a
more interesting alternative (Lahav and Green, 1998; Qiu et al., 2010;
Wu et al., 2008; He et al., 2007; Almutairi and Weatherley, 2015), but
https://doi.org/10.1016/j.envres.2020.109412
Received 10 May 2019; Received in revised form 12 March 2020; Accepted 19 March 2020
*
Corresponding author.
E-mail address: azzouz.a@uqam.ca (A. Azzouz).
Environmental Research 185 (2020) 109412
Available online 21 March 2020
0013-9351/ © 2020 Elsevier Inc. All rights reserved.
T