- Citado por SciELO
versión impresa ISSN 0103-5053versión On-line ISSN 1678-4790
J. Braz. Chem. Soc. v.20 n.1 São Paulo 2009
Denis L. Guerra; Claudio Airoldi*
Instituto de Química, Universidade Estadual de Campinas, CP 6154, 13084-971 Campinas-SP, Brazil
Brazilian kaolinite clay was used to study urea intercalation (KUR) and delamination (Kur/DL) processes. The intercalated sample was delaminated by ultrasonic treatment in acidic solution. The basal distance changed from 0.72 to 1.08 nm with increasing surface area from 20.3 to 90.5 m2 g-1 for KUR and KUR/DL. Suspended pristine, intercalated and delaminated clays at pH 5.0 adsorbed copper and lead cations at the solid/liquid interface. The Langmuir, Redlich-Peterson and Toth adsorption isotherm models were employed in linear and nonlinear regression processes, to give b and KL values for all kaolinites. The highest adsorption capacity of 12.8 mmol g-1 was obtained with delaminated kaolinite. The kinetic parameters analyzed by the Lagergren and Elovich models gave a good fit for a pseudo-second order reaction with k2 in the 5.0 to 11.0 and the 4.9 to 13.0 mmol-1 min-1 ranges for copper and lead cations, respectively.
Keywords: kaolinite, adsorption, heavy metals, kinetics, delamination
Amostras brasileiras de caulinita foram usadas no estudo dos processos de intercalação com uréia (KUR) e de deslaminação (KUR/DL). A amostra intercalada foi deslaminada por tratamento com ultra-som em solução ácida. A distância basal inicial de 0,72 nm passa a 1,08 nm com aumento na área superficial de 20,3 para 90,5 m2 g-1 para KNAT e KUR/DL. Amostras de argila intercalada e deslaminada adsorveram cátions cobre e chumbo na interface sólido/líquido. Os modelos de isotermas de adsorção de Langmuir, Redlich-Peterson e Toth foram utilizados em processo de regressão linear e não linear para a obtenção de valores de b e KL para todas as amostras de caulinita. A capacidade de adsorção mais alta, de 12,8 mmol g-1, foi obtida com a caulinita deslaminada. Os parâmetros cinéticos analisados pelos modelos de Lagergren e Elovich forneceram um bom ajuste para uma reação de pseudo-segunda ordem com valores de k2 variando de 5,0 a 11,0 e de 4,9 a 13,0 mmol-1 min-1 para cátions cobre e chumbo, respectivamente.
Some undesirable heavy metals can be removed from aqueous solution through chemical precipitation, ion exchange, electrodeposition, solvent extraction, membrane separation, reverse osmosis and adsorption processes. For this last procedure, the development of low cost adsorbents with easy manipulation and regeneration for possible reuse has been an object of significant attention, mainly when effluents are involved. Various conventional and non-conventional adsorbents have been explored for removal of different metal ions from aqueous solutions.1-7 For example, materials containing micro and macropores, such as pillared and intercalated/delaminated clays, are often employed in such operations. In particular, kaolinite and smectite group clay minerals have been successfully explored in many adsorption procedures.8-10
From the structural viewpoint, kaolinite is a 1:1 dioctahedral aluminosilicate with two distinct basal cleavage faces.11 One of them consists of a tetrahedral siloxane surface formed by very chemically inert -Si-O-Si- bonds, while the other is constituted by an octahedral gibbsite sheet, Al(OH)3. The neutral layered 1:1 structure can be disrupted and the broken bonds have the ability to accommodate OH groups.
Kaolinite is one of the most important clay minerals and its diverse industrial applications depend on the ability to modify the original properties for different uses. The methodology of surface modification includes, in principle, intercalation of species such as urea, dimethylsulfoxide and potassium acetate, among others. As expected, ion intercalation into the kaolinite structure results in changing the amount of reactive acidic and basic sites on the internal and external surfaces.12-18
The aim of the present investigation is to study the structural and physical-chemical characteristics of three different kaolinite forms: natural, urea-intercalated and also urea intercalated and delaminated samples. Various parameters, such as synthetic intercalation and delaminated procedures, the influence caused on adsorption capacity due to the intercalation and delamination processes, the kinetics of adsorption and applications for divalent copper and lead from aqueous solution, were explored. The Langmuir, Redlich-Peterson and Toth adsorption isotherm models have been applied to fit the experimental data by using linear and nonlinear regressions. The effect of the variation of parameters on the structure of the modified kaolinite samples was analyzed by different techniques and the kinetics of adsorption was studied through the Lagergren and Elovich models, by applying linear and nonlinear regressions.
The clay sample used in this investigation was obtained from the Perus area, São Paulo state, Southeast of Brazil. A natural kaolinite sample, named KNAT, with less than 2 μm particles, was separated by sedimentation. The cation-exchange capacity (CEC) was measured in order to evaluate the potential use of that clay for intercalation and delamination. The exchange was followed by the ammonium acetate method with a concentration of 2.0 mol dm-3 at pH 8.0, giving 0.15 mmol g-1 on an air-dried basis.11
The samples were dried at 333 K to reach humidity in the 12 to 15% range, controlled by thermogravimetry. The solid was ground and passed through a USS sieve No. 200 (0.074 mm). Part of the kaolinite clay was dispersed in doubly deionised water for several hours and was further purified using an established method.11 The sample examined by powder X-ray diffractometry identified the presence of clay similar to those resulting from conventional sample preparation procedures, such as air-dried oriented mounts, ethylene glycol solvated and heated at 573 and 773 K.
Intercalation and delamination procedures
The kaolinite sample was intercalated by mixing about 10 g of the clay with 2.0 g of urea through a grinding procedure, in an agate vibratory mill for a period of 360 min at room temperature. The resulting solid, named KUR, was washed with deionized water and dried for 2 h at 333 K. To perform the delamination, initially 5 g of the intercalated KUR sample was suspended in 5.0 cm3 of 0.10 mmol dm-3 hydrochloric acid solution. This suspension was maintained for 1 h in an ultrasonic bath, Bedelin RK 1028 ultrasonic cleaner, operated at 35 kHz. After filtration through sintered glass, the solid named KUR/DL was dried in vacuum for 12 h at room temperature.
The batch adsorption methodology studies were carried out with about 60 mg of the natural, intercalated or delaminated kaolinite samples in a series of flasks containing 20.0 cm3 of aqueous solution containing the metal ion, varying in concentration from 7.0 × 10-3 to 7.0 × 10-4 mol dm-3 at 298 ± 1 K. Firstly, the effect of pH on adsorption for all clay samples was evaluated by varying this parameter over the range from 1.0 to 5.0, with addition of 0.10 mol dm-3 of nitric acid or sodium hydroxide. For these determinations, the number of moles adsorbed per gram (Nf) is calculated by the difference between the number of moles initially present (Ni) and the number of moles of metal remaining in the supernatant (Ns) divided by the mass (m) of the compound,19-21 using equation 1.
The time required to reach equilibrium was obtained through specific isotherms, by considering concentration versus time. Equilibrium was reached in less than 10 h; however, a time period of 12 h was chosen to ensure maximum adsorption. Then, after establishing this experimental condition, the same procedure was used to obtain the isotherm with maximum adsorption at chosen pH. Based on these data the final concentration isotherm was obtained using this condition, which enabled obtaining the maxima adsorption capacity. Thus, the number of moles of cation adsorbed (Nf) increased with its concentration in the supernatant (Cs) as a function of pH during 12 h, until a plateau was reached, indicating total saturation of the acidic centers in the layered structure.19-21
The most commonly used isotherm is that proposed by Langmuir, which was originally derived for gas adsorption on planar surfaces such as glass, mica and platinum. However, this procedure has also been applied to cation adsorption on porous surfaces in the classical Langmuir form. For this adsorption model, the amount of the adsorbate in the equilibrium solution upon reaching the plateau of the isotherm enabled determination of the KL and b parameters, which reflect the activity of the surface for the adsorbing species. The constant b establishes the upper limit for adsorption and represents the maximum value, determined by the number of reactive surface sites in kaolinite structure,19-21 as represented by equation 2:
Then, the Cs/Nf and the so-called distribution coefficient KL can be plotted against the concentration of the supernatant in the metal-containing solutions. If the Langmuir equation can be applied, the measured data should fall on a straight line with the slope giving KL and the intercept KLb values, since 1/KLb is the angular and 1/b the linear coefficients,10,21 as represented by equation 3.
Another fitting of the adsorption process was established by the Redlich-Peterson and Toth procedures as represented by equations 4 and 5, respectively:
where KRP and KT are constants related to adsorption capacity and n is an affinity constant of the adsorbent. Although equation 4 was previously employed empirically, it can be derived with the assumption of a continuous variation in thermal effect during adsorption. There is no assurance that the derivations of the Redlich-Peterson and Toth equations are unique; consequently, if the collected data can fit the equations, it is only probable, but not proven, that the surface is heterogeneous. The Redlich-Peterson and Toth models unfortunately predict both infinite adsorption at infinite concentration and a corresponding thermal effect related to the adsorption at zero coverage.
Non-linear regression was compared to obtain the optimum kinetic sorption and isothermal parameters. A trial and error procedure was employed for non-linear methods using the solver add-in functions of Microsoft Excel software. In the trial and error procedure, isotherm and kinetic parameters were determined by maximizing the coefficients of determination values.21 The least square method was used to analyze the linear form of the kinetic and isotherm models.
The coefficient of determination values (r2) were used in order to find the degrees of fit of the isotherm adsorption and kinetic models with the experimental data,22 as defined by equation 6:
where NfEXP (mmol g-1) is the experimental amount of divalent cation exchanged by the original and modified kaolinite samples and NfCAL (mmol g-1) is the amount of cation obtained by kinetic isotherm models.
X-ray powder diffraction (XRD) patterns were recorded with a Philips PW 1050 diffractometer using CuKα (0.154 nm) radiation in the 2q region between 2 to 65ºat a speed of 2º per min and steps of 0.05º.
The samples for infrared spectroscopy were oven-dried at 393 K to remove adsorbed water. Each sample of about 1.3 mg was finely ground for 1 min, combined with 100.0 mg of oven-dried spectroscopic grade KBr and pressed with 7.0 ton into a disc under vacuum. The spectrum of each sample was recorded in triplicate between 400 and 4000 cm-1 by accumulating 64 scans at 4 cm-1 resolution, using a Perkin-Elmer 1760X Fourier transform infrared instrument.
BET (Brunauer-Emmett-Teller) surface areas and porosity measurements of the natural, intercalated and delaminated kaolinite samples were determined using a Quantachome/Nova Surface Area-Pore Volume Analyzer, Model 1200/5.01. The mesopore size distribution was obtained by applying the BJH (Barret-Joyner-Halenda) method to the adsorption branch of the isotherm.
The natural kaolinite (KNAT) and the intercalated (KUR) and intercalated-delaminated (KUR/DL) forms were analyzed by inductively coupled plasma optical emission spectrometry (ICP OES), using a Perkin Elmer 3000 DV instrument. The oven-dried powdered samples weighing 231.0, 230.0 and 234.0 mg, respectively, were placed separately on weighed glass dishes and transferred quantitatively to pre-cleaned nitric acid digestion bottles. The samples were then digested with 7.0 cm3 of concentrated nitric and hydrochloric acids in 1:3 proportions in volume, with an identical volume of hydrofluoric acid over 5 days. The samples were cooled in an ice-bath and 25.0 cm3 of 0.10 mol dm-3 boric acid was added with stirring, followed by 50 cm3 of deionized water, and the solution was then diluted to 100.0 cm3. For each sample, a blank and a set of elemental standards were run to calibrate the instrument.
Transmission electron microscopy (TEM) images were recorded on a JEM 3010 URP microscope at the LNLS/Brazil with an accelerating voltage of 300 kV. For this determination the samples were prepared by placing a drop of a suspension of particles dispersed in isopropanol onto a carbon-coated copper grid.
The samples for scanning electron microscopy (SEM) were prepared on orientated blades at 298 ± 1 K and sputtered with gold. The instrument used was a model LEO-ZEISS, 430 Vp, using conditions of analysis for secondary images obtained to 20 kV, with a working distance of 11 mm.
Results and Discussion
Elemental analyses from the ICP OES technique for the original clay sample, KNAT, gave results consistent with kaolinite, with aluminum being the major component. The total mineralogical composition is given by 46.46; 39.42; 0.48; 0.27; 0.26; 0.22 and 0.18% of SiO2, Al2O3, Fe2O3, MgO, Na2O, CaO and K2O, respectively, and 12.63% of mass was lost in the ignition process.
X-ray powder diffraction
The determination of the total mineralogical composition of the pristine natural clay sample was carried out on oriented mounts, exhibiting mainly kaolinite, quartz and goethite, besides the existence of mica in low concentration, as shown in Figure 1a, in agreement with the elemental analysis. These considerations are based on chemical analyses and characteristics X-ray diffraction (XRD) peaks of these minerals.4
From diffraction patterns, the d001 values were determined and the results are listed in Table 1. After the intercalation process the kaolinite presented, as expected, an increase in the basal distance, changing the d001 value from 0.72 nm for natural kaolinite to 1.08 nm for the intercalated form, as shown in Figures 1Aa and 1Ab. It was also observed that the KNAT sample presents a slightly broader and less intense peak, in comparison with KUR, a behavior that could be attributed to differences in the degree of crystallinity, which was calculated by using the Biscaye equation,8 as listed in Table 1, due to the effect of urea insertion, to give 0.90 and 0.88 for the natural and intercalated forms. The delaminated clay sample gave characteristics of a collapsed structure and low crystallinity, as shown in Figure 1Ac, which suggested the clear influence of the delamination process on the kaolinite structure. The natural kaolinite and its intercalated form, in expanded scale in part B of Figure 1Bb, presents the new peak with d001 at 1.27 nm that is attributed to urea interaction inside the kaolinite layer. When hydrated kaolinite was intercalated with 20% urea and washed with water under ultrasound, a distance of 0.84 nm was obtained.14 The d001 values for the delaminated kaolinite are in agreement with previous results.15,16
The Fourier-transform infrared spectra of the natural kaolinite KNAT, intercalated KUR and the delaminated form KUR/DL are shown in Figure 2. The original KNAT sample exhibited all characteristic hydroxyl stretching bands5 attributed to the inner-surface hydroxyls oriented towards the interlayer at 3695 cm-1. The bands at 3622 and 3463 cm-1 are assigned to those hydroxyl groups oriented towards the vacant sites in the external layers of the kaolinite structure.6 Additional weak, broad bands of kaolinite at 3463 cm-1 and another weak one at 1639 cm-1 can be associated with water adsorbed on the external surface.14
The spectrum of the intercalated material presented a similar set of frequencies for hydroxyl vibrations as does natural KNAT, which is in agreement with other kaolinite-urea complexes.14 The bands located at 3505, 1683 and 1463 cm-1 were assigned to N-H, C=O and C-N stretching vibrations, respectively. The band at 3505 cm-1 is attributed to the formation of a hydrogen bond between the NH2 urea group and oxygen atoms from the basal tetrahedral sheet.17 The intercalated KUR displayed characteristic hydroxyl stretching bands at 3670 and 3650 cm-1, but with reduced intensity and strongly broadened. This behavior may be attributed to the loss of hydrogen bonding of the outer hydroxyls between the layers. In addition, there are two new sets of weak bands: (i) the formation of hydrogen bonds between NH2 urea groups and O-Si-O groups of kaolinite in the 3381 to 3505 cm-1 interval and (ii) the symmetric and asymmetric vibrational modes of NH2 urea groups that interact with oxygen atoms of the Si2O5 layers in the 3204 to 3413 cm-1 region.17 The C=O stretching vibration of the urea molecule is also observed at 1683 cm-1 for the intercalated urea-kaolinite, as observed before.18
The gaseous nitrogen adsorption values for natural, intercalated and delaminated kaolinite samples are listed in Table 1. The nitrogen BET data was used to calculate the specific surface areas for comparative purposes. The BET surface areas of the kaolinite samples demonstrated that intercalation and delamination processes caused the formation of mesopores in the solid particles, resulting in a higher surface area, 90.5 m2 g-1, relative to the natural sample, KNAT, with 20.3 m2 g-1. The pore size distribution in the mesopores region was obtained by applying the BJH method from the nitrogen isotherms at 77 K. The pore size distribution was compared by considering natural and intercalated samples, as shown in Figure 3. The natural kaolinite sample exhibited a pore volume of 3.54 cm3 g-1, while the intercalated and delaminated kaolinites gave values of 3.90 cm3 g-1 and 8.75 cm3 g-1 respectively. The KUR and KUR/DL samples presented a unimodal distribution of pore sizes, while KNAT has a bimodal distribution. The present values of surface areas are in agreement with those reported before in the 5 to 25 m2g-1 interval for kaolinite,24 which depends on particle size distribution, particle shape, and distribution of cracks and pores in the material, and therefore, cannot be represented as a general characteristic of a particular type of material.25
The TEM and SEM images were obtained in parallel position related to the layers, in 010 or 100 planes, as shown in Figures 4 and 5, respectively. The images for natural and delaminated kaolinites in the 001 plane are shown in Figures 4a and 4b, respectively. The individual crystals presented themselves as flakes in a pseudo-hexagonal form, as confirmed by TEM images, and the delaminated kaolinite structure is shown in Figure 4b. The reduction of particle size after the delamination process is shown in the TEM image, where the separation and disintegration into small stacks of flakes is clear, in comparison with Figure 4a, which could be attributed to the use of ultrasonic procedure.
SEM images were used to probe the changes in the morphological features of KNAT and KUR/DL samples, as shown in Figures 5a and 5b, respectively. The surface morphology of a natural sample presents corn-flake like crystals with a cottony appearance, revealing its extremely fine plate-like structure, Figure 5a. However, after intercalation, the clay becomes more porous and fluffy, Figure 5b. This appearance is probably due to the change in the surface charge of the particle, as a result of the intercalation process, and the reduction in amorphous phase originally associated with the natural clay sample. However, both samples present thick stacks with thin single flakes, as are observed for other chemically modified kaolinites. This texture is not consistent with the propensity of KUR/DL to convert spontaneously into individual flakes or small stacks of pseudo-hexagonal flakes as shown in Figure 5b.
Effect of pH
The pH of the aqueous solution, which increased almost linearly up to pH 5.0, is an important controlling parameter in the adsorption process. Both the extent of adsorption and the amount adsorbed (Nf) showed positive changes. The influence of the pH on the concentration adsorbed for natural and modified kaolinites is shown in Figure 6, demonstrating that the cation exchanges strongly as the acidity of the solution decreases. The adsorption experiments at pH values higher that 5.0 were not carried out due to the risks of cation hydrolysis.21
For a strongly acidic medium, the proton concentration outnumbers the lead ions in the adsorptive solution. Thus, and it is expected that, at low pH, the adsorptive sites will be covered by protons. By increasing the pH, the surface sites become free for adsorption of the various lead species. Similar observations have already been reported for lead in natural and chemically modified clay adsorption processes.19
The number of available hydrogen ions is high at low pH values and copper cations must compete with them to exchange all adsorption sites on the inorganic surface. These active sites on the adsorbent surface are gradually deprotonated with the increase in pH, favoring copper uptake, with an adsorption mechanism similar to that previously reported.1-3
Adsorption processes involve an array of phenomena that can alter the distribution of undesirable agents on the constituent phases and interfaces of a given system.20 Thus, adsorption at a surface or interface is mainly a result of binding forces between the individual atoms, molecules or ions of the adsorbate to the surface, all of these forces having some electrostatic effects to promote interaction.21 Divalent cations (M2+) can be adsorbed on the available surface sites, denoted by ΞSOH, where S represents silicon or aluminum atoms in the inorganic structure, these atoms being main elements in the clay composition, as listed in Table 2. For this process, the reactive edge sites (OH and NH2 groups) on the surface can interact with cations in solution, as given by equations 7 to 9:
On the surface sites the original ΞSOH group can exchange with cations (M2+), as represented in equations 10 and 11:
During the course of the adsorption the inner-sphere interactive process is predominant over that of the outer-sphere for divalent metal cations adsorbed by edge sites.20 Both cations presented similar isotherms with kaolinite and its intercalated and delaminated forms, as exemplified for copper in Figure 7 and lead in Figure 8. As observed, for the matrix containing urea, the adsorption amounts are higher at the saturation isotherm plateau. The maximum adsorption capacities, Nfmax, for each metal on natural and modified kaolinites are listed in Table 2. The adsorptions are higher for modified matrices.
These results were adjusted to fit the Langmuir, Redlich-Peterson and Toth models, as listed in Table 3, and the linear and nonlinear correlation adjustments from these equations are shown in Figure 9. All three adsorption models can be used to explain the significant adsorptive capacity of the intercalated matrix and to quantify copper and lead interactions with these inorganic matrices, although the Langmuir model presents a significant advantage in comparison with the others. It allows the quantification of the capacity of cations in the structure of the matrix and the evaluation of the constant related to the binding energy.
The interaction of these cations with the intercalated surfaces of the kaolinite structure is governed by the microenvironment around each arrangement, which is usually composed of basic centers, mainly in the internal structure of hydration. Hydroxyl groups act as bridges that result in the kaolinite matrix intercalation process.
Pseudo-first order kinetics using the Lagergren equation26-38 is generally expressed by equation 12:
After integration and applying the boundary conditions, Nt = 0 for t = 0 and Nt = Nt at t = t, the integrated form of equation 12 becomes:
where NfEQ and Nf are the amounts of metal adsorbed at equilibrium and at a given time t (mmol g-1), respectively, and k1 is the rate constant for pseudo-first order adsorption (min-1).
When the rate of reaction of an adsorption reaction is controlled by chemical exchange, then a pseudo-second order model can be better adjusted to the experimental kinetic data,26-39 as expressed by equation 14.
After integration and applying the boundary conditions, Nt = 0 for t = 0 and Nt = Nt at t = t, the integrated form of equation 14 becomes:
where k2 is the pseudo-second order rate (mmol-1 min-1). The values of k2 can be obtained from the y-intercept of the linear plot of t / Nf versus t.
Carrying out a set of experiments at constant temperature and monitoring the amount adsorbed with time, the kinetics of the adsorption process should be known. The adsorption using the Lagergren model can also be explored,26-38 as proposed in equation 12.
The useful Elovich equation for energetically heterogeneous solid surfaces is represented by equations 16 and 17 in nonlinear and linear1 forms, respectively:
where α and β, the Elovich coefficients, represent the initial adsorption rate (mmol g-1 min-1) and the desorption coefficient (g mmol-1), respectively.
The modified and natural kaolinites showed identical behavior towards copper and lead uptake with increasing interaction time at pH 5.0. Adsorption increased rapidly up to 1 h and slowly increased as equilibrium was reached, as shown in Figure 10. The lead uptake became almost constant after 200 min for natural and after 150 min for intercalated kaolinite samples, which can be considered reaching the equilibrium condition. The initial high rate of adsorption can be attributed to the existence the exposed basic centers for interaction on the readily accessible surfaces. However, as the coverage increased, the number of available surface sites for adsorption decreases until it reaches equilibrium, when the uptake is controlled by the rate at which the adsorbate is transported from the exterior to the interior sites of the adsorbent particles.
Second order kinetic plots presented better linearity with R > 0.99, and the second order rate constant, k2, varied from 4.8 to 10.9 and from 4.9 to 12.9 g mg-1 min-1 with the linear method and from 5.0 to 11.0 and 4.9 to 13.0 g mg-1 min-1 with the nonlinear method for copper and lead cations, respectively, as listed in Table 4. A comparison of Nf experimental values and those obtained from the slopes of the second order plots showed values in the 11.40 to 2.5 mmol g-1 range for copper with kaolinite and lead for intercalated urea matrices with linear and nonlinear analyses, respectively, as shown in Figures 11 and 12. Considering all the above results, the kinetics of second order for cation adsorption on natural and modified kaolinites is better adjusted for both metals.1
Second order kinetics suggests that the number of adsorption sites on the clay surface and the number of heavy metal cations in the liquid phase together determine the kinetics. Depending on pH, different cationic species may be held to the clay surface at appropriate ion-exchange sites.27
Synthesized urea-intercalated kaolinite, originally from the Perus region, Brazil, has high stability, into which active basic sites can be introduced, improving the physical-chemical properties of the precursor clay. For example, the specific area of the original kaolinite, 20.3 m2 g-1, changed after intercalation and delamination to 44.5 and 90.5 m2 g-1, respectively. Identically, the modified clays, when applied to the metal adsorption process, increased their capacities for divalent lead and copper removal, a favorable condition attributed to the available edge sites on the inorganic backbone, to give the order Pb > Cu.
Adsorption either on natural or intercalated clays increased continuously with pH, by limiting the hydrolysis of both cations and NH2 anchored in the kaolinite surface. The most appropriate condition was chosen to be pH 5.0 at room temperature, presenting a plateau at 200 and 150 min for natural and modified kaolinites, respectively. The copper and lead cations showed very rapid initial uptakes on both inorganic supports before reaching the plateau. Langmuir, Redlich-Peterson and Toth isotherms yielded good fits with the adsorption data for cation/clay interactions.
The kinetics of adsorption of both heavy metals used in this investigation on natural, intercalated and delaminated kaolinites were complex, but it seems that this interactive effect is better expressed by a pseudo-second order process. Linear and nonlinear regression methods were compared to evaluate the experimental data with a pseudo-second order kinetic model. Non-linear regression exhibited a higher coefficient of determination for the isotherm and the kinetic analyses than a linear regression.
The authors are indebted to CNPq for fellowships and financial support, and LNLS from Campinas for the HRTEM measurements.
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Received: December 7, 2007
Web Release Date: October 16, 2008