Natural Science
 Vol.4 No.11(2012), Article ID:24596,13 pages DOI:10.4236/ns.2012.411114

Adsorption of Cu(II) on maghnite from aqueous solution: Effects of pH, initial concentration, interaction time and temperature

Mohamed Amine Zenasni1,2*, Said Benfarhi3, André Merlin2, Stéphane Molina2, Béatrice George2, Bahia Meroufel1,2

1Institute of Sciences and Technology, Department of Sciences, Bechar University, Bechar, Algeria; *Corresponding Author: am.zenasni@gmail.com

2Laboratory of Studies and Research on Material Wood (LERMAB), University of Lorraine, Nancy, France

3Istitute of Sciences, Department of Chemistry, Batna University, Batna, Algeria

Received 19 September 2012; revised 20 October 2012; accepted 30 October 2012

Keywords: Adsorption; Isotherms; Natural Maghnite; Heavy Metal; Cu(II)

ABSTRACT

The adsorption behaviour of Cu2+ onto maghnite was conducted under batch conditions. The effect of time, pH of the dispersion, temperature and initial metal concentration on the adsorption of Cu2+ onto maghnite was investigated. In this study, 94% of Cu(II), was adsorbed on the maghnite clay when the equilibrium was reached at 120 min. The adsorption of Cu2+ was a fast process that followed the pseudo-second-order kinetics. This process could be described by the Langmuir model and gave a maximum Cu2+ adsorption capacity of 21.78 mg/g at 293 K. The thermodynamic parameters such as variation of enthalpy ΔH, variation of entropy ΔS and variation of Gibbs free energy ΔG were calculated from the slope and intercept of lnKd vs. 1/T plots. The adsorption was endothermic reaction. The adsorption process for this natural maghnite is more spontaneous because the values of ΔG are less negative. The results suggested that natural maghnite was suitable as sorbent material for the recovery and adsorption of metal ion from aqueous solutions.

1. INTRODUCTION

Many toxic heavy metals have been discharged to the environment as industrial wastes, causing serious soil and water pollution [1]. Over the past few decades the huge increase in the use of heavy metals has resulted in an increased flux of metallic substances in aquatic environment.

They are also common groundwater contaminants at industrial and military installations. Heavy metal ions can be removed by several ways, e.g., precipitation and sorption by various media. The choice of which media depends upon the type and concentration of both sorptive material and sorbent employed, as well as their costs.

In the recent years the adsorption of heavy metals by a variety of substances has been the subject of many studies. One of the powerful treatment processes for the removal of metal ions from water with a low cost is adsorption. Several adsorbents are eligible for such a purpose. Activated carbon is the most popular adsorbent and has been used with great success [2]. A large number of low-cost adsorbents have been treated for metal ions removal. Other known natural materials like clay and zeolite have been investigated for their potential use of adsorbents for heavy metal [3,4].

Clays (especially maghnite) are widely used to study the adsorption of pollutants. These clays are chosen to avoid pollutant release into the environment, low cost and ubiquitous presence in most soils. Maghnite as a representative clay mineral is a clay mainly composed of montmorillonite, a 2:1 type of aluminosilicate. Maghnite is highly valued for their sorption [5].

The reactions of metals at the solid-solution interface play important role in determining their treatment by adsorption process, as well as in determining their fate in the environment [6,7]. These reactions which include adsorption, precipitation and polymerisation are often collectively called sorption [7]. Adsorption is a much faster process than precipitation. Adsorption of metals at mineral-water interface is often initially fast followed by a decrease in the adsorption rate [6,8].

The objective of the research described here was to investigate sorption characteristics of Cu2+ onto maghnite. The ability of maghnite to adsorb metal ions in solution was shown as a function of some experimental parameters. Values of well-known thermodynamic functions and isotherm studies for adsorption of Cu2+ onto maghnite have been investigated and reported.

2. MATERIALS AND METHODS

2.1. Clay Minerals

The maghnite used in this work came from a quarry located in Maghnia (North West of Algeria) and was supplied by company “ENOF” (an Algerian manufacture specialized in the production of nonferric products and useful substances). The different chemical elements of the native maghnite were transformed into oxides and analysed by Xray fluorescence (experiment carried out at ENOF). Results are given in Table 1. These results confirm that the maghnite used consists essentially of montmorillonite, since the ratio SiO2/Al2O3 is equal to 3.77 and thus belongs to the family of the phyllosilicates. This maghnite form is was stable suspensions in water and had flat platelets or needle-like structures. Granulometry of the crude maghnite have been prepared in the Civil Engineering Department of Tlemcen University (EDTU) in Algeria using a sedimentation technique with a 0.1% solution of sodium hexametaphosphate; 95% of the particles were found to have a diameter of less than 80 μm. The cation exchange capacity was measured to be 101.25 meq/100g of clay, and the surface area was 27 m2/g, with an average pore size of 7 nm [9,10].

2.2. Reagents

The reagents used in this study were all extra pure analytical grades: CuSO4·5H2O, NaOH (0.1 M) and HCl (0.1 M). A stock of Cu(II) solution of 1000 ppm, were prepared by dissolving 3.929 g of CuSO4·5H2O (Fluka) in 1 L of deionized water. The range of concentrations prepared from stock solution was varied. The pH of solution was adjusted by using 0.1 M NaOH and/or 0.1 M HCl.

2.3. Instrumentation

The pH of all solution was measured by a TitraLab Instrument TIM800 Model pH meter. The adsorption experiments have been studied by batch technique using a thermostated shaker bath GFL-1083 Model. A Eppendorf 5702 Model digital centrifuge was used to centrifuge the samples. Cu(II) concentrations of solutions before and after adsorption were measured by using flame atomic absorption spectrophometer (Varian, SpectrAA-100, AAS).

The Fourier transform infrared (FT-IR) spectra using KBr pressed disk technique were conducted by Perkin Elmer Spectrum 2000 Infrared spectrometer. Natural maghnite and KBr were weighted and then were ground in an agate mortar for 10 min prior to pellet making. The spectrums were collected for each measurement over the spectral range of 400 - 4000 cm−1.

TG-DTA thermograms were plotted using the multimodule 92 - 10 Setaram analyser operating from room temperature up to 1000˚C in a Al2O3 crucible, at 10˚C/mn heating rate.

Nanomorphology was characterized by scanning electron microscopy (SEM) and transmission electron microscopy (TEM). The SEM study was carried out using Hitachi S-4800 equipped with energy dispersive spectrometry for chemical analysis (EDS) and operating at 15 kV acceleration voltage. TEM study was performed with a Philips CM10 microscope operating at 100 kV.

2.4. Adsorption Study

The effect of contact time on the adsorption capacity of maghnite was studied in the range 1 - 360 min at an initial concentration of 100 mg/L. Adsorption kinetics was studied using an initial concentration of 100 mg/L with the sorbent dosage of 0.2 g/20 mL at pH 5.5. Adsorption isotherms were studied at various initial concentrations of Cu(II) ion in the range of 10 - 500 mg/L and the experiments were conducted at different constant temperatures in the range 20˚C - 60˚C. The maximum adsorption capacity was calculated from Langmuir, Freundlich and Dubinin-Radushkevich isotherms plot. The amount of Cu(II) adsorbed per unit mass of maghnite was calculated by using the mass balance equation given in Eq. 1 [11].

(1)

where qe is the maximum adsorption capacity in mg/g, C0 is the initial concentration and Ce is the concentration at equilibrium of Cu(II) solution in mg/L, V is the volume of the Cu(II) solution in mL and m is the mass of the maghnite in grams.

Adsorption percentage (%) was derived from the difference of the initial concentration (C0, mol/L) and the final one (Ce, mol/L) (Eq. 2):

Table 1. Chemical composition of the maghnite.

(2)

3. RESULTS AND DISCUSSIONB

3.1. Properties of Natural Maghnite

Chemical analysis data of the natural maghnite are presented in Table 1.

This study showed that natural maghnite contained sodium, potassium and calcium ions. Low-silica members are enriched with calcium, where as high-silica montmorillonite are enriched with potassium, sodium and magnesium.

FT-IR studies of these adsorbents help the identification of various forms of the minerals that are present in the clay. Infrared spectra of the charge maghnite, illustrated in Figure 1, show the presence of absorption bands of clay phase and absorption characteristic bands of impurities.

A strong band at 3623.90 cm–1 and 3464.43 cm–1 indicates the possibility of the hydroxyl linkage. However, a broad band at 3464.43 cm–1 and a band at 1631.34 cm–1 in the spectrum of clay suggest the possibility of water of hydration in the adsorbent. The bands due to free (or weakly hydrogen-bonded water molecule to the surface oxygen of tetrahedral sheet) water molecules, water-water hydrogen bond (Mn+-O-H-O-H-) and water bending modes are observed near 3623.90, 3464.43 and 1631.34 cm–1, respectively. The strong band near 1037.10 cm–1 is due to Si-O-Si stretching vibration in tetrahedral sheetswhich corresponds to the characteristic band of montmorillonite [12]. The coupled vibrations are appreciable due to the availability of various constituents. In the IR studies of maghnite, the Si-O stretching vibrations were observed at 697.86 cm–1, 524.86 cm–1 and 469.95 cm–1 showing the presence of quartz. The appearance of ν (Si-O-Si) and δ (Si-O) bands also support the presence of quartz [13]. The vibrations observed at 912.24 cm–1 indicate the possibility of the presence of hematite [14].

Result from thermal analysis is reported in Figure 2. The TG curve of the natural maghnite shows three main steps of weight loss. In the first step (T < 200˚C) a weight loss (about 18.50%) corresponding to both adsorbed and interlayer water loss takes place. After this step, the TG curve shows a slight gradual decrease (about 2.10%) in the range 200˚C - 580˚C, which is attributed to the water loss of maghnite. Finally, a third main loss occurs at temperatures in the range 580˚C - 900˚C, where the TG curve displays a step weight loss (about 4.11%) related to the release of structural OH of natural maghnite. The dehydroxylation temperature of about 650˚C (see Figure 2) is in agreement with the classical range of dehydroxylation temperature (600˚C - 700˚C) observed by various authors for cis vacant montmorillonites [15].

SEM micrograph of the untreated maghnite sample suggests a very cohesive material (Figure 3). The micrograph confirms that the material is forming micronsize agglomerates. A higher magnification micrograph of the same structure shows that the micro-size particles are composed of individual platelets, which conglomerate into larger size particles.

Figure 1. Infrared (IR) spectra of natural maghnite.

Figure 2. TG-DTA analyse of natural maghnite.

Figure 3. SEM image of maghnite sample.

The obtained chemical analysis by energy dispersive spectroscopy (Figure 4) shows the presence of framework Al and Si elements. The molar Si/Al ratio for used maghnite is about 2.78. The presence also of the Na, K and Mg elements in the structure of maghnite.

The TEM micrographs at low magnification showed (Figure 5) a higher tendency of the maghnite to aggregate.

3.2. Effect of Initial Concentration of Cu(II)

Effect of initial concentration of Cu(II) on adsorption capacity of maghnite was investigated by varying initial concentration of Cu(II) from 10 to 500 mg/L. For this study, pH, temperature, adsorbent dosage and contact time have been fixed as 20˚C, 0.2 g/20mL and 24 h. The results are presented in Figure 6. An increase of Cu(II)

Figure 4. SEM-EDS spectra of maghnite sample.

Figure 5. TEM micrograph of the maghnite.

concentration accelerates the diffusion of Cu(II) ions from solution to the adsorbent surface due to the increase in driving force of concentration gradient. Hence, the amount of adsorbed Cu(II) at equilibrium increased from 0.99 to 21.6 mg/g as the Cu(II) concentration is increased from 10 to 500 mg/L.

Figure 6. Effect of initial concentration of Cu(II) on adsorption capacity of maghnite.

3.3. Effect of Initial pH on Adsorption Capacity of Maghnite

Effect of initial pH on the adsorption capacity of maghnite for Cu(II) was studied by varying solution pH from 1.5 to 5.5 at the adsorbent dosage of 0.2 g/20mL using an initial concentration of Cu(II) as 100 mg/L. The pH range of 1.5 - 5.5 was chosen, as the precipitation of Cu(II) is found to occur at pH ≥ 6 [16]. Variation of adsorption capacity of maghnite for Cu(II) ions with pH is shown in Figure 7. It is evident that the adsorption of Cu(II) ions on maghnite is strongly dependant on the pH of the solution. The adsorption of Cu(II) ions increases steadily with increase in initial pH from 1.5 to 5.5 and the maximum adsorption capacity of 9.94 mg/g is observed at pH 5.5.

3.4. Effects of Interaction Time and Kinetics of Adsorption

The adsorption of Cu(II) on maghnite as a function of contact time at pH 5.5 ± 0.1 is shown in Figure 8.

The Cu(II) interacted with the maghnite rapidly and within 40 min, the maximum uptake was observed (Figure 8). Afterwards, the interactions slowed down and approached equilibrium in nearly 120 min under the given set of experimental conditions.

Attainment of equilibrium is influenced by several factors including the nature of the adsorbent and the adsorbate, and the interactions between them.

Initially, the rate of adsorption on the bare surface was very high, but as the sites got covered with the Cu(II), the rate decreased. The rate now becomes predominantly dependent on the rate at which metal ions are transported from the bulk liquid phase to the adsorbent-adsorbate interface. The kinetics of the interactions is thus likely to be dependent on different rate processes as the interacttion time increases [17].

In this study, 94% of Cu(II), was adsorbed on the maghnite clay when the equilibrium was reached at 120 min. On the basis of this result, it can be observed that natural maghnite clay can be used to remove this metal ion.

The fast adsorption of Cu(II) on maghnite suggested that the uptake of Cu(II) from solution to maghnite was mainly dominated by chemical adsorption rather than physical adsorption [18,19].

To analyze the kinetic adsorption of Cu(II) on maghnite, a pseudo-second-order rate equation was used to simulate the kinetic adsorption (Eq. 3) [20]:

(3)

where qt (mg/g) is the amount of Cu(II) adsorbed on maghnite at time t (min), qe (mg/g) is the equilibrium adsorption capacity and (g/(mg·min)) is the pseudosecond-order rate constant of adsorption. The values of and qe calculated from the intercept and slope of equation are 0.19 g/(mg·min) and 9.43 mg/g, respectively. The correlation coefficient of the pseudo-second-order rate equation for the linear plot is 1.00 (see Figure 9), which suggests that the kinetic adsorption can be described by the pseudo-second-order rate equation.

Figure 7. Effect of pH on adsorption capacity of maghnite for Cu(II).

Figure 8. Effect of contact time on the adsorption of Cu(II) to natural maghnite, pH = 5.5 ± 0.1, T = 293 K, clay 10 g/L, C[Cu(II)]initial = 100 mg/L.

3.5. Construction of Isotherms and Model Fitting

Sorption isotherms were constructed by plotting the amount of metal sorbed (mg/g) against the equilibrium concentration of metal in solution (mg/L).

Three models have been adopted in this paper, namely: Langmuir, Freundlich and DubininRadushkevich (D-R) equilibrium isotherm models. The Langmuir and Freundlich isotherms are used most commonly to describe the adsorption characteristics of metal ions in water and wastewater treatment [21].

3.5.1. Langmuir Isotherm

The data conform the linear form of Langmuir model (Eq. 4) [22] expressed below:

(4)

where Ce is equilibrium concentration of Cu(II) (mg/L)

Figure 9. Lagergren pseudo second-order plots for Cu(II) adsorbed on maghnite at 293K, pH (5.5).

and qe is the amount of the Cu2+ adsorbed (mg) by per unit of maghnite (g). qm and KL are the Langmuir constants related to the adsorption capacity (mg/g) and the equilibrium constant (L/g), respectively. The Langmuir monolayer adsorption capacity (qm) gives the amount of the metal required to occupy all the available sites per unit mass of the sample (see Figure 10). The Langmuir monolayer adsorption capacities of maghnite was estimated as 21.78 mg/g, (Table 2). The value of maximum adsorption capacity (qm) calculated from the Langmuir isotherm in this study is much higher than that of those reported in the literature. For example, adsorption of Cu(II) at 308 K on waste iron oxide follows the Langmuir isotherm model with an adsorption capacity of 14.10 mg/g [23]. Langmuir adsorption capacity for Cu(II) adsorption on shells of lentil, wheat, and rice has been shown to be 8.97, 16.07 and 2.31 mg/g, respectively, by Aydın et al. [24]. The uptake of Cu(II) on spent activated clay has Langmuir monolayer capacity qm = 13.2 mg/g at pH 6.0 [25].

3.5.2. Freundlich Isotherm

The adsorption equilibrium data was also applied to the Freundlich model (Eq. 5) [26] given below:

(5)

where Kf and n are Freundlich constants related to adsorption capacity and adsorption intensity, respectively. Freundlich parameters (Kf and n) indicate whether the nature of adsorption is either favorable or unfavorable.

The intercept is an indicator of adsorption capacity and the slope is an indicator of adsorption intensity. A relatively slight slope n 1 indicates that adsorption intensity is good (or favorable) over the entire range of concentrations studied, while a steep slope (n > 1) means that adsorption intensity is good (or favorable) at high concentrations but much less at lower concentrations [27]. A high value of the intercept, Kf, is indicative of a high adsorption capacity. In the adsorption system, n value is 2.63 which indicates that adsorption intensity is good (or favorable) over the entire range of concentrations studied. The Kf value of the Freundlich equation (Table 2) also indicates that maghnite has a very high adsorption capacity for copper ions in aqueous solutions (see Figure 11).

3.5.3. Dubinin-Radushkevich (D-R)

The equilibrium data were also applied to the DubininRadushkevich (D-R) isotherm model to determine if adsorption occurred by physical or chemical processes. The linearized form of the D-R isotherm [28-32] is as follows (Eq. 6):

(6)

where β is the activity coefficient related to mean adsorption energy (mol2/J2) and ε is the Polanyi potential (Eq. 7) :

(7)

The D-R isotherm is applied to the data obtained from

Figure 10. Langmuir isotherm plot for adsorption of Cu2+ on the maghnite. T = 293 K, initial pH 5.5, m/V = 10 g/L.

Table 2. Langmuir, Freundlich and D-R isotherm parameters for the adsorption of Cu2+ onto maghnite sample.

Figure 11. Freundlich isotherm plot for adsorption of Cu2+ on the maghnite. T = 293 K, initial pH 5.5, m/V = 10 g/L.

the empirical studies. A plot of ln qe against ε2 is given in Figure 12. D-R isotherm constants, qm, for maghnite was found to be 10.2 mg/g (Table 2).

The difference of qm derived from the Langmuir and

Figure 12. D-R isotherm plot for adsorption of Cu2+ on the maghnite. T = 293 K, initial pH 5.5, m = 10 g/L.

D-R models is large. The difference may be attributed to the different definition of qm in the two models. In Langmuir model, qm represents the maximum adsorption of metal ions at monolayer coverage, whereas it represents the maximum adsorption of metal ions at the total specific micropore volume of the adsorbent in D-R model. Thereby, the value of qm derived from Langmuir model is higher than that derived from D-R model. The differences are also reported in previous studies [28,30]. The mean adsorption energy, E (kJ/mol) is as follows (Eq. 8):

(8)

This adsorption potential is independent of the temperature, but it varies depending on the nature of adsorbent and adsorbate. The magnitude of E is used for estimating the type of adsorption mechanism. If the E value is between 8 and 16 kJ/mol, the adsorption process follows by chemical adsorption and if E < 8 kJ/mol, the adsorption process is of a physical nature [28-32]. The calculated values of E are 2.55 kJ/mol for maghnite, and they are in the range of values for physical adsorption reactions. The similar results for the adsorption of Cu(II) was reported by earlier worker [27].

3.6. Thermodynamic Studies

Using the following equations, the thermodynamic parameters of the adsorption process were determined from the experimental data (Eqs. 9-11):

(9)

(10)

(11)

where Kd is the distribution coefficient for the adsorption, ΔS, ΔH and ΔG are the changes of entropy, enthalpy and the Gibbs energy, T (K) is the temperature, R (J·mol–1·K–1) is the gas constant. The values of ΔH and ΔS were determined from the slopes and intercepts of the plots of ln Kd vs. 1/T (show Figure 13).

The negative values for the Gibbs free energy change, ΔG, show that the adsorption process for the maghnite is spontaneous and the degree of spontaneity of the reaction increases with increasing temperature. The increase in adsorption with temperature may be attributed to either increase in the number of active surface sites available for adsorption on the adsorbent or the desolvation of the adsorbing species and the decrease in the thickness of the boundary layer surrounding the adsorbent with temperature, so that the mass transfer resistance of adsorbate in the boundary layer decreases. The values of ΔG are less negative for the maghnite suggesting that the adsorption process for this material is more spontaneous. These results suggest that the internal domains of this sample are more suitable environments for Cu(II) cations than the maghnite. The data shown in Table 3 show that the heats

Figure 13. Plot of lnKd against 1/T for the adsorption of Cu(II) on maghnite.

Table 3. Thermodynamic parameters for the adsorption of Cu(II) onto maghnite.

of adsorption are positive for both types of the maghnite. These positive value of ΔH indicate the endothermic behavior of the adsorption reaction of Cu(II) ions and suggest that a large amount of heat is consumed to transfer the Cu(II) ions from aqueous into the solid phase. As was suggested by Nunes and Airoldi [33], the transition metal ions must give up a larger share of their hydration water before they could enter the smaller cavities. Such a release of water from the divalent cations would result in positive value of ΔS. This mechanism of the adsorption of Cu(II) ions is also supported by the positive value of ΔS, which show that Cu(II) ions are less hydrated in the maghnite layers than in the aqueous solution. Also, the positive value of ΔS indicates the increased disorder in the system with changes in the hydration of the adsorbing Cu(II) cations.

4. CONCLUSION

The adsorption of Cu(II) depends upon the nature of the adsorbent surface and the species distribution of Cu(II) in solution, which mainly depends on the pH of the system. The plots have good linearity in both the cases (Freundlich plot, R2 = 0.967, Langmuir plot, R2 = 0.995) at 298 K. The values of the adsorption coefficients indicate the favorable nature of adsorption of Cu(II) on the natural maghnite.

5. ACKNOWLEDGEMENTS

The authors gratefully acknowledge to the Dr Yves PILLET (Faculty of Sciences et Technology, group PGCM, University of Lorraine, Nancy, France) because of contribution to our study, and thankful for Joint Service Electronic Microscopy and Microanalysis at the University Henri Poincare of Nancy for MEB-EDS analysis.

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