Peculiarities of Holmium and Iron Triad Ions Co-Reduction: Formation of Ho x Ni y (Ho x Co y , Ho x Fe y ) Intermetallic Compounds in Chloride Melts

: The present paper is focused on the analysis of Ni 2+ , Co 2+ , Fe 3+ , and Ho 3+ ion co-reduction in the background equimolar NaCl-KCl melt at 973 K using the method of cyclic voltammetry. It was found that the co-reduction potentials of Ho 3+ and iron triad ions differ greatly. The depolarization of metallic holmium electrodeposition on one of the iron triad metals preliminary deposited on the tungsten electrode was determined. This process resulted in the formation of the Ho x Ni y , Ho x Co y , and Ho x Fe y intermetallic compounds. It was observed that the Ho x Ni y , Ho x Co y , and Ho x Fe y intermetallic compounds may be synthesized in a kinetic regime. The inﬂuence of the current density, electrolytic bath composition, and electrolysis time on the composition of the obtained intermetallic compounds was studied. The possibility of synthesizing cathode deposits composed solely of intermetallic compounds is veriﬁed. It is demonstrated that the intermetallic compounds may be formed by the addition of the iron triad metals (in particular, metallic iron) via anode dissolution. Synthesized Ho x Ni y , Ho x Co y , and Ho x Fe y samples were characterized by X-ray diffraction analysis


Introduction
In recent years, the development and improvement of the technologies used to obtain rare-earth metal (REM) alloys with iron triad metals have attracted increasing research interest.This is explained by the great number of unique physical-chemical properties of REM elements and their compounds, including high catalytic and sorption activity, superconductivity, effective magnetic characteristics, and increased heat resistance.
Thus, intermetallic compounds based on rare-earth and iron triad metals reveal wide perspectives for the creation of small-sized independent sources of a constant magnetic field.To date, such materials have demonstrated maximum magnetic characteristics among all known solid magnetic materials.Alloy coatings based on intermetallic compounds of Co REM increase the corrosion and heat resistance of cobalt items.Such materials may be used for the nodes of gas-turbine power units and aero engines [1][2][3].
Nowadays, the methods of thermal reduction of the stoichiometric oxide or halide mixtures of iron triad and REM by metallic calcium or calcium hydrate are mainly used to obtain materials based on REM and iron triad metals with various functional applications [4][5][6][7][8].At the same time, high-temperature synthesis in molten salts is highly promising for the production of compounds and materials based on refractory and REM intermetallic compounds [9,10].
Thus, the authors [11][12][13] obtained Ho and Ni intermetallic compounds (Ho 2 Ni 17 , HoNi 5 , HoNi 3 , HoNi 2 , HoNi) on a nickel cathode during electrolysis by diffusion saturation of the nickel substrate by metallic holmium.The authors [14,15] determined the free energies of the formation of the intermetallic Ho and Ni compounds, their diffusion coefficients, and holmium atoms' diffusion activation in the intermetallic phase.
The principal possibility of the electrochemical synthesis of Sa, La, Ho, Ce, Co, and Ni intermetallics was revealed in [16][17][18][19][20]. Later Su et al. [21] reported on the co-reduction of Dy 3+ and Al 3+ ions.Kushkhov et al. analyzed Dy 3+ and Nd 3+ ion co-reduction with Ni 2+ , Co 2+ , and Fe 3+ ions [22].The co-reduction of Ho 3+ and Al 3+ ions was studied in [23,24].The current achievements and perspectives of the electrochemical synthesis of intermetallic and refractory compounds based on refractory and rare-earth metals in chloride melts are revealed in [10,24].The presented data illustrates the possibilities and diversity of electrochemical synthesis.This method is increasingly frequently used in the development of functional and construction materials.
To synthesize electrochemically intermetallic compounds based on holmium and iron triad metals, data on the kinetics and mechanism of the electrode processes of their interaction in molten chloride media is required.However, there is a lack of literature data.Electroreduction of holmium ions in a eutectic KCl-LiCl melt was studied in [11][12][13].Bushuyev and Kondratyev et al. investigated holmium ion electroreduction in a KCl-NaCl melt [2,25].Several papers are devoted to the electroreduction of iron triad ions [22,[26][27][28][29]. Electroreduction of holmium and aluminum ions was analyzed in [23,24].However, the processes and mechanisms of co-reduction of holmium and iron triad ions require further study.
The present paper is aimed to study of the mechanism of co-reduction of nickel, cobalt, iron, and holmium in an equimolar KCl-NaCl melt.Using the obtained data on the co-reduction mechanism, highly dispersed powders of nickel, cobalt, iron, and holmium intermetallic compounds were electrochemically synthesized.

Experimental Section 2.1. Electrochemical Cell and Electrodes
Experiments were performed in a hermetically sealed three-electrode cell in a pure dry argon atmosphere.To eliminate any oxygen traces, zirconium wool was placed in the electrolytic cell as an oxygen getter.A glassy carbon crucible of 30 cm 3 in volume served as the anode and container for the melt.A chlorine-silver Ag|KCl-NaCl (1:1)-AgCl (2.5 mol.%) electrode served as the reference electrode.A tungsten wire (1.00 mm in diameter) served as the cathode and was covered by an alundum tube so that 40 mm of the wire remained open.The area of the working electrode was calculated according to the depth of immersion in the melt (10 ÷ 15 mm).
The cell was prepared and assembled in a glove box mBraun Labstar 25 in a pure argon atmosphere.To reach an operating temperature of 973 K, we used a shaft resistance furnace with silit rods as heating elements.The temperature was regulated automatically with an electron regulator OVEN-TRM-1 and a chromel-alumel thermocouple (the accuracy of the temperature regulation was ±1 • C).Cyclic voltammograms were recorded using an electrochemical complex Autolab PGSTAT 30 (Ecochemie, Utrecht, The Netherlands) equipped with IF-030 interphase.The voltammograms were processed using the program software GRES 4.9 (Ecochemie, Utrecht, The Netherlands).

Electrolyte Preparation
An equimolar KCl-NaCl melt was chosen as a background electrolyte.Individual KCl and NaCl salts were used for the electrolyte preparation.Before the experiment, the salts were dried in a vacuum chamber drier for 10 h and annealed in a muffle furnace for 5 h at 723 K. Commercial-grade NiCl 2 , CoCl 2 , FeCl 3 , and HoCl 3 salts were used as sources of iron triad and holmium ions.

Electroreduction of Ho 3+ Ions in the Equimolar KCl-NaCl Melt at 973 K
The cyclic voltammograms of the equimolar KCl-NaCl melt containing 1.0 mol.% of HoCl 3 illustrate a well-reproducible wave of holmium ion electroreduction in the region of potentials ranging from 1.8 to 2.0 V (Figure 1).
Germany) were used to determine the phase, elemental, and granulometric compositions of the obtained powder cathode deposits.

Electrolyte Preparation
An equimolar KCl-NaCl melt was chosen as a background electrolyte.Individual KCl and NaCl salts were used for the electrolyte preparation.Before the experiment, the salts were dried in a vacuum chamber drier for 10 h and annealed in a muffle furnace for 5 h at 723 K. Commercial-grade NiCl2, CoCl2, FeCl3, and HoCl3 salts were used as sources of iron triad and holmium ions.

Electroreduction of Ho 3+ Ions in the Equimolar KCl-NaCl Melt at 973 K
The cyclic voltammograms of the equimolar KCl-NaCl melt containing 1.0 mol.% of HоCl3 illustrate a well-reproducible wave of holmium ion electroreduction in the region of potentials ranging from 1.8 to 2.0 V (Figure 1).Electroreduction of holmium ions on the tungsten electrode in the molten KCl-NaCl mixture at 973 K was studied at different polarization rates ranging from 0.05 to 1.0 V/s (Figure 2).As the potential sweep increases, the wave corresponding to the Ho 3+ reduction shifts to the negative region and the height of the wave increases.A clearly observed cathode peak was not detected on the cyclic voltammograms.This is obviously explained by the significantly negative region of the Ho 3+ reduction potentials, which are close to the potentials of the background electrolyte decomposition.Electroreduction of holmium ions on the tungsten electrode in the molten KCl-NaCl mixture at 973 K was studied at different polarization rates ranging from 0.05 to 1.0 V/s (Figure 2).As the potential sweep increases, the wave corresponding to the Ho 3+ reduction shifts to the negative region and the height of the wave increases.A clearly observed cathode peak was not detected on the cyclic voltammograms.This is obviously explained by the significantly negative region of the Ho 3+ reduction potentials, which are close to the potentials of the background electrolyte decomposition.
At different potential sweep rates, one wave of holmium ion electroreduction and one wave of cathode product oxidation were observed on the cathode and anode branches.
To determine the mechanism and character of the electroreduction of holmium ions in the KCl-NaCl-HoCl 3 melt, the voltammetry dependencies were analyzed using the diagnostic criteria.We calculated the density of the current peak and determined the potentials of the peaks and half-peaks and the values of the peak half-width at different HoCl 3 concentrations and potential sweep rates.The numerical values of these parameters are presented in Table 1.At different potential sweep rates, one wave of holmium ion electroreduction and one wave of cathode product oxidation were observed on the cathode and anode branches.
To determine the mechanism and character of the electroreduction of holmium ions in the KCl-NaCl-HоCl3 melt, the voltammetry dependencies were analyzed using the diagnostic criteria.We calculated the density of the current peak and determined the potentials of the peaks and half-peaks and the values of the peak half-width at different HоCl3 concentrations and potential sweep rates.The numerical values of these parameters are presented in Table 1.
Table 1.Parameters of HоCl3 electroreduction in the KCl-NaCl melt on the tungsten electrode at T = 973 K.

V, V/s
Ip, A/cm 2 Ip/V  Table 1.Parameters of HoCl 3 electroreduction in the KCl-NaCl melt on the tungsten electrode at T = 973 K.
V, V/s I p , A/cm 2 I p /V Therefore, considering the structure of the chloride melts containing holmium ions [25], it was found that Ho 3+ ions exist in the form of HoCl 6 3− chloride complexes; a reversible three-electrode reaction of the electrochemical cathode reduction has the following form: 3.2.Co-Reduction of Ho 3+ and Ni 2+ Ions in the KCl-NaCl Equimolar Melt at 973 K There is data on the formation of a number of Ho x Ni y compounds in the Ho-Ni system: HoNi, HoNi 2 , HoNi 3 , HoNi 5 , Ho 3 Ni, and Ho 2 Ni 7 [30].
To determine the possibility of the electrochemical synthesis of these intermetallic compounds, we studied the processes of holmium and nickel ion co-reduction in the equimolar KCl-NaCl melt.
Figure 3 illustrates the cyclic voltammograms recorded on the tungsten electrode in the equimolar KCl-NaCl melt containing HoCl 3 and NiCl2 at 973 K and at different reverse potentials, corresponding both to the potential of nickel electrodeposition −(0.1-0.2) V and to the potential of holmium electrodeposition −(1.8-2.0)V relative to the chlorine-silver reference electrode.For the experiments on the nickel and holmium ion co-reduction in the molten KCl-NaCl mixture, the NiCl 2 concentration (0.25 mol.%) added to the melt was less than the HoCl 3 concentration (1.5 mol.%).This is why the electrochemical reduction current of the Ni 2+ ions in the KCl-NaCl-HoCl 3 -NiCl 2 melt is smaller than that of the Ho 3+ ion reduction.Figure 4 illustrates that the increase in the polarization rate from 0.05 to 1.0 V/s results in an increase in the height of the electroreduction waves.In addition, the cathode wave shifts to the region of negative potentials and the anode wave shifts to the region of positive values.The cathode branch of the cyclic voltammogram (Figure 3, curve 4) has five reduction waves.The appearance of wave A is associated with the reduction of Ni 2+ ions, which is in good agreement with the data reported in [22].Waves B, C, and D correspond to the coreduction of Ho 3+ and Ni 2+ ions on metallic nickel, which was preliminary extracted with a definite depolarization on the tungsten electrode.Wave E is associated with the reduction of Ho 3+ ions in the Ho x Ni y intermetallic phase.The anode branch of the cyclic voltammogram also has five waves of the cathode branch oxidation.The correspondence between the cathode reduction waves and anode waves of the cathode product electrooxidation is proved by the voltammetry curves recorded before different reverse potentials, which are associated with the termination of each phase of the cathode reduction wave (Figure 3).It is observed that the reduction waves that were observed on the voltammograms at different potentials correspond to the processes of intermetallic compound formation.The phases with the largest holmium concentrations correspond to the reduction waves at the most negative potentials.Apart from this, the potentials of nickel and holmium deposition on the tungsten electrode coated with the preliminary deposited nickel differ by more than 1.0 V.This is why electrolysis of the intermetallic compounds based on holmium and nickel is possible only in the kinetic regime [9].
Electrochemical synthesis of holmium and nickel intermetallic compounds was performed in the KCl-NaCl-HoCl3-NiCl2 melt under a galvanostatic regime.The electrolysis was carried out in a high-temperature quartz cell in an argon atmosphere at 973 K.A highpurity tungsten rod of 3 mm in diameter served as the cathode.A glassy carbon crucible was used as the anode and as a container for the melt.
During the electrolysis of the molten KCl-NaCl mixture containing holmium trichloride (0.5 ÷ 2.5 mol.%) and nickel dichloride (0.1 ÷ 2.5 mol.%), a metal-salt "pear-shaped" object formed on the tungsten electrode at the current density of 0.5 ÷ 2.0 A/cm 2 .The end product in the majority of cases fell from the tungsten cathode onto the alundum support located at the bottom of the crucible.
After multiple rinses in distilled water, the deposit was dried in a vacuum drier at temperatures of 373-423 K.The phase composition of the cathode deposit is illustrated in Figure 5 and Table 2.The ratio of the metallic nickel and intermetallic HoNi, HoNi5, and HoNi3 phases depends on the composition of the electrolysis bath and the electrolysis parameters.It is observed that the reduction waves that were observed on the voltammograms at different potentials correspond to the processes of intermetallic compound formation.The phases with the largest holmium concentrations correspond to the reduction waves at the most negative potentials.Apart from this, the potentials of nickel and holmium deposition on the tungsten electrode coated with the preliminary deposited nickel differ by more than 1.0 V.This is why electrolysis of the intermetallic compounds based on holmium and nickel is possible only in the kinetic regime [9].
Electrochemical synthesis of holmium and nickel intermetallic compounds was performed in the KCl-NaCl-HoCl 3 -NiCl 2 melt under a galvanostatic regime.The electrolysis was carried out in a high-temperature quartz cell in an argon atmosphere at 973 K.A high-purity tungsten rod of 3 mm in diameter served as the cathode.A glassy carbon crucible was used as the anode and as a container for the melt.
During the electrolysis of the molten KCl-NaCl mixture containing holmium trichloride (0.5 ÷ 2.5 mol.%) and nickel dichloride (0.1 ÷ 2.5 mol.%), a metal-salt "pear-shaped" object formed on the tungsten electrode at the current density of 0.5 ÷ 2.0 A/cm 2 .The end product in the majority of cases fell from the tungsten cathode onto the alundum support located at the bottom of the crucible.
After multiple rinses in distilled water, the deposit was dried in a vacuum drier at temperatures of 373-423 K.The phase composition of the cathode deposit is illustrated in Figure 5 and Table 2.The ratio of the metallic nickel and intermetallic HoNi, HoNi 5 , and HoNi 3 phases depends on the composition of the electrolysis bath and the electrolysis parameters.To determine the optimal concentrations of HoCl3 and NiCl2, we need to consider that during the first synthesis stage, the most electropositive component, i.e., nickel, is deposited.The electroreduction of holmium ions starts when nickel chloride is nearly consumed.The optimal concentration of nickel chloride is about 0.5 mol.%.At higher concentrations of nickel chloride, the deposit contains metallic nickel.The dependence of the cathode deposit composition on the nickel and holmium chloride concentrations and their ratio in the KCl-NaCl (1:1) melt were studied (Table 2).
Table 2. Dependence of the phase composition and particle size of the deposits obtained by galvanostatic electrolysis on the composition of the KCl-NaCl-HoCl3-NiCl2 electrolysis bath.Electrolysis duration was 60 min; T = 973 K; S = 2.43 cm 2 ; i = 1.2 A/cm 2 .The concentration of the intermetallic compounds increases both as the concentration of holmium chloride in the melt increases and as the concentration ratio of the holmium and nickel chlorides increases.The metallic nickel phase prevails in the cathode deposit when the concentration ratio is [HoCl3]:[NiCl2] = 1:1.As the ratio increases, the fraction of the metallic nickel decreases and the concentration of the intermetallic HoNi, HoNi3, and HoNi5 compounds increases.When [HoCl3]:[NiCl2] = 5:1, the metallic nickel phase is not detected in the cathode deposit.The mixture of intermetallic phases with a large holmium concentration is formed.To determine the optimal concentrations of HoCl 3 and NiCl 2 , we need to consider that during the first synthesis stage, the most electropositive component, i.e., nickel, is deposited.The electroreduction of holmium ions starts when nickel chloride is nearly consumed.The optimal concentration of nickel chloride is about 0.5 mol.%.At higher concentrations of nickel chloride, the deposit contains metallic nickel.The dependence of the cathode deposit composition on the nickel and holmium chloride concentrations and their ratio in the KCl-NaCl (1:1) melt were studied (Table 2).

No
The concentration of the intermetallic compounds increases both as the concentration of holmium chloride in the melt increases and as the concentration ratio of the holmium and nickel chlorides increases.The metallic nickel phase prevails in the cathode deposit when the concentration ratio is [HoCl 3 ]:[NiCl 2 ] = 1:1.As the ratio increases, the fraction of the metallic nickel decreases and the concentration of the intermetallic HoNi, HoNi 3 , and HoNi 5 compounds increases.When [HoCl 3 ]:[NiCl 2 ] = 5:1, the metallic nickel phase is not detected in the cathode deposit.The mixture of intermetallic phases with a large holmium concentration is formed.
Color mapping of the studied intermetallic samples' surfaces according to the X-ray spectra illustrates the distribution of intermetallic compounds (Figure 6a).Simultaneously, we obtained the information on the qualitative and quantitative elemental analysis (Figure 6b).Color mapping of the studied intermetallic samples' surfaces according to the X-ray spectra illustrates the distribution of intermetallic compounds (Figure 6a).Simultaneously, we obtained the information on the qualitative and quantitative elemental analysis (Figure 6b).

Co-Reduction of Ho 3+ and Co 2+ Ions in the Equimolar KCl-NaCl Melt at 973 K
The equilibrium diagram of Ho 3+ and Ni 2+ ions was studied over the whole concentration range [30].
The formation of eight compounds was determined in the Ho-Co system.Three compounds Co Ho (1370 ℃), Co Ho (1390 ℃), and Co Ho (795 ℃) form in the melt, and four compounds form according to the peritektic reactions [30]: Ж + Co Ho ⇆ Co Ho at 1365 ℃ Ж + Co Ho ⇆ Co Ho Ho at 1330 ℃ Ж + Ho ⇆ CoHo Ho at 895 ℃ The Co .compound exists in a narrow temperature interval of 1355-1150 ℃.The phase Co Ho is formed according to the peritektic reaction [30]: The mutual solubility of components in a solid state is nearly absent.Four eutectics crystallize in the system: Co Ho + Co Ho at 755 ℃ Co Ho + Co .Ho at 1340 ℃ Co Ho + (Co) at 1345 ℃ (10) Figure 7 illustrates the cyclic voltammograms of the equimolar KCl-NaCl melt containing cobalt chloride (0.25 mol.%) and holmium chloride (1.0 mol.%).As the polarization rate increases from 0.05 to 1.0 V/s, the reduction waves grow.The cathode wave shifts to the region of negative values of the potential and the anode wave shifts to the region of positive values.The cathode branch of the voltammogram has four waves of electroreduction: wave A corresponds to the electroreduction of Co 2+ ions and waves B and C  A distinctive feature of the holmium trichloride reduction wave is that when cobalt chloride is present in the melt, holmium is deposited on the tungsten electrode coated with metallic cobalt.Due to this, the holmium ion reduction wave becomes more prolonged along the axis of potentials and shifts to the region of more positive potentials (Figure 7).The observed depolarization of holmium deposition is associated with the formation of holmium and cobalt intermetallic compounds.The voltammetry measurements illustrate that the potentials of cobalt and holmium extraction on the tungsten electrode coated by the preliminary extracted cobalt differ by more than 1.0 V.This is why the electrolysis of the intermetallic compounds based on holmium and cobalt is possible only under a kinetic regime.In addition, the concentration of cobalt ions should not be excessively large, because at high values of the limiting current of the more electropositive component, i.e., cobalt, the electrochemical reduction current of holmium cannot be achieved.
Electrochemical synthesis of holmium and cobalt intermetallics was performed under a galvanostatic regime in the KCl-NaCl-HoCl3-CоCl2 melt.The X-ray pattern of the cathode deposit and crystallographic parameters of the obtained phases are presented in Figure 8. Depending on the composition of the electrolysis bath and electrolysis parameters, the mixture of the metallic cobalt and intermetallic HоCо2, HoCо3, HoCо5, and Ho2Cо17 phases was obtained.A distinctive feature of the holmium trichloride reduction wave is that when cobalt chloride is present in the melt, holmium is deposited on the tungsten electrode coated with metallic cobalt.Due to this, the holmium ion reduction wave becomes more prolonged along the axis of potentials and shifts to the region of more positive potentials (Figure 7).The observed depolarization of holmium deposition is associated with the formation of holmium and cobalt intermetallic compounds.The voltammetry measurements illustrate that the potentials of cobalt and holmium extraction on the tungsten electrode coated by the preliminary extracted cobalt differ by more than 1.0 V.This is why the electrolysis of the intermetallic compounds based on holmium and cobalt is possible only under a kinetic regime.In addition, the concentration of cobalt ions should not be excessively large, because at high values of the limiting current of the more electropositive component, i.e., cobalt, the electrochemical reduction current of holmium cannot be achieved.
Electrochemical synthesis of holmium and cobalt intermetallics was performed under a galvanostatic regime in the KCl-NaCl-HoCl 3 -CoCl 2 melt.The X-ray pattern of the cathode deposit and crystallographic parameters of the obtained phases are presented in Figure 8. Depending on the composition of the electrolysis bath and electrolysis parameters, the mixture of the metallic cobalt and intermetallic HoCo 2 , HoCo 3 , HoCo 5 , and Ho 2 Co 17 phases was obtained.To determine the optimum concentrations of HoCl3 and CоCl2, we need to consider that cobalt, being the most electropositive component, is deposited during the first stage of synthesis.The electroreduction of holmium ions starts when cobalt chloride is nearly consumed.The optimum concentration of cobalt chloride is about 0.5 mol.%.At the higher concentrations of cobalt chloride, the deposit contains metallic cobalt.The dependence of the cathode deposit composition on the HoCl3 and CоCl2 concentrations and their ratio in the KCl-NaCl (1:1) melt is presented in Table 3.
Table 3. Dependence of the phase composition and particle size of the deposit obtained by galvanostatic electrolysis on the composition of the KCl-NaCl-HoCl3-CоCl2 electrolysis bath.The electrolysis duration was 60 min; T = 973 K; S = 1.48 cm 2 ; i = 1.2 A/cm 2 .To determine the optimum concentrations of HoCl 3 and CoCl 2 , we need to consider that cobalt, being the most electropositive component, is deposited during the first stage of synthesis.The electroreduction of holmium ions starts when cobalt chloride is nearly consumed.The optimum concentration of cobalt chloride is about 0.5 mol.%.At the higher concentrations of cobalt chloride, the deposit contains metallic cobalt.The dependence of the cathode deposit composition on the HoCl 3 and CoCl 2 concentrations and their ratio in the KCl-NaCl (1:1) melt is presented in Table 3.

No. C (CоCl2
Table 3. Dependence of the phase composition and particle size of the deposit obtained by galvanostatic electrolysis on the composition of the KCl-NaCl-HoCl 3 -CoCl 2 electrolysis bath.The electrolysis duration was 60 min; T = 973 K; S = 1.48 cm 2 ; i = 1.2 A/cm 2 .The structure, morphology, and elemental composition of the obtained samples were quantitatively and qualitatively studied using a scanning emission electron microscope VEGA3 LMH.The obtained images testify that the electrolytic co-reduction of holmium and cobalt and electrochemical synthesis of Ho x Co y intermetallic compounds are possible (Figures 8 and 9).The structure, morphology, and elemental composition of the obtained samples were quantitatively and qualitatively studied using a scanning emission electron microscope VEGA3 LMH.The obtained images testify that the electrolytic co-reduction of holmium and cobalt and electrochemical synthesis of HoxCoy intermetallic compounds are possible (Figures 8 and 9).3+ and Fe 3+ Ions in the Equimolar KCl-NaCl Melt at 973 K Alloys of the Fe-Ho systems were studied in detail in [31].The equilibrium diagrams of the Fe-Ho system are provided in [32].In addition, according to [30], the assumption regarding the polymorphic transformation of Ho and the associated reactions should not be considered.

Electrolytic Co-Reduction of Ho
Four compounds are formed in the Fe-Ho system [30].Two compounds, Fe Ho and Fe Ho , are formed in the melt on the peaks of the phase diagram of the Fe-Ho system at 1343 and 1332 ℃, respectively [30].Another two compounds, Fe Ho and Fe Ho, are formed according to the peritectic reactions: Ж + Fe Ho⇆Fe Ho (1288 ℃) However, (γFe)+ Fe Ho , Fe Ho +Fe Ho , and Fe Ho+(Ho) eutectics were found to crystallize at the Fe (9.18 at.%) and Ho (63.4 at.%) concentrations and temperatures of  3+ and Fe 3+ Ions in the Equimolar KCl-NaCl Melt at 973 K Alloys of the Fe-Ho systems were studied in detail in [31].The equilibrium diagrams of the Fe-Ho system are provided in [32].In addition, according to [30], the assumption regarding the polymorphic transformation of Ho and the associated reactions should not be considered.

Electrolytic Co-Reduction of Ho
Four compounds are formed in the Fe-Ho system [30].Two compounds, Fe 17 Ho 2 and Fe 23 Ho 6 , are formed in the melt on the peaks of the phase diagram of the Fe-Ho system at 1343 and 1332 • C, respectively [30].Another two compounds, Fe 3 Ho and Fe 2 Ho, are formed according to the peritectic reactions: Ж + Fe 3 Ho Fe 2 Ho (1288 However, (γFe)+ Fe 17 Ho 2 , Fe 17 Ho 2 +Fe 23 Ho 6 , and Fe 2 Ho+(Ho) eutectics were found to crystallize at the Fe (9.18 at.%) and Ho (63.4 at.%) concentrations and temperatures of 1338, 1285, and 875 • C, respectively.The mutual solubility of the components is almost absent.
To determine the conditions of the electrolytic co-reduction of holmium and iron, we performed voltammetry measurements in the equimolar KCl-NaCl melt containing iron and holmium trichlorides.
The cathode branch of the cyclic voltammogram (Figure 10) at the potentials −(0.5 ÷ 0.6) V has a wave of Fe 3+ iron ion reduction.In the region of potentials −(1.6 ÷ 1.8) V, wave B is observed.The appearance of wave B is associated with the co-reduction of Ho 3+ and Fe 3+ ions on metallic iron preliminary deposited with a definite depolarization on the tungsten electrode and with the formation of Ho x Fe y intermetallic compounds.
Processes 2022, 10, x FOR PEER REVIEW 13 of 18 To determine the conditions of the electrolytic co-reduction of holmium and iron, we performed voltammetry measurements in the equimolar KCl-NaCl melt containing iron and holmium trichlorides.
The cathode branch of the cyclic voltammogram (Figure 10) at the potentials −(0.5 ÷ 0.6) V has a wave of Fe 3+ iron ion reduction.In the region of potentials −(1.6 ÷ 1.8) V, wave B is observed.The appearance of wave B is associated with the co-reduction of Ho 3+ and Fe 3+ ions on metallic iron preliminary deposited with a definite depolarization on the tungsten electrode and with the formation of HoxFey intermetallic compounds.
Unlike electrolytic co-reduction of Ho 3+ ions with Ni 2+ and Co 2+ , in the case of Ho 3+ and Fe 3+ ion co-reduction, the waves corresponding to the electroreduction of holmium and iron intermetallic compounds of various compositions are not observed on the cathode branch of the cyclic voltammogram.This is likely explained by the smaller value of the free energy of the formation of HoxFey intermetallic compounds as opposed to those of HoxNiy and HoxCoy intermetallic compounds.The values of the free energy of the formation of different phases of HoxFey intermetallic compounds also differ slightly.This is verified by the prolonged anode wave of the cathode product oxidation, having a tendency to duplicate along the axis of potential (Figure 11).Unlike electrolytic co-reduction of Ho 3+ ions with Ni 2+ and Co 2+ , in the case of Ho 3+ and Fe 3+ ion co-reduction, the waves corresponding to the electroreduction of holmium and iron intermetallic compounds of various compositions are not observed on the cathode branch of the cyclic voltammogram.This is likely explained by the smaller value of the free energy of the formation of Ho x Fe y intermetallic compounds as opposed to those of Ho x Ni y and Ho x Co y intermetallic compounds.The values of the free energy of the formation of different phases of Ho x Fe y intermetallic compounds also differ slightly.This is verified by the prolonged anode wave of the cathode product oxidation, having a tendency to duplicate along the axis of potential (Figure 11).High-temperature electrochemical synthesis of holmium and iron intermetallic compounds was performed in the KCl-NaCl-HoCl3 melt with holmium chloride concentrations of 0.5 ÷ 2.5 mol.%.An iron plate simultaneously served as an anode and the source of iron ions.The initial cathode current density ranged within the interval of 3.0-4.0A/cm 2 .The real value of the current density during galvanostatic electrolysis is known only during the initial time period because the cathode area changes significantly during the electrolysis.However, we can clearly state that as the current density increases, the powder size increases.The electrolysis was performed for 60 min at 973 K.
To separate the end product of the reaction from the salt phase, cathode deposit leaching in hot distilled water and magnet treating were applied.The obtained pure holmium and iron intermetallic powders were characterized using X-ray diffraction and Xray fluorescence methods.The results of the X-ray diffraction analysis are presented in Figure 12. Figure 11 illustrates that the waves grow as the polarization rate increases from 0.05 to 1.0 V/s.The cathode wave shifts to the region of negative values of the potential and the anode wave shifts to the region of positive potentials.
High-temperature electrochemical synthesis of holmium and iron intermetallic compounds was performed in the KCl-NaCl-HoCl 3 melt with holmium chloride concentrations of 0.5 ÷ 2.5 mol.%.An iron plate simultaneously served as an anode and the source of iron ions.The initial cathode current density ranged within the interval of 3.0-4.0A/cm 2 .The real value of the current density during galvanostatic electrolysis is known only during the initial time period because the cathode area changes significantly during the electrolysis.However, we can clearly state that as the current density increases, the powder size increases.The electrolysis was performed for 60 min at 973 K.
To separate the end product of the reaction from the salt phase, cathode deposit leaching in hot distilled water and magnet treating were applied.The obtained pure holmium and iron intermetallic powders were characterized using X-ray diffraction and X-ray fluorescence methods.The results of the X-ray diffraction analysis are presented in Figure 12.
The structure, morphology, and elemental composition of the obtained samples were qualitatively and quantitatively studied using an electron scanning microscope VEGA3 LMH.The images illustrated in Figure 13 testify the presence of the holmium and iron co-reduction.
The greater iron concentration in the samples results in greater assimilation of the cathode deposits to the structure of metallic iron and in a greater particle size, caused by the formation of dendrites (Figure 14).The structure, morphology, and elemental composition of the obtained samples were qualitatively and quantitatively studied using an electron scanning microscope VEGA3 LMH.The images illustrated in Figure 13 testify the presence of the holmium and iron coreduction.The structure, morphology, and elemental composition of the obtained samples were qualitatively and quantitatively studied using an electron scanning microscope VEGA3 LMH.The images illustrated in Figure 13 testify the presence of the holmium and iron coreduction.The greater iron concentration in the samples results in greater assimilation of the cathode deposits to the structure of metallic iron and in a greater particle size, caused by the formation of dendrites (Figure 14).

Conclusions
Based on the voltammetry studies of the Ni 2+ , Co 2+ , Fe 3+ , and Ho 3+ ion co-reduction in the equimolar melt of potassium and sodium chlorides at 973 K, it was shown that electrochemical synthesis of holmium with iron triad metals may be performed under a kinetic regime.The activity of the iron triad metals during the interaction with metallic holmium that resulted in the intermetallic compound formation was found to decrease in a row as follows: nickel-cobalt-iron, where nickel was the most active metal.
It is demonstrated that depending on the electrolysis regime, potentiostatic or galvanostatic, the process of electrochemical synthesis has the following parameters.The metallic phases of nickel, cobalt, and iron are deposited on the cathode during galvanostatic electrolysis at current densities that do not exceed the limiting diffusion current densities of the Ni 2+ , Co 2+ , and Fe 3+ ion reduction or during the potentiostatic electrolysis performed at potentials that do not exceed the limiting current densities of the Ni 2+ , Co 2+ , and Fe 3+ ion electroreduction.Intermetallic nickel, cobalt, iron, and holmium phases form during potentiostatic electrolysis together with the phases of metallic nickel, cobalt, and iron at cathode current densities that exceed the limiting diffusion current densities of Ni 2+ , Co 2+ , and Fe 3+ ion reduction at the potentials of the corresponding cyclic voltammetry waves.At a constant concentration of the holmium and iron triad chlorides in the equimolar KCl-NaCl melt, the higher cathode current densities and more negative electrolysis potentials result in a decrease in the concentration of the metallic phase in the cathode deposit and in an increase in the concentrations of both the holmium intermetallic phases and intermetallic phases with a high holmium concentration.Therefore, we state that the process of electrochemical synthesis of nickel, cobalt, iron, and holmium intermetallic compounds under a kinetic regime is determined by the following interconnected parameters: the composition of the electrolysis bath (concentrations of iron triad metal chlorides and holmium trichloride and their ratio), cathode current density, electrolysis potential (bath voltage), and electrolysis duration.

Conclusions
Based on the voltammetry studies of the Ni 2+ , Co 2+ , Fe 3+ , and Ho 3+ ion co-reduction in the equimolar melt of potassium and sodium chlorides at 973 K, it was shown that electrochemical synthesis of holmium with iron triad metals may be performed under a kinetic regime.The activity of the iron triad metals during the interaction with metallic holmium that resulted in the intermetallic compound formation was found to decrease in a row as follows: nickel-cobalt-iron, where nickel was the most active metal.
It is demonstrated that depending on the electrolysis regime, potentiostatic or galvanostatic, the process of electrochemical synthesis has the following parameters.The metallic phases of nickel, cobalt, and iron are deposited on the cathode during galvanostatic electrolysis at current densities that do not exceed the limiting diffusion current densities of the Ni 2+ , Co 2+ , and Fe 3+ ion reduction or during the potentiostatic electrolysis performed at potentials that do not exceed the limiting current densities of the Ni 2+ , Co 2+ , and Fe 3+ ion electroreduction.Intermetallic nickel, cobalt, iron, and holmium phases form during potentiostatic electrolysis together with the phases of metallic nickel, cobalt, and iron at cathode current densities that exceed the limiting diffusion current densities of Ni 2+ , Co 2+ , and Fe 3+ ion reduction at the potentials of the corresponding cyclic voltammetry waves.At a constant concentration of the holmium and iron triad chlorides in the equimolar KCl-NaCl melt, the higher cathode current densities and more negative electrolysis potentials result in a decrease in the concentration of the metallic phase in the cathode deposit and in an increase in the concentrations of both the holmium intermetallic phases and intermetallic phases with a high holmium concentration.Therefore, we state that the process of electrochemical synthesis of nickel, cobalt, iron, and holmium intermetallic compounds under a kinetic regime is determined by the following interconnected parameters: the composition of the electrolysis bath (concentrations of iron triad metal chlorides and holmium trichloride and their ratio), cathode current density, electrolysis potential (bath voltage), and electrolysis duration.

Figure 4 18 Figure 4 .
Figure4illustrates that the increase in the polarization rate from 0.05 to 1.0 V/s results in an increase in the height of the electroreduction waves.In addition, the cathode wave shifts to the region of negative potentials and the anode wave shifts to the region of positive values.Processes 2022, 10, x FOR PEER REVIEW 7 of 18

Figure 6 .
Figure 6.(a) Color map of the elemental distribution at the surface of the sample containing holmium and nickel intermetallics; (b) elemental analysis of the sample obtained by galvanostatic electrolysis of the equimolar KCl-NaCl melt containing HoCl3 = 2.5 mol.% and NiCl2 = 0.5 mol.% on the tungsten electrode.ik = 1.2 A/cm 2 .T = 973 K. S = 2.43 cm 2 .

Figure 8 .
Figure 8. X-ray pattern of the deposit obtained on the tungsten cathode by galvanostatic electrolysis of the equimolar KCl-NaCl melt containing 2.0 mol.%HoCl3 and 0.5 mol.%CоCl2.Crystallographic parameters of the obtained phases.

Figure 8 .
Figure 8. X-ray pattern of the deposit obtained on the tungsten cathode by galvanostatic electrolysis of the equimolar KCl-NaCl melt containing 2.0 mol.%HoCl 3 and 0.5 mol.%CoCl 2 .Crystallographic parameters of the obtained phases.

Figure 11
Figure 11 illustrates that the waves grow as the polarization rate increases from 0.05 to 1.0 V/s.The cathode wave shifts to the region of negative values of the potential and the anode wave shifts to the region of positive potentials.