This protocol describes the measurement of the electromotive force of alkaline-earth elements in liquid metal alloys at high temperatures (723-1,123 K) to determine their thermodynamic properties, including activity, partial molar entropy, partial molar enthalpy, and phase transition temperatures, over a wide composition range.
A novel electrochemical cell based on a CaF2 solid-state electrolyte has been developed to measure the electromotive force (emf) of binary alkaline earth-liquid metal alloys as functions of both composition and temperature in order to acquire thermodynamic data. The cell consists of a chemically stable solid-state CaF2-AF2 electrolyte (where A is the alkaline-earth element such as Ca, Sr, or Ba), with binary A-B alloy (where B is the liquid metal such as Bi or Sb) working electrodes, and a pure A metal reference electrode. Emf data are collected over a temperature range of 723 K to 1,123 K in 25 K increments for multiple alloy compositions per experiment and the results are analyzed to yield activity values, phase transition temperatures, and partial molar entropies/enthalpies for each composition.
Electromotive force (emf) measurements can directly determine the partial molar Gibbs free energy change of a chemical reaction and provide accurate thermodynamic properties such as activity, partial molar enthalpy, and partial molar entropy1. The acquisition of thermochemical data is crucial to a variety of research topics in the materials community, from the refinement of multi-component phase diagrams, to the experimental validation of first-principle materials modeling, to the synthesis of new intermetallic species with advantageous properties. Recently, Kim et al. utilized emf measurements to assess the viability of using liquid metal electrodes to separate alkaline-earth species from molten salt electrolytes2.
Electrochemical separation using molten salts (e.g., LiCl-KCl) is a promising technology for separating uranium and transuranic metals from used nuclear fuel for recycling3. As used fuel is processed as an anode in the molten salt, fission products with lower standard reduction potentials than uranium are oxidized and accumulate in the molten salt as dissolved ions (e.g., Ba2+, Sr2+, Cs+, and rare-earth metal cations)4. Consequently, the molten salt electrolyte must be periodically replaced and/or processed further to separate the accumulated fission products4. Of particular concern are alkali/alkaline-earth fission products (Ba2+, Sr2+, and Cs+) because these ions exhibit the lowest standard reduction potentials among the constituent cations, making them difficult to separate from the molten salt solution.
However, Lichtenstein et al. recently demonstrated that barium exhibits low thermodynamic activity in liquid bismuth (8.7 x 10-12 at barium mole fraction xBa(in Bi) = 0.05, 1,123 K), implying strong atomic interactions between barium and bismuth5. Kim et al. observed that these interactions caused a shift in the deposition potentials of barium ions into a liquid bismuth electrode (-3.74 V to -2.49 V vs. Cl–/Cl2(g)), resulting in a preferential deposition of barium from the electrolyte solution (BaCl2-LiCl-CaCl2-NaCl, 16-29-35-20 mol%) at 773 – 973 K6. This shift in deposition potential could be leveraged by using liquid metal electrodes to selectively separate alkali/alkaline-earth fission products from the electrolyte used for electrochemical processing of used nuclear fuel. To determine the viability of separating alkali/alkaline-earth fission products from molten salt electrolyte, the thermodynamic properties of these elements in the prospective liquid metals (e.g., Bi, Sb) must be determined.
In previous studies, Delcet et al. utilized coulometric titration to determine the thermodynamic properties of binary alloys (e.g., Ba-Bi, Ba-Sb, Ba-Pb)7. For Ba-Bi alloys up to xBa = 0.50, they employed coulometric titration using a single-crystal BaF2 electrolyte at 1,123 K and observed comparable activity values of barium in bismuth (2.4 x 10-12 at xBa(in Bi) = 0.05, 1,123 K). However, it was reported that the results were inaccurate due to the uncertainty regarding barium content in the binary alloys. Barium metal is highly reactive and soluble in its halide salts (~15 mol% in BaCl2 at 1,163 K), which can cause increased electronic conduction in the halide salt at higher temperatures and lead to inaccurate compositional accounting during coulometric titration. To determine the thermodynamic properties (e.g., excess partial molar Gibbs free energy, partial molar enthalpy, partial molar entropy) of binary alloys containing highly reactive elements, the emf method described in this protocol was used.
Thermochemical properties of binary alloys can be determined by measuring the equilibrium cell potential Ecell (i.e., emf) of an alloy (A-B) relative to the reference potential of the pure metal A. Then, the cell potential is directly related to the change in partial molar Gibbs free energy (or chemical potential) of the cell reaction according to the Nernst relation ().
For emf measurements of alkaline-earth alloys in this work, the fluoride-ion conducting CaF2 is chosen as the base electrolyte because the Ca2+/Ca redox potential (E0 = -5.59 V) is more negative than other alkaline-earth redox potentials (e.g., , versus F–/F2(g) at 873 K) in the fluoride system8. This implies that CaF2 is more chemically stable than the other alkaline-earth fluoride AF2 (A = Sr or Ba), and that Ba2+ or Sr2+ ions are the electroactive species in the CaF2-BaF2 and CaF2-SrF2 electrolyte, respectively. Utilizing the high stability of CaF2, which minimizes side reactions with Ba or Sr alloys as well as the ionic conductivity of CaF2 at elevated temperatures, the single-phase binary CaF2-AF2 electrolyte was successfully employed to accurately measure the emf of binary alkaline earth-liquid metal alloys. Confirmation of the formation of the single-phase binary electrolyte is confirmed with x-ray diffraction (XRD) analysis in Figure 19.
To measure the cell potential of an alkaline-earth alloy, the following electrochemical cell was implemented using a solid-state binary CaF2-AF2 (97 mol% CaF2, 3 mol% AF2) electrolyte10:
,
where the pure alkaline-earth metal A (A = Ca, Sr, or Ba) acts as the reference electrode (RE), solid CaF2-AF2 as the electrolyte, fixed composition A-B alloys as working electrodes (WE), and B is a candidate liquid metal such as Bi or Sb. The half-cell reactions in the electrochemical cell are:
and the overall cell reaction is:
where e– is an electron exchanged in the cell reactions and z is the number of electrons exchanged (z = 2 for alkaline-earth elements). For this overall reaction, the change in partial molar Gibbs free energy of the A metal, , is given by:
where is the partial molar Gibbs free energy of A metal in the metal B, is the standard Gibbs free energy of pure A metal, R is the ideal gas constant, T is the temperature in Kelvin, and aA is the activity of A in the metal B. The measured cell emf, Ecell, is directly related to the change in partial molar Gibbs free energy of A by the Nernst equation,
where F is the Faraday constant.
The emf cell in this work uses a CaF2-based solid electrolyte and electrode materials at fixed compositions, compared to an emf cell that uses a coulometric titration technique where the electrode composition is changed at a constant temperature. With coulometric titration, the electrode composition is determined by Faraday's law, assuming perfect coulombic efficiency. However, highly reactive alkaline-earth metals are moderately soluble (e.g., Ba ~15 mol% solubility in BaCl2) in their own halide salts, which can promote electronic conduction through the electrolyte and prevent accurate control of the composition of the electrode during coulometric titration7,13. The electrochemical cell in this work operates with electrode materials at fixed compositions, thus eliminating uncertainty in compositional accounting by coulometric titration, and enables accurate emf measurements of alkaline-earth alloys. Furthermore, the unique electrochemical cell in this work measures the emf values of four alloy compositions simultaneously within the same experiment to accelerate the evaluation of the thermodynamic properties over a wide range of compositions and temperatures.
As the arc-melter is used to fabricate the binary alloys, it is possible that the final composition of the alloys can deviate from the initial composition due to the high temperature of the electric arc and the high vapor pressures of the metals. To accurately report the emf-temperature relationship of the binary alloys, their composition was confirmed using inductively coupled plasma atomic emission spectroscopy (ICP-AES), as shown in Table 3 for the Ba-Sb system12.
Before drying the electrochemical cell components according to step 2.3.4, difficulties in obtaining high-quality vacuum (<10 mtorr) may occur. The o-ring in the vacuum chamber setup may not be seated correctly in its stainless-steel groove. There may also be a gap in the epoxy seals of the alumina tubes, to which additional epoxy may be applied to plug possible leaks. During emf measurements, if the electrical leads lose contact with the A-B alloys and large fluctuations in emf values are observed, contact may be re-established with the alloys by gently twisting the alumina tube, thereby wetting the liquid alloy to the lead.
Occasionally the emf values may exhibit a large hysteresis between the cooling and heating cycles. In general, a hysteresis of emf values between cooling/heating cycles may originate from (1) the degradation of electrolyte with reactive electrode compositions, especially at high alkaline-earth concentrations; (2) the degradation of electrode materials due to vaporization at elevated temperatures and oxidation with the residual oxygen inside the test chamber; or (3) non-equilibrium phase behavior of electrode materials, including undercooling effects and the formation of metastable phases during the cooling cycle.
When the degradation reaction between the electrode and the electrolyte is evident, the experimental set-up can be modified to mitigate the degradation of the electrochemical cell by decreasing the maximum operating temperature. In the presence of undercooling effects, emf values obtained during the heating cycle may be utilized in determining equilibrium thermodynamic properties. When the formation of metastable phases causes a hysteresis in emf measurements, the phase behavior of electrode materials requires scrutiny through complementary techniques, e.g., structural characterization by XRD, analysis of phase constituents by scanning electron microscopy (SEM) with energy-dispersive spectroscopy (EDS), and phase transition temperatures by DSC. Phase transition data may also be difficult to obtain with the described emf measurement technique above 1,223 K, as the CaF2-AF2 electrolyte may begin to degrade.
The emf measurement technique in this work can be used to determine the empirical thermodynamic properties of binary alkaline earth-liquid metal alloys, including activity, partial molar entropy, partial molar enthalpy, and phase transition temperatures. These thermodynamic data are utilized as an experimental basis for refining binary phase diagrams of alkaline-earth alloys with complementary techniques (XRD, DSC, and SEM), as exemplified in Figure 85. Based on the activity values of each alkaline-earth metal (A = Ca, Ba, and Sr) in liquid metals (B = Bi and Sb), the strength of atomic interactions between alkaline-earth elements and liquid metals can be leveraged to electrochemically separate out alkaline-earth fission products from molten salt solutions.
The authors have nothing to disclose.
This work was supported by the US Department of Energy, Office of Nuclear Energy's Nuclear Energy University Programs (Award No. DE-NE0008425); Integrated University Program Graduate Fellowship (Award No. DE-NE0000113); and the Ministry of Trade, Industry & Energy, Republic of Korea, the Energy Efficiency & Resources Core Technology Program of the Korea Institute of Energy Technology Evaluation and Planning (KETEP) (No. 20142020104190). Publication of this article was funded in part by The Pennsylvania State University Libraries Open Access Publishing Fund.
1 L bottle | US Plastic | 69032 | HDPE, wide mouth |
Acetone, 99.5% | Alfa Aesar | 30698 | ACS Grade |
Alumina dish | AdValue Technology | AL-4120 | 81 mm OD, 30 mm height |
Alumina plate | AdValue Technology | AL-D-82-6 | 10 cm in diameter, 4.65 mm thickness |
Alumina powder | AluChem | AC99 tabular alumina | |
Alumina tube | Coorstek | 66631-12.0000 | 0.25 in. OD, 12 in. length |
Arc-Melter | Edmund Buhler GmbH | MAM1 | |
Argon, 99.999% | Praxair | AR 5.0UH-K | Ultrahigh purity |
Ball mill | Norton Chemical Process Products Corporation | CF-70109 | 6 sets of 2 12.5 in. rollers, RPM 1725/1425 |
Barium | Alfa Aesar | 653 | 99.2% purity |
Barium fluoride | Sigma-Aldrich | 652458 | 99.999% purity |
Bismuth | Sigma-Aldrich | 556130 | 99.999% purity |
Boron nitride | Saint-Gobain | AX-05 | |
Calcium fluoride | Alfa Aesar | 11055 | 99.95% purity |
Cotton tip applicator | Dynarex | 4301 | 100 count, 3 in. long |
Die press | Carver, Inc. | 3850 | Clamping force: 12 tons; Platens: 6 x 6 in. |
Drill bit 29 piece set | Chicago-Latrobe | 45640 | 1/16 in. – 1/2 in. x 1/64 in. |
Drying pan | Pyrex | 5300114 | 15.5 in. x 9.5 in. x 2.25 in. |
Emery paper | McMaster-Carr | 4681A21 | Grit size: 100 |
Fiberglass insulation | McMaster-Carr | 9346K38 | |
Flowmeter | Brooks | MR3A00SVVT | Range: 0.1 to 1 standard cubic feet per hour (SCFH) of Air |
Gas bubbler | Ace Glass | 8761-10 | |
High temperature box furnace | Thermolyne | F48020-80 | 48000 Furnace, 8-segment program, Max. 1,200 °C |
High temperature crucible furnace | Mellen | CC12-6X12-1Z | 6 in. ID, 12 in. depth. Max temp 1,200 °C. 208 V |
High vacuum grease | Sigma-Aldrich | Z273554 | Brand: Dow Corning |
Inert atmopshere glovebox | Mbraun | MB200 | |
Isopropyl alcohol | Macron Chemicals | 3032-21 | ACS Grade |
Large pellet die set | MTI Corporation | EQ-Die-75D | |
Polyvinyl alcohol, 99+% | Sigma-Aldrich | 341584-5KG | Hydrolyzed, molecular weight (MW): 89,000-98,000 |
Potentiostat | Autolab | PGSTAT302N | |
Potentiostat-multiplexing switch box | Autolab | MUX SCANNER16 F/16 X WE | Multiplexer (MUX) SCANNER16 |
Potentiostat control software | NOVA | NOVA 1.11 | |
Precision mini lathe | Harbor Freight Tools | 93212 | Brand: Central Machinery |
Quick cure epoxy | Grainger | 5A462 | Brand: Devcon |
Recirculating chiller | VWR International | 13271-204 | Model: 1175PD |
Small pellet die set | MTI Corporation | EQ-Die-18D-B | |
Sonicator | VWR International | 97043-968 | |
Squeeze bottle | VWR International | 16650-022 | LDPE, 500 mL |
Stainless steel mesh sieve | Amazon | 10 mesh, 2 mm holes | |
Strontium | Sigma-Aldrich | 343730 | 99% purity |
Strontium fluoride | Sigma-Aldrich | 450030 | 99.99% purity |
Thermocouple | Omega | KMQXL-125U-18 | K-type thermocouple |
Thermocouple acquisiton board | National Instruments | NI-9211 | |
Tungsten wire | ThermoShield | 88007-0.100 | 99.95% wire |
Vacuum pump | Pfeiffer | PK D56 707 | Duo Line 1.6 |
Wipes | Kimtech | S-8115 | ULine distributor |
Wire cutters | McMaster-Carr | 5372A4 | |
Yttria-stabilized zirconia milling media | Tosoh, USA | 3 mm diameter |