Investigations of different kinetic models for zinc ions uptake by a natural zeolitic tuff
Introduction
Groundwater contamination with heavy metals represents a serious threat to human health and environmental resources. Heavy metals are not biodegradable and tend to accumulate as metalloorganic complexes in living organisms, which increase their concentrations in biological cycles. One of the most dangerous types of contamination is the continuous release of liquid effluents with relatively high concentrations, primarily of Cr, Pb, Ni, Zn, Cu and Cd ions. Many of these metals are essential for life in trace concentrations, but higher concentrations have various toxic effects. Zinc is also a trace element that is essential for human health. But oral contamination or exposure to an environment contaminated with a high concentration of zinc causes serious health problems such as stomach and skin irritations, respiratory disorders and disturbance of protein metabolism. The conventional methods of heavy metals removal, such as precipitation methods, usually do not meet the standard criteria for releasing heavy metal cations to the environment (Alvarez-Ayuso et al., 2003, Cerjan-Stefanović et al., 1996, Vaca Mier et al., 2001). These techniques produce a large amount of sludge, which is disposed of in landfills of solid waste and could cause contamination of the soil due to the leaching by rainwater. An alternative method for purification of contaminated waters and wastewaters with heavy metal cations is using low-cost sorbents such as natural zeolites. The porous three-dimensional structure of natural zeolites consisting of (Si, Al)O4 tetrahedra is negatively charged. The negative charge in the zeolite framework is compensated by hydrated exchangeable cations such as Na, K, Ca, Mg, Ba, and Sr (Stolz et al., 2000). Zeolites have the ability to exchange most of their exchangeable cations as well as hydrate or dehydrate without major change of the structural framework. Besides their ion exchange capacity zeolites exhibit sorption behaviour that is based on the theory of acidic and basic sites in the framework structure. Sorption is the general term used to define the surface retention process without specifying the exact retention mechanism (Alvarez-Ayuso et al., 2003). Their structural properties give them a wide range of capabilities such as molecular sieves, e.g. uptaking of ammonium ions, radionuclides and heavy metal ions from wastewaters (Perić et al., 2004), adsorbents for odour and gas emissions control, as well as agricultural fertilizers. Furthermore, natural zeolites show high cation exchange capacity, good thermal and radiation resistance, and excellent compatibility with the environment.
The rate of heavy metals uptake in natural minerals (such as in clays and zeolites) is a critical parameter that could be used for determination of the rate of their contamination of the environment. This strongly depends on the hydrodynamics of the system, concentration of heavy metal ions, and porosity and heterogeneity of the soil. In the literature, the kinetic models that describe adsorption/ion exchange on porous particles with heterogeneous composition (such as zeolites) have been classified into three categories; staged equilibrium models, interference theory model, and rate equation models (Kithome et al., 1998, Robinson et al., 1994). In the literature, these models are applied to the experimental results of heavy metal ions removal, considering the possibilities of other resistances to the mass transfer process. The rate equation models consider diffusion as the mass transfer mechanism responsible for the overall rate of the processes in a zeolite–aqueous solution system. These models are the most applicable to the experimental results and will be discussed in this paper (Guibal et al., 1998, Jardine and Sparks, 1984, Liang and Tsai, 1995, Rengaraj and Moon, 2002).
The aim of this paper is to evaluate the kinetic models that can be used to describe the rate of zinc ions uptake within heterogeneous and porous zeolitic particles.
Section snippets
Reagents
Zinc ion solutions were prepared by dissolving the appropriate amount of ZnSO4×7H2O salt in double distilled water. The solutions with different initial concentrations of zinc (597.7, 420.6, 200.4, 128.6, and 68.3 mg/l) were prepared by dilution in double distilled water, and the exact concentration was determined by a complexometric method in acidic medium, using the highly selective indicator 3,3-dimetilnaphtidyne according to Complexometric Assay Methods with Triplex (Merck, 1982).
Characterization and modification of zeolitic tuff sample
The
Results of kinetic studies and discussion
The chemical analysis of zeolitic samples has shown that the deposit contained sodium, potassium, calcium and magnesium exchangeable ions. In the modified sample K+, Ca2+ and Mg2+ ions were mainly exchanged with Na+ ions, depending on their position in the clinoptilolite structure (Arcoya et al., 1996). During the ion exchange process, exchangeable cations of zeolite are replaced by zinc ions, resulting in a decrease in zinc concentration vs time until equilibrium is attained as shown in Fig. 2
Conclusions
The mobility of hydrated exchangeable ions from the solution to the exchangeable site inside the particle depends on the initial concentration, specific zeolitic framework structure and mineralogical heterogeneity of the sample used. The time interval needed for the equilibrium of zinc uptake increased with a decrease in the initial concentration in the solution. The mass transfer kinetics in the Zn-containing-solution/natural zeolitic tuff system cannot be described by a simplified kinetic
Acknowledgements
We are grateful to the Croatian Ministry of Science and Technology, which has been financing the project a part of which is presented in this paper.
References (21)
- et al.
Purification of metal electroplating waste waters using zeolites
Water Res.
(2003) - et al.
Role of the counteractions on the molecular sieve properties of a clinoptilolite
Microporous Mater.
(1996) - et al.
Kinetics of adsorption of Co(II) removal from water and wastewater by ion exchange resins
Water Res.
(2002) - et al.
Cd-exchanged heulandite: symmetry lowering and site preference
Micropor. Mesopor. Mater.
(2000) - et al.
Interaction of the zeolitic tuff with Zn-containing simulated pollutant solutions
J. Colloid Interf. Sci.
(2003) - et al.
Heavy metal removal with Mexican clinoptilolite: multi-component ionic exchange
Water Res.
(2001) - et al.
Kinetics of soil chemical reactions—a theoretical treatment.
In: Soil Science Society of America (Ed.), Rates of Soil Chemical Processes,
(1991) - et al.
Kinetics of soil chemical reaction: relationships between empirical equation and diffusion models
Soil. Sci. Soc. Am. J.
(1991) - et al.(1982)
- et al.
Metal ion exchange by natural zeolites
Croat. Chim. Acta.
(1996)
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