# Electrochemical Deposition of U and RE Elements Using the Stirred Liquid Cadmium Cathode in LiCl-KCl Molten Salts

Authors: Gha-Young Kim; Chang Hwa Lee; Dalsung Yoon; Junhyuk Jang; Sung-Jai Lee
Journal: Science and Technology of Nuclear Installations
 (2021)

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## Abstract

This study was conducted in an attempt to understand the effect of a stirred liquid cadmium cathode (LCC) on the electrodeposition of U and U/RE on Cd. For this purpose, a series of electrowinning tests were performed using an LCC equipped with a Cd stirrer. Initially, three runs of the U electrodeposition tests were conducted using LiCl-KCl-UCl3 at 500°C under a constant current. From the results obtained from the initial three runs, it was found that the maximum deposited amount of U was 7.4 wt% U/Cd. U dendrite formation on the LCC crucible was not observed across each of the three runs. Three additional runs were conducted using LiCl-KCl-UCl3-RECl3 to determine the extent of U/RE electrodeposition. The maximum number of moles of U + RE metals deposited was 0.07, a value estimated to be 2.14 times higher than the solubility limits exhibited by these metals in Cd. The results of this study show that the use of a Cd stirrer significantly improves the extent of U deposition.


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## Body

## 1. Introduction

The acute global issue concerning the accumulation of spent nuclear fuel (SNF) has accelerated the development of abatement technologies that reduce the volume of radioactive waste. Pyroprocessing is a technology that enables the extraction of useful nuclear elements from SNF for use in fast reactors. Its commercial viability was successfully demonstrated through the EBR-II (Experimental Breeder Reactor-II) project [1, 2]. Pyroprocessing consists of several unit processes to separate and recover the radioactive elements from within the SNF [3, 4]. In the head-end process, the spent oxide fuel is separated from the hull, which then undergoes a heat treatment to achieve an appropriate size and density for the subsequent electrochemical processes. Subsequently, the processed spent oxide fuel is immersed in molten Li2O-LiCl salt at 650°C and reduced via electrolytic reduction. From here, the reduced spent fuel undergoes an electrorefining process in a eutectic LiCl-KCl melt with a predetermined volume of UCl3 at 500°C to facilitate uranium (U) recovery at the solid cathode. Subsequently, the residual U and transuranic elements (TRU) are recovered via electrowinning at the liquid cadmium cathode (LCC). After both electrorefining and electrowinning recovery steps have been applied, rare earth (RE) elements in the molten salt are treated to minimize salt waste and to facilitate the fabrication of a durable waste form. Among these unit processes, electrowinning is regarded as a key step owing to its nuclear proliferation resistance. Nuclear nonproliferation through the electrowinning process is achieved through the use of an LCC; however, an inevitable problem arises in the formation of U dendrites at the surface of the LCC. If the volume of U deposited exceeds the solubility limit of U in Cd, the U dendrites expand into the electrolyte phase which hinders the codeposition of U and TRU as it acts as a solid cathode. The problem arises as only U can be deposited on the U dendrites. In an attempt to solve this problem, a number of studies have focused on designing the LCC in such a way as to inhibit the formation of U dendrites. In Japan, a paddle-type stirrer was developed which prevented U dendrite formation by introducing turbulent flow [5]. In the USA, a pounder-type LCC was designed which pushed any U deposits down into the LCC [6]. At the Korea Atomic Energy Research Institute (KAERI), a mesh-type LCC structure was devised which allowed significant U deposition of over 5 wt% in the LCC without inducing U dendrite formation [7]. In this study, a series of U and U/RE electrodeposition tests were performed, utilizing a stirred LCC. The Cd stirrer was designed to improve actinide recovery by preventing the formation and growth of U dendrites at the Cd surface. In order to evaluate the performance of the stirred LCC, electrodeposition experiments using the novel LCC with the Cd stirrer were conducted in LiCl-KCl-UCl3 and LiCl-KCl-UCl3-RECl3 (RE: Nd, Ce, and La) at 500°C.


## 2. Materials and Methods

All experiments were performed in a glove box under an Ar(g) atmosphere (H2O < 1 ppm and O2 < 3 ppm). The liquid Cd cathode was prepared in a rectangular alumina crucible. The crucible was used as the Cd container into which a lead wire and Cd stirrer were added in parallel, as shown schematically in Figure 1. The stirrer consisted of a three-blade impeller and a head motor (IG-32GM 03TYPE DC 12 V + encoder), with the areas in contact with Cd being fabricated from alumina. The Cd lead wire was insulated by an alumina shroud except for a portion of the bottom section. The reference electrode consisted of a Mullite tube into which the LiCl-KCl eutectic mixture containing 1 mol% AgCl was added. An Ag wire (1 mm diameter, Nilaco, Japan) was then immersed into the LiCl-KCl-AgCl salt. The stainless steel (SS) anode basket contained approximately 270 g of U pellets. The U electrodeposition tests (runs 1–3) were performed in LiCl-KCl-2.85 wt% UCl3 salt, which was prepared by adding LiCl-KCl-10 wt% UCl3 to LiCl-KCl eutectic salt (99.99% purity, Sigma-Aldrich). UCl3 was prepared via the reaction of CdCl2 with U metal in molten LiCl-KCl at 500°C, which produced a purple salt containing 10 wt% UCl3 [8]. After the U electrodeposition tests had been performed, RECl3 (RE: Nd, Ce, and La, 99.99% purity, Alfa Aesar) was added to the salt for the U/RE electrodeposition tests (runs 4–6), which were performed in accordance with the initial conditions of the LCC electrowinning process shown in the KAERI flow sheet. The composition of the prepared LiCl-KCl salts containing U and RE elements is shown in Table 1. The metal chloride concentrations in the LiCl-KCl eutectic melts were determined through inductively coupled plasma-atomic emission spectroscopy (ICP-AES). The electrochemical experiments were performed using a Biologic SP-300 potentiostat/galvanostat. The electrodeposition tests were performed under a constant current density (100 mA/cm2). At the end of the electrodeposition test, the LCC crucible was removed from the electrolyte bath and naturally cooled at room temperature. Subsequently, the Cd ingot, containing U or U/RE deposits, was separated from the crucible. The mass of U or U/RE deposited onto the Cd surface was calculated based on the total charge transferred during each run, assuming 100% current efficiency.Figure 1
Schematic of the experimental setup.Table 1
Salt composition for each of the U/RE electrodeposition tests.
wt%UCl3NdCl3CeCl3LaCl3Runs 1–32.85———Runs 4–62.761.980.810.42


## 3. Results and Discussion

Prior to starting the LCC electrodeposition test, cyclic voltammetry (CV) measurements were performed using the stirred LCC immersed in LiCl-KCl-2.85 wt% UCl3 at 500°C. Figure 2 shows the CV results obtained under various Cd stirring rates. It was observed that the CV curve was distorted by stirring Cd. As the stirring rate of Cd increased, the cathodic peak potential exhibited a negative shift, while the peak current exhibited a positive increase. This was attributed to the surface enlargement of Cd induced through agitation. No further changes to the CV values were observed when the stirring rate surpassed 60 rpm. Thus, a Cd stirring rate of 60 rpm was used throughout these experiments.Figure 2
Cyclic voltammograms of the liquid Cd electrode in LiCl-KCl-UCl3 at 500°C with various Cd stirring rates.Three runs of the U electrodeposition tests were performed in LiCl-KCl-2.85 wt% UCl3 at 500°C, under a constant applied current (1.25 A, 100 mA/cm2). Run 1 was conducted for approximately 2.4 h and used 330 g of Cd. As shown in Figure 3, the anode’s potential was maintained at −1.10 V, while the cathode’s potential of −1.62 V exhibited fluctuations as a result of the Cd stirring. After 2.39 h, the cathode’s potential shifted to a negative trajectory, and run 1 was terminated. The total amount of charge transferred was 4.19 Ah, and the amount of U deposited was calculated to be 3.76 wt% U/Cd. This was 1.6 times higher than the U solubility limit in Cd, which is 2.35 wt% U/Cd. Despite the sharp decrease in the cathode potential recorded at the end of the test, there was no observable U dendrite formation over the crucible (Figure 4).Figure 3
Potential profiles of run 1 using the stirred LCC immersed in LiCl-KCl-UCl3 at 500°C.Figure 4
Photographs of the LCC crucible and Cd ingot after run 1.Subsequently, two further U electrodeposition runs were performed at the same applied current. Run 2 used 335 g of Cd and was conducted for approximately 4.08 h. The initial potential at the anode was −1.1 V, which gradually increased to −0.9 V. The potential at the cathode was −1.7 V during the first 2 h of operation, which then gradually decreased to −2.0 V at the end of the test (data not shown). The total amount of charge transferred was 5.09 Ah which corresponded to a deposition amount of approximately 4.5 wt% U/Cd, a value 1.9 times higher than the solubility limit of U in Cd. U dendrite formation was not observed on either the LCC crucible or the Cd surface. In contrast to runs 1 and 2, run 3 was conducted using 200 g of Cd over a period of 4 h. Owing to the constraints imparted by the physical environment, it was not possible to extend the period of time over which the test was performed. Therefore, it was necessary to reduce the initial mass of Cd to increase the extent of the electrodeposition (wt%) over the same time period. As shown in Figure5, the cathode potential was in the range between −1.8 and −1.9 V during the first 2 h of operation before continually decreasing over the remainder of the test period to reach −2.1 V. Throughout the test, the potential at the anode remained relatively stable around −1.1 V. The total amount of charge transferred was 5.00 Ah, which corresponded to an electrodeposition amount of approximately 7.4 wt% U/Cd. This value is 3.0 times higher than the solubility limit of U in Cd. The LCC product after run 3 is shown in Figure 6. In runs 1–3, U dendrites on Cd and/or over the LCC crucible were not found, which is confirmed by the photographs of LCC products (Figures 4 and 6). It was proved by no increasing of the cathodic potentials during the electrodeposition of U (Figures 3 and 5). This indicates there was no variation of Cd surface area induced by the formation of U dendrites. If there was any growth of U dendrite, it would either sink or be crushed into Cd by operating the Cd stirrer. Each of the results, including the deposited mass of metal across runs 1–6, is summarized in Table 2.Figure 5
Potential profiles obtained during run 3 using the stirred LCC immersed in LiCl-KCl-UCl3 at 500°C.Figure 6
Photographs of the LCC crucible and Cd ingot after run 3.Table 2
Results of electrodeposition runs 1–6 in this study.
Run no.Cd (g)Q (Ah)Assumption: current efficiency of 100%U (wt%/Cd)(U + RE)deposited/(U + RE)saturated13304.193.8—23355.094.5—32005.007.4—41012.50—∼1.0051063.75—1.4361055.69—2.14After each of the U electrodeposition tests had been completed, three U/RE electrodeposition runs were performed in the same manner using LiCl-KCl-UCl3-RECl3. Run 4 used 101 g of Cd, and a constant current of 1.25 A was applied for approximately 2 h (data not shown). The initial cathode potential was −1.8 V, which incrementally increased to −1.2 V before stabilizing at −1.6 V. The anode potential repeatedly and periodically fluctuated before stabilizing around −1.0 V. The total amount of charge transferred was 2.50 Ah. Run 5 used 106 g of Cd and was conducted for 2.5 h. The potential at the anode was maintained at −1.3 V, while the potential at the cathode was maintained at −1.6 V (data not shown). The total amount of charge transferred during run 5 was 3.75 Ah. Finally, run 6 used 105 g of Cd and was conducted for 3.8 h (Figure 7). The anode potential fluctuated over a 0.50 h cycle during the initial 1.67 h of operation before stabilizing at −0.55 V. The initial cathode potential was approximately −1.8 V. This potential exhibited significant fluctuations during the first 1.00 h of operation before increasing slightly to −1.6 V for the remainder of the test. The total amount of charge transferred in run 6 was 5.69 Ah. As both U and RE were deposited onto the LCC during the U/RE electrodeposition tests (runs 4–6), it was necessary to convert the total amount of charge transferred across runs 4–6 to the number of moles of the electrodeposited metal. Considering this conversion, the total number of moles of U + RE deposited across runs 4–6 was 0.031, 0.047, and 0.071, respectively. These values were compared with the solubility limits of the metals in Cd at 500°C (Table 3) [9]. By considering the weight of Cd used in each run, it was determined that a volume corresponding to the solubility limit was electrodeposited during run 4. During runs 5 and 6, the volume of the electrodeposited metal (U + RE) exceeded the solubility limit by 1.40 and 2.14 times, respectively. After the tests had ended, the Cd ingots which had been subjected to U/RE deposition were easily and distinctly separated from their alumina crucibles, and there was no U dendrite formation observed in each ingot (Figure 8).Figure 7
Potential profiles gathered during run 6 using the stirred LCC immersed in LiCl-KCl-UCl3-NdCl3-CeCl3-LaCl3 at 500°C.Table 3
Solubility limit of metal elements in Cd at 500°C [9].
ElementSolubility limitwt%/Cdg (based on Cd 100 g)Number of moles (based on Cd 100 g)U2.352.350.0099Nd1.891.890.0131Ce0.7540.7540.0054La0.40.40.0029Figure 8
Photographs of the LCC crucible and Cd ingot after run 6.


## 4. Conclusions

The effect of the stirred LCC on the electrowinning performance was evaluated by the extent of the electrodeposition exhibited by LiCl-KCl salts containing U or U/RE at 500°C. Three tests were performed using LiCl-KCl-UCl3 (runs 1–3), and the amount of deposited U was estimated as 3.8, 4.5, and 7.4 wt% U/Cd, across runs 1, 2, and 3, respectively. The formation of U dendrites on the LCC crucible was not observed in any of the three runs. Considering that the solubility limit of U in Cd is 2.35 wt% U/Cd, it was possible to determine that the use of a Cd stirrer facilitated an increase in the efficiency of U recovery. Three additional electrodeposition tests (runs 4–6) were performed using LiCl-KCl-UCl3-RECl3 under an applied current density of 100 mA/cm2. The number of moles of the metal (U, Nd, Ce, and La) deposited on Cd was 0.031, 0.047, and 0.071, across runs 4, 5, and 6, respectively. These values were compared with the solubility limits exhibited by each metal in Cd. According to the results, the amounts of metal (U and RE) deposited on Cd were between 1.00 and 2.14 times higher than the proposed solubility limits in Cd. Although these results were obtained through calculations rather than chemical analysis, it was found that the use of a Cd stirrer enhanced the LCC performance during the electrowinning process through the inhibition of U dendrite formation.



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*Source: 5788732-2021-10-28.xml*