Abstract
Pertechnetate anion sorption was investigated on modified bentonites. Mn-, Cr-, Sn-bentonites were prepared by ion exchange process to sorb radioactive pertechnetate ions. In the case of Mn-, Cr-bentonite the sorb amount of metal ion was 70–90% of the cation exchange capacity of the bentonite which is expected. Interestingly in the case of Sn-bentonite this amount was 1.42 times higher than the cation exchange capacity. On Mn-bentonite the sorption was 35% at pH 5. The removal of pertechnetate ions was 100% on Cr-, Sn-bentonites and the significant sorption was achieved below 650 mV/SHE.
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Introduction
Long-lived low- and medium-level radioactive waste and spent fuel assemblies are difficult to store because fissile products can get into the environment. Natural geological barriers do not bind anions from the fission products of 235U [1]. Among the fission products 99Tc is a β-emitter, has no stable isotope, has a half-life of 2.13 × 105 years. 99Tc forms by spontaneous fission of 238U in the earth’s crust. It is also produced in medical diagnostic uses by the decay of 99mTc [2]. It is hard to bind, very little is known about its chemistry, but we can assume that it is similar to elements in a column VII B. (e.g., Mn, Re).
In the literature, several methods can be found for the removal of 99Tc in most cases as pertechnetate ions such as ion exchange [3], reductive immobilization [4], adsorption [5], liquid–liquid extractions [6].
Several organic and inorganic, natural and artificial adsorbents was found to remove 99Tc from the environment for example chitosan [7], resins and sponges [3, 8], polymers [9], metal–organic frameworks (MOFs) [10].
In this study we are looking for adsorbents which can be suitable for the construction of waste containers as pertechnetate sorbents. They should be used as an engineering barrier and should be resintance to radioactive radiation.
There are also other adsorbents in the literature such as activated carbon [11, 12], layered double hydroxide (LDHs) [13], alumina and goethite [14], and there are the clay minerals which play an important role in the environment because by removing cations and anions either through ion exchange, adsorption and precipitation, or all these combined, they can act as natural decontaminating agents of numerous pollutants. Bentonite as geological and engineering barrier is present to isolate the radioactive waste deposited in underground disposal and the environment. The main clay mineral of bentonite is montmorillonite, which is a good sorbent because it has a large specific surface area and high cation exchange capacity. Shakira et al. [15], Vinsova, [16] Jedináková-Křížová [17]; Jaisi [18]; Milutinović-Nikolić [19], Hamárová [20] dealt with modified clays, for example Vinsova et al. [16] used mixtures of bentonite, bentonite activated carbon, iron powder, FeSO4 and graphite to bind pertechnetate ions.
The main purpose of our work was to prepare Mn-, Cr-, Sn modified bentonites to sorb pertechnetate ions in a high degree. Our work dealt with 99Tc, labeled with 99mTc.
Pertechnetate anion sorption was investigated with Mn(II), Sn(II), Cr(III)-TcO4− redox reaction. It is assumed that a metal ion with a reducing effect is capable to sorb 99mTc(VII) ions in the form of TcO2. In this form it can be sorbed.
For example Tc behaves similarly to its manganese chemistry in different reactions. Mn(II) is capable of redox reaction with Mn(VII) ions to form Mn(IV). During the permanganometric titration of Mn(II), a precipitate of MnO2 is formed according to the following equations: (1), (2), (3)
If it is assumed that 99mTcO4− ions react similarly to Mn(II) ions as MnO4− ions, then the radionuclide can theoretically be precipitated in 99mTcO2 form, thereby it can be sorbed. Our experiences would be interpreted focusing on the pH and redox potential values that determine the chemistry forms, and on thermodynamic data.
Experimental
The modification of the cation exchanged bentonites
Modified bentonites were prepared by cation exchange procedure using Ca-bentonite (Istenmezeje, Hungary) and Mn(ClO4)2; Cr(ClO4)3; SnCl2 solutions.
The cation exchange capacity (CEC) of Ca-bentonite determined by ammonium acetate method [21] is 4.1 × 10−4 mol g−1 for divalent ions and 2.7 × 10−4 mol g−1 for trivalent ions [22]. Chemical composition of the original Ca-bentonite were measured with EDAX. It has the following composition: 73.29% SiO2, 18.71% Al2O3, 1.48% FeO, 2.29% CaO and 4.23% MgO. The X-ray diffraction and thermoanalytical results are: 71 m/m % montmorillonite, 12 m/m% cristobalite/opal CT, 8 m/m% illite, 4 m/m% quartz, 3 m/m% kaolinite, and 2 m/m% calcite.
Mn(ClO4)2 solution was prepared from analytically pure MnCO3 (Reanal). 2.87536 g MnCO3 was dissolved in ~ 167 cm3 of 0.3 mol dm−3 perchloric acid solution. Cr(ClO4)3 solution was prepared by the dissolution of Cr-powder (Alfa Aesar, pur. 99%) in 2 mol dm−3 perchloric acid solution. For SnCl2 solution 7 g of Sn chips (Reanal, puris.) was dissolved in 10 cm3 cc. 37% HCl solution during heating to 60 °C. The dissolution took 3 days. The concentration of Mn(ClO4)2 determined by complexometric titration; and Cr(ClO4)3; SnCl2 solutions determined by MP-AES (Agilent Technologies 4200) were 0.09442; 6.95 × 10−2;1.1 × 10−1 mol dm−3 respectively.
After preparing the modifying solutions the cation exchange procedure was carried out by suspending equivalent amount of metal-solutions and Ca-bentonite. In the case of Mn-bentonite the mixture was shaken for 5 h, and in the case of Cr- and Sn-bentonites, due to the low pH and to avoid the significant destruction of bentonite, the mixture was shaken 3 × 5 min.
After shaking, the modified bentonites were filtered through a Labex Ltd. 0.45 µm pore size nylon bio-filter. The bentonite on the filter was returned to the beaker and the same amount and concentration of solution was added. This operation was repeated two more times. After the third change, the modified bentonites were dried in room temperature and powdered into agate mortar.
The Mn, Cr, Sn concentration of bentonite was determined by X-ray fluorescence analysis (XRF) using tungsten X-ray tube and 241Am isotope source. The parts of XRF were Si(Li) detector with 20 mm2 surface and 3.5 mm evaporated layer (Atomki, Debrecen, Hungary), Canberra DSA 1000 digital spectrum analyzer (Canberra Industries, Meriden, CT 06450, USA) and Canberra Genie 2000 3.0 spectroscopy software.
The d(001) basal spacing of the initial Ca-montmorillonite and the Mn-, Cr-, Sn-montmorillonites were determined with X-ray diffraction (XRD). The parts and settings of XRD are the following: a Philips PW1710 powder diffractometer equipped with a CuKα source and a graphite monochromator (operating at 30 mA, 40 kV). The scan rate was 2°2Θ/min.
Pertechnetate ion sorption kinetic on modified bentonites
The sorption kinetic of 99mTcO4− (Drytec 2.5–100 GBq radioactive isotope generator) was studied in batch experiments. 25 cm3 physiological NaCl solution was used to eluate the isotope from the generator (Drytec 2.5–100 GBq). 100 mg modified-bentonite was added to 19 cm3 distilled water. All samples were placed in a Bühler KS15A shaking bath at 25 °C for 30 min to reach the equilibrium between the liquid and the solid phase. After this time, 1 cm399mTcO4− solution was added to the samples. All samples were shaken for 5–120 min then filtered through a Labex Ltd. 0.45 µm pore size nylon bio-filter and the radioactive intensity of the solution (ce) and the solid phase was measured with a multi-channel gamma spectrometer equipped with (NaI)Tl scintillation detector, it had to be calibrated due to the different geometry of the solid and solution samples. pH of the solution was measured with a Clean pH200 pH meter and a Clean Cs1030 combined glass electrode.
The redox potential was measured using a platinum electrode and a calomel reference electrode containing 1 mol dm−3 KCl solution. The measured redox potentials were converted to potentials measured against a standard hydrogen electrode (SHE). The measurement was needed to determine the oxidation state of the 99mTc ion in the solution based on the potential-pH diagram.
The pertechnetate ion sorption was investigated on Mn-bentonite at different pH values (3.5; 4.5; 5) on Cr-, Sn-bentonites without adjusting the pH. The pH values were 4.5 for Cr-bentonite and 3.1 for Sn-bentonite. The sorption was determined at room temperature.
Results and discussion
Characterization of modified bentonites
The Mn, Cr, Sn concentrations in modified bentonites were 7 × 10−4; 1.86 × 10−4 5.8 × 10−4 mol g−1, so 0.86 0.69 and 1.42 times of the cation exchange capacity was sorbed in bentonite, respectively.
X-ray diffractograms of the modified bentonites as well as the initial Ca-bentonite are shown in Fig. 1. The structure of the bentonites were not damaged, just the same peaks are shown. Table 1 shows that after modification with Cr and Sn the d(001) basal spacing of montmorillonites decreased, because the ionic radii of the metal ions (Table 1) are less than that of Ca-ion. In the case of Mn-bentonite, the d(001) basal spacing of montmorillonite is the same as Ca-bentonite, because there is no big difference in ionic radii and Ca and Mn are bivalent ions, so they coordinate the same number of water molecules.
Results of sorption experiments
Table 2 shows the average results of 5–120 min sorption of pertechnetate ion on 100 mg modified bentonites. On Mn-bentonite, the pH 5 of the three pH ranges was the most effective, approx. 35%. Kinetics was so fast that there is an equilibrium after 5 min. Based on the results it can be concluded that the relative sorbed amount of pertechnetate ions was approx. 100% after 5 min on Cr-, Sn-bentonite.
Pourbaix diagram show the electrochemical stability for different redox states of an element as a function of pH. Figure 2 shows the Pourbaix diagram of Tc on which are summarized our experimental results. The colored shapes indicate the modified bentonites and their associated pH values. The straight lines refers to equilibrium between Tc species. In the case of Mn-bentonite with increasing sorption, the potential values are approaching the TcO2 state. In the case of Cr-, Sn-bentonites the measured redox potential values do not fall into the region of Tc(IV) oxidation sate despite the 100% sorption, but in all cases the dominant chemical form is pertechnetate. Figure 2 shows information only about the chemical species typical of technetium, but not only Tc ions are present in this solution. It is possible that a part of the modifying ions (manganese, chromium, tin) desorbed from the surface, e.g., by exchange with the hydrogen ions in the solution. Since the concentration of Tc is small (cca. 10−15 mol/dm3), the concentration of manganese, chromium, tin ions can significantly exceed it. Thus the redox potential does not provide information about the oxidation state of Tc, but rather the oxidation state of the modifying metal ions and this state is taken by the Tc. So we have to consider the Pourbaix diagram of the metals in each case. Figure 3 shows that in all three cases, the dominant chemical species are dissolved species, so it can be assumed that they also effect the measured redox potential values.
On the Pourbaix diagram of Sn it can be seen that Sn is in + 4 oxidation state and preliminary Mössbauer-measurements indicate the + 4 oxidation state. The + 2 oxidation state also appears to a lesser extent. Thus, Sn ions are assumed to be present in + 2 oxidation state in the interlayer space of the bentonite, and on the surface Sn ions are precipitated in + 4 oxidation state, this explains the sorption over the cation exchange capacity of bentonite (1.42 times of CEC). From the pH-Eh predominance diagrams coprecipitation is assumed.
Our results correlate well with literature data (Table 3). Vinsova et al. [16] examined bentonite mixtures to remove pertechnetate ions. Bentonite-graphite and bentonite–FeSO4 mixtures showed negligible sorption capacity, while bentonite showed less than 15%. Greater sorption was achieved with iron powder and activated carbon mixed bentonites. In both cases a soprtion of 80–90% was observed. Almost 100% soprtion was achieved after 30 min on activated carbon [12]. On Sn-apatite > 92% removal of technetium was observed [20]. Hercigonja et al. [5] used several types of zeolites for technetium removal. In this study firstly Tc(VII) was reduced to Tc(IV) with SnCl2 and then adsorbed. COY (Co2+ was introduced into the zeolite) zeolite could adsorb 95% of TcO2 after 30 min and 98.8% after 1440 min. The advantage of our adsorbent compared to literature is that it can sorb technetium very fast with high efficiency without reducing.
Conclusion
Mn-, Cr-, Sn cation modified bentonite were prepared from Ca-bentonite. These modified bentonites were used for pertechnetate ion removal.
From the redox potential and relative sorption values, it can be seen that the sorption on Mn-bentonite was the most effective at pH 5, approx. 35%. On Cr-, Sn-modified bentonites the removal of Tc was 100% after 5 min. According to the results found in the literature the studied modified bentonites are suitable for faster and large-scale sorption of 99mTc ions.
Cr- and Sn-bentonites can be suitable for the construction of waste containers as pertechnetate sorbents.
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Acknowledgements
Open access funding provided by University of Debrecen (DE). The authors thank Peter Konya for the X-ray diffraction measurements, Ernő Kuzmann for Mössbauer measurements. The research was supported by the EU and co-financed by the European Regional Development Fund under the project GINOP-2.3.2-15-2016-00008. The work was supported by the Hungarian National Research, Development, and Innovation Office (NKFIH K 120265).
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Buzetzky, D., Kovács, E.M., Nagy, M.N. et al. Sorption of pertechnetate anion by cation modified bentonites. J Radioanal Nucl Chem 322, 1771–1776 (2019). https://doi.org/10.1007/s10967-019-06852-8
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DOI: https://doi.org/10.1007/s10967-019-06852-8