Journal of Hazardous Materials 143 (2007) 8–16
The removal of Cu(II) and Co(II) from aqueous solutions
using cross-linked chitosan—Evaluation by the
factorial design methodology
Antonio R. Cestari
a,∗
, Eunice F.S. Vieira
a
,
Iataanderson A. de Oliveira
a
, Roy E. Bruns
b
a
Laboratory of Materials and Calorimetry, Departamento de Qu´ ımica/CCET, Universidade Federal de Sergipe,
CEP 49100-000 S ˜ ao Crist ´ ov˜ ao, Sergipe, Brazil
b
Universidade Estadual de Campinas, Instituto de Qu´ ımica, CP 6154, 13083-970 Campinas, S ˜ ao Paulo, Brazil
Received 31 May 2006; received in revised form 27 July 2006; accepted 28 August 2006
Available online 1 September 2006
Abstract
A2
3
factorial design was employed to evaluate the quantitative removal of Cu(II) and Co(II) on glutaraldehyde-cross-linked chitosan from
kinetic isotherms, using chitosan masses of 100 and 300 mg and temperatures of 25 and 35
◦
C. The adsorption parameters were analyzed
statistically using modeling polynomial equations and a cumulative normal probability plot. The results indicated the higher quantitative pref-
erence of the chitosan for Cu(II) in relation to Co(II). Increasing the chitosan mass decreases the adsorption/mass ratio (mol g
-1
) for both
metals. The principal effect of the temperature did not show statistical importance. The adsorption thermodynamic parameters, namely
ads
H,
ads
G and
ads
S, were determined. Exothermic and endothermic results were found in relation to a specific factorial design experiment. A
comparison of
ads
H values was made in relation to some metal–adsorbent interactions in literature. It is suggested that the adsorption thermo-
dynamic parameters are determined by the influence of the principal and interactive experimental parameters and not by the temperature changes
alone.
© 2006 Elsevier B.V. All rights reserved.
Keywords: Removal of metals; Chitosan; Adsorption thermodynamics; Chemometrics
1. Introduction
Metals from aqueous and non-aqueous solutions have
become increasingly important in many industries, including
battery and power storage, coatings, electroplating, and power
industries. Traditional metal elimination are often of limited
effectiveness in order to decrease allowable levels specified
by regulatory agencies [1]. These metals inevitably make their
way into plant discharge streams in at least dilute concentra-
tions, despite application of remediation technologies [2]. The
limitations and cost of traditional treatment methods has led
researchers to search for alternative treatments. One promising
area of development has been adsorption.
Activated carbon is the most common adsorbent due to its
effectiveness, versatility, and good capacity for the adsorption
∗
Corresponding author. Tel.: +55 79 32126656; fax: +55 79 32126684.
E-mail address: cestari@ufs.br (A.R. Cestari).
of metals, dyes and other organic compounds. However, it suffers
from a number of disadvantages, mainly its high cost on large-
scale uses [3]. This has led many workers to search for the use
of cheap and efficient alternative adsorbent materials such as the
biopolymers chitin and chitosan [4].
Chitin is a biodegradable and nontoxic polysaccharide
widely spread among marine and terrestrial invertebrates and
fungi [3,4]. It is usually obtained from waste materials of the
sea food-processing industry, mainly shells of crab, shrimp,
prawn and krill. Its isolation calls for chemical treatments to
eliminate natural contaminants, such as inorganics, proteins,
lipids and pigments. By treating crude chitin with aqueous
40–50% sodium hydroxide in the 383–388 K range chitosan
is obtained. Chitin and chitosan are closely related since both
are linear polysaccharides containing 2-acetamido-2-deoxy-
d-glucopyranose and 2-amino-2-deoxy-d-glucopyranose units
joined by (1 → 4) glycosidic bonds [5]. The chemical and
physical properties of these polymers are different in nature
0304-3894/$ – see front matter © 2006 Elsevier B.V. All rights reserved.
doi:10.1016/j.jhazmat.2006.08.063