Contamination of the environment by heavy metals is a major concern. Lead is an extremely toxic heavy metal that enters the environment through various industrial activities, agricultural applications and improper waste disposal (Jaishankar et al., Reference Jaishankar, Tseten, Anbalagan, Mathew and Beeregowda2014; Joseph et al., Reference Joseph, Jun, Flora, Park and Yoon2019). Metals from all sources accumulate in the environment and, in most cases, extreme levels of lead in ecosystems lead to environmental contamination (Raj & Das, Reference Raj and Das2023). Hence, the pollution of the environment by Pb, among the other heavy metals, has been studied worldwide. For instance, Pb pollution in Türkiye was reported at 23.8–178 ppm in İzmit Bay (Pekey, Reference Pekey2006), 141–797 ppm in Golden Horn Estuary (Ergin et al., Reference Ergin, Saydam, Basturk, Erdem and Yoruk1991), 11.6–305 ppm in Demirören Alteration area (Vural, Reference Vural2015) and 7.78–19.7 ppm in the sediments and 8.48–24.1 ppm in the water of Süreyyabey Dam Lake (Erdoğan et al., Reference Erdoğan, Başaran Kankılıç, Seyfe, Tavşanoğlu and Akın2023). Pb pollution in sediments was reported at 36–83 ppm in Bangladesh (Islam et al., Reference Islam, Ahmed, Raknuzzaman, Habibullah-Al-Mamun and Islam2015), 26.39–77.66 ppm in China (Liu et al., Reference Liu, Xu, Liu, Zhang and Dai2009) and 55–450 ppm in Brazil (Pereira et al., Reference Pereira, Baptista-Neto, Smith and McAllister2007). Lead persists in the environment as it is non-biodegradable, and it accumulates in humans and animals via their consumption of contaminated food and water (Joseph et al., Reference Joseph, Jun, Flora, Park and Yoon2019). Uptake of lead by humans causes cumulative toxicity in the body, which affects multiple systems and organs, causing serious health problems (Njoroge et al., Reference Njoroge, Njagi, Orinda, Sekadde-Kigondu and Kayima2008).
Lead has both stable (204Pb, 206Pb, 207Pb and 208Pb) and radioactive (210Pb, 211Pb, 212Pb and 214Pb) isotopes present in the environment. In addition to its toxic property, lead also has a radiotoxic property due to its radioactive isotopes. Among these isotopes, 210Pb, formed during the 238U decay chain, is the most radiotoxic isotope of lead due to its long half-life of 22.23 (12) years (Nucleide Lara, 2023). As can be seen from the decay scheme in Fig. 1, 210Pb first decays to 210Bi, emitting β-particles (15.0 and 61.5 keV) and γ-rays (46.6 keV), then 210Bi decays to 210Po, emitting β-particles (1161 keV), and then 210Po decays to stable 206Pb, emitting α-particles (5305 keV; Anokhina et al., Reference Anokhina, Aoki, Ariga, Arrabito, Autiero and Badertscher2008). It can be understood from this scheme that until stable 206Pb is formed, 210Pb, 210Bi and 210Po also contribute to the radioactivity and hence the radiotoxicity of lead in the environment. For this reason, the remediation of both stable and radioactive lead from the environment is of critical importance. It should be mentioned that the allowable lead concentration is limited to 10 μg L–1 in drinking water according to the World Health Organization (WHO) and European Union (EU; WHO, 2017; EU, 2020; Dettori et al., Reference Dettori, Arghittu, Deiana, Castiglia and Azara2022). Moreover, WHO limits 210Pb isotopes in drinking water as 0.1 Bq L–1 (WHO, 2017).
The decay scheme of 210Pb to 210Bi and 210Po. The half-lives of the radioisotopes are given in parentheses (Anokhina et al. Reference Anokhina, Aoki, Ariga, Arrabito, Autiero and Badertscher2008; Nucleide Lara 2023).
Conventionally, Pb(II)-contaminated water is treated using various physicochemical treatment techniques, including chemical precipitation, coagulation, flocculation, ion exchange, adsorption and filtration (Fu & Wang, Reference Fu and Wang2011; Kumar et al., Reference Kumar, Dwivedi and Oh2022). Among these techniques, chemical-based treatment techniques are used most often; however, their adverse effects on the environment increase demand for cleaner treatment processes such as membrane filtration, adsorption and electrochemical, hydrogel, photocatalysis, biological and bio-integrated treatment techniques (Kumar et al., Reference Kumar, Dwivedi and Oh2022). Adsorption has been the most used technology for the removal of heavy metals from wastewater (Fei & Hu, Reference Fei and Hu2023). In this method, the adsorbate (contaminant) adheres to the surface of the adsorbent through physical (electrostatic attraction) or chemical (ion exchange, complexation, precipitation) means. However, environmental conditions (e.g. pH, temperature, adsorbent-to-adsorbate ratio, stirring rate, etc.) affect the adsorption capacities of the adsorbents.
Treatment of industrial wastewater by adsorption for the removal of heavy metals using long-term durable, cheap, sustainable and environmentally friendly adsorbents with high adsorption capacity and selectivity, rapid kinetics of adsorption and desorption and low energy penalties for regeneration is of great importance (Velarde et al., Reference Velarde, Nabavi, Escalera, Antti and Akhtar2023). This requires adsorbents to have a large accessible surface area providing abundant exposed active sites for strong and selective binding with heavy metal ions. The effective surface area of an adsorbent exposed to heavy metal ions in an aqueous solution is also influenced by water dispersibility, hydrophilicity, functionality and other properties (Fei & Hu, Reference Fei and Hu2023). There are various kinds of adsorbents, such as activated carbon, carbon nanotubes, graphene oxide, mesoporous silica, mesoporous carbon, clays, zeolites, metal–organic frameworks and adsorbents from industrial/agricultural byproduct residues (Fei & Hu, Reference Fei and Hu2023; Velarde et al., Reference Velarde, Nabavi, Escalera, Antti and Akhtar2023). Naturally occurring minerals are preferred as adsorbents due to their chemical structures, adsorption properties and global abundance. In addition to the use of these raw minerals, minerals modified and treated through heat treatment, acid activation, ion exchange and mechanochemical processing have also been studied extensively in the literature for the adsorption of heavy metals in terms of their ability to increase the adsorption, cation-exchange capacity (CEC) and specific surface area of such minerals (Bhattacharyya & Gupta, Reference Bhattacharyya and Gupta2008; Novikau & Lujaniene, Reference Novikau and Lujaniene2022). Surfaces modified with metal-binding groups have a greater ability to capture heavy metal ions. For instance, it has been shown that phosphate-modified kaolinite clay (Unuabonah et al., Reference Unuabonah, Adebowale and Olu-Owolabi2007), lanthanum oxide-modified bentonite (Lingamdinne et al., Reference Lingamdinne, Amelirad, Koduru, Karri, Chang, Dehghani and Mubarak2023), hexadecyltrimethylammonium (HDTMA)- and phenyl fatty hydroxamic acid (PFHA)-modified bentonite (Hamadneh et al., Reference Hamadneh, Abu-Zurayk, Abu-Irmaileh, Bozeya and Al-Dujaili2015) and alkaline-treated zeolite (El-Arish et al., Reference El-Arish, Zaki, Miskan, Setiabudi and Jaafar2022) demonstrate greater adsorption capacities, leading to greater Pb2+ ion removal percentages. Synthesized adsorbents based on mesoporous silica, such as SBA-15, MCM-41 and MCM-48, with or without modification, have also been used for the removal of heavy metals due to their large surface areas and porous structures (Benhamou et al., Reference Benhamou, Baudu, Derriche and Basly2009; Hernández-Morales et al., Reference Hernández-Morales, Nava, Acosta-Silva, Macías-Sánchez, Pérez-Bueno and Pawelec2012; Anbia et al., Reference Anbia, Kargosha and Khoshbooei2015; Guo et al., Reference Guo, Liu, Zhao, Gong, Guo and Huang2017; Albayati et al., Reference Albayati, Sabri and Abed2019).
Bentonites are naturally occurring clays that consist primarily of smectite minerals, usually montmorillonite. Bentonites are abundantly occurring clay minerals of the 2:1 layer type (i.e. a central octahedral alumina sheet sandwiched between two tetrahedral silica sheets; Abdullahi & Audu, Reference Abdullahi and Audu2017; Kloprogge, Reference Kloprogge, Gates, Kloprogge, Madejova and Bergaya2017). Zeolites are hydrated aluminosilicates composed of networks of [SiO4]4− and [AlO4]5− tetrahedra linked to each other with oxygen atoms (Delkash et al., Reference Delkash, Ebrazi Bakhshayesh and Kazemian2015; Khaleque et al., Reference Khaleque, Alam, Hoque, Mondal, Haider and Xu2020). Each oxygen atom within Si–O and Al–O bonds connects two cations and is shared between the two tetrahedra (Moshoeshoe et al., Reference Moshoeshoe, Nadiye-Tabbiruka and Obuseng2017). The isomorphic substitution within the sheets of bentonite, involving the substitution of Al3+ for Si4+ in the tetrahedral layer and Mg2+ or Fe3+ for Al3+ in the octahedral layer (Eren et al., Reference Eren, Afsin and Onal2009) or the isomorphic substitution of Al3+ for Si4+ within the tectosilicate framework of zeolite (Moshoeshoe et al., Reference Moshoeshoe, Nadiye-Tabbiruka and Obuseng2017), generates a negative charge. This negative charge is balanced by the exchangeable cations such as Ca2+, Mg2+ and Na+ located in the interlayer spaces (Delkash et al., Reference Delkash, Ebrazi Bakhshayesh and Kazemian2015; Abdullahi & Audu, Reference Abdullahi and Audu2017; Kloprogge, Reference Kloprogge, Gates, Kloprogge, Madejova and Bergaya2017; Khaleque et al., Reference Khaleque, Alam, Hoque, Mondal, Haider and Xu2020).
Perlite is an aluminosilicate hydrated volcanic glass of obsidian that has a rhyolitic composition with generally >70% silica. It also contains exchangeable cations such as K+ and Na+ and up to 5% water. The adsorbent nature of perlite is due to the hydroxyl groups bound to the silicon atoms on the surface of the perlite. The silicon atoms at the surface tend to maintain their tetrahedral coordination with oxygen and attach to the monovalent hydroxyl groups, forming silanol groups (Alkan & Doğan, Reference Alkan and Doğan2001; Ghassabzadeh et al., Reference Ghassabzadeh, Torab-Mostaedi, Mohaddespour, Maragheh, Ahmadi and Zaheri2010). A hyper-light material (i.e. expanded perlite) can be obtained by heating the perlite to 760–1100°C, causing the material to expand up to 20 times its original volume (Çelik et al., Reference Çelik, Kılıç and Çakal2013; Aghabeyk et al., Reference Aghabeyk, Azadmehr and Hezarkhani2022).
Lead removal from aqueous solutions has been reported in the literature by utilizing either natural or treated clinoptilolite (Günay et al., Reference Günay, Arslankaya and Tosun2007; Wang et al., Reference Wang, Terdkiatburana and Tadé2008; Rakhym et al., Reference Rakhym, Seilkhanova and Kurmanbayeva2020), bentonite (Donat et al., Reference Donat, Akdogan, Erdem and Cetisli2005; Guerra et al., Reference Guerra, Mello, Resende and Silva2013; Pawar et al., Reference Pawar, Lalhmunsiama Bajaj and Lee2016) or perlite (Sari et al., Reference Sari, Tuzen, Citak and Soylak2007; Ghassabzadeh et al., Reference Ghassabzadeh, Torab-Mostaedi, Mohaddespour, Maragheh, Ahmadi and Zaheri2010; Irani et al., Reference Irani, Amjadi and Mousavian2011). Although there have been various studies on the adsorption of lead on raw, modified or treated minerals, we found no study in the literature to have investigated the adsorption of radioactive lead on aluminosilicate-based adsorbent materials and the use of a liquid scintillation counter (LSC; β-spectrometer) as a 210Pb determination technique in an adsorption study. In addition, we found no study to have compared the lead adsorption capacities of bentonite, zeolite and perlite.
Therefore, this study aims: (1) to characterize bentonite, zeolite and perlite minerals from various provinces in Türkiye in detail; (2) to study and compare the adsorption of Pb2+ ions using these minerals by varying the experimental conditions; (3) to fit the experimental data using various adsorption isotherm models; (4) to discuss the adsorption mechanisms of Pb2+ ions on the adsorbents; (5) to characterize the adsorbents after Pb2+ ion adsorption; (6) to repeat the adsorption experiments by contaminating the Pb2+ ion solution with radioactive 210Pb isotopes; and (7) to compare the removal percentages according to the obtained stable Pb2+ ion (inductively coupled plasma optical emission spectroscopy; ICP-OES) and radioactive 210Pb2+ isotope (LSC) results.
Materials and methods
Materials
Bentonite (Ordu, Türkiye), zeolite (clinoptilolite, Nevşehir, Türkiye) and expanded perlite (İzmir, Türkiye) were used as adsorbents throughout the study. The zeolite and bentonite minerals were first washed with Milli-Q water before characterization and batch adsorption experiments to remove water-soluble impurities and then dried at 110°C (Mipro MLF-120, Türkiye) for 4 h, whereas expanded perlite was used as received. Pb (NO3)2 (≥99.0% purity, Sigma-Aldrich) and a sample with known 210Pb activity concentration were used as lead sources. All of the other chemicals used in this study were purchased as analytical grade.
Mineralogical and petrographic analyses of the adsorbents
The crystal structure of the adsorbents was investigated using an Inel Equinox 1000 X-ray diffractometer (XRD) equipped with a Co X-ray tube. XRD traces were recorded at 5–60°2θ at steps of 0.02°. The chemical analysis of the adsorbents was performed using a Spectro X-LAB 2000 polarized energy dispersive X-ray fluorescence (PED-XRF) spectrometer. Infrared spectra of the adsorbents were recorded in the 4000–400 cm–1 region on a Varian/660-IR Fourier-transform infrared (FTIR) spectrometer. The surface morphology and elemental composition of the adsorbents were obtained using scanning electron microscopy (SEM)–energy-dispersive spectrometry (EDS) analysis with a ZEISS EVO 40 device. XRF and FTIR analyses of the adsorbents were also carried out after the batch adsorption experiments.
Physicochemical properties of the adsorbents
Water absorption capacities
The water adsorption capacities of the adsorbents were determined according to the ASTM C127-88 (1993) standard. First, a known amount of dried sample was kept in Milli-Q water for 24 h at room temperature. After removing the excess water from the samples, ~1 g of wet sample was weighed and dried in an oven at 110°C for 4 h. The mass loss was calculated to determine the water absorption capacity of the adsorbent samples. This procedure was repeated three times and the values were averaged.
Cation-exchange capacities
The CEC values of the adsorbents were found by means of the ASTM C837-09 standard and following work by Topal (Reference Topal1996) using the methylene blue (MB) adsorption test. This test was carried out to determine the amount of MB dye absorbed by the sample through ion exchange, which was also correlated with the CEC of the adsorbent samples. For this test, 2 g of clay sample were added to 300 mL Milli-Q water. After uniform dispersion of the adsorbent samples in water (stirring for 5 min), small increments (2–5 mL) of MB dye were added to the samples. Then a small drop was dripped from this solution onto filter paper every few minutes until a blue halo appeared around the drop. The blue halo indicated that the endpoint had been reached, which also denoted that there was excess MB dye in the solution that was not absorbed by the mineral. Once the halo was seen, the volume of MB dye added to the solution was recorded to calculate the CEC of the mineral. The CEC (meq 100 g–1) was determined using Equation 1 (Topal, Reference Topal1996):
where W B is the dry mass of the adsorbent sample used (g), V MB is the volume of MB dye added into the clay mixture until the endpoint is reached (mL) and N MB is the normality of the MB solution (N), which was 0.03125 N in this test.
Dissolution in water
The dissolution of the adsorbents in Milli-Q water was observed at room temperature after keeping the samples in water for 24 h. The dissolved ions were determined according to ICP-OES analysis of the filtrates. The solid residues were also dried in an oven at 80°C for 4 h and the mass loss of the samples was determined to evaluate the amount dissolved.
Particle size
The Sauter mean particle size of the adsorbents was determined using a Malvern Mastersizer 3000E. The samples were dispersed in water and the measurements were performed at a stirring speed of 500 rpm.
BET surface area
The Brunauer–Emmett–Teller (BET) surface areas of the adsorbents were determined using Quantachrome Autosorb 6B.
Point of zero charge
The salt addition technique was used to determine the point of zero charge (PZC) of the adsorbent materials (Bakatula et al., Reference Bakatula, Richard, Neculita and Zagury2018). In this technique, 0.2 g of adsorbent material was added to 40.0 mL of 0.1 M NaNO3 solution in a series of 50 mL glass bottles. The pH was adjusted with 0.1 M HNO3 and 0.1 M NaOH to obtain the appropriate pH range of 3, 5, 7, 9 and 11 (±0.1 pH units). First, the initial pH values (pHi) of the supernatant solutions were recorded. Then, the samples were shaken at 200 rpm for 24 h using an orbital shaking incubator (Mipro MLI-120, Türkiye). The final pH values (pHf) were measured and the difference in the pH values (ΔpH = pHf – pHi) was calculated. The PZC values were found from the linear ΔpH–pHi plots for each adsorbent. The PZC values were determined at ΔpH = 0, as at this PZC value the positive and negative charges on the surface of the adsorbent were equal.
Ζ-potential
The ζ-potential values of the samples were determined at pH 7 using a Malvern Zetasizer Nano ZS90 device.
Batch adsorption experiments using stable Pb2+ ion solution
The batch adsorption experiments of lead-contaminated waters were performed in 50 mL glass bottles according to ASTM 4646-03 (2016) to determine the effects of the initial pH value of the solution (3–9), adsorbent dosage (1–10 g L–1), initial Pb2+ concentration (100–800 ppm), temperature (25–60°C), contact time (15–1440 min) and shaking rate (0–150 rpm). The effect of pH was examined by dispersing 0.25 g of adsorbent in a 50 mL Pb2+ solution at a concentration of 200 ppm and adjusting the pH of the solution using 1 M HCl or 1 M NaOH. The effect of the shaking rate was determined using an orbital shaking incubator (Mipro MLI-120, Türkiye). After the batch adsorption experiments, the filtrate was separated from the adsorbent using filter paper, and Pb2+ concentration in the filtrate was determined used ICP-OES. A schematic diagram showing the batch adsorption experiments is given in Fig. 2. Reproducibility experiments were also performed. The differences in Pb2+ ion concentrations under the same experimental conditions were found to be ~5%.
Schematic diagram of the batch adsorption experiments for stable Pb2+ and radioactive 210Pb. The batch adsorption experiments for the adsorption of stable Pb2+ were performed using Pb(NO3)2 and the batch adsorption experiments for the adsorption of radioactive 210Pb were performed using both Pb(NO3)2 and 210Pb as contaminants.
The adsorption capacity (qt, mg g–1), removal rate (R, %) and distribution coefficient (Kd, mL g–1) were calculated using Equations 2, 3 and 4, respectively.
where C 0 is the initial mass concentration of the adsorbate (ppm), C t is the mass concentration of the adsorbate at any t (ppm), V is the volume of the aqueous solution (L), M is the mass of the adsorbent (g) and q t = q e at C t = C e, with q e and C e denoting the equilibrium adsorption capacity and equilibrium mass concentration, respectively.
Adsorption isotherms were determined using the Langmuir, Freundlich and Dubinin–Radushkevich equations. The thermodynamic parameters such as the change in Gibbs free energy (ΔG°), enthalpy (ΔH°) and entropy (ΔS°) related to the adsorption of Pb2+ ions on the adsorbents were evaluated using Equations 5 and 6 and plotting ln(Kd) vs 1/T graphs.
In Equations 5 and 6, T is temperature in Kelvin and R is the universal gas constant (8.314 J mol–1 K–1).
Batch adsorption experiments using radioactive 210Pb isotope solution
The batch adsorption experiments were also performed with 210Pb-contaminated (17.86 ± 1.28 Bq L–1) 400 ppm Pb2+ ion solution at pH 7, contact time 2 h, adsorbent dosage 5 g L–1, shaking rate 75 rpm and temperature 25°C (Fig. 2). In addition to these experiments, two successive adsorption experiments were carried out at the same adsorption conditions with the filtrates of the previous adsorption in order to determine the complete adsorption of the isotopes by the adsorbents.
After each experiment, 5 mL of the filtrate were mixed with 15 mL of scintillation cocktail (Optiphase HiSafe 3, Perkin Elmer) and assessed at least three times for 200 min in a LSC (Quantulus 1220, Perkin Elmer). The count values were then averaged. The calibration of LSC was performed according to Çakal et al. (Reference Çakal, Güven and Yücel2015) before the analyses. The counts for gross α (210Po) and gross β (210Pb and 210Bi) were acquired separately, and then the total β-spectrum was evaluated as stated by Limon (Reference Limon2016). The net 210Pb count was calculated by subtracting the counts belonging to 210Bi (counts between 350 and 650 channels) from the total count in the β-spectrum. The activity concentrations were calculated using Equation 7:
where A is the activity concentration (Bq L–1), N is the net count, t c is the counting time (s), ε is the detector efficiency (%) and V is the sample volume (L). The minimum detectable concentrations (MDCs) of the LSC system were calculated as MDCα = 0.03 Bq L–1 and MDCβ = 0.26 Bq L–1.
Results and discussion
Mineralogical and petrographic analyses of the adsorbent materials
XRD analysis
XRD traces were acquired for bentonite, zeolite and perlite (Fig. 3). It was found that bentonite was mainly composed of montmorillonite (Mt), with the other reflections on the diffraction traces belonging to vermiculite (V), kaolin (K) and illite (I). The main constituent of zeolite was clinoptilolite (Cl). Trace amounts of mordenite (Mr) and quartz (Q) were also present in its structure. Perlite consisted of amorphous mineral phases with albite (A) and opal-CT (O) present as impurities.
XRD traces of the adsorbents.
XRF analysis
The chemical analysis of the adsorbent materials is given in Table 1. It was observed that the main components of the adsorbents were Si (30.65–33.04%) and Al (6.90–7.52%). The main cations were Mg (1.06%) and Ca (2.56%) in bentonite, K (1.56%) and Ca (2.24%) in zeolite and Na (2.63%), Mg (1.60%) and K (3.60%) in perlite.
Elemental compositions (%) of the adsorbent materials before and after batch adsorption experiments as obtained from XRF spectrometry.
LOI = loss on ignition.
As is known, the Si/Al ratio plays an important role in the adsorption performance of materials. A greater Si/Al ratio results in greater thermal and physical stability, whereas a lower Si/Al ratio exhibit greater CEC (Delkash et al., Reference Delkash, Ebrazi Bakhshayesh and Kazemian2015; Costafreda & Martin, Reference Costafreda and Martín2021) because the greater the amount of aluminium in the adsorbent structure, the more cationic sites that will be formed. A Si/Al ratio of 4–5, indicating very high physicochemical durability and relatively high cation exchange, was reported previously (Delkash et al., Reference Delkash, Ebrazi Bakhshayesh and Kazemian2015). The Si/Al ratios of bentonite, zeolite and perlite were found to be 4.12, 4.22 and 4.79, respectively.
SEM–EDS analysis
SEM images of the adsorbent samples are given in Fig. 4a–c. Bentonite (Fig. 4a) had structural defects on the surface of the particles, which increased its surface area. Zeolite (Fig. 4b) was formed from platelets that conglomerated into non-porous, large-sized particles of submicron size on their flat surface. Perlite (Fig. 4c) was formed from thin, transparent, glassy layers.
SEM images of (a) bentonite (20,000× magnification), (b) zeolite (20,000× magnification) and (c) perlite (10,000× magnification) and EDS analyses of (d) bentonite, (e) zeolite and (f) perlite.
Results of the EDS analyses of the adsorbents are given in Fig. 4d–f and the elemental compositions of the samples are presented in Table 2. The elemental compositions of the adsorbents obtained using EDS were different from those determined using XRF spectrometry for some of the elements, despite the same bulk sample being analysed. These differences were due to the fact that XRF analysis was performed by using the bulk composition, whereas EDS analysis was conducted using a spot-sized sample.
Elemental composition (wt.%) of the adsorbent materials as obtained from EDS.
FTIR analysis
The FTIR spectra of bentonite, zeolite and perlite were recorded in the 4000–400 cm–1 region (Fig. 5). All the FTIR spectra of these adsorbents demonstrated similar bands in their structures. The bands at 3630–3560 cm–1 were assigned to structural OH stretching vibrations in the Si–OH and Al–OH groups (Wang et al., Reference Wang, Dong, He, Chen and Yu2009; Abdullahi & Audu, Reference Abdullahi and Audu2017), with the 3630 cm–1 band originating from the Al2OH stretching vibration (Tabak et al., Reference Tabak, Yilmaz, Eren, Caglar, Afsin and Sarihan2011). The peaks at 1650–1610 cm–1 corresponded to bending vibrations of the hydroxyl groups of physisorbed free water (Wang et al., Reference Wang, Dong, He, Chen and Yu2009; Tabak et al., Reference Tabak, Yilmaz, Eren, Caglar, Afsin and Sarihan2011; Hannachi et al., Reference Hannachi, Homri and Boubaker2013; Abdullahi & Audu, Reference Abdullahi and Audu2017; Vicentin & Costa da Rocha, Reference Vicentin and Costa da Rocha2021). The bands at 1010 cm–1 represented the stretching vibrations of Si–O bonds (Korkuna et al., Reference Korkuna, Leboda, Skubiszewska-Zieba, Vrublevs'ka, Gun'ko and Ryczkowski2006; Abdallah & Yilmazer, Reference Abdallah and Yilmazer2011; Hannachi et al., Reference Hannachi, Homri and Boubaker2013; Abdullahi & Audu, Reference Abdullahi and Audu2017). The bands at 790–750 cm–1 corresponded to Si–O bond stretching of the silicate (Abdallah & Yilmazer, Reference Abdallah and Yilmazer2011; Vicentin & Costa da Rocha, Reference Vicentin and Costa da Rocha2021). The bands at 520 cm–1 were due to Al–Si–O bending vibrations (Wang et al., Reference Wang, Dong, He, Chen and Yu2009; Abdallah & Yilmazer, Reference Abdallah and Yilmazer2011; Hannachi et al., Reference Hannachi, Homri and Boubaker2013).
FTIR spectra of the adsorbents before and after Pb2+ ion adsorption.
Physicochemical properties of the adsorbents
The results obtained during the physicochemical investigation of the bentonite, zeolite and perlite samples are given in Table 3. The minerals used in this study had bulk densities and mean particle sizes in the ranges of 1.97–2.76 g cm–3 and 21.6–34.7 μm, respectively. As is known, the water absorption capacity, CEC and BET surface area of the materials are the main physicochemical properties to consider when an adsorbent is being selected for the remediation of contaminated water sources. Although these properties affect the adsorption capacity, these data should be evaluated together with the adsorption capacity data attained from the batch adsorption experiments. If the BET surface area is high in addition to the water absorption capacity of the material being high, contaminated water is transferred more into the pores and the adsorbate has a greater chance of exchanging with the cations of the adsorbent materials. Bentonite (Fig. 4a), having the greatest BET surface area (85.25 m2 g–1), had the highest CEC (40.63 meq 100 g–1). Perlite (Fig. 4c), on the other hand, having the greatest water absorption capacity (58.2%), had the lowest CEC (7.81 meq 100 g–1) and BET (3.42 m2 g–1) values. CEC has been reported in the literature as 65 and 108 meq 100 g–1 (Özgüven et al., Reference Özgüven, Pekdemir, Önal and Sarıkaya2020), 74 meq 100 g–1 (Tabak et al., Reference Tabak, Yilmaz, Eren, Caglar, Afsin and Sarihan2011), 85 meq 100 g–1 (Roulia & Vassiliadis, Reference Roulia and Vassiliadis2008) and 33.2 meq 100 g–1 (Juang et al., Reference Juang, Lin, Huang and Cheng2004) for bentonite, 2.7–3.2 mg g–1 (Delkash et al., Reference Delkash, Ebrazi Bakhshayesh and Kazemian2015), 60.5 and 57.2 meq 100 g–1 (Yukselen-Aksoy, Reference Yukselen-Aksoy2010), 2.60–2.80 meq g–1 (Krol, Reference Krol2019) and 12 mmol 100 g–1 (Andryushchenko et al., Reference Andryushchenko, Safonov, Babich, Ivanov, Konevnik and Kondrashova2017) for zeolite, 6 mmol 100 g–1 (Andryushchenko et al., Reference Andryushchenko, Safonov, Babich, Ivanov, Konevnik and Kondrashova2017), 25 meq 100 g–1 (Roulia & Vassiliadis, Reference Roulia and Vassiliadis2008) and 25.9 meq 100 g–1 (Alkan et al., Reference Alkan, Demirbaş and Dogan2005) for perlite and 35 meq 100 g–1 (Roulia & Vassiliadis, Reference Roulia and Vassiliadis2008) and 33.3 meq 100 g–1 (Alkan et al., Reference Alkan, Demirbaş and Dogan2005) for expanded perlite. BET surface areas have been given as 27 and 43 m2 g–1 (Özgüven et al., Reference Özgüven, Pekdemir, Önal and Sarıkaya2020), 43.1 m2 g–1 (Roulia & Vassiliadis, Reference Roulia and Vassiliadis2008), 35.5 m2 g–1 (Anirudhan & Ramachandran, Reference Anirudhan and Ramachandran2015), 29.5 m2 g–1 (Li et al., Reference Li, Hu, Sheng, Zhao and Huang2009) and 226–318 m2 g–1 (Juang et al., Reference Juang, Lin, Huang and Cheng2004) for bentonite, 35.85 m2 g–1 (Roshanfekr Rad & Anbia, Reference Roshanfekr Rad and Anbia2021), 13.69 m2 g–1 (Wijesinghe et al., Reference Wijesinghe, Dassanayake, Sommer, Jayasinghe, Scales and Chen2016) and 140 m2 g–1 (Nurliati et al., Reference Nurliati, Krisnandi, Sihombing and Salimin2015) for natural zeolite, 1.30 m2 g–1 (Roulia & Vassiliadis, Reference Roulia and Vassiliadis2008), 1.92 m2 g–1 (Irani et al., Reference Irani, Amjadi and Mousavian2011) and 1.22 m2 g–1 (Doğan et al., Reference Doğan, Alkan and Çakir1997) for perlite and 4.70 m2 g–1 (Roulia & Vassiliadis, Reference Roulia and Vassiliadis2008) and 2.30 m2 g–1 (Doğan et al., Reference Doğan, Alkan and Çakir1997) for expanded perlite. As can be seen, the CEC and BET values varied significantly among these previous studies. This is due to the chemical structure and composition of the adsorbent varying with its origin.
Physicochemical analyses of bentonite, zeolite and perlite.
PZC and ζ-potential are the other important parameters for adsorbents, as pH affects both the formation of lead compounds and the surface charge of the adsorbent. PZC was calculated to determine the pH value at which the positive and negative charges are equal and ζ-potential was calculated to determine the potential difference between the dispersion medium and the stationary layer of the fluid of the adsorbent, indicating the charge present on the adsorbent. At lower pH levels, H+ ions were adsorbed more than the other cations (adsorbate), leading to a positively charged surface. In contrast, at greater pH levels, OH– ions increased, leading to a negatively charged surface. By determining the PZC and ζ-potential, the experimental pH was selected to be in line with the preferred surface charge. For instance, during the adsorption of the Pb2+ ions, a negatively charged surface is desired so that the adsorption capacity of the adsorbent increases, enabling adsorption of cations through electrostatic attraction in addition to cation exchange. As can be seen from Table 3, the PZC values of all of the adsorbents were less than pH 7, indicating that the surface charges of the adsorbents were negative above their respective PZC values. The ζ-potentials being negative at pH 7 also supported this finding. The increase in the PZC values and the decrease in the ζ-potential values (Table 3) were observed to become greater with the amount of the exchangeable cations (K+, Na+, Ca2+, Mg2+; Tables 1 & 2). The PZC values have been reported in the literature as 3.0 (Mekhamer, Reference Mekhamer2010) and 6.3 (Li et al., Reference Li, Hu, Sheng, Zhao and Huang2009) for bentonite, 6.24–6.47 (Eberle et al., Reference Eberle, Börnick and Stolte2022), 4.7 (Roshanfekr Rad & Anbia, Reference Roshanfekr Rad and Anbia2021) and 2.2 (Nguyen et al., Reference Nguyen, Loganathan, Nguyen, Vigneswaran, Kandasamy and Naidu2015) for natural zeolite and 4.3 (Irani et al., Reference Irani, Amjadi and Mousavian2011) for perlite, all below pH 7. Besides these studies, reports have shown ζ-potentials of <0 within all of the studied pH ranges for bentonite (Onen & Gocer, Reference Onen and Gocer2019), zeolite (Yu et al., Reference Yu, Murthy, Shapter, Constantopoulos, Voelcker and Ellis2013) and perlite (Doğan et al., Reference Doğan, Alkan and Çakir1997).
While selecting the correct adsorbent for the remediation studies, the dissolution of the adsorbent should be controlled so as not to contaminate the water sources with the unwanted (toxic) ions released from the adsorbent materials. As can be seen in Table 3, bentonite demonstrated the greatest dissolution percentage, and so greatest amount of ions released into the environment (Table 4). As is shown, aluminium was released from bentonite (2.54 ppm) and zeolite (1.01 ppm), which could limit their use if they are to be used in large amounts. The results of the analysis of Milli-Q water before the dissolution test are also given in Table 4 for comparison.
Elemental analysis results of the dissolved elements of the adsorbents (ppm).
Batch adsorption experiments using stable Pb2+ ions
Effect of initial pH of the solution on Pb2+ ion adsorption
Initial pH is one of the most important parameters on Pb2+ ion adsorption, as pH affects both the formation of lead compounds and the surface charge of the adsorbent. The effect of the initial pH of the solution (pHi) on the adsorption of Pb2+ ions from the contaminated aqueous solution by bentonite, perlite and zeolite was investigated in the pH range of 3.0–9.0 at 25°C for 1440 min, an initial Pb2+ ion concentration of 200 ppm, a shaking rate of 75 rpm and an adsorbent dosage of 5 g L–1. As can be seen in Fig. 6, the removal percentage in terms of Pb2+ ion adsorption increased from 50% to 97% for zeolite and from 12% to 81% for perlite in the pH range of 3.0–9.0, whereas it increased from 74% to 96% in the pH range of 3.0–5.0 and further increased to 100% at pH 7.0–9.0 for bentonite. The low removal percentages at low pH values (pH < PZC) are due to the electrostatic repulsion between Pb2+ ions and the edge groups with a positive charge (Si–OH2+) on the surface of the adsorbents and to the excess amount of H3O+ ions in the solution (Sharifipour et al., Reference Sharifipour, Hojati, Landi and Cano2015). The adsorption of Pb2+ at pH < 6 can be attributed to the ion exchange between Pb2+ and H+/Mn + on the surface ion-exchange sites (Bourliva et al., Reference Bourliva, Michailidis, Sikalidis, Filippidis and Betsiou2013). From the Pourbaix diagram of lead (Lehto & Hou, Reference Lehto and Hou2010), it can be seen that lead exists in the form of Pb2+ until pH 7.5 and as PbOH+ in the pH range of 7.5–9.5. Hence, the initial pH of the solution was set at 7.0 in all of the batch adsorption experiments.
Effect of pH on the adsorption of Pb2+ ions using bentonite, zeolite and perlite. Adsorption conditions: initial concentration of Pb2+ = 200 ppm; adsorbent dosage = 5 g L–1; contact time = 1440 min; temperature = 25°C; shaking rate = 75 rpm.
The ζ-potentials of all adsorbents were found to be negative at pH 7.0 (Table 3), implying a negative potential difference between the dispersion medium and the stationary layer of the fluid of the adsorbent. Thus, the removal of lead can be caused by electrostatic attraction between the negatively charged adsorbent surface and the positively charged Pb2+ ions and also by ion exchange. In a study performed at pH 4–6 by Mao et al. (Reference Mao, Liu, Chu, Chen, Zou and Chen2023), it has been shown that Pb2+ was adsorbed by various minerals in the following order: montmorillonite > goethite > ferrihydrite > kaolinite. It was stated that due to its high electronegativity and typical CEC, montmorillonite had excellent adsorption properties (69.20 mg g–1 at pH 6.0; Mao et al., Reference Mao, Liu, Chu, Chen, Zou and Chen2023), which was similar to that observed in the present study.
Effect of contact time on Pb2+ ion adsorption
To investigate the effect of contact time on Pb2+ ion adsorption, the experiments were carried out at pH 7.0, temperature 25°C for 15–1440 min, an initial Pb2+ ion concentration of 400 ppm, a shaking rate of 75 rpm and an adsorbent dosage of 5.0 g L–1. As can be seen in Fig. 7, there was a rapid increase in the adsorption of lead on the adsorbents with increasing contact time, with the majority of the metal ions being adsorbed in the first 15 min. The removal percentage of Pb2+ ions increased from 92% (15 min) to 95% (120 min) for bentonite, from 40% (15 min) to 42% (60 min) for zeolite and from 19% (15 min) to 27% (60 min) for perlite. After the stated contact times, the removal percentages did not change as all of the available adsorbing sites on the adsorbent surface were occupied with the metal ions. This can be attributed to the instantaneous saturation of the adsorbent surface and the achievement of equilibrium within the first 1–2 h. Therefore, the contact time was set to 120 min in each experiment.
Effect of contact time on the adsorption of Pb2+ ions using bentonite, zeolite and perlite. Adsorption conditions: initial concentration of Pb2+ = 400 ppm; adsorbent dosage = 5 g L–1; temperature = 25°C; shaking rate = 75 rpm; pH = 7.
Effect of adsorbent dosage on Pb2+ ion adsorption
The effects of the adsorbent dosage on the adsorption of Pb2+ ions by bentonite, zeolite and perlite are given in Fig. 8. The amount of adsorbent dosage was varied between 1 and 10 g L–1 at pH 7.0, temperature 25°C, a contact time of 120 min, a shaking rate of 75 rpm and an initial Pb2+ ion concentration of 400 ppm. It is apparent that the removal percentage of Pb2+ ions increased with increasing adsorbent dosage (i.e. increasing the number of unsaturated adsorption sites) and hence the metal ion concentration in the solution decreased. Bentonite, having the greatest BET surface area (Table 3), had a removal percentage of 95% at the adsorbent dosage of 5 g L–1. On the other hand, zeolite and perlite had removal percentages of 82% and 41% at the adsorbent dosage of 10 g L–1, respectively. Although it is advantageous to achieve a progressive increase in the removal percentages with increasing adsorbent dosage, it should be noted that the ions that are released into the solution (Table 4) also increase with the adsorbent dosage, which may increase the contamination of the aqueous solution.
Effect of adsorbent dosage on the adsorption of Pb2+ ions using bentonite, zeolite and perlite. Adsorption conditions: initial concentration of Pb2+ = 400 ppm; temperature = 25°C; shaking rate = 75 rpm; pH = 7; contact time = 120 min.
Effect of initial Pb2+ ion concentration on Pb2+ ion adsorption: adsorption isotherms
The effect of initial Pb2+ ion concentration on Pb2+ ion adsorption was studied by varying the initial Pb2+ ion concentrations between 100 and 800 ppm at pH 7.0, temperature 25°C, a contact time of 120 min, a shaking rate of 75 rpm and an adsorbent dosage of 5 g L–1. As can be seen in Fig. 9, the adsorption capacity increased with increasing initial Pb2+ ion concentration. This is due to the fact that the mass transfer driving force becomes greater at greater initial adsorbate concentrations (Fayazi et al., Reference Fayazi, Afzali, Ghanei-Motlagh and Iraji2019). At greater Pb2+ ion concentrations, the number of Pb2+ ions that will interact with the active sites on the surfaces of the adsorbent materials increases, which, after some time, causes the adsorbent surface to reach saturation, leading to a decrease in the removal percentage. The removal percentages of adsorbents at 400 ppm initial Pb2+ ion concentration were found to be 95%, 27% and 42% for bentonite, zeolite and perlite, respectively. These percentages dropped drastically at 800 ppm for zeolite and perlite; however, a removal percentage of 79% was reached for bentonite at this initial concentration.
Effect of initial Pb2+ ion concentration on the adsorption of Pb2+ ions using bentonite, zeolite and perlite. Adsorption conditions: temperature = 25°C; shaking rate = 75 rpm; pH = 7; contact time = 120 min; adsorbent dosage = 5 g L–1.
The isotherm studies provide information on the adsorption capacities of the adsorbents, which is the most essential parameter in adsorption studies. The adsorption capacities obtained at varying ion concentrations for each adsorbent were used to evaluate certain constants that characterize the adsorption system. The experimental data regarding q e and C e were correlated using the linear forms of the Langmuir, Freundlich and Dubinin–Radushkevich isotherms (Fig. 10 & Table 5). By considering the correlation coefficients (R 2), it was observed that the Langmuir isotherm showed the best correlation within the studied concentration range for all adsorbents. The maximum adsorption capacities were 131.6, 36.1 and 21.5 mg g–1 for bentonite, zeolite and perlite, respectively. Their fit to the Langmuir isotherm confirms that the adsorption of Pb2+ ions on the adsorbents occurred through a single layer establishing the chemical bonds. Previous studies on the adsorption of Pb2+ ions from aqueous solutions using bentonite, perlite and zeolite reported similar results in the literature. Some of the maximum adsorption capacities found in the literature are compared with the results from this study in Table 6.
Isotherm models for Pb2+ adsorption on bentonite, zeolite and perlite. D–R = Dubinin–Radushkevich isotherm.
Isotherm models, model constants and coefficients of correlation (R 2) for the adsorption of Pb2+ ions onto bentonite, zeolite and perlite.
a q m is the maximum adsorption capacity of the adsorbents, KL and KF are the adsorption coefficients, n is the Freundlich constant, Ḱ is the adsorption energy constant, E is the average adsorption energy (E = 1/(2Ḱ)1/2) and ɛ is the adsorption potential (kJ mol–1; ɛ = RTln(1 + 1/C e)).
Pb(II) adsorption capacities of bentonite zeolite and perlite reported in the literature.
Effect of temperature on Pb2+ ion adsorption: adsorption thermodynamics
The effect of temperature on the adsorption of Pb2+ ion by bentonite, zeolite, and perlite was studied at temperatures of 25-60°C, pH 7.0 for 120 min, adsorbent dosage of 5 g/L, shaking rate of 75 rpm, and the initial Pb2+ ion concentration of 400 ppm. It was found that the removal percentage of bentonite and perlite changed slightly (0.9% for bentonite and 0.1% for perlite) with increasing temperature. However, the removal percentage of zeolite was increased from 42% (25°C) to 53% (60°C).
Thermodynamic parameters such as the Gibbs free energy change (ΔG°), enthalpy change (ΔH°) and entropy change (ΔS°) of adsorption were evaluated using Equations 4–6 (Table 7), with ΔH° and ΔS° being obtained from the slope and intercept of the lnKd – 1/T plot (Fig. 11). The Gibbs free energy change (ΔG°) indicates the degree of spontaneity of the adsorption process, enthalpy change (ΔH°) shows whether the adsorption is exothermic or endothermic and entropy change (ΔS°) reflects the degree of randomness. As can be seen in Table 7, adsorption occurred spontaneously for all of the adsorbents, with this behaviour increasing with increasing temperature. It was also observed that the process was endothermic and its randomness at the solid/liquid interface increased during the adsorption of Pb2+ ions onto the adsorbents.
The thermodynamic parameters for Pb2+ ion adsorption onto bentonite, zeolite and perlite.
The graph of ln(Kd) as a function 1/T for the adsorption of Pb2+ ions using bentonite, zeolite and perlite. Adsorption conditions: shaking rate = 75 rpm; pH = 7; contact time = 120 min; adsorbent dosage = 5 g L–1; initial concentration of Pb2+ = 400 ppm.
Effect of shaking rate on Pb2+ ion adsorption
The effect of shaking rate on Pb2+ ion adsorption was studied by varying the shaking rate between 0 and 150 rpm at pH 7.0, temperature 25°C, a contact time of 120 min, an adsorbent dosage of 5 g L–1 and a Pb2+ ion concentration of 400 ppm. As can be observed, the removal percentages increased from 67%, 39% and 8% (0 rpm) to 95%, 42% and 27% (75 rpm) for bentonite, zeolite and perlite, respectively (Fig. 12). In addition, increasing the shaking rate to 150 rpm did not affect the removal percentages for all adsorbents. Increasing the shaking rate also had a positive impact on Pb2+ ion adsorption, as has been reported previously in the literature (Murithi et al., Reference Murithi, Onindo and Muthakia2012; Shaheen et al., Reference Shaheen, Akram, Karim, Mehmood, Farooq and Iqbal2016).
Effect of shaking rate on the adsorption of Pb2+ ions using bentonite, zeolite and perlite. Adsorption conditions: temperature = 25°C; pH = 7; contact time = 120 min; adsorbent dosage = 5 g L–1; initial concentration of Pb2+ = 400 ppm.
Characterization of the adsorbents after Pb2+ ion adsorption
The adsorbents containing Pb2+ ions after the batch adsorption experiment at pH 7, a contact time of 120 min, an adsorbent dosage of 5 g L–1, a shaking rate of 75 rpm and a temperature of 25°C using an initial Pb2+ ion concentration of 400 ppm were examined with XRF (Table 1) and FTIR (Fig. 5) analyses. The XRF analysis showed that Pb2+ was adsorbed onto the surfaces of bentonite (5.4%), zeolite (2.3%) and perlite (0.5%) successfully either by electrostatic interaction or by ion exchange. The decrease in the elemental percentages of Na, Mg, K and Ca indicated that these elements were exchanged with Pb2+ ions. The FTIR spectra of bentonite, zeolite and perlite also showed the exchange process between Pb2+ and the exchangeable cations through the changes in the positions and shapes of the fundamental vibrations of the OH and Si–O groups. For instance, the stretching OH band at 3630–3560 cm–1 shifted to 3500 cm–1 for Pb2+-saturated samples, showing a broad band of water due to the overlapping of (H–O–H) stretching vibrations, and the absorption near 1636 cm–1 (H–O–H) bending vibrations confirmed the presence of the Pb2+ ions in the previously vacant sites. The band near 2360 cm–1 also shifted to 2390 cm–1, giving a sharp peak for Pb2+-saturated samples. The band near 1010 cm–1 assigned to Si–O stretching vibrations moved to 1050 cm–1 after Pb2+ ion adsorption, suggesting the interaction of the minerals with Pb2+. The involvement of Si–O–Si and OH present in the clay in interaction with Pb2+ has also been reported previously (Hannachi et al., Reference Hannachi, Homri and Boubaker2013; Kushwaha et al., Reference Kushwaha, Rani and Patra2019). The distinctions in the OH vibrational peaks are due to the differences in the binding abilities of Pb2+ cations towards the interlayer water molecules, as they are preferably coordinated with the interlayer cations, and the residual water is retained by the interlayer holes. The water molecules coordinating with the cations can emigrate to the bi-trigonal cornered holes on the siloxane surface, affecting the OH groups and thus changing the intensities of the corresponding peaks (Tabak et al., Reference Tabak, Yilmaz, Eren, Caglar, Afsin and Sarihan2011).
Radioactive 210Pb adsorption and determination of 210Pb using the LSC system
The batch adsorption experiments were repeated with 210Pb-contaminated (17.86 ± 1.28 Bq L–1) Pb2+ ion solution having a concentration of 400 ppm at pH 7, a contact time of 120 min, an adsorbent dosage of 5 g L–1, a shaking rate of 75 rpm and a temperature of 25°C. 210Pb, 210Bi and 210Po isotopes were present in radiochemical equilibrium in the stock solution of 210Pb. Therefore, during the batch adsorption experiments, 210Pb, 210Bi and 210Po isotopes were present in the solution, and 210Bi and 210Po could also be adsorbed on the surface of the adsorbents. The presence of 210Pb and 210Bi (β-emitters) and 210Po (α-emitter) isotopes in the stock solution and the filtrates of the consecutive adsorption experiments using perlite can be seen in the β-spectra (Fig. 13a) and α-spectra (Fig. 13b), respectively. The activity concentrations of 210Pb and 210Po isotopes, calculated by using Equation 7, are given in Table 8. As is known, the radiochemical equilibrium was disturbed after the first adsorption. Hence, the activity concentrations of 210Pb, 210Bi and 210Po changed in the filtrate. Due to the short half-life of 210Bi (5.012 (5) days; Nucleide Lara, 2023) and the time interval between the adsorption and LSC measurements not being constant for all of the adsorbents, the activity concentration of 210Bi was not reported.
(a) Gross β and (b) gross α LSC spectra of the stock solution and the filtrates of the successive batch adsorption experiments using perlite.
The activity concentrations of 210Pb and 210Po in the stock solution and the filtrates of the successive batch adsorption experiments.
MDCα = 0.03 Bq L–1; MDCβ = 0.26 Bq L–1.
As can be seen from Table 8, bentonite removed 95% of 210Pb and 75% of 210Po in the first adsorption experiment. The removal percentages after the second adsorption experiment were found to be >99% for both of the radionuclides, as the activity concentrations were below their corresponding MDC values. Additionally, the gross β-activity concentration of bentonite was also less than the MDCβ value, indicating that all β-emitters, including 210Bi, were also adsorbed on the surface of bentonite. The removal percentages of zeolite and perlite were lower than the removal percentage of bentonite in the first adsorption experiment. Zeolite adsorbed 38% of 210Pb and 60% of 210Po, whereas perlite adsorbed 30% of 210Pb and 74% of 210Po. However, the activity concentrations of 210Pb and 210Po were less than the MDCβ and MDCα values after the third and second adsorption experiments, respectively, demonstrating that >99% of the radionuclides were removed from the solution.
In this study, the removal percentages of the stable and radioactive Pb2+ ions under the same adsorption conditions were compared for all adsorbents. Even though the stable Pb2+ ion concentration was determined using ICP-OES and the radioactive 210Pb activity concentration was determined using LSC, the removal percentages were found to be within 5% of each other, as was expected, due to the fact that both of them are isotopes of the same element and they have the same chemical behaviour.
Conclusion
In this study, the Pb2+ adsorption capacities of bentonite, zeolite and perlite obtained from various locations in Türkiye were investigated. The results illustrated that the minerals had an adsorption capacity for Pb2+ in the following order: bentonite > zeolite > perlite. It was found that all minerals fit the Langmuir isotherm, indicating chemical bond formation between the adsorbent and Pb2+ ions during the adsorption process. The maximum adsorption capacities (q m) were found to be 131.6, 36.1 and 21.5 mg g–1 for bentonite, zeolite and perlite, respectively. It should be mentioned that the adsorption of Pb2+ was a result of the ion exchange of the cations as observed from the FTIR analysis as well as the electrostatic attraction of Pb2+ ions to the adsorbent surface due to the negative surface charge of the adsorbents. It was also observed that the Pb2+ adsorption process was a spontaneous (ΔG° < 0) and endothermic (ΔH° > 0) process. Furthermore, the removal percentages of stable Pb2+ ions and radioactive 210Pb2+ isotopes by these minerals were compared using various analysis techniques. LSC (β-spectrometer) was used in an adsorption study for the first time. The removal percentages of radioactive 210Pb isotope were found to be 95%, 38% and 30% for bentonite, zeolite and perlite, respectively, which were in accordance with the stable Pb2+ ion removal percentage results of 95%, 42% and 27%. The LSC results showed that 210Po and 210Bi were also adsorbed on the surface of the minerals, with the removal percentages of 210Po being 75%, 60% and 74% for bentonite, zeolite and perlite, respectively. This study also showed the applicability of bentonite, zeolite and perlite to 210Po and 210Bi adsorption, which had not been demonstrated previously in the literature.
Acknowledgements
We thank MCL Bentonite for the bentonite samples, Prof Dr Yusuf Kağan Kadıoğlu for the zeolite samples and Eti Mine Menderes Works for the expanded perlite samples, the Earth Sciences Application and Research Center (YEBİM) at Ankara University for the XRD, XRF and ICP-OES analysis support, Prof Dr Hande Çelebi at Eskisehir Technical University for the FTIR analysis support, the Institute of Nuclear Sciences at Ankara University for the SEM-EDS analysis support, Middle East Technical University (METU) Central Laboratory for the ζ-potential and BET analysis support and the Superconductor Technologies Application and Research Center at Ankara University for the particle-size analysis support.
Financial support
This work was partially supported by Ankara University via project number BAP-21L0405003.
Conflicts of interest
The authors have no relevant financial or non-financial interests to disclose.
Availability of data and materials
Data are available upon request.
Author contributions
Conceptualization: G.Ö. Çakal; methodology: R. Güven, G.Ö. Çakal; formal analysis and investigation: O. Uygun, R. Güven, G.Ö. Çakal; supervision: G.Ö. Çakal; writing – original draft preparation: O. Uygun; writing – review and editing: R. Güven, G.Ö. Çakal.
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