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Colloids and Surfaces B: Biointerfaces 62 (2008) 97–104
Biosorption of Ni(II) from aqueous solutions by living and
non-living ureolytic mixed culture
Mustafa Is ¸ik
∗
Aksaray University, Engineering Faculty, Environmental Engineering Department, 68100 Aksaray, Turkey
Received 25 July 2007; received in revised form 13 September 2007; accepted 19 September 2007
Available online 25 September 2007
Abstract
The present study explores the ability and the comparison of living and non-living ureolytic mixed culture (UMC) to remove Ni(II) from aqueous
solution. Time dependency experiments for the Ni(II) uptake showed that adsorption equilibrium was reached almost 110 and 60 min after addition
Ni(II) of 100 mg/L. The kinetic data were analyzed in term of pseudo-first-order and pseudo-second-order expressions. Ni(II) sorption of living
UMC was appropriate with pseudo-first-order kinetic (k
1
= 2.15 h
-1
, R
2
= 0.93) while non-living UMC sorbed Ni(II) with respect to second-order
kinetics (k
2
= 1.64 g/mg h, R
2
= 0.98). Also, comparison between the biosorption capacity of untreated living and non-living biomass was conducted
for removal of Ni(II). The biosorption process was investigated in equilibrium batch tests for Langmiur, Freundlich and Temkin isotherm models.
The data pertaining to the sorption dependence upon Ni(II) ion concentration ranged from 5 to 320 mg/L could be fitted to a Freundlich isotherm
model. The capacity constants K of Freundlich model for living and non-living UMC were 1.55 and 0.38 mg/g, respectively; the affinity constants
1/n were 0.47 and 0.75, respectively. Based on the results, the UMC appear to be a potential biosorbent for removal of Ni(II) from wastewater.
© 2007 Elsevier B.V. All rights reserved.
Keywords: Biosorption; Living; Non-living; Ureolytic; Nickel; Kinetics
1. Introduction
Enhanced industrial activity after the industrial revolution has
led to the discharge of chemicals, which causes environmen-
tal and public health problems. The important group of toxic
chemicals is heavy metals, due to their high toxicity, pose a
serious threat to biota and the environment. The presence of
heavy metals in the environment is of major concern because
of their extreme toxicity and tendency for bioaccumulation in
the food chain even in relatively low concentrations [1,2] Heavy
metals pollute the environment from various industries such as
metal plating, electroplating, mining, ceramic, batteries, pig-
ment manufacturing [3]. Although there are many methods for
the removal of metal ions from solutions, such as chemical
precipitation, complexation, solvent extraction and membrane
processes, biosorption processes show many advantages over
these methods. It is selective, effective and cheap and is able to
remove very low levels of heavy metals from solutions [4]. In
∗
Tel.: +90 382 2150953/132; fax: +90 382 2150592.
E-mail address: misik@aksaray.edu.tr.
addition, most of these processes are not eco-friendly because
of the production of sludge causing a solid disposal problem [5].
Recently, bioadsorbents have emerged as an eco-friendly,
effective and low cost material option. These bioadsorbents
include some agricultural wastes, fungi, algae and bacteria. Stud-
ies using bioadsorbents have shown that both living and dead
microbial (non-living) cells are able to adsorb metal ions and
offer potential inexpensive alternative to conventional adsor-
bents [6]. However, living cells are subject to toxic effect of
the heavy metals, resulting in cell death. Moreover, living cells
often require the addition of nutrients and hence increase the
biochemical oxygen demand (BOD) and/or chemical oxygen
demand (COD) in the effluent. For these reasons, the use of
non-living biomaterials or dead cells as metal-binding com-
pounds has been gaining advantage because toxic ions do not
affect them. In addition, dead cells require less care, mainte-
nance and they are cheaper. Furthermore, dead biomass can be
easily regenerated and reused [6].
Microbial metal uptake generally involves the rapid,
metabolism-independent uptake of metals to cell walls and
other external surfaces (passive uptake), followed by a slow,
metabolism-dependent transport across the cell membrane
0927-7765/$ – see front matter © 2007 Elsevier B.V. All rights reserved.
doi:10.1016/j.colsurfb.2007.09.022