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Effect of radiolysis of TODGA on the extraction of TODGA/n-dodecane toward Eu(III): An experimental and DFT study

NUCLEAR CHEMISTRY, RADIOCHEMISTRY, AND NUCLEAR MEDICINE

Effect of radiolysis of TODGA on the extraction of TODGA/n-dodecane toward Eu(III): An experimental and DFT study

Hang Zhang
Yin-Yong Ao
Yue Wang
Shang-Jie Zhao
Jia-Yang Sun
Mao-Lin Zhai
Jiu-Qiang Li
Jing Peng
Hui-Bo Li
Nuclear Science and TechniquesVol.34, No.4Article number 48Published in print Apr 2023Available online 11 Apr 2023
50700

N,N,N’,N’-Tetraoctyl diglycolamide (TODGA) is one of the most promising extractants tailored for high-level liquid radioactive waste treatment during nuclear fuel reprocessing. The γ-radiolysis of TODGA (0.2 mol/L) in n-dodecane (nDD) solution with and without pre-equilibrated 3.0 mol/L HNO3 was investigated using HPLC and UPLC-QTOF-MS and compared with the γ-radiolysis of neat TODGA in this study. With increased absorbed doses, the concentration of TODGA decreased exponentially for the studied systems. Moreover, pre-equilibration with HNO3 (3.0 mol/L) slightly influenced the γ-radiolysis of TODGA in nDD. Seven radiolytic products generated from the rupture of the C – C, C – O, and C – N bonds in TODGA were identified in the studied extraction system. The influence of γ-radiation on TODGA/nDD for the extraction of Eu(III) was evaluated using the first combination of extraction experiments and density functional theory (DFT) calculations, in which the complexations of Eu(III) with TODGA and its radiolytic products were systematically compared. Based on the radiolysis kinetic model of TODGA, the slope curve of the distribution ratio of Eu(III) (DEu) and the absorbed dose, and fluorescence titration analysis, the empirical equation of the absorbed dose and DEu was obtained successfully. Below 300 kGy, the experimental DEu agreed well with the obtained empirical equation for TODGA/nDD. Conversely, at a high absorbed dose, the experimental DEu was higher than the theoretical DEu based on the empirical equation because the radiolytic products of TODGA with similar coordination structures still possessed partial complexation toward Eu(III) This was confirmed by DFT calculations. This work provides a method to predict the extraction distribution ratio of an irradiated extractant system and to understand the complex extraction process.

TODGARadiolytic productsExtractionDensity functional theoryComplexation
1

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.

2

Experimental

2.1
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.

2.2
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.

2.3
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.

2.4
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.

2.5
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)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. DEu=(CiCf)/Cf, (1) where Cf and Ci represent the final and initial Eu (III) concentrations in the diluted aqueous phase, respectively. The extraction had an error rate of less than 5%.

2.6
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.

2.7
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].

3

Results and discussion

3.1
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].

Fig. 1
(Color online) CTODGA/CTODGA0 of irradiated TODGA/nDD, HNO3-TODGA/nDD, and neat TODGA as a function of the absorbed dose (R) (y: CTODGA/CTODGA0, x: R)
pic

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): dCTODGAdR=CTODGAk. (2)

The solution to the rate equation is presented as Eq. (3): CTODGACTODGA0=ekR, (3) where CTODGA (mol/L) is the concentration of TODGA, CTODGA0 (mol/L) is the original concentration of TODGA before γ-radiation, R (kGy) is the absorbed dose, and the dose constant k (kGy-1) is the coefficient obtained by fitting the exponential curve.

The dose constant k can be used to scale the absorbed dose when exponential behavior occurs [47]. Using all the information acquired during the irradiation experiment provides more accurate results, and standard statistical methods can be used to assess the accuracy of the results. The application of k to characterize an exponential curve in terms of the absorbed dose is very similar to that of traditional time-dependent kinetics. As expressed by exponential Eq. (3), the reciprocal absorbed dose is governed by the first-order rate law instead of the reciprocal time.

If the dose constants k of different systems can be obtained, Equation (4) can be used to calculate the G value (µmol/J), which is known as the radiation chemical yield: G=103CTODGA0kρ1 (4) where ρ is the solution density (kg/L) (ρTODGA= 0.91 and ρ0.2 mol/L TODGA/nDD = 0.77 (25 °C). The measurement results are shown in Table S1.

Table 1 shows the dose constants k and radiation chemical yields G of irradiated TODGA/nDD, HNO3-TODGA/nDD, and neat TODGA. The dose constant k of TODGA in nDD is higher than that of neat TODGA because of the “sensitization effect”, while the radiation chemical yields G of TODGA/nDD and HNO3- TODGA/nDD are lower than that of neat TODGA because of the different initial concentrations of irradiated TODGA. These results agree with the literature in which Sugo et al. reported that the k value of 0.2 mol/L TODGA/nDD was 2.2×10-3 kGy-1[43, 48]. By using the k value, we can predict that the absorbed doses for the half-loss of TODGA concentration (R0.5) in irradiated TODGA/nDD, HNO3-TODGA/nDD, and neat TODGA will be approximately 330, 315, and 1060 kGy, respectively.

Table 1
Dose constants k, radiation chemical yields G, and absorbed dose for half-loss of concentration of TODGA R0.5 of irradiated TODGA/nDD, HNO3-TODGA/nDD, and neat TODGA
Samples CTODGA0(mol/L) k(kGy-1) G(µmol/J) 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
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3.2
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.

Table 2
Radiolytic products of TODGA determined by the QTOF-MS
Radiolytic products Chemical formula Theoretical neutral mass  Observed neutral mass  Structure
P1 C28H56N2O3 468.4291 468.4274 pic
P2 C20H39NO4 357.2879 357.2892 pic
P3 C18H37NO2 299.2824 299.2825 pic
P4 C18H37NO 283.2875 283.2867 pic
P5 C17H35NO 269.2719 269.2719 pic
P6 C16H35N 241.2770 241.2772 pic
P7 C19H39NO2 313.2981 313.2994 pic
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Scheme 1
Radiolysis routes of TODGA after γ-irradiation
pic

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].

Fig. 2
(Color online) Semi-quantitative analysis of radiolytic products P1 – P7 in: (a) irradiated neat TODGA, and (b) HNO3-TODGA/nDD with absorbed doses ranging from 20 to 500 kGy
pic
3.3
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, DEu decreased as the absorbed dose increased, but it was slower for irradiated TODGA than for irradiated HNO3-TODGA/nDD, indicating that γ-ray irradiation of the ligand significantly affected the extraction of Eu(III). This further proves that the presence of nDD increased the radiolysis of TODGA. However, the HNO3-TODGA/nDD system after γ-ray irradiation still possesses a high DEu (2.2×103), even at 500 kGy.

Fig. 3
(Color online) Deu of irradiated neat TODGA and HNO3-TODGA/nDD for extraction of Eu(III) versus the absorbed dose.
pic

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.

3.4
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): Eu(aq.)3++3NO3(aq.)+nTODGA(org.)Eu(NO3)3TODGAn(org.) (5)

The extraction equilibrium concentration constant, Kex, is described as Eq. (6): Kex=[Eu(NO3)3TODGAn](org.)[Eu3+](aq,)[NO3](aq.)3[TODGA](org.)n (6)

The distribution ratio, DEu, is defined as Eq. (7): DEu=[Eu(NO3)3TODGAn](org.)[Eu3+](aq.) (7)

Equation (7) was substituted into Eq. (6), and Eq. (6) was then transformed into a logarithmic form to obtain Eq. (8). logDEu=logKex+nlog[TODGA](org.)+3log[NO3](aq.) (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 logDEulog[TODGA](org.) at a constant aqueous solution of 3.0 mol/L HNO3 shows that the slope is 3.10 ± 0.11, which indicates that Eu(III) would form complexes with three TODGA molecules.

Fig. 4
(Color online) Plot of logDEu versus log[TODGA](org.) at a constant aqueous 3.0 mol/L HNO3 solution (x: log[TODGA](org.), y: logDEu)
pic

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].

Fig. 5
(Color online) Normalized Eu(III) emission spectra as a result of the transitions of 5D0→7F1 and 5D0→7F2 for the complexation of Eu(III) with increasing TODGA in acetonitrile
pic

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.

Fig. 6
(Color online) Single-component spectra of the [Eu(TODGA)n]3+ complexes (n = 1 – 3) and Eu(III) solvent species
pic

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 DEu values at different concentrations of TODGA can also be obtained using Eq. (8). Equation (9) is obtained by linear fitting, as shown in Fig. 4. logDEu=3.10 log[TODGA](org.)+6.75 (9)

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. CTODGACTODGA0=e2.20×103R (10)

We can obtain Equation (11) for DEu and the absorbed dose by substituting Eq. (10) into Eq. (9). This empirical equation enables us to construct a mathematical relationship between the DEu and absorbed dose in this system. logDEu=2.965×103R+4.583 (11)

The theoretical DEu with absorbed doses ranging from 50 to 500 kGy was obtained using Eq. (11). As shown in Fig. 7, the experimental DEu was higher than the theoretical DEu after irradiation, particularly at a high absorbed dose above 300 kGy for the HNO3-TODGA/nDD system. The experimental DEu is close to the theoretical DEu below 300 kGy, indicating that the decrease in DEu is mainly related to the loss of TODGA concentration, with a slight influence from radiolytic products.

Fig. 7
Experimental logDEu and theoretical logDEu after irradiation for HNO3-TODGA/nDD
pic

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.

3.5
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.

Fig. 8
(Color online) Optimized structures of the ligands (TODGA, P1 and P2) and complexes formed by Eu(III); the ligands (light pink, blue, green, red, and white spheres represent Eu(III), N, C, O, and H, respectively).
pic

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 DEu of TODGA was higher than the theoretical DEu from the loss of TODGA with the increase in radiolytic products at a high absorbed dose. Furthermore, if the contents of P1 and P2 are determined exactly, by combining the TODGA contents, we can predict the DEu of the irradiated TODGA/nDD system more precisely. This study will be conducted in future works. In our previous experiments, we found that the radiolytic products P1 and P2 were difficult to synthesize, and the radiolytic product P1 was not sufficiently stable. Therefore, we used DFT calculations to evaluate the coordination abilities of these radiolytic products, thereby justifying the experimental result that the experimental DEu was higher than the theoretical DEu due to the high dose TODGA losses in this study.

Table 3
Changes in Gibbs free energy, entropy, and enthalpy (298.15 K, kJ/mol) for the complexes formed by ligands (TODGA, P1 and P2) and Eu(III) were acquired separately in (a) gas phase, as well as (b) nDD at the level of B3LYP/6-31G(d)/RECP.
(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
Show more
Table 4
Changes in Eu – O bond length of complexes formed by Eu(III) and ligands (unit: Å)
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
Show more

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.

4

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 DEu of the irradiated systems decreased after irradiation, but the HNO3-TODGA/nDD system irradiated with an absorbed dose of 500 kGy maintained a high DEu of 2.2×103. For the irradiated HNO3-TODGA/nDD, we obtained an empirical equation between DEu and the absorbed dose by combining the radiolysis kinetics of TODGA and the complexation equation of TODGA with Eu(III), which fits well with the experimental results with absorbed doses below 300 kGy. DFT calculations demonstrated that the radiolytic products of TODGA with similar coordination structures possessed good coordination abilities with Eu atoms, which led to the experimental DEu being higher than the theoretical DEu based on the ligand content at high absorbed doses.

References
1. S.A. Ansari, P.K. Mohapatra,

A review on solid phase extraction of actinides and lanthanides with amide based extractants

. J. Chromatogr. A. 1499, 1-20 (2017). doi: 10.1016/j.chroma.2017.03.035
Baidu ScholarGoogle Scholar
2. S.A. Ansari, P. Pathak, P.K. Mohapatra et al.,

Chemistry of diglycolamides: Promising extractants for actinide partitioning

. Chem. Rev. 112, 1751-1772 (2012). doi: 10.1021/cr200002f
Baidu ScholarGoogle Scholar
3. M. Salvatores, G. Palmiotti,

Radioactive waste partitioning and transmutation within advanced fuel cycles: Achievements and challenges

. Prog. Part. Nucl. Phys. 66, 144-166 (2011). doi: 10.1016/j.ppnp.2010.10.001
Baidu ScholarGoogle Scholar
4. L. Rodríguez-Penalonga, B. Moratilla Soria,

A review of the nuclear fuel cycle strategies and the spent nuclear fuel management eechnologies

. Energies 10, 1235 (2017). doi: 10.3390/en10081235
Baidu ScholarGoogle Scholar
5. X.L. Liu, G. Verma, Z.S. Chen et al.,

Metal-organic framework nanocrystal-derived hollow porous materials: Synthetic strategies and emerging applications

. The Innovation 3, 100281 (2022). doi: 10.1016/j.xinn.2022.100281
Baidu ScholarGoogle Scholar
6. Y.F. Zhang, H.X. Liu, F.X. Gao et al.,

Application of MOFs and COFs for photocatalysis in CO2 reduction, H2 generation, and environmental treatment

. EnergyChem. 4, 100078 (2022). doi: 10.1016/j.enchem.2022.100078
Baidu ScholarGoogle Scholar
7. X. Wang, S.Q. Pan, Q.K. Zhao et al.,

The status of ITER radioactive waste management and enlightenment to CFETR radioactive waste management

. Nucl. Tech. 45, 090603 (2022). doi: 10.11889/j.0253-3219.2022.hjs.45.090603 (in Chinese)
Baidu ScholarGoogle Scholar
8. L.Y. Zhen, J.J. Zhang, Y.H. Lin et al.,

Analysis of the accuracy of 14C in gaseous effluent of nuclear power plant by direct measurement method

. Nucl. Tech. 45, 090301 (2022). doi: 10.11889/j.0253-3219.2022.hjs.45.090301 (in Chinese)
Baidu ScholarGoogle Scholar
9. G. Yang, J.R. Lin, X.Y. Yang et al.,

Adsorption properties of surrounding rock for 137Cs in a cavern-type low and intermediate radioactive waste repository

. Nucl. Tech. 45, 080301 (2022). doi: 10.11889/j.0253-3219.2022.hjs.45.080301 (in Chinese)
Baidu ScholarGoogle Scholar
10. S.Q. Meng, Y.S. Hu, T.M. Ruan,

Impact of nickel and iron on PWR zirconium alloy surface CRUD formation and boron precipitation

. Nucl. Tech. 45, 060602 (2022). doi: 10.11889/j.0253-3219.2022.hjs.45.060602 (in Chinese)
Baidu ScholarGoogle Scholar
11. M. Nilsson, K.L. Nash,

Review Article: A review of the development and operational characteristics of the TALSPEAK process

. Solvent Extr. Ion Exch. 25, 665-701 (2007). doi: 10.1080/07366290701634636
Baidu ScholarGoogle Scholar
12. W.H. Duan, T.X. Sun, J.C. Wang,

An industrial-scale annular centrifugal extractor for the TRPO process

. Nucl. Sci. Tech. 29, 46 (2018). doi: 10.1007/s41365-018-0395-z
Baidu ScholarGoogle Scholar
13. Y. Sugo, Y. Sasaki, S. Tachimori,

Studies on hydrolysis and radiolysis of N, N, N’, N’-tetraoctyl-3-oxapentane-1,5-diamide

. Radiochim. Acta. 90, 161-165 (2002). doi: 10.1524/ract.2002.90.3_2002.161
Baidu ScholarGoogle Scholar
14. D. Whittaker, A. Geist, G. Modolo et al.,

Applications of diglycolamide based solvent extraction processes in spent nuclear fuel reprocessing, Part 1: TODGA

. Solvent Extr. Ion Exch. 36, 223-256 (2018). doi: 10.1080/07366299.2018.1464269
Baidu ScholarGoogle Scholar
15. Z. Dong, W.J. Yuan, C. Liu et al.,

Th(IV) and U(VI) removal by TODGA in ionic liquids: extraction behavior and mechanism, and radiation effect

. Nucl. Sci. Tech. 28, 62 (2017). doi: 10.1007/s41365-017-0214-y
Baidu ScholarGoogle Scholar
16. A. Geist, U. Müllich, D. Magnusson et al.,

Actinide(III)/Lanthanide(III) separation via selective aqueous complexation of Actinides(III) using a hydrophilic 2,6-bis(1,2,4-Triazin-3-Yl)-pyridine in nitric acid

. Solvent Extr. Ion Exch. 30, 433-444 (2012). doi: 10.1080/07366299.2012.671111
Baidu ScholarGoogle Scholar
17. P.K. Nayak, R. Kumaresan, K.A. Venkatesan et al.,

Extraction behavior of Am(III) and Eu(III) from nitric acid medium in tetraoctyldiglycolamide-bis(2-ethylhexyl)phosphoric acid solution

. Sep. Sci. Technol. 49, 1186-1191 (2014). doi: 10.1080/01496395.2013.874357
Baidu ScholarGoogle Scholar
18. M.B. Singh, S.R. Patil, A.A. Lohi et al.,

Insight into nitric acid extraction and aggregation of N, N, N’, N’-Tetraoctyl diglycolamide (TODGA) in organic solutions by molecular dynamics simulation

. Sep. Sci. Technol. 53, 1361-1371 (2018). doi: 10.1080/01496395.2018.1445107
Baidu ScholarGoogle Scholar
19. A. Wilden, G. Modolo, P. Kaufholz et al.,

Laboratory-scale counter-current centrifugal contactor demonstration of an innovative-SANEX process using a water soluble BTP

. Solvent Extr. Ion Exch. 33, 91-108 (2015). doi: 10.1080/07366299.2014.952532
Baidu ScholarGoogle Scholar
20. G. Modolo, A. Wilden, P. Kaufholz et al.,

Development and demonstration of innovative partitioning processes (i-SANEX and 1-cycle SANEX) for actinide partitioning

. Prog. Nucl. Energ. 72, 107-114 (2014). doi: 10.1016/j.pnucene.2013.07.021
Baidu ScholarGoogle Scholar
21. J. Brown, F. McLachlan, M. Sarsfield et al.,

Plutonium loading of prospective grouped actinide extraction (GANEX) solvent systems based on diglycolamide extractants

. Solvent Extr. Ion Exch. 30, 127-141 (2012). doi: 10.1080/07366299.2011.609378
Baidu ScholarGoogle Scholar
22. K. Bell, C. Carpentier, M. Carrott et al.,

Progress towards the development of a new GANEX process

. Procedia Chemistry. 7, 392-397 (2012). doi: 10.1016/j.proche.2012.10.061
Baidu ScholarGoogle Scholar
23. R. Malmbeck, D. Magnusson, S. Bourg et al.,

Homogenous recycling of transuranium elements from irradiated fast reactor fuel by the EURO-GANEX solvent extraction process

. Radiochim. Acta. 107, 917-929 (2019). doi: 10.1515/ract-2018-3089
Baidu ScholarGoogle Scholar
24. I. Kajan, M. Florianová, C. Ekberg et al.,

Effect of diluent on the extraction of europium(III) and americium(III) with N, N, N’, N’-tetraoctyl diglycolamide (TODGA)

. RSC Adv. 11, 36707-36718 (2021). doi: 10.1039/D1RA07534A
Baidu ScholarGoogle Scholar
25. S. Panja, P.K. Mohapatra, S.C. Tripathi et al.,

Role of organic diluents on Am(III) extraction and transport behaviour using N, N, N’, N’-tetraoctyl-3-oxapentanediamide as the extractant

. J. Membr. Sci. 403–404, 71-77 (2012). doi: 10.1016/j.memsci.2012.02.022
Baidu ScholarGoogle Scholar
26. J. Veliscek-Carolan,

Separation of actinides from spent nuclear fuel: A review

. J. Hazard. Mater. 318, 266-281 (2016). doi: 10.1016/j.jhazmat.2016.07.027
Baidu ScholarGoogle Scholar
27. Y. Wang, Y.Y. Ao, W.J. Yuan et al.,

Extraction performance of Eu3+ by using heterocyclic N-donor ligands with different structures in ionic liquids: an experimental and theoretical study

. New J. Chem. 42, 7206-7212 (2018). doi: 10.1039/C8NJ00517F
Baidu ScholarGoogle Scholar
28. C. Marie, P. Kaufholz, V. Vanel et al.,

Development of a selective americium separation process using H4TPAEN as water-soluble stripping agent

. Solvent Extr. Ion Exch. 37, 313-327 (2019). doi: 10.1080/07366299.2019.1643569
Baidu ScholarGoogle Scholar
29. Y. Wang, J. Peng, W. Huang et al.,

A new strategy for identifying the water-insoluble radiolytic products of BPC6/ionic liquids and accessing their influence on the Cs extraction

. Radiat. Phys. Chem. 165, 108408 (2019). doi: 10.1016/j.radphyschem.2019.108408
Baidu ScholarGoogle Scholar
30. C.A. Zarzana, G.S. Groenewold, B.J. Mincher et al.,

A comparison of the γ -radiolysis of TODGA and T(EH)DGA using UHPLC-ESI-MS analysis

. Solvent Extr. Ion Exch. 33, 431-447 (2015). doi: 10.1080/07366299.2015.1012885
Baidu ScholarGoogle Scholar
31. P. Zsabka, K. Van Hecke, A. Wilden et al.,

Gamma radiolysis of TODGA and CyMe4BTPhen in the ionic liquid tri-n-octylmethylammonium nitrate

. Solvent Extr. Ion Exch. 38, 212-235 (2020). doi: 10.1080/07366299.2019.1710918
Baidu ScholarGoogle Scholar
32. Y. Sugo, M. Taguchi, Y. Sasaki et al.,

Radiolysis study of actinide complexing agent by irradiation with helium ion beam

. Radiat. Phys. Chem. 78, 1140-1144 (2009). doi: 10.1016/j.radphyschem.2009.06.031
Baidu ScholarGoogle Scholar
33. W.T. Xu, Y.F. Zhou, D.C. Huang et al.,

Luminescent sensing profiles based on anion- responsive lanthanide(III) quinolinecarboxylate materials: solid-state structures, photophysical properties, and anionic species recognition

. J. Mater. Chem. C. 3, 2003-2015 (2015). doi: 10.1039/C4TC02369B
Baidu ScholarGoogle Scholar
34. C. Lee, W. Yang, R.G. Parr,

Development of the Colle-Salvetti correlation-energy formula into a functional of the electron density

. Phys. Rev. B. 37, 785-789 (1988). doi: 10.1103/PhysRevB.37.785
Baidu ScholarGoogle Scholar
35. A.D. Becke,

Density‐functional thermochemistry. III. The role of exact exchange

. J. Chem. Phys. 98, 5648-5652 (1993). doi: 10.1063/1.464913
Baidu ScholarGoogle Scholar
36. W. Küchle, M. Dolg, H. Stoll et al.,

Energy‐adjusted pseudopotentials for the actinides. Parameter sets and test calculations for thorium and thorium monoxide

. J. Chem. Phys. 100, 7535-7542 (1994). doi: 10.1063/1.466847
Baidu ScholarGoogle Scholar
37. X. Cao, M. Dolg,

Segmented contraction scheme for small-core actinide pseudopotential basis sets

. J. Mol. Struct. 673, 203-209 (2004). doi: 10.1016/j.theochem.2003.12.015
Baidu ScholarGoogle Scholar
38. M. Dolg, H. Stoll, A. Savin et al.,

Energy-adjusted pseudopotentials for the rare earth elements

. Theoret. Chim. Acta. 75, 173-194 (1989). doi: 10.1007/BF00528565
Baidu ScholarGoogle Scholar
39. M. Dolg, H. Stoll, H. Preuss,

A combination of quasirelativistic pseudopotential and ligand field calculations for lanthanoid compounds

. Theoret. Chim. Acta. 85, 441-450 (1993). doi: 10.1007/BF01112983
Baidu ScholarGoogle Scholar
40. M. Dolg, H. Stoll, H. Preuss,

Energy‐adjusted ab initio pseudopotentials for the rare earth elements

. J. Chem. Phys. 90, 1730-1734 (1989). doi: 10.1063/1.456066
Baidu ScholarGoogle Scholar
41. H. Struebing, Z. Ganase, P.G. Karamertzanis et al.,

Computer-aided molecular design of solvents for accelerated reaction kinetics

. Nature Chem. 5, 952-957 (2013). doi: 10.1038/nchem.1755
Baidu ScholarGoogle Scholar
42. A.V. Marenich, C.J. Cramer, D.G. Truhlar,

Universal solvation model based on solute electron density and on a continuum model of the solvent defined by the bulk dielectric constant and atomic surface tensions

. J. Phys. Chem. B. 113, 6378-6396 (2009). doi: 10.1021/jp810292n
Baidu ScholarGoogle Scholar
43. Y. Sugo, Y. Izumi, Y. Yoshida et al.,

Influence of diluent on radiolysis of amides in organic solution

. Radiat. Phys. Chem. 76, 794-800 (2007). doi: 10.1016/j.radphyschem.2006.05.008
Baidu ScholarGoogle Scholar
44. H. Galán, A. Núñez, A.G. Espartero et al.,

Radiolytic stability of TODGA: Characterization of degraded samples under different experimental conditions

. Procedia Chem. 7, 195-201 (2012). doi: 10.1016/j.proche.2012.10.033
Baidu ScholarGoogle Scholar
45. H. Galán, C.A. Zarzana, A. Wilden et al.,

Gamma-radiolytic stability of new methylated TODGA derivatives for minor actinide recycling

. Dalton Trans. 44, 18049-18056 (2015). doi: 10.1039/C5DT02484F
Baidu ScholarGoogle Scholar
46. W.J. Yuan, C.Z. Wang, Y.Y. Ao et al.,

γ-Radiation effect on Th4+ extraction behaviour of TODGA/[C2mim][NTf2]: identification and extractability study of radiolytic products

. RSC Adv. 6, 7626-7632 (2016). doi: 10.1039/C5RA25364K
Baidu ScholarGoogle Scholar
47. B.J. Mincher, R.D. Curry,

Considerations for choice of a kinetic fig. of merit in process radiation chemistry for waste treatment

. Appl. Radiat. Isot. 5 (2000). doi: 10.1016/S0969-8043(99)00161-X
Baidu ScholarGoogle Scholar
48. R. Malmbeck, N.L. Banik,

Radiolytic behaviour of a TODGA based solvent under alpha irradiation

. J. Radioanal. Nucl. Chem. 326, 1609-1615 (2020). doi: 10.1007/s10967-020-07444-7
Baidu ScholarGoogle Scholar
49. S.P. Mezyk, B.J. Mincher, S.B. Dhiman et al.,

The role of organic solvent radical cations in separations ligand degradation

. J. Radioanal. Nucl. Chem. 307, 2445-2449 (2016). doi: 10.1007/s10967-015-4582-7
Baidu ScholarGoogle Scholar
50. B. Rajamouli, P. Sood, S. Giri et al.,

A dual‐characteristic bidentate ligand for a ternary mononuclear Europium(III) molecular complex – synthesis, photophysical, electrochemical, and theoretical study

. Eur. J. Inorg. Chem. 2016, 3900-3911 (2016). doi: 10.1002/ejic.201600508
Baidu ScholarGoogle Scholar
51. A. Wilden, G. Modolo, S. Lange et al.,

Modified diglycolamides for the An(III) + Ln(III) co-separation: Evaluation by solvent extraction and time-resolved laser fluorescence spectroscopy

. Solvent Extr. Ion Exch. 32, 119-137 (2014). doi: 10.1080/07366299.2013.833791
Baidu ScholarGoogle Scholar
52. A. Sengupta, P.K. Mohapatra, M. Iqbal et al.,

Spectroscopic investigations of Eu3+-complexes with ligands containing multiple diglycolamide pendant arms in a room temperature ionic liquid

. J. Lumin. 154, 392-401 (2014). doi: 10.1016/j.jlumin.2014.05.001
Baidu ScholarGoogle Scholar
53. M.R. Antonio, D.R. McAlister, E.P. Horwitz,

An europium(III) diglycolamide complex: insights into the coordination chemistry of lanthanides in solvent extraction

. Dalton Trans. 44, 515-521 (2015). doi: 10.1039/C4DT01775G
Baidu ScholarGoogle Scholar
54. А.N. Turanov, V.К. Karandashev,

Synergistic extraction of U(VI), Th(IV), and Lanthanides(III) from nitric acid solutions using mixtures of TODGA and dinonylnaphthalene sulfonic acid

. Solvent Extr. Ion Exch. 36, 257-271 (2018). doi: 10.1080/07366299.2018.1459157
Baidu ScholarGoogle Scholar
55. P.N. Pathak, S.A. Ansari, S.V. Godbole et al.,

Interaction of Eu3+ with N, N, N’, N’-tetraoctyl diglycolamide: A time resolved luminescence spectroscopy study

. Spectroc. Acta Pt. A-Molec. Biomolec. Spectr. 73, 348-352 (2009). doi: 10.1016/j.saa.2009.02.040
Baidu ScholarGoogle Scholar
56. Y. Sasaki, P. Rapold, M. Arisaka et al.,

An additional insight into the correlation between the distribution ratios and the aqueous acidity of the TODGA system

. Solvent Extr. Ion Exch. 25, 187-204 (2007). doi: 10.1080/07366290601169345
Baidu ScholarGoogle Scholar
57. Z.X. Zhu, Y. Sasaki, H. Suzuki et al.,

Cumulative study on solvent extraction of elements by N, N, N’, N’-tetraoctyl-3-oxapentanediamide (TODGA) from nitric acid into n-dodecane

. Anal. Chim. Acta. 527, 163-168 (2004). doi: 10.1016/j.aca.2004.09.023
Baidu ScholarGoogle Scholar
58. A. Kimberlin, D. Guillaumont, S. Arpigny et al.,

An experimental and computational look at the radiolytic degradation of TODGA and the effect on metal complexation

. New J. Chem. 45, 12479-12493 (2021). doi: 10.1039/D1NJ01143J
Baidu ScholarGoogle Scholar