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Marouane El Alouani, Saliha Alehyen, Mohammed El Achouri, M’hamed Taibi, "Preparation, Characterization, and Application of Metakaolin-Based Geopolymer for Removal of Methylene Blue from Aqueous Solution", Journal of Chemistry, vol. 2019, Article ID 4212901, 14 pages, 2019. https://doi.org/10.1155/2019/4212901
Preparation, Characterization, and Application of Metakaolin-Based Geopolymer for Removal of Methylene Blue from Aqueous Solution
Metakaolin-based geopolymers are aluminosilicate materials that can be used as cationic dye adsorbents in aqueous system treatment. Our aim in this paper is to study the ability of geopolymer powder produced from metakaolin and alkaline activators to act as an adsorbent to remove methylene blue (MB). The solid materials were systematically analyzed by X-ray fluorescence (XRF), X-ray diffraction (XRD), Fourier-transform infrared spectrometery (FTIR), scanning electron microscopy (SEM), energy dispersive X-ray analysis (EDX), and the point of zero charge. XRF, FTIR, XRD, SEM, and EDX analyses confirmed the formation of a geopolymer composite by geopolymerization reaction. The influence of various experimental factors such as geopolymer dosage, pH, initial dye concentration, contact time, and temperature was assessed. Adsorption isotherms were evaluated by Langmuir, Freundlich, Temkin, and Dubinin–Radushkevich isotherms. Kinetics data were studied using pseudo-first-order, pseudo-second-order, and intraparticle diffusion models. The thermodynamic parameters, namely, Gibbs free energy (ΔG°), enthalpy (ΔH°), and entropy (ΔS°), were determined. The results indicated that the maximum decolorization was found in high pH values. The collected isotherm data were best fitted by the Langmuir isotherm, and the maximum adsorption capacity of dye onto the geopolymer was 43.48 mg/g. The experiment kinetics followed the pseudo-second-order kinetic models. The thermodynamic results demonstrated that the adsorption of the obtained material occurs spontaneously as an endothermic process. The results confirmed that the prepared adsorbent can be used for remediation of water contaminated by MB dye.
The rapid industrial growth has led to the release of different dyes in the aquatic environment, and the treatment of effluents has become a challenging topic in environmental sciences. With the wide applications of dyes in multiple fields such as textile, leather, additives, petroleum product, paper, cotton, wool, plastic, and pharmaceutical industries, water pollution caused by the colorants is increased, which has attracted the attention of the scientific community [1, 2]. Generally, synthetic nondegradable dyes not only pollute water resources but also affect the human health because of their toxic nature . In addition, their presence in aquatic systems, even at low concentrations, reduces the penetration of light and therefore has a detrimental effect on photosynthesis . Consequently, the presence of trace amounts of these micropollutants (<1 ppm) in industrial wastewater is extremely noticeable and unwanted . Among the most used industrial dyes, methylene blue (MB) is a basic dyestuff widely used in various industries such as textile dyeing, petroleum industries, and color photography. Therefore, the treatment of water contaminated by these chemicals is necessary both for the protection of the environment and for the reuse of these unconventional waters. In recent years, different techniques have been developed and tested to recover toxic substances from wastewaters before discharging into an aquatic environment, such as coagulation , advanced oxidation , photocatalytic degradation , ultrafiltration , ion-exchange , electrochemical treatment , and adsorption [12–15]. Among various physicochemical processes, adsorption is a technique of choice due to its low cost, simple design, and reusability [16, 17]. Different categories of natural and synthetic adsorbents were utilized for the removal of this organic material from aquatic media, such as kaolin , zeolite , activated carbon , mesoporous birnessite , natural clay , magnetic chitosan , fruit peels , biochar microparticles , silica , loofah sponge-based porous carbons , pyrophyllite , and Fe3O4/activated montmorillonite nanocomposite . Among the synthesized adsorbents mostly used to remove organic matters are geopolymers . Geopolymers, firstly named by Joseph Davidovits , are formed by activation of aluminosilicate precursors, and these solids can be natural (kaolin, mica, andalusite, spinelle, illite, or Slag Hill) or synthetic (metakaolin, fly ash, calcined by-products, or industrial residues) activated by alkali silicate solution (typically Na or K) at temperatures between 20°C and 100°C . Corresponding to different Si/Al ratios, the materials are composed of network structures of (Na, K)-poly(sialate) (-O-Si-O-Al-O-)n, (Na, K)-poly(sialat-siloxo) (-O-Si-O-Al-O-Si-O)n, and (Na, K)-poly(sialate-disiloxo) (O-Si-O-Al-O-Si-O-Si-O-)n . The geopolymers or inorganic polymers have also gained significant attention as efficient adsorbents with good physical and chemical properties. Recently, several studies were conducted in the interest of activation of aluminosilicate precursors characterized and tested for removal of dyestuffs and hazardous materials from aquatic environment [8, 31, 32].
In this work, a geopolymerization method was applied to synthesize the metakaolin-based geopolymer. The structural and morphological properties of the elaborated adsorbent were characterized by XRF, XRD, FTIR, and SEM analyses. The adsorption properties of the elaborated sample were studied in different experimental conditions, including adsorbent mass, pH, contact time, initial dye solution, and temperature. The adsorption kinetics, isotherms, and thermodynamics data of the adsorption were investigated to study the batch adsorption process of the basic dye using the synthesized metakaolin-based geopolymer.
2. Materials and Experimental Methods
2.1. Materials and Chemicals
Kaolin was collected from Bab Mssila situated at Ribat El Kheir next to Sefrou city in the northwest of Morocco. The raw clay was subjected to calcination at temperatures of 800°C for 3 h.
The industrial-grade sodium silicate powder (Honeywell Riedel-de Haën, Germany; 18 wt.% Na2O, 63 wt.% SiO2, 18 wt.% loss on ignition) and commercial sodium hydroxide (NaOH; 99% purity) (ACS AR-grade pellets) were provided by Sigma-Aldrich. Methylene blue (MB) dye with the chemical composition C16H18ClN3S and a MW of 319,852 g/mol was supplied by Sigma-Aldrich.
2.2. Geopolymer Synthesis
The geopolymer sample was synthesized in several steps. The first step was to synthesize the activator solution by initially dissolving Na2SiO3 powder and sodium hydroxide NaOH (12 M) at a mass ratio of 2.5 . The mixture was stirred at room temperature for a period of 15 min. The second step of the elaboration is the mixing of metakaolin with the activator solution, which was conducted using in a mixer with constant stirring at ambient temperature for 15 min to obtain good homogenization. Then, distilled water was added at a ratio water/metakaolin of 0.34 to obtain the desired workability of the geopolymer paste. The mixture was placed in a cylindrical mould and treated at 60°C for 24 hours. Finally, the matrix was sieved to particle sizes <200 μm and stored in a desiccator for characterization and investigation of the adsorption tests. The mix proportions of the metakaolin-based geopolymer pastes are displayed in Table 1.
2.3. Adsorption Experiments
A series of batch adsorption experiments were carried out under different operating conditions related to adsorbent mass (0.05–0.35 g), contact time (0–220 min), initial solution pH (2–13), initial dye concentration (5–60 mg/L), and temperature (20–70°C), at a constant agitation speed (250 rpm) (Table 2). The solution pH was adjusted to optimum values using 0.1 M NaOH or 0.1 M HCl. Afterwards, the sample was centrifuged at 2500 rpm for 10 min. The initial and the residual concentrations of MB were measured using a spectrophotometer at a wavelength of 664 nm. The removal efficiency of the metakaolin-based geopolymer was calculated using equation (1), adsorption capacity at any time qt (mg·g−1) was obtained using equation (2), and adsorption capacity at equilibrium qe (mg·g−1) was determined using equation (3):where Ci (mg·L−1) is the initial concentration of MB solution, Ce (mg·L−1) and Ct (mg·L−1) are, respectively, the liquid-phase concentration of MB at initial time and at any time t after the adsorption process, m (g) is the weight of geopolymer, and V (L) is the volume of the MB solution.
2.4. Instrument Analysis
The chemical compositions of materials and the prepared adsorbent were determined by X-ray fluorescence using a spectrometer dispersion wavelength-type Axios. The crystalline phases of the sample were detected using an X-ray diffractometer (Philips model 1840 equipment). The functional groups of samples were detected using Fourier-transform infrared spectrometry bruker platinum ATR apparatus, in the range of 4000–400 cm−1 wavelengths. The microstructure of metakaolin and metakaolin-based geopolymer was observed using the JEOL-6300F field-scanning electron microscope (SEM/EDX). The concentration of MB was determined using the spectrophotometer JASCO V-630 UV/VIS. A pH-meter model (M 210) was used for pH measurement.
The pH at the point of zero charge (pHpzc) of the geopolymer was determined by the method described by Pawar et al. . A series of (0.01 M) KNO3 solution (V = 100 mL) were prepared, and the initial pH of KNO3 was adjusted to a given value from pH 2 to 13 by the addition of HCl (0.1 M) or NaOH (0.1 M). To each solution, 0.1 g of geopolymer was added and shaken for 48 h with an agitation speed of 120 rpm at room temperature. The differences between the pH value of the initial solution (pHI) and the final solution (pHF) were plotted as a function of pHI. The point of intersection of this curve yielded the point of zero charge.
3. Results and Discussion
3.1. Structural Analysis
3.1.1. Chemical Analysis of Solids
The chemical composition of metakaolin and the synthesized sample is illustrated in Table 3. The XRF analysis indicates that the metakaolin is basically formed by SiO2, Al2O3, and Na2O. After activation of metakaolin by the alkali solution, it was found that a new inorganic material with an Si/Al ratio of approximately 2.04 was formed, indicating the poly(sialate-siloxo) (PSS) (-Si-O-Al-O-Si-O-)n nature of the formed material .
3.1.2. X-Ray Diffraction
Figure 1 shows the XRD patterns of kaolin, metakaolin, and geopolymer. The results of DRX analysis for kaolin show that the material is rich in kaolinite and quartz. After calcination, the disappearance of the peaks corresponding to kaolinite is observed, which is explained by the dehydroxylation of the water molecules that exist in the kaolinite structure in metakaolinite by heat treatment . After the activation process, the crystalline phases were dissolved in the alkaline solution and the aluminosilicate phase was formed in the surface of metakaolin by geopolymerization reaction . These results indicated the formation of a new product with a structure different from that of metakaolin.
3.1.3. Infrared Spectroscopy
The FTIR spectra of kaolin, metakaolin, and elaborated matrix are depicted in Figure 2, and all the band assignments are presented in Table 4. In kaolin, the bands at 3350 and 1622 cm−1 correspond to OH stretching and deformation of the hydroxyl group, respectively. The adsorption band appearing at 1436 cm−1 is related to the stretching vibrations of O-C-O due to atmospheric carbonation on the surface of kaolin. The band at 1151 cm−1 is due to the Si-O outside of the plane-stretching vibration. The most intensive band at 998 was due to Si-O-Al stretching vibration. Bands which exist between 757 cm–1 and 532 cm–1 correspond to stretching vibrations of Si-O-Al. The band at 437 cm−1 is related to the Si-O-Si bending vibration. After calcination, no bands were observed between 3350 and 1622 cm−1 in metakaolin, suggesting that the thermal treatment was adequate to convert kaolin to metakaolin. The asymmetric stretching vibration of Si-O-T (T = Al or Si) at 988 cm−1 in metakaolin shifted approximately 9 cm−1 after the geopolymerization reaction to 979 cm−1. The shifting and reduction of peaks in FTIR spectrum confirms the formation of a the poly(sialate-siloxo) chain in the structure by geopolymerization reaction .
3.1.4. Microstructural Analysis (SEM/EDX)
Figure 3 shows the representative SEM images of metakaolin and the synthesized matrix. The surface morphology of metakaolin was different from that of the geopolymer matrix. SEM images (Figure 3(a)) of metakaolin showed that the sample is a heterogeneous material consisting of irregularly shaped particles. After the geopolymerization reaction (Figure 3(b)), the morphology of the geopolymer is constituted by a chain of polysilicate layers by the complete disappearance of metakaolin particles. This morphological change observed in the synthesized geopolymer is due to the dissolution of metakaolin aluminosilicates in the activator solution leading to the formation of aluminosilicate gel. EDX microanalysis was used to characterize the elemental composition of the metakaolin and geopolymer (Figure 3). According to the EDX analysis (Figure 3(a)), the major elements were oxygen, silicon, and aluminum, with proportion values of 49.87, 20.77, and 14.88%, respectively. The percentage of sodium elements increased from 0.61 to 14.17% (Figure 3(b)); this is due to the alkali activator used in the geopolymerization process.
3.2. Batch Adsorption Test
3.2.1. Effect of Adsorbent Dose
The effect of adsorbent dose on the removal of MB was investigated, and the results are shown in Figure 4. As can be seen, when the geopolymer mass increased from 0.05 to 0.35 g/L, the MB removal efficiency increased from 55% to 99.77%. This result might attribute to the increasing number of binding sites in the geopolymer for MB removal by increasing the quantity of adsorbents . A similar trend was obtained for this toxic dye removal on the geopolymer paste  and phosphoric acid-based geopolymers . Optimizing the mass of the adsorbent is a very important parameter for controlling the adsorption capacity. According to the experimental results, the adsorption assays should be performed using 0.1 g/100 mL for MB.
3.2.2. Effect of pH on the Removal Efficiency and pH Point of Zero Charge (pHpzc) of Geopolymer
The influence of pH is an important factor for removal of organic matter from water. Figure 5(a) represents the effect of the solutionʼs initial pH in the adsorption process. It is observed that the removal efficiency increases with the rise in the pH value and reaches 91.2% at a pH value of 12.06. The removal is affected by the change in the pH value of the solution. In acidic medium, the surface of the geopolymer is surrounded by H+ ions, which decrease the interaction of the solute ions (MB+) with the sites of the geopolymeric material. On the contrary, in the basic medium, the concentration of H+ ions decreases and generates a good interaction between the dye ions and the sites of the surface. Similar adsorption behaviors of MB were reported by several investigations [20, 51]. In order to confirm this result, it is necessary to determine the pHpzc of the adsorbent. The zero point of charge (PZC) is defined as the number of positive charges equal to the number of negative charges that exist on the surface of the adsorbent. The pHPZC of the geopolymer is shown in Figure 5(b) and the pHPZC value of the adsorbent was found almost to be 9. Thus, at pH < 9, the surface of the geopolymer is positively charged and becomes negatively charged at pH > 9. Therefore, with increasing pH above pHpzc = 9, the removal of cationic dye by the geopolymer increased slightly. The removal increase can be explained by electrostatic attraction between the particles of the geopolymer, which is negatively charged, and the cationic dye, which is positively charged . These results show that the attraction between the inorganic framework (negatively charged) and the methylene blue (positively charged) depends on pH.
3.2.3. Effect of Contact Time and Kinetics
(1) Effect of Contact Time. The effect of contact time on the removal of MB by the geopolymer is shown in Figure 6. The results demonstrate that the removal percentage of MB is rapid in the first 30 min of contact time. Afterwards, the equilibrium time is reached within 180, 180, and 150 min for 20, 30, and 40 mg/L, respectively. After the equilibrium, no significant change in the removal percentage of the geopolymer was observed in the different dye concentration. It was observed that for an increased contact time from 30 to 240 min, the efficiency augmented from 87.50 to 100%, 90 to 99%, and 87.50 to 97.90% for concentrations of 20, 30, and 40 mg/L, respectively. It can be seen that the decrease of MB removal with increasing initial MB concentration is due to the saturation of the adsorbent surface at high dye concentrations. Similar result was reported by Hamid et al. .
(2) Kinetics Studies. There are several mathematical models used to describe the adsorption kinetics of pollutants onto the adsorbent material. In this study, three kinetic models (pseudo-first-order, pseudo-second-order, and intraparticle diffusion) were applied for the adsorption of MB by the geopolymer to describe the adsorption process.
The pseudo-first-order model  is expressed as follows:
The pseudo-second-order model  is represented by the following equation:
The intraparticle diffusion model  is given by the following equation:where qe (mg/g) is the adsorption capacity at equilibrium, qt (mg/g) is the adsorbed concentration of MB at time t, k1 (1/min) is the pseudo-first-order rate constant for the adsorption process, k2 (g/mg·min) is the pseudo-second-order rate constant for the adsorption process, kI (mg/(g·min0.5)) is the intraparticle diffusion rate constant, and I (mg/g) is the intercept.
The fitting results are shown in Figures 7(a)–7(c), and the kinetics constants and correlation coefficients calculated for pseudo-first-order, pseudo-second-order, and intraparticle-diffusion equations are listed in Table 5. These results revealed that the adsorption of MB on the geopolymer matrix is best described by the pseudo-second-order kinetic model with a high correlation coefficient (0.999), and the calculated qe(cal) values are in agreement with experimental qe(exp) values at different initial MB concentrations. These results indicate that the chemical interaction process involves electron sharing and exchange between MB and functional groups of the geopolymer . Similar results were also found in previous studies [23, 58].
The sialate geopolymer network consists of (SiO4) and (AlO4) groups connected by covalent bond Si-O-Al-. The (Na+) cations present in the structural cavities of the poly(sialate) balance the negative charge of Al3+ in coordination (IV) . During the adsorption phenomena, the removal of MB by the adsorbent can be explained by the interactions between the positive charge of (MB+) and the negative charge of Al tetrahedral (-Si-O-Al−-O-Si-O) in the metakaolin-based geopolymer (Figure 8). This proposed mechanism explains the chemisorption of methylene blue by the metakaolin-based geopolymer.
3.2.4. Effect of Initial Concentration Dye and Isotherms
(1) Effect of Initial Concentration Dye. The effect of varying MB initial concentration on the adsorption capacity of MB by the geopolymer is shown in Figure 9. It can be seen that the adsorption capacity of MB increased as the initial MB concentration increased. Adsorption capacities of the geopolymer increase with the initial MB concentration increase due to the increase in the driving force of the concentration gradient . A similar observation was reported previously for MB removal on mesoporous birnessite  and Cu-BTC .
(2) Isotherm Studies. To investigate the adsorption mechanism of the distribution of adsorbate molecules between the liquid and the solid phase, four different models (Langmuir, Freundlich, Temkin, and Dubinin–Radushkevich) were employed to fit the adsorption data.
3.3. Langmuir Isotherm
Langmuir isotherm model is applied to explain the adsorption mechanism onto a homogeneous surface and calculate the monolayer adsorption capacity in the surface of the adsorbent . This model is expressed by the following:where qe is the amount of dye at equilibrium (mg/g), Ce is the equilibrium concentration of the pollutant (mg/L), qm is the amount of monolayer adsorption capacity (mg/g), and KL is the Langmuir constant (L/mg).
The essential characteristic of the Langmuir isotherm can be expressed by the dimensionless constant separation factor RL defined by following relationship:where KL (L/mg) is the Langmuir adsorption constant, C0 (mg/L) is the initial MB concentration. The RL values classification is given in Table 6 .
3.4. Freundlich Isotherm
The Freundlich model is applicable to describe the multilayer adsorption process on active sites .
A linear form of the Freundlich model may be written as follows:where KF (mg(1−n)Lng−1) is the adsorption capacity and 1/n is the adsorption intensity.
3.5. Dubinin–Radushkevich (D–R) Isotherm
The D–R isotherm model is a simple model applied to explain the nature of adsorption on the homogeneous or heterogeneous surface of an adsorbent and validated in high concentrations of adsorbate to determine the type of adsorption (physical or chemical) [63–65]. The simplified D–R isotherm equation is expressed as follows:where K is the D–R constant of the sorption energy (mol2/kJ2) and ε is the Polanyi potential which is given bywhere T is the temperature (K), R is the gas constant (8.314 J·mol−1·K−1), Ce (mg/L) is the equilibrium concentration of MB left in solution, and qm is the D–R maximum adsorption capacity.
The value mean energy of sorption, E (kJ/mol), equation can be calculated from D–R parameter K as follows:
The value of E is useful for estimating the mechanism of the adsorption reaction (chemical or physical adsorption). The value of E between 1 kJ/mol and 8 kJ/mol corresponds to physical adsorption, the E value between 8 and 16 kJ/mol corresponds to adsorption by chemisorption, and when the value of E is greater than 16 kJ/mol, adsorption may be dominated by particle diffusion [66, 67].
3.6. Temkin Isotherm
The Temkin isotherm assumes that the sorption decreases linearly when the interaction between the surface of the adsorbent and adsorbate increases. The linear Temkin model has been used in the following form :where BT = RT/bT, bT is the Temkin constant related to heat of sorption (J/mol), AT is the Temkin isotherm constant (L/g), R is the universal gas constant (8.314 J/mol·K), and T is the temperature (K).
Figure 10 represents the Langmuir, Freundlich, Temkin, and Dubinin–Radushkevich isotherm models. The constants calculated from the model equations (Langmuir, Freundlich, Temkin, and Dubinin–Radushkevich isotherm) are shown in Table 7. As observed, the value of R2 obtained from the Langmuir isotherm equation (0.994) was higher than that from the Freundlich (0.963), Dubinin–Radushkevich (0.915) and Temkin (0.980) isotherm equations. These results showed that the adsorption experiments data could be well described by the Langmuir model. The adsorption occurred on the homogeneous surface as a monolayer, and the maximum monolayer adsorption capacity (qmax) was found to be 43.48 mg/g. The RL value was obtained within the range 0 < RL < 1, indicating that the adsorption of cationic dye on the geopolymer material is favorable. In addition, Table 8 presents a summary of the maximum adsorption capacity qmax of the developed adsorbents for MB dyestuff in the aqueous medium. A comparison with other reported adsorbents showed that the qmax value for the geopolymer used in this study is the highest, indicating that this new solid is an excellent adsorbent for the treatment of water containing MB dye.
3.6.1. Thermodynamic of Adsorption
Thermodynamic parameters have an important role to evaluate the phenomenon of the adsorption process. The thermodynamic parameters, namely, free energy (ΔG°), enthalpy (ΔH°), and entropy (ΔS°), for adsorption process were obtained using the following equations :where qe is the amount of dye adsorbed per unit mass of the adsorbent at equilibrium (mg/g), Ce is the equilibrium concentration (mg/L), R is the universal gas constant (8.314 J·mol−1·K−1), and T is the solution temperature (K).
The values of enthalpy (ΔH°) and entropy (ΔS°) were calculated from the slope and intercept of the plot of ln Kd versus 1/T (Figure 11). The thermodynamic parameters for methylene blue adsorption on the composite adsorbent at various temperatures are summarized in Table 9. The positive values of entropy (ΔS°) indicate a random increase during adsorption. The negative values of enthalpy ΔH° indicate the endothermic nature of the process. Moreover, the values of ΔG° determined are negative, thus confirming that the adsorption process is spontaneous and thermodynamically favorable. A similar phenomenon has been observed in the adsorption of MB on pomegranate peel activated carbon .
In summary, a metakaolin-based geopolymer was produced from metakaolin and alkali activators and used as an adsorbent for cationic dye removal. XRF, XRD, FTIR, and SEM studies show that a geoadsorbent was formed by the geopolymerization process. The optimum conditions of adsorption by geopolymer were found to be a geopolymer mass of 0.1 g in 100 mL of MB, an initial concentration of MB 40 mg/L, a contact time of 120 min, and a basic pH. The kinetics study of initial concentration demonstrated that adsorption equilibrium was found to follow the pseudo-second-order equation. The isotherm models data were better described by Langmuir isotherm equation with a maximum monolayer adsorption capacity of 43.48 mg/g. The values of the thermodynamic parameters indicated that the adsorption was spontaneous and endothermic in nature. The overall results prove that the geopolymer has a great potential and a high selectivity and can be considered an economical adsorbent for the elimination of methylene blue from aqueous medium by batch operation.
The data used to support the findings of this study are available from the corresponding author upon request.
Conflicts of Interest
The authors declare that they have no conflicts of interest.
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