Introduction
Spent nuclear fuel (SNF) reprocessing generates high-level liquid radioactive waste (HLLW), which is composed of unextracted U and Pu, long-lived fission products (129I, 99Tc, 135Cs, and 93Zr), short-lived fission products (90Sr and 137Cs), minor actinides (MAs) (Np, Am, and Cm), and stable lanthanide isotopes (Eu, Nd, La, Tb, Pr, Gd, Sm, Ce, and Pm)[1-10]. To reduce the radiotoxicity and volume of HLLW and improve resource utilization, partitioning and transmutation strategies have been explored to shorten the half-life of long-lived radioisotopes. However, the transmutation efficiency of MAs is limited by the high thermal neutron capture cross-sections of several lanthanide isotopes owing to competition for available neutrons[11, 12]. Thus, separating MAs from lanthanides (Lns) before transmutation is crucial.
During the liquid–liquid extraction process, N,N,N’,N’-tetraoctyl diglycolamide (TODGA) has proven to be efficient in extracting actinides (Ans) and lanthanides [2, 13-16]. Furthermore, TODGA is a tridentate ligand that shows high distribution ratios for Lns(III)/Ans(III) because the hydrophilic groups exhibit stable metal coordination in the aqueous phase and the hydrophobic groups ensure its solubility in the organic phase[17, 18]. It has been used in some processes, such as the innovative Selective ActiNide EXtraction (i-SANEX) process[19, 20] and the EUROpean Grouped Actinide EXtraction (EURO-GANEX) process[21, 22]. The i-SANEX process was first arranged utilizing an organic solution with TODGA (0.2 mol/L) and 1-octanol (5% v/v) to enable co-extraction of trivalent Lns and Ans from simulated HLLW. At the same time, Pd and Zr were masked by cyclohexane diamine tetraacetic acid (CDTA). Second, the co-extracted Mo and Sr were stripped using 3.0 mol/L HNO3 aqueous solution with CDTA (0.05 mol/L) and oxalic acid (0.2 mol/L) as scrubbing solvents, followed by a back-extraction step using an aqueous solution containing 2,6-bis(5,6-di(sulfophenyl)-1,2,4-triazin-3-yl)pyridine (SO3-Ph-BTP) (1.8×10-2 mol/L) in HNO3 (0.35 mol/L) for selective stripping of Ans(III). The final step was the stripping of Lns(III) using a citrate buffer solution. The experimental results obtained by Wilden et al.[19] demonstrated the effectiveness of this process. In the Ans product fraction, Cm(III) and Am(III) were efficiently stripped (more than 99.8%) and regained within six stages. The purity of the Cm(III) and Am(III) products was found to be very good, with only Ru (0.4%), Sr (0.3%), and Lns(III) (0.1%) contamination. Lns(III) stripping is efficient (more than 99.5%) within only four stages using a stripping solution containing citric acid with a pH of 3. The EURO-GANEX process consists of two cycles. In the first cycle, hydrogenated tetrapropene (TPH) containing N,N-di (2-ethylhexyl) isobutyramide (DEHiBA) (1.0 mol/L) was applied to extract U(VI) selectively. In the second cycle, the extraction of Cm(III), Am(III), Pu(IV), Np(VI), and Lns(III) from the first cycle raffinate was achieved using N,N’-dimethyl-N,N’-dioctyl-2(2-hexyloxyethyl)-malonamide (DMDOHEMA) (0.5 mol/L) and TODGA (0.2 mol/L) in a kerosene diluent, while CDTA (0.055 mol/L) was applied as a masking agent, to prevent the extraction of Zr(IV) and Pd(Ⅱ). The Sr and Fe were extracted using HNO3 (0.5 mol/L) from the loaded solvent, and trans-uranium elements (TRU) were back-extracted by applying an aqueous solution containing aceto-hydroxamic acid (AHA) and SO3-Ph-BTP, while Lns(III) was retained in the organic solution. The EURO-GANEX process was successfully demonstrated by the hot test performed by Malmbeck et al.[23]. Moreover, Pu(IV), Np(VI), Am(III), and Lns(III) were efficiently co-extracted from the raffinate of the EURO-GANEX process during the first cycle; Mo and Zr were also co-extracted, whereas the other fission products were successfully refused. Within six strip stages, 99.91% Np, 99.85% Pu, 99.90% Am, and co-extracted Mo and Zr were well back-extracted, whereas 99.9% Lns(III) was retained in the organic solution within four strip stages using an aqueous solution containing AHA and SO3-Ph-BTP.
Previous studies have shown that TODGA provides significantly higher distribution ratios in alkanes such as n-dodecane (nDD) than in other studied diluents, such as secondary ketones, primary alcohols, and secondary alcohols [24, 25]. The extraction system of TODGA/nDD can be applied to separate MAs and Lns from other fission products. Once separated, the extraction of individual elements can be simplified with additional processing, culminating in the separation of MAs from Lns [26-28].
Because the extraction system is exposed to the radioactive environment formed by the radionuclides, its radiation stability is an important factor to be examined before its practical application [29]. In the solvent extraction process, the γ-radiolysis of TODGA is problematic because of the highly radioactive HLLW. Because the loss of TODGA and the radiolytic products of TODGA formed during γ-radiation can adversely affect the extraction performance in the liquid–liquid extraction process toward metal ions, it is essential to measure the γ-radiolysis yield and radiolytic products of TODGA and to study their effects on the performance of extracting metal ions. Radiolysis of TODGA in nDD under different conditions has been investigated in some studies [30, 31]. It was found that the magnitude of α-radiolysis of TODGA is lower than that of γ-radiolysis, and they have similar radiolytic products [32]. This is attributed to the fact that the linear energy transference of α particles is higher than that of γ particles, and the radical yield of nDD decreases by recombination in α-radiolysis. Although the γ-radiolysis and extraction of TODGA have been investigated, the effect of γ-radiolysis and radiolytic TOGDA products on extraction in the TODGA/nDD system has rarely been reported. In addition, if we could predict the extraction performance of the irradiated extractant system using equations, it would be very beneficial and important in controlling the partition process. To the best of our knowledge, the mathematical correlation between the radiolysis of the extractant and the distribution ratio has seldom been studied.
In this work, because α and γ rays result in similar radiolysis products of TODGA and γ-radiation is easier to carry out in the laboratory, the radiolytic behavior and γ-radiation stability of TODGA in the 0.2 mol/L TODGA/nDD system (TODGA/nDD) and the 0.2 mol/L TODGA/nDD that was pre-equilibrated with 3.0 mol/L HNO3 system (HNO3-TODGA/nDD) were studied qualitatively and quantitatively. They were also compared with radiolysis of neat TODGA. The content and radiolysis products of TODGA were determined using HPLC and UPLC-QTOF-MS, respectively. Considering the chemical similarity between trivalent lanthanides and minor actinides, and to avoid the dangers of handling radioactive isotopes in standard laboratories, Eu(III) was selected as a model metal ion in our extraction experiment to assess the extraction performance of TODGA/nDD after γ-radiation. The density functional theory (DFT) calculation, which can estimate the coordination abilities of TODGA and its radiolytic products, was applied to explain the effect of the radiolytic products on our extraction of Eu(III). For the first time, a combination of theoretical calculations and extraction experiments was used to demonstrate that the radiolytic products maintain partial complexation, which capably explains the extraction behavior of irradiated samples. For the TODGA/nDD system, an in-depth understanding of the effects of γ-irradiation on the extraction behavior was obtained from this study.
Experimental
Materials
Sichuan University synthesized TODGA (≥98%); its purity was confirmed by FT-MS (ESI+) and 1H NMR (Fig.S1–S2). Moreover, Eu(NO3)3·6H2O (99.99%) was obtained from MREDA Technology Co. Ltd. Formic acid, liquid chromatography-mass spectrometry (LC-MS) grade, was purchased from Thermo Fisher Scientific. Methanol (LC-MS grade) was purchased from Honeywell Trading (Shanghai) Co., Ltd. The aqueous dilution was performed using ultrapure water (18.2 MΩ·cm). All other chemicals were of analytical grade, and the chemicals were not further purified.
Gamma irradiation
TODGA and TODGA/nDD solutions equilibrated with and without HNO3 (3.0 mol/L) before γ-radiation were irradiated in the air at room temperature (25 ± 5 °C) using a 60Co source (Department of Applied Chemistry in the College of Chemistry, Peking University, China) with an absorbed dose rate of 6.6 kGy/h, as determined by a Fricke dosimeter.
Quantitative analysis of TODGA after irradiation
An HPLC method with UV detection (SPD-16, Shimadzu, Japan) was used to quantitatively analyze the TODGA concentration in the irradiated samples. Additionally, HPLC was carried out at 25 ± 5 °C using an Agilent HC-C18 liquid chromatography column (5 μm, 4.6 mm × 150 mm) to achieve chromatographic separation with a UV wavelength fixed at 210 nm. The aqueous component was ultrapure water with formic acid (1‰ v/v) (A1); the organic component was methanol (B1). The elution program in our liquid chromatography was listed hereafter: 0–10 min, 30–100% B1; 10–20 min, 100% B1; 20–22 min, 100–30% B1. The error values in the quantitative analysis experiments were within 5%. The flow rate was 1.0 mL/min, and the injection volume was 20 µL.
Identification and semi-quantification of radiolytic products
Ultra-high pressure liquid chromatography (UPLC) (ACQUITY I-Class, Waters, USA) was carried out using an Agilent HC-C18 liquid chromatography column (5 μm, 4.6 mm × 150 mm) at 40 °C to achieve chromatographic separation. The aqueous component was ultrapure water with formic acid (1‰ v/v) (A2), and the organic component was methanol with formic acid (1‰ v/v) (B2). The liquid chromatography elution program was listed hereafter: 0–4 min: 30–100% B2; 4–13 min: 100% B2; 13–13.1 min: 100–30% B2; 13.1–15 min: 30% B. The flow rate was 0.8 mL/min with a 1 µL injection volume. The mass-spectrometer conditions of the quadrupole time-of-flight mass spectrometry (QTOF-MS) (Vion IMS QToF, Waters, USA) are listed here: desolvation temperature: 300 °C; source temperature: 120 °C; desolvation gas flow: 800 L/h; capillary voltage: 2.8 kV; cone gas flow: 50 L/h; positive mode. The data were acquired and processed using a Waters UNIFI Scientific Information System with a mass target match tolerance of less than 5 ppm.
Extraction experiment
The TODGA was dissolved with nDD to obtain a 0.7 ml organic phase with a concentration of 0.2 mol/L. The Eu(NO3)3·6H2O was dissolved in 3.0 mol/L HNO3 to obtain a 0.7 ml aqueous phase with a concentration of 1000 mg/L. Pre-equilibration of the organic extraction phase with 3.0 mol/L HNO3 was performed before extraction. A vortex mixer at a speed of 2500 rpm (LPD2500, Leopard Scientific Instrument Co., Ltd, Beijing) was used to perform the extraction experiments at 298 ± 1 K. To achieve complete separation between the two phases, the mixtures were centrifuged for 1 min at 5000 rpm in a centrifuge (TGL-16M, Cence, Hunan). After dilution with ultrapure water, the aqueous phase was detected using an ICP-MS (ELEMENT XR, Thermo Scientific, USA) to estimate the concentration of Eu(III).
The distribution ratio of Eu(III) (DEu) was calculated using Eq. (1). The phase ratio equals 1:1 in the extraction experiment.
Fluorescence spectra titration
The fluorescence emission spectra of the titration experiments were investigated at 298 ± 1 K in a cuvette cell with a 1 cm path length using a fluorescence spectrophotometer (F7000, Hitachi, Japan). The concentration of TODGA was 0.1 mol/L in acetonitrile and the initial concentration of Eu(III) was 0.001 mol/L in 2.0 mL acetonitrile. Next, 4 µL of TODGA solution was added at a time. The solution was mixed using a vortexer (VORTEX 3, IKA, Germany) for 5 min after the addition of each ligand. The titration experiments used an excitation wavelength of 395 nm; the bandwidth of the excitation and emission was 2.5 nm. The interval was 1 nm and the spectra were recorded between 550 and 700 nm. Single-component spectra of the metal–ligand complexes and metal solvent species were obtained using the HyperSpec program.
Theoretical calculations
DFT calculations incorporating electron correlation effects were performed at the level of B3LYP using the Gaussian 09 package [33-35]. The relativistic effects of Eu atoms were investigated using the quasi-relativistic effective core potentials (RECPs) and associated valence basis sets, which were improved by the Stuttgart and Dresden groups [36-40]. The large-core RECPs used in the structural optimization of Eu(III) contained 52 electrons [39, 40]. All other C, N, O, and H atoms utilized the 6-31G (d) basis set. Geometrical optimization and the electronic calculations of all structures were first performed at the level of B3LYP/6-31G(d)/RECP under the gas phase conditions. The Gibbs free energy (Gg), entropy (Sg), and enthalpy (Hg) were obtained under the gas phase conditions at 298.15 K using the same theory level. To obtain the Gibbs free energy (Gaq), entropy (Saq), and enthalpy (Haq) of the species in the nDD phase at 298.15 K, all species were optimized at the B3LYP/6-31 G (d)/RECP level in nDD to better predict their solvation energy[41]. This theory is based on the SMD universal continuum solvation model[42].
Results and discussion
Quantitative analysis of TODGA under different conditions after γ-ray irradiation
TODGA/nDD, HNO3-TODGA/nDD, and neat TODGA were subjected to γ-irradiation with absorbed doses ranging from 20 to 500 kGy. The irradiated samples were measured quantitatively using HPLC-UV and their radiolytic stability was analyzed. Figure 1 shows that the TODGA concentration decreased exponentially with increasing absorbed doses, suggesting pseudo-first-order degradation kinetics for TODGA/nDD, HNO3-TODGA/nDD, and neat TODGA. By comparing TODGA/nDD and HNO3-TODGA/nDD, it was found that HNO3 had little influence on the radiolysis of TODGA. Moreover, in the nDD solution, the radiolysis rate of TODGA was higher than that of the neat TODGA. A dodecane-induced "sensitization effect" is responsible for the sensitization of TODGA to radiolysis [43] due to the fact that the radiolysis of TODGA is accelerated by nDD solvents because of the efficiency of nDD in transferring positive charges [44-46].
-202304/1001-8042-34-04-001/alternativeImage/1001-8042-34-04-001-F001.jpg)
Because the radiolysis behavior of TODGA depends on its concentration in pseudo-first-order kinetics, the rate of radiolysis causes an exponential drop in the TODGA concentration. The radiolysis rate equation is defined by Eq. (2):
The solution to the rate equation is presented as Eq. (3):
The dose constant
If the dose constants k of different systems can be obtained, Equation (4) can be used to calculate the
Table 1 shows the dose constants
Samples | R0.5 (kGy) | |||
---|---|---|---|---|
TODGA/nDD | 0.20 | (2.08±0.05)×10-3 | 0.54±0.013 | 330 |
HNO3-TODGA/nDD | 0.20 | (2.20±0.03)×10-3 | 0.57±0.008 | 315 |
Neat TODGA | 1.57 | (6.54±0.31)×10-4 | 1.13±0.053 | 1060 |
Identification and semi-quantitative analysis of radiolytic products
Ultra-high-performance liquid chromatography with quadrupole time-of-flight mass spectrometry (UPLC-QTOF-MS) can be used to identify and quantify complex mixtures of unknown compounds owing to its high resolution and mass accuracy.
The major radiolytic products of TODGA were identified using QTOF-MS; these are presented in Table 2, and their UPLC-QTOF-MS spectra are shown in Figures S3–9. Seven mass signals were identified and attributed to the possible radiolytic products of TODGA (P1 – P7, Table 2). These radiolytic products were formed by the rupture of the C – N, C – O, and C – C bonds of TODGA. Four radiolysis routes after irradiation are shown in Scheme 1.
Radiolytic products | Chemical formula | Theoretical neutral mass | Observed neutral mass | Structure |
---|---|---|---|---|
P1 | C28H56N2O3 | 468.4291 | 468.4274 | ![]() |
P2 | C20H39NO4 | 357.2879 | 357.2892 | ![]() |
P3 | C18H37NO2 | 299.2824 | 299.2825 | ![]() |
P4 | C18H37NO | 283.2875 | 283.2867 | ![]() |
P5 | C17H35NO | 269.2719 | 269.2719 | ![]() |
P6 | C16H35N | 241.2770 | 241.2772 | ![]() |
P7 | C19H39NO2 | 313.2981 | 313.2994 | ![]() |
-202304/1001-8042-34-04-001/alternativeImage/1001-8042-34-04-001-F009.jpg)
Figure 2 shows the semi-quantitative analysis of the radiolytic products P1 – P7 in the irradiated HNO3-TODGA/nDD and neat TODGA. The absorbed doses ranged from 20 to 500 kGy. Seven radiolytic products were found to exist in the two systems. The detector counts of the radiolytic products P1 – P7 roughly increased with increasing absorbed dose. However, some radiolytic products, such as P1 in irradiated neat TODGA, showed a decrease in detector counts with absorbed doses from 400 kGy to 500 kGy. This is probably because the contents of the radiolytic products during irradiation increased from the radiolysis of the TODGA and decreased by self-radiolysis. The concentration's rate of increase was less than the rate of decrease with absorbed doses from 400 to 500 kGy for P1 in irradiated neat TODGA. The detector counts of all radiolytic products in irradiated TODGA/nDD were higher than those in neat TODGA (Figure S10), indicating the “sensitization effect” of nDD. This agreed well with the above result of the radiolysis kinetics of the TODGA with or without nDD. However, the relative detector counts of some radiolytic products differed between the two irradiation systems. For example, the detector count of P6 was less than that of P4 in irradiated neat TODGA; however, the converse was true for irradiated HNO3-TODGA/nDD. This can be attributed to the different reaction mechanisms, wherein irradiated neat TODGA produces radical cations by direct ionization reaction. Conversely, in irradiated TODGA/nDD, nDD radical cations may transfer their charge to TODGA molecules, leading to radiolysis of TODGA[43, 49].
-202304/1001-8042-34-04-001/alternativeImage/1001-8042-34-04-001-F002.jpg)
Influence of γ-ray irradiation on the extraction of TODGA system toward Eu(III)
HNO3-TODGA/nDD and neat TODGA were subjected to γ-ray irradiation at absorbed doses ranging from 50 to 500 kGy. The irradiated neat TODGA was diluted with nDD to 0.2 mol/L. These organic phases were used to extract Eu(III) from the 3.0 mol/L HNO3 aqueous phase to evaluate the extraction performance.
As shown in Fig. 3,
-202304/1001-8042-34-04-001/alternativeImage/1001-8042-34-04-001-F003.jpg)
The loss of extractants was the main cause of the decline in extractability after irradiation. Owing to the presence of TODGA and its liquid radiolysis products in the irradiated organic extraction phase, the complexation of radiolytic products on Eu(III) was studied using DFT calculations. This determined the effect if any of the radiolytic products of TODGA on the extraction behavior of the irradiated extraction system.
Slope analysis and fluorescence titration
Before DFT calculations were conducted to investigate the complexation of TODGA and its radiolytic products with Eu(III), we assessed the stoichiometry of Eu ions and TODGA ligands in the extraction reaction, which could be obtained by the slope analysis in the curve of logDM-log[L](org).
The extraction reaction of Eu(III) by TODGA is expressed by Eq. (5):
The extraction equilibrium concentration constant,
The distribution ratio,
Equation (7) was substituted into Eq. (6), and Eq. (6) was then transformed into a logarithmic form to obtain Eq. (8).
The n value can be calculated from Eq. (8), which represents the average number of TODGA coordinated to one metal ion. The plot in Fig. 4 of
-202304/1001-8042-34-04-001/alternativeImage/1001-8042-34-04-001-F004.jpg)
Complexation studies were also performed with TODGA and Eu(III) using fluorescence titration. Figure 5 displays the normalized fluorescence emission spectra with different ratios of Eu(III) and TODGA resulting from the transitions of 5D0→7F1 and 5D0→7F2. The transition of 5D0→7F1 at 593 nm, owing to the magnetic-dipole transition, was considered independent of the ligand field. The transition of 5D0→7F2 at 617 nm owing to the electric–dipole transition is considered to be hypersensitive to the ligand field, and its intensity depends on the coordination symmetry around the metal ions [50]. With the addition of the TODGA ligand, the change in the ligand field led to a gradual transformation of the single peak at 617 nm into a double peak, which was finally formed at M: L = 1:3. This indicated that the inner coordination sphere of Eu(III) was gradually occupied by TODGA with the addition of the ligand, which is similar to some results from the literature [51, 52].
-202304/1001-8042-34-04-001/alternativeImage/1001-8042-34-04-001-F005.jpg)
The spectra of each component were obtained from the fluorescence emission spectra (Fig. 6). The [Eu(TODGA)n]3+ (n = 1 – 3) complexes and Eu(III) solvent species were also discovered. No complexes with TODGA values greater than or equal to 4 were found in the fluorescence emission spectra, proving that the ratio of Eu(III) to TODGA equals 1:3.
-202304/1001-8042-34-04-001/alternativeImage/1001-8042-34-04-001-F006.jpg)
The slope value was disputable, although many studies showed that the Ln(III): DGA structures are 1:3 complexes. Antonio et al. elucidated the inner coordination sphere of Eu(III) and TODGA using X-ray absorption spectroscopy (XAS)[53]. One ether O atom and two carbonyl O atoms of a TODGA molecule make up each ligand's tridentate to Eu(III). The coordination number is nine, with twelve distant carbon neighbors, six closest ones from carbonyl carbon atoms, and six slightly farther ones from the ether carbon atoms. Turanov et al.[54] found that the calculated slope value of Eu(III) extracted by TODGA in n-decane containing 0.002 mol/L dinonylnaphtalene sulfonic acid (HDNNS) was 3.28 ± 0.04. This was estimated by the plot of logDEu – log[TODGA] and the existence of EuLn(NO3)3 species by the slope of logDEu – log[HNO3], which was equal to 2.86 ± 0.08. Pathak et al.[55] investigated the influence of solvent type, acidity of extraction, and concentration of TODGA on luminescence lifetime and found that various ratios of TODGA to Eu ions resulted in the formation of Eu(TODGA)33+ species when Eu(III) was complexed with TODGA. According to the findings of Sasaki et al.[56], extracted Eu(III) complexes require three or four TODGA molecules and three nitrate ions to maintain stability in non-polar diluents by slope analysis. Zhu et al.[57] performed a slope analysis of TODGA to extract some Lns(III) and found that the slope was 3.9 for Eu(III), suggesting that the M(TODGA)4(NO3)3 species finally formed. However, in this work, a 1:3 complexation ratio for TODGA with Eu(III) was determined.
The theoretical
Equation (10) can be obtained from Fig. 1 for irradiated HNO3-TODGA/nDD. It is an exponential radiolysis equation for the concentration of TODGA and the absorbed dose.
We can obtain Equation (11) for
The theoretical
-202304/1001-8042-34-04-001/alternativeImage/1001-8042-34-04-001-F007.jpg)
Because some radiolytic products remained in coordination structures similar to those of TODGA, such as P1 and P2, which were identified by UPLC-QTOF, the complexation of radiolytic products on Eu(III) was investigated further using DFT calculations.
Theoretical calculations of complexation of TODGA and radiolytic products with Eu(III)
According to the slope and fluorescence titration analyses, the Eu(III): TODGA stoichiometry was 1:3. In addition, Kimberlin et al.[58] reported that several radiolytic products with the TODGA skeleton are involved in heteroleptic complexes with TODGA with a stoichiometry of 1:3 from the ESI-MS spectra. The time-resolved laser fluorescence results showed no change in the peak shape of the fluorescence spectra before and after irradiation (Fig. S11). However, the fluorescence lifetime gradually decreased with increasing absorbed dose (Fig. S12), indicating that γ radiation did not change the M: L ratio of 1:3 but caused a slight partial change in the original fluorescent species.
DFT calculations were employed to investigate the coordination abilities of TODGA and its radiolytic products with TODGA skeletons (P1 and P2). Figure 8 shows the optimized structures of the complexes formed by Eu(III) and the ligands. Theoretical calculations were performed for the [Eu(TODGA)2(Pn)]3+ (n = 1 – 2) species and [Eu(TODGA)3]3+ complexes. It is realistic that one TODGA molecule in the initial complex is replaced by one radiolytic product to form mixed Ln-radiolytic product-TODGA complexes during γ irradiation, which was already found in the ESI-MS spectra by Kimberlin et al. [58]. In addition, we investigated the optimized structures and coordination abilities of [Eu(Pn)3]3+ (n = 1 – 2), which were formed using three radiolytic products to represent a more extreme coordination environment of Eu(III) after γ irradiation.
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The changes in the Gibbs free energy, entropy, and enthalpy for the complexes formed by the ligands (TODGA, P1 and P2) and Eu(III) are shown in Table 3. It can be seen that the formation of [Eu(TODGA)3]3+ complex has more negative ΔG in the gas phase (–2527.3 kJ/mol) and in the nDD phase (–1115.0 kJ/mol) than that of the [Eu(TODGA)2(Pn)]3+ and [Eu(Pn)3]3+ (n = 1– 2) complexes in the two phases. Moreover, the coordination abilities of the radiolytic products of TODGA decreased, as reflected by the changes in the Eu–O bond length (Table 4). The average Eu – O bond length of the complexes changed from 2.4911 Å ([Eu(TODGA)3]3+) to 2.5000 Å ([Eu(P2)3]3+), indicating a decline in the coordination ability of the complex. These results indicate that TODGA shows better coordination ability than the radiolytic products of TODGA; the complexation order is TODGA > P1 > P2. However, the formation of the [Eu(TODGA)2(Pn)]3+ and [Eu(Pn)3]3+ complexes (n = 1 – 2) had a high negative ΔG in the two phases. Theoretical calculations also indicated that the radiolytic products of TODGA, such as P1 and P2, still maintain a good coordination ability with Eu atoms, proving that the radiolytic products retain partial complexation for Eu(III). Consequently, the experimental
(a) Complexation in the gas phase | ΔHg | ΔGg | TΔSg |
---|---|---|---|
Eu3+ + 3TODGA → [Eu(TODGA)3]3+ | –2693.7 | –2527.3 | –166.4 |
Eu3+ + 2TODGA+ P1 → [Eu(TODGA)2(P1)]3+ | –2681.7 | –2506.1 | –175.6 |
Eu3+ + 2TODGA+ P2 → [Eu(TODGA)2(P2)]3+ | –2657.8 | –2487.8 | –170.0 |
Eu3+ + 3P1 → [Eu(P1)3]3+ | –2674.4 | –2462.8 | –211.6 |
Eu3+ + 3P2 → [Eu(P2)3]3+ | –2568.0 | –2380.8 | –187.2 |
Structure | Eu-O | Eu-O | Eu-O | Eu-O | Eu-O | Eu-O | Eu-O | Eu-O | Eu-O | Average |
---|---|---|---|---|---|---|---|---|---|---|
[Eu(TODGA)3]3+ | 2.4284 | 2.4293 | 2.4306 | 2.4325 | 2.436 | 2.439 | 2.6022 | 2.6088 | 2.6131 | 2.4911 |
[Eu(TODGA)2(P1)]3+ | 2.4219 | 2.4222 | 2.4266 | 2.4306 | 2.4363 | 2.4532 | 2.6024 | 2.6111 | 2.6270 | 2.4924 |
[Eu(TODGA)2(P2)]3+ | 2.3868 | 2.4142 | 2.4147 | 2.4215 | 2.4237 | 2.5415 | 2.5813 | 2.5957 | 2.6879 | 2.4964 |
[Eu(P1)3]3+ | 2.4187 | 2.4217 | 2.4270 | 2.4371 | 2.4381 | 2.4408 | 2.6138 | 2.6146 | 2.6213 | 2.4926 |
[Eu(P2)3]3+ | 2.3628 | 2.3821 | 2.3931 | 2.4798 | 2.4799 | 2.5147 | 2.6043 | 2.6271 | 2.6559 | 2.5000 |
In conclusion, by combining the exponential equation for the radiolysis kinetics of TODGA in nDD and the equation for slope analysis of the concentration of TODGA and DEu, we can derive a mathematical equation that includes the absorbed dose and DEu, which could be used to predict the extraction performance at low absorbed doses. This method can be used to study other extractant systems. This work provides in-depth insights into the effect of γ irradiation on the extraction behavior of the TODGA/nDD system and provides useful information on the use of nuclear fuel reprocessing.
Conclusion
In summary, γ-radiolysis of TODGA/nDD and HNO3-TODGA/nDD was investigated and compared with γ-radiolysis of neat TODGA by analyzing the loss of TODGA and liquid radiolytic products. When the absorbed dose was increased, the TODGA concentration decreased exponentially, and the dose constant of TODGA in nDD was higher than that of neat TODGA because of the “sensitization effect” of nDD. However, the radiolysis of TODGA in nDD was only slightly affected by the pre-equilibration with HNO3. Seven radiolytic products of TODGA were identified and semi-quantified using UPLC-QTOF-MS, and four radiolysis routes for TODGA were proposed. The
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