Stephen T.
Lam
*ab,
Qing-Jie
Li
a,
Jonathan
Mailoa
c,
Charles
Forsberg
a,
Ronald
Ballinger
ad and
Ju
Li
ad
aDepartment of Nuclear Science and Engineering, Massachusetts Institute of Technology, Cambridge, MA 02139, USA. E-mail: stephen_lam@uml.edu
bDepartment of Chemical Engineering, University of Massachusetts Lowell, Lowell, MA 01854, USA
cBosch Research and Technology Center, Cambridge, MA 02139, USA
dDepartment of Materials Science and Engineering, Massachusetts Institute of Technology, Cambridge, MA 02139, USA
First published on 21st December 2020
Interest in molten salts has increased significantly over the last decade due to their potential application in various clean-energy technologies including hydrogen generation, solar heat storage, advanced fission nuclear power plants, and compact fusion energy systems. In nuclear fission and fusion power plants, high heat capacity molten salts allow operation at high temperature and atmospheric pressure, which could dramatically increase efficiency, reduce capital cost, and enable passive safety features. In many of these systems, the hydrogen isotope is of particular importance due to its ability to corrode structural materials as 3H+ in fluoride salts, and its potential to cause significant radioactive release as diffusive 3H0, which are cited as key barriers to technological deployment. Yet, the chemistry and transport behavior of the hydrogen species remain poorly understood due to the difficulties in handling toxic salts and radioactive materials. Here, using ab initio molecular dynamics, we present a coupled examination of hydrogen speciation in the most common prototypical salts 66.6% LiF–33.3% BeF2 (Flibe) and 46.5% LiF–11.5% NaF–42% KF (Flinak). Using extensively validated calculations on the local structure and dynamics, we find significant difference between 3H0 and 3H+ transport behaviors that are usually overlooked. We find that 3H0, which always exists as H2, diffuses 3–5 times faster than 3H+, which can be ascribed to hydrogen bonding and complexation in solution. This work explains contradicting experimental results and provides useful species transport data for designing hydrogen capture and corrosion control systems for molten salts.
Fluoride molten salts are of particular interest in the development of next-generation nuclear reactors, since they offer a combination of high heat capacity, high boiling point, and low neutron absorption.10 While existing water-cooled nuclear power generates more than 50% of the carbon-free electricity in the U.S. today, total nuclear capacity is projected to steadily decrease towards 2050 and new nuclear installations will be limited by concerns of safety, and economic viability.11,12 A step-change improvement in nuclear technology is therefore required for nuclear power to significantly contribute to decarbonization of the electrical grid. Thus, there has been a significant push towards the development of advanced molten salt nuclear systems, which could enable greatly increased heat removal, thermodynamic efficiency, and operation at near-atmospheric pressure. As a result, the use of molten salts could enable design simplification, economic competitiveness, and inherent safety via passive heat rejection.
Molten-salt cooled advanced reactors of all types have proposed the use of lithium-based salts since the addition of lithium depresses the melting point, making them easier to handle.13–15 Among candidate salts, 66.6LiF–33.3BeF4 (Flibe) and 46.5LiF–11.5KF–42NaF (Flinak) are the most popular choices for their superior heat transfer properties.16,17 One of the greatest known challenges however, is that radioactive tritium (3H) is generated by the neutronic reaction 6LiF + n → 4He + 3HF.18 The presence of 3HF drives up the redox potential in the system,7 as hydrogen is less electropositive than lithium, which causes corrosion of metallic species such as chromium via the equilibrium reaction: 23HF(g) + Cr(s) ↔ CrF2(soln) + 3H2(g), forming diatomic tritium gas. The relative concentration of the Mn+/M (M = Cr, Fe, Ni or other structural metal elements) and HF/H2 couples depend on the temperature and redox potential, which is established by the Nernst equation. The diffusion of hydrogen/tritium into structural materials can cause hydrogen-induced embrittlement, as well as tritium permeation and tritium inventory problems that are nuclear safety concerns. Furthermore, corrosion products like CrF2 have the potential to precipitate in the system, which leads to heat exchanger fouling and the presence of these dissolved species can also change the physical, thermodynamic and chemical properties of a molten salt mixture.8 In order to minimize oxidation in structural steels, the salt must be sufficiently reducing such that the vast majority of the tritium is converted to H2, with a HF to H2 ratio less than 0.01. On the other hand, the potential must remain sufficiently high (oxidizing) to prevent precious metal precipitation, resulting in a narrow operating window [Ulower, Uupper] (Uupper − Ulower) ∼ 0.1 V for Flibe) at reactor operating temperatures. Charge neutral H2 in coolant fluid and atomic H in some metals are highly diffusive and must be continuously removed from the system and captured to minimize the potential for a significant radiological release.19
The removal of tritium from salt is a coupled problem of redox chemistry and transport that requires understanding and accurate prediction of the in situ behavior of possible tritium species. Differences in diffusion and reaction rates can result in differential species removal rates. Depending on the system design, this can change the relative quantities of the H oxidation states present in the salt, in which ½ H2(molten-salt) ↔ H+(molten-salt) + e−(U), where the left-hand side is one-half of a charge-neutral molecule that is solvated in the liquid molten salt, and the right-hand side is a proton/triton cation living in the same liquid phase with dynamic coordinations of fluorides, plus an excess quantum mechanical free electron living in the metal electrode of Fermi energy EF = −eU. At thermodynamic equilibrium, the concentration quotient [H+]/[H2]½ in the molten-salt phase can shift the voltage U of the metal.20,21 By metal–salt interactions (corrosion or deposition), U can also affect the concentrations of other charge-neutral or charged species (impurities or fission products) in the melt, which can produce unwanted changes in performance. Thus, the valence-dependent transport and chemical properties of tritium must be precisely quantified and understood. Yet, little reliable experimental data is available due to the costly handling of toxic salts and radioactive tritium. Thus, tritium control has been repeatedly emphasized as a bottleneck in the road to developing any reactor using lithium-based molten salts.22,23
In this work, we examine the chemical behavior of tritium species in both prototypical salts Flibe and Flinak. First-principles simulation is used to interpret experimental results and predict salt properties, elucidating the chemical structure and transport properties required to predict tritium evolution in the system. This work establishes a link between tritium chemistry and transport behaviors over the thermodynamic conditions for a typical operating reactor. By comparing disparate experimental results with predictions from first principles, we highlight experimental methods and provide further guidance for measuring radioactive salts. Lastly, our validated calculations also generate useful engineering data that can be directly used in the design of tritium or salt handling systems.
In this work, tritium local structure, chemistry and transport are investigated using ab initio simulation with realistic dynamics and thermochemistry.37,38 Dilute tritium as 3H+ and 3H0 are separately introduced into the prototypical molten salts. The simulation and analysis protocols are described in detail in the methods section. In addition to tritium-in-salt systems, calculated properties of various fluoride salts including LiF, KF, LiF–KF, BeF2, NaF, Flibe and Flinak are compared and supported by experimental data, increasing confidence in simulation data. These salts were chosen due to their chemical similarity with the prototypical salts of interest, availability of data, and relevance in fuel processing, spent fuel recycling, cooling advanced fission reactors, or as potential for tritium fuel production in fusion devices.39–42 The results of these supporting calculations are discussed in ESI.†
For Flinak, H–F coordination is very similar to that of Flibe. The H–F RDF, where tritium has a + 1 oxidation state shows a distinct peak at 1.1 Å, with a calculated coordination number of 1.83, which indicates a coordination of either 1 or 2 atoms. Coordination tallying shows that the tritium was coordinated to two fluorine atoms 95% of the time, and only one fluorine for 5% of the simulation. The coordination number and peak distances are summarized in Table 1.
Salt | Ion pair | First peak radius (Å) | Coordination number |
---|---|---|---|
Flibe | H+–F− | 0.9 | 1.76 |
H0–F− | 2.7 | — | |
Flinak | H+–F− | 1.1 | 1.85 |
H0–F− | 2.7 | — |
For 3H0 in Flibe, no reactions were found and tritium existed solely in H2 with a H–H interatomic distance of 0.76 Å at 973 K. The dissolution of 3H+ is confirmed in Fig. 2, which shows the interatomic distance between a single 3H3H+ atom and different fluorine atoms in the mixture. 3H+ becomes coordinated to fluorine with an average interatomic distance of 1 Å, and jumps between different fluorine atoms during the simulation. In addition, tritium can coordinate to two fluorine atoms simultaneously as shown between t = 15–24 ps (the overlapping time period on 1 and 2 in Fig. 2a) with fluorine atoms ‘1’ and ‘2’ (see Fig. 2b for the snapshots). In contrast, 3H0 remains un-coordinated to fluorine and the interatomic distance is always greater than 1.5 Å. Thus, 3H+ appears much more reactive in Flibe than 3H3H0. This suggests that 3H+ has a higher solubility than 3H0 in Flibe, which agrees with the relative magnitudes of their Henry's coefficients in literature.46,47
We found 3H+ exists in various chemical forms, including HF, HF2−, BeF4HF2−, and Be2F7HF3−, in the fractions shown in Fig. 3d. A snapshot of the simulation is shown in Fig. 3a, numerical representation of molecules is shown in Fig. 3b, and an example reaction is shown in Fig. 3c. Simple fluorides HF and HF2− were the most common states with mean life-time τ = 4.4 and 1.8 ps at 973 K respectively, while tritium bound to BeF42− (τ = 0.43 ps) tetrahedral and tetrahedral polymer chains were found to exist less than 15% of the simulation time (60 ps). The “other” category in Fig. 3d consists of rare (single-event) structures making up the remainder of the simulation, which includes free tritium ion or tritium complexes with larger BeF complexes such as Be3F10HF4− (τ = 0.33 ps) or Be4F13HF−5 (τ = 0.097 ps), which existed for less than 0.1% of the simulation. With increasing temperature, free tritium and other transition states become more common, occupying 5% of the simulation at 973 K, and up to 20% of at 1373 K. The average lifetime of H+ complexes reduces with increasing temperature with τ = 1.4, 1.0 and 0.8 ps for 973, 1173 and 1373 K respectively.
Reactions with H+ involving the most common complexes are shown in Table 2, all of which involve the combination with HF to an existing atom or molecule in the solution. The first reaction shows that the formation of the HF2− complex from F− ion and HF combination with ΔE = −0.4 eV calculated for the isolated molecules. For this reaction, the rate of association and dissociation of F− with HF increases with increasing temperature, likely dependent on the amount of free fluorine that is available from the surrounding mixture. The second reaction involves a HF molecule bonding to a BeF42− tetrahedral complex with ΔE = −0.6 eV. Reaction two is more than twice as frequent at 973 K than 1173 K and 1373 K, which corresponds to the availability of BeF4HF2− at lower temperatures as shown in Fig. 3d. The last reaction shows the bonding of an HF molecule to two corner-sharing BeF42− tetrahedral complexes with ΔE = −0.6 eV. The ‘other’ reactions all involve less common species, such as transition complexes swapping F− ions with solution, or HF breaking and joining with larger Beryllium complexes: Be3F10HF4− ↔ BeF3− + Be2F7HF3−. The frequency of these reactions increases with increasing temperature due to the increase in transient high-energy structures that are discovered at higher temperatures.
Reaction | Count | |||
---|---|---|---|---|
T = 973 K | T = 1173 K | T = 1373 K | ||
1 | F + HF ↔ HF2− | 22 | 32 | 35 |
2 | BeF42− + HF ↔ BeF4HF2− | 54 | 16 | 20 |
3 | Be2F7− + HF ↔ Be2F7HF− | 8 | 18 | 3 |
Other | 50 | 59 | 166 |
This analysis suggests high 3H+ reactivity to fluorine and beryllium mixture in Flibe, which are in agreement with the RDFs analysis and further confirm that solvation of 3H3H+ is significantly stronger than that of 3H0.
In Flinak, all the cations are monovalent and form fewer complex molecules, in contrast to Flibe where longer chains of Be–F complexes are found. Li or K do not form detectable reaction products, indicating free lithium and potassium ions in solution. Most sodium atoms in the simulation were also freely dissociated; only ∼11% of the Na found in a polyhedral configuration (3% as NaF4, 8% as NaF5). Further, Na complexes usually have lifetimes on the order of 102 fs and readily react or exchange with fluorine in the solution. As a result, relatively few H+ reactions were found in the solution. A handful of reactions found included HF2− combination reactions with NaF complexes such as: HF2− + NaF43− ↔ NaF5HF4− (ΔE = −0.5 eV), and NaF5HF4− + F− ↔ HF2− + NaF54− (ΔE = −0.1 eV). At the higher temperatures of 1173 K and 1373 K, some dissociative behavior was observed for HF2− with the fluorine ejection reaction HF2− ↔ HF + F− (ΔE = 0.5 eV) observed 4 times.
In Flinak, the behavior of 3H0 is similar to that in Flibe, where tritium exists purely as H2 with |H–H| = 0.77 Å at 973 K. This again agrees with the result of the radial distribution function in Fig. 1, which shows weak solvation of hydrogen with fluorine. Thus, in both clean Flibe and Flinak, 3H0 shows little chemical interaction with surrounding ions compared to 3H+.
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Fig. 5 Experiments versus simulation. Calderoni used tritium 3H gas diffusing across a 1-D nickel membrane, Oishi used 3H created by salt irradiation and measured diffusion in a capillary, Anderl used 2H diffusion in a cylindrical cell, and Nakamura used 1H in a cylindrical cell. The shaded region represents 95% confidence interval of regression.24–27 |
The calculated diffusivity for 3H0, as a result of H2 molecular diffusion, was found to be on average 3–4 times larger than that of 3H+. Such a large difference in diffusivity is related to the coordination of 3H+ with beryllium fluoride complexes and fluorine in the mixture. The calculated diffusivity and activation energies are shown in Table 3. The diffusion equation for two oxidation states are expressed:
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Temperature (K) | 3H+ diffusivity × 109 (m2 s−1) | 3H0 diffusivity × 109 (m2 s−1) |
---|---|---|
973 | 3.0 ± 0.5 | 6.3 ± 1.4 |
1173 | 7.0 ± 1.3 | 16.3 ± 3.3 |
1373 | 11.1 ± 1.6 | 27.0 ± 4.1 |
The calculated activation energies for 3H0 and 3H+ are similar, 40.0 ± 3.0 kJ mol−1 and 36.0 ± 2.0 kJ mol−1 respectively. Compared to the experimental data, the simulation results are within error bounds of Calderoni's and Oishi's experiments. In Oishi's experiment,25 tritium is generated as 3H+ from salt irradiation. However, some of the tritium is likely to chemically react with the Ni container to generate 3H2. In Calderoni's experiment,24 hydrogen purge gas is used, which likely isotopically exchanges with 3HF to form 3H1H in the solution. Further, both experiments purified the salt by hydro-fluorination and thus may contain some proportion of 1H molecules which could react or exchange with 3HF or 3H2. Thus, in both experiments, the diffusivity measurement likely corresponds to a combination of tritium species and oxidation states. The activation energy calculated using Oishi's data was 36.0 ± 6.0 kJ mol−1, and the activation energy from Calderoni was found to be 42.0 ± 7.0 kJ mol−1, which are similar to the computational values.
In the other two studies, data collection was limited (2–3 experimental measurements), and data significantly diverged from simulation and previous experiments. Both used diffusion in a similar cylindrical diffusion cell. In Anderl's experiment,26 diffusivity measured was 0.8 × 10−5 cm2 s−1, which is 80% lower than computed 3H0 diffusivity and 40% lower than 3H+ calculated from eqn (1) and (2). In Anderl's experiment, impurity analysis found 600 ppm of oxygen impurity in the salt before the start of the experiment. This combined with any potential oxygen ingress could cause reactions with HF via: BeO + 2HF → BeF2 + H2O. In this case, the measured diffusivity could actually be that of H2O or other intermediate reaction complexes. Further, their analytical model used diverged from their experimental data over time. This suggests a systematic error in the transport model, possibly due to increasing air ingress or other interfacial effects.26 Similarly, Nakamura's experiment under-predicted by the same order of magnitude at 823 K.27 The experimental activation energy was also lower than the calculated values at 25.2 ± 8 kJ mol−1. In Nakamura's study, the lower diffusivities and activation energies could be caused by potential impurities (not measured) or temperature gradients in the experimental cell.
While previous studies have found that impurities can significantly increase in corrosion and change the thermochemical properties of salt, the specific impact of different impurities on tritium is not well understood.8,9 Here, additional simulations were performed for tritium and Flibe in the presence of a single unit of Cr (dominant corrosion product) and H2O (atmospheric moisture) at 973 K. In these cases, tritium diffusivity decreased by 25% and 15% respectively. From structure analysis, tritium was found to coordinate with the impurities (Cr–3H and 3H–O bonding), which likely resulted in the observed differences in diffusivity relative to pure Flibe. The structures discovered can be found in the ESI in Fig. S7.† Similarly, it was found that the introduction of corrosion impurities (CrF, HF) can alter the diffusivities and activation energies of Li and F ions in Flibe shown in Fig. S6.† These results support the idea that impurity effects can impact experimental results summarized in Fig. 5 and provides further evidence that impurities can significantly impact chemical and transport properties. However, many more atmospheric and fission-generated impurities can exist simultaneously, which can have unpredictable effects in real systems. As such, the role of impurities in a variety of chemical forms, oxidation states, and conditions warrants a more detailed investigation in future studies.
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Fig. 6 Comparison of hydrogen diffusivity between ab initio simulations and three experiments. Experiment by Zeng and Fukada diffuse H2 across a 1-D nickel membrane, while experiment by Nakamura was done by radial diffusion across a cylindrical Monel window. The highlighted region represents the 95% confidence interval from regression of the collected data.27–29 |
Temperature (K) | 3H+ diffusivity × 109 (m2 s−1) | 3H0 diffusivity × 109 (m2 s−1) |
---|---|---|
973 | 2.9 ± 0.5 | 10.6 ± 2.3 |
1173 | 6.7 ± 0.7 | 23.4 ± 3.1 |
1373 | 8.25 ± 1.25 | 31.0 ± 5.1 |
The activation energies of both oxidation states are similar at 29.0 ± 6.4 kJ mol−1 for 3H0 and 29.0 ± 9 kJ mol−1 for 3H+ in Flinak. From analysis of chemical structure, the lower diffusivities of 3H+ can be attributed to the fact that the molecule exists as a larger and more chemically reactive molecule HF2− in the melt, whereas 3H0 exits as H2. The lower activation energies of tritium in Flinak compared to Flibe indicate a lower diffusion barrier. This can be rationalized in terms of chemical structures in both salts; the formation of BeF42− chains in Flibe obstructs transport while relatively free ions dominate in the Flinak solution. Like Flibe, the redox condition in Flinak can be either reducing or oxidizing depending on the impurities in the salt.
Fukada suggested that their results measured H0, which showed the most similarity to the calculated diffusivity of 3H0 compared to other studies. In this experiment, tests were performed to ensure low corrosion of nickel due to contact with Flinak. Further, both pH measurement and mass spectroscopy were performed during the diffusion measurement to confirm H2 measurement was up to a sensitivity of 1 ppm and HF up to sensitivity of 1 ppb. Here, the simulations again confirm the importance of accurately confirming the redox and impurity state. The activation energy calculated from their data from 800 K to 1000 K was 43.0 ± 4.7 kJ mol−1, which is higher than the simulated values. This is likely due to the higher temperatures used in simulation. Fukada found that, the activation energy for diffusion increased at lower temperatures due to increased mass transfer resistance at interfaces caused by increased H+ interaction. Thus, these results show good agreement with our simulations in general.
In contrast, corrosion impurities and chemical species were not measured explicitly in the other two studies. In both studies, this is combined with a limited number of experimental data points, yielding high uncertainty in the overall result. The activation energy calculated by Nakamura was found to be near-zero to slightly negative −5.4 ± 5.7 kJ mol−1, which has not been observed in any other species transport in molten salts.30 Here, we note that Nakamara's Flinak study uses the same experimental procedure as their Flibe study discussed in Section 3.2.1, both of which show significant deviations from simulations in this work and other experiments in the literature. This suggests a systematic error in the study, possibly caused by the measurement protocol (cylindrical diffusion with analytical model), or the use of hydrogen interacting materials (Monel). This effect, along with impurity interaction as examined for Flibe in Section 3.2.1, should be explored more thoroughly since the diffusivity and activation energies differ dramatically from other experimental data and these simulations.
Chemical-structural analyses suggest that, in fluoride salt, 3H+ shows soluble and dissociative behaviors in both Flibe and Flinak. Specifically, 3H+ coordinates with BeF42− tetrahedral corner-sharing polymer-like structures in Flibe, while, in Flinak, 3H+ exists as HF2− with some association to NaF polyhedra. In contrast, 3H0 remained bound as a gaseous dimer H2 in both Flibe and Flinak. As a result, the diffusivity of 3H0 is 3–4× and up to 5× higher than that of 3H+ in Flibe and Flinak, respectively. Further, the diffusion activation energies in Flibe (40.0 ± 3.0 kJ mol−1 for 3H0 and 36.0 ± 2.0 kJ mol−1 3H+) are higher than those in Flinak (29.0 ± 6.4 kJ mol−1 for 3H0 and 29.0 ± 9 kJ mol−1 for 3H+) due to the formation of BeF networks that lower overall ionic transport in Flibe, in comparison to Flinak where ions are predominately free. In both salts, the 3H+ activation energy is similar to 3H0, showing fairly weak association with similar characteristic to hydrogen bonding between hydrogen and fluorine atoms.
In interpreting the limited experimental results with wide discrepancies spanning more than an order of magnitude, our ab initio simulations provide a deeper understanding of experimental sources of error like impurity concentration, surface effects, and corrosion. Furthermore, we provide atomistic level insight into the interplay among oxidation states, structures and transport properties of tritium in both Flibe and Flinak, as well as useful engineering data that is difficult to obtain experimentally. The relative differences between H0 and H+ can greatly impact the design of impurity removal and corrosion control systems in both nuclear and non-nuclear salt-based systems. In advanced nuclear reactors, diffusive radiological release and corrosion are two of the most prominent challenges that are tightly coupled through tritium transport and chemistry. This work elucidates hydrogen behavior that must be accounted for in future experiments and modeling of molten salts.
In each system, the cell size was chosen to match the experimental density of the salt. For systems where accurate density is not known, it can be estimated by running a series of simulations to fit an equation of state, or by running the isobaric-isothermal ensemble (NPT) until equilibrium is reached. The relatively small system sizes are chosen for computational efficiency. While periodic effects might be expected for smaller system sizes, it has been shown by simulating larger cells of up to 200 atoms that properties like diffusion and local structure are generally converged on the smaller system sizes.37
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The second method allows for the detection of extended molecular structures and reactions by using graph-theory based searching algorithms followed by statistical filtering for noise removal. The method follows that of Martinez,45,56 which has previously been used to study reactions and transport in organic systems and surfaces.44,57–59 At each step in the trajectory, the system is represented by an atomic graph with nodes N and edges E. The nodes represent individual atoms, while the edges represent bonds between atoms, defining the graph Gt as below:
Gt = (N:{A1, …, An}, E:|Rij ≤ RCij) | (6) |
For each molecular subgraph found in the simulation, a binary time series Em(t) is constructed valued at 1 or 0 is constructed to indicate whether the subgraph exists (value of 1) at each time step in the simulation. The observed signal E, is modeled using a two-state Hidden Markov Model (HMM) in which there exists an underlying lower-frequency signal X, representing the true signal. The HMM is defined by the joint probability:61
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The transition probability of switching states, tp was set between 10−6 to 10−7, which is markedly low to provide a stronger noise filter that removes false transitions in the observed signal. This is necessary due to the high-temperature liquid state causing high-frequency fluctuations in the system. The Viterbi algorithm is used to find the likely sequence X that produced observation E.
With the filtered sequences Xm for each molecule, chemical reactions are then found. The generation of a new product is characterized by a 0 → 1 transition in the sequence occurring at time τp and the destruction of a reactant is characterized by a 1 → 0 transition at τr. At each product time, the nearest reactants and products in time are located and a chemical balance is performed, checking for stoichiometric conservation among the reactants and products. If a reaction is not found, the search window for reactants and products is iteratively expanded, until chemical balance can be achieved or a maximum search window Δτ = 150 fs is reached. If no atom-conserving reaction can be found for a generated product, it is disregarded as unfiltered noise. The reaction energies are determined by performing geometry optimized DFT calculations on the reactants and products extracted from the trajectory.
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Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/d0ta10576g |
This journal is © The Royal Society of Chemistry 2021 |