Trans. Nonferrous Met. Soc. China 31(2021) 2522-2531

Physicochemical properties of DMI-LiNO₃ solvated ionic liquid and its application in electrodeposition of neodymium at room temperature

Ai-min LIU¹, Yu YAO¹, Meng-xia GUO¹, Yu-bao LIU², Zhong-ning SHI³, Feng-guo LIU¹, Xian-wei HU¹, Wen-cai HE¹, Zhao-wen WANG¹

1. Key Laboratory for Ecological Metallurgy of Multimetallic Mineral (Ministry of Education), Northeastern University, Shenyang 110819, China;

2. State Key Laboratory of Baiyunobo Rare Earth Resource Researches and Comprehensive Utilization, Baotou Research Institute of Rare Earths, Baotou 014030, China;

3. State Key Laboratory of Rolling and Automation, Northeastern University, Shenyang 110819, China

Received 24 July 2020; accepted 14 January 2021

Abstract: The density, conductivity, and viscosity of the 1,3-dimethyl-2-imidazolinone and lithium nitrate (DMI- LiNO₃) solvated ionic liquid were measured as a function of temperature. Additionally, the electrochemical mechanism and electrodeposition of neodymium from the DMI-LiNO₃ solvated ionic liquid were investigated. Cyclic voltammetry results indicate that the electrochemical reduction of Nd(III) is irreversible and proceeds via one-step with three-electron transfer, which is controlled by diffusion with a diffusion coefficient of 5.08×10^-8 cm²/s. Energy- dispersive X-ray spectrometry and X-ray photoelectron spectroscopy data confirm that the electrodeposit obtained after electrodeposition at -4 V (vs Ag) using the DMI-LiNO₃-Nd(CF₃SO₃)₃ solvated ionic liquid contains metallic neodymium.

Key words: electrodeposition; neodymium; ionic liquid; physicochemical properties; cyclic voltammetry

1 Introduction

Rare earth (RE) elements are known as industrial vitamins and “mother of new materials” because of their outstanding optical and electro- magnetic properties [1-3]. As the additive, RE elements can significantly improve the qualities and performances of materials with a wide range of properties [4]. Therefore, RE metals have been widely used in fields such as metallurgy, machinery, petrochemical industry, and aerospace. Currently, molten salt electrolysis in LiF-REF₃-RE₂O₃ electrolytes at 1273-1373 K has been applied for RE metal production in the industry, but it is limited by the high electrolysis temperature and low energy efficiency [5,6]. Therefore, identifying a suitable electrolyte from which RE metals can be produced at low temperatures or room temperature is desirable.

Ionic liquids have the advantages such as low melting points, wide electrochemical window, good thermal stabilities, and high electrical conductivities. Thus, the application of ionic liquids for the electrodeposition of RE metals (particularly La and Nd) has been extensively studied. For example, TSUDA et al [7] found that the solubility of LaCl₃ increased with an increase in the acidity of aluminum chloride-1-ethyl-3-methylimidazolium chloride (AlCl₃-EMICl) ionic liquid, and metallic La was electrodeposited at -1.95 V (vs Al) with LiCl and SOCl₂ as additives. LEGEAI et al [8] reported that the electrochemical window of the 1-octyl-1-methyl-pyrrolidinium bis(trifluoro methyl- sulfonyl)imide (OMPTf₂N) ionic liquid was 4.8 V (vs Ag/AgCl), and a La film with 350 nm-thickness was formed by electrodeposition method at -1.5 V (vs Ag/AgCl) for 2 h. KIM et al [9] investigated  the electrochemical behavior of La(III) in 1-ethyl- 3-methyl-imidazolium tetrafluoroborate ([EMIM]-[BF₄]) ionic liquid with 0.1 mol/L LiCl as an additive, and the results suggested that the reduction of La(III) was an irreversible one-step process controlled by the diffusion with a diffusion coefficient of (1.07-1.19)×10^-6 cm²/s.

KONDO et al [10] studied the electrochemical behavior of Nd(III) in triethyl-pentyl-phosphonium bis(trifluoromethyl-sulfonyl)amide ([P₂₂₂₅][TFSA]) ionic liquid, and the diffusion coefficient of Nd(III) at 373 K was of the order of 10^-7 cm²/s. Fine and uniform Nd particles were electrodeposited on a copper substrate at -1.95 V (vs Pt) and identified by X-ray photoelectron spectroscopy (XPS). OTA et al [11] investigated the electrochemical behavior of Nd(III) in [P₂₂₂₅][TFSA] using cyclic voltam- metry and electrochemical quartz crystal microbalance (EQCM). A clear cathode peak was observed at -2.79 V (vs Pt) with a mass change of 140.4 g/mol, which was close to the theoretical value (144.2 g/mol) for the electrochemical reaction [Nd(TFSA)₅]^2-+3e→Nd+5[TFSA]^-. In addition, metallic Nd could be electrochemically recovered from the waste of Nd-Fe-B magnets using [P₂₂₂₅][TFSA] ionic liquid as the electrolyte [12]. MATSUMIYA et al [13] studied the electro- chemical mechanism of Nd(III) in N,N-diethyl- N-methyl-N-(2-methoxyethyl) ammonium bis(tri- fluoromethyl-sulfonyl) amide ([DEME] [TFSA]) ionic liquid, and the reduction of Nd(III) was an irreversible one-step process controlled by the diffusion with a diffusion coefficient of 1.35×10^-9 cm²/s at 353 K. The electrodeposits obtained at -3.40 and -3.60 V (vs Ag) on a copper substrate were mixtures of neodymium and its oxide.

Considering the electrodeposition of RE  alloys, numerous studies have been carried out in eutectic solvents by induced co-deposition. For instance, GUO et al [14,15] and LIU et al [16] prepared a series of RE-transition metal alloys including La-Co, La-Ni, and Nd-Fe alloys via induced co-deposition in the acetamide-urea-NaBr melts. The maximum mass fractions of RE metals in the deposited La-Co, La-Ni, and Nd-Fe alloys were 66.32%, 78.81%, and 60.4%, respectively. YANG et al [17] studied the electrochemical behavior and nucleation mechanism of Ni(II) and La(III) in 1-ethyl-3-methylimidazolium chloride- ethylene glycol (EMIC-EG) eutectic ionic liquid, while inductively coupled plasma-atomic emission spectrometry (ICP-AES) and X-ray diffraction (XRD) analyses showed that Ni-La alloys containing 0.2-9.48 wt.% La were deposited at current densities of 3-7 mA/cm².

In summary, RE metals can be electro- deposited in ionic liquids such as AlCl₃-EMICl, OMPTf₂N, [EMIM][BF₄]-LiCl, [P₂₂₂₅][TFSA], and [DEME][TFSA]. However, AlCl₃-based ionic liquids show disadvantage of high hygroscopicity, while other conventional ionic liquids have drawbacks such as high cost and synthetic complexity [18]. Eutectic solvents are inexpensive and suitable for the preparation of RE alloys, but it is difficult to produce pure RE metals because their electrochemical windows are narrow. Recently, ZHANG et al [19] have developed a novel 1,3-dimethyl-2-imidazolidinone-lithium nitrate (DMI-LiNO₃) solvated ionic liquid, which was air stable and readily available with a wide electrochemical window. Furthermore, XRD and XPS characterization confirmed that metallic La could be electrochemically deposited on a highly pure Al substrate at –2.3 V (vs Ag) from the DMI- LiNO₃ solvated ionic liquid containing LaCl₃. In this study, the physical properties including density, conductivity, and viscosity of the DMI-LiNO₃ solvated ionic liquid were measured at different temperatures. In addition, the electrochemical mechanism of Nd(III) reduction was investigated by cyclic voltammetry, and the coatings obtained by potentiostatic electrodeposition were analyzed.

2 Experimental

DMI (99%) and LiNO₃ (99.9%) were purchased from Shanghai Aladdin Bio-Chem Technology Co., Ltd., while neodymium trifluoro- methanesulfonate (Nd(CF₃SO₃)₃, 98%) was purchased from Alfa Aesar Chemical Co., Ltd., China. Owing to the high hygroscopicity of LiNO₃, the DMI-LiNO₃ solvated ionic liquid was prepared in a glove box. The contents of water and oxygen in the glove box were kept below 0.0001%. Firstly, the DMI solvent was added to a beaker and heated on a magnetic heating plate. Then, LiNO₃ was slowly added to DMI, and the mixture was heated with magnetic stirring until a homogeneous clear liquid containing 0.5 mol/L LiNO₃ was formed. Finally, 0.05 mol/L Nd(CF₃SO₃)₃ was dissolved in the DMI-LiNO₃ solvate ionic liquid for Nd electrodeposition.

The physicochemical properties of the DMI-LiNO₃ solvated ionic liquid were measured in a glove box. The densities of the ionic liquid at room temperature (298 K) to 358 K were measured using the Archimedes method, where the calibration was performed using deionized water. The electrical conductivities were measured using the fixed conductivity cell method by employing an LCR meter (Agilent 4263B; Agilent Technologies, Palo Alto, USA), which was calibrated using a standard potassium chloride solution (1 mol/L KCl). The viscosities were measured using a Ubbelohde viscometer (HAD-1834; Heng Odd Instrument, Beijing, China).

Cyclic voltammetry experiments were performed using an electrochemical workstation (CHI600E; CH Instruments, Shanghai, China). A tungsten wire (99.95%) with an immersion area of 0.8 cm² was selected as the working electrode, while platinum (99.99%) and silver (99.99%) wires with a diameter of 0.5 mm were used as the counter and reference electrodes, respectively. The electro- chemical workstation was also used to perform electrodeposition experiments using a three- electrode system. The working electrode comprised an aluminum sheet (99.99%), while the counter electrode and reference electrode constituted a tungsten sheet (99.99%) and a silver wire (99.99%), respectively. The electrodes used before each experiment were polished using sandpaper and cleaned with deionized water. The phase compositions of the products were analyzed by XRD (D8 Advance; Bruker, Karlsruhe, Germany), and the morphologies and elemental compositions of the products were determined by scanning electron microscopy (SEM, Ultra Plus; Zeiss, Oberkochen, Germany) coupled with an energy-dispersive X-ray spectroscopy (EDS) system. In addition, the electrodeposits were characterized using XPS (Axis Ultra DLD, Kratos, Japan).

3 Results and discussion

3.1 Physical properties of ionic liquid

The densities of the DMI solvent and DMI-LiNO₃ solvated ionic liquid (containing 0.5 mol/L LiNO₃) were measured using the Archimedes method at 298-358 K. As shown in Fig. 1, the density of DMI decreases from 1.064 to 1.021 g/cm³ with an increase in temperature from 298 to 358 K, while the density of the DMI-LiNO₃ solvated ionic liquid decreases from 1.133 to 1.087 g/cm³. The addition of LiNO₃ to the DMI solvent results in an increase in its density. The decrease in density with increasing temperature is mainly due to an increase in the thermal motion  of the particles as the number of particles per unit volume decreases with increasing  temperature [20,21]. Moreover, the density of the DMI-LiNO₃ solvated ionic liquid (ρ, g/cm³) is linearly correlated to temperature (T, K), as described by Eq. (1).

ρ=-7.64×10^-4T+1.36                     (1)

Fig. 1 Densities of DMI solvent and DMI-LiNO₃ solvated ionic liquid at different temperatures

The conductivities of the DMI solvent and DMI-LiNO₃ solvated ionic liquid (containing 0.5 mol/L LiNO₃) at 301-350 K are shown in Fig. 2(a). With an increase in temperature from 301 to 350 K, the conductivity of DMI increases from 0.04 to 0.11 mS/cm, while the conductivity of the DMI-LiNO₃ solvated ionic liquid increases from 1.02 to 6.14 mS/cm. The addition of LiNO₃ to DMI results in an obvious increase in conductivity. The conductivity increases with an increase in temperature because of a decrease in the viscosity and increase in the diffusion or migration rate of ions at high temperature. Moreover, the conductivity of the DMI-LiNO₃ solvated ionic liquid at 318 K is 1.78 mS/cm, which is of the same order of magnitude for the values of conventional ionic liquids such as urea-acetamide-AlCl₃ (1.5 mS/cm at 323 K), N-propyl-N-methyl pyrro- lidinium bis(trifluoro methanesulfonyl)imide (2.3 mS/cm at 298 K), and [BMIM][BF₄] (3.5 mS/cm at 298 K) [22-24].

Fig. 2 Conductivities (σ) of DMI solvent and DMI- LiNO₃ solvated ionic liquid at different temperatures (a) and relationship between ln σ and T ^-1 for DMI-LiNO₃ solvated ionic liquid (b)

Arrhenius equation is generally applied to determining the transport properties in non-aqueous solutions including the molten salts and ionic liquids, and the relationship between conductivity and temperature can be described by Eq. (2) [25]:

ln σ=ln σ₀-E_a/(RT)                        (2)

where σ is the conductivity (mS/cm); σ₀ is the pre-exponential factor (mS/cm); E_a is the diffusion activation energy (J/mol); R is the mole gas constant (8.314 J/(mol·K)); T is the experimental temperature (K). As shown in Fig. 2(b), the logarithmic conductivity of the DMI-LiNO₃ solvated ionic liquid (ln σ) is linearly related to the reciprocal of temperature (T^-1). Based on Eq. (2) and the slope of the plot in Fig. 2(b), the diffusion activation energy for the DMI-LiNO₃ solvated ionic liquid is 33.53 kJ/mol. Therefore, conductivity as a function of temperature can be expressed by Eq. (3):

σ=611530.43exp(-4032.58/T)               (3)

The viscosities of DMI solvent and DMI- LiNO₃ solvated ionic liquid (containing 0.5 mol/L LiNO₃) at 298-348 K were measured using a viscometer. As shown in Fig. 3(a), viscosity of DMI is significantly lower than that of the DMI-LiNO₃ solvated ionic liquid. The viscosity of DMI at 298 K is 1.93 mPa·s, which is consistent with the viscosities of general organic solvents. After the addition of 0.5 mol/L LiNO₃ to DMI, the viscosity at 298 K significantly increases to 69.59 mPa·s, indicating that the structure of the electrolyte changes from the initial molecular solvent to that of an ionic liquid. The viscosity of the DMI-LiNO₃ solvated ionic liquid increases upon the addition of LiNO₃ because of an increase in ionic association and decrease in the mobility of the [Li(DMI)_n]⁺ solvated species [19,26]. BARGHAMADI et al [27] investigated the effect of LiNO₃ additive on the viscosity of several ionic liquids, and the viscosity of 1,2-dioxolane and 1,2-dimethoxyethane solvent with 1 mol/kg lithium bis(trifluoro- methanesulfonyl)imide increased from 2.9 to 3.6 mPa·s after the addition of 0.1 mol/kg LiNO₃ at 296 K. In addition, the viscosity of the DMI-LiNO₃ solvated ionic liquid is lower than those of some conventional ionic liquids and deep eutectic solvents because the latter have lower conductivities compared to electrolytes containing organic solvents [27]. For example, the viscosities of 1-butyl-1-methyl pyrrolidinium bis(trifluoro-methylsulfonyl) imide([BMPyrr][NTf₂]) ionic liquid, [BMIM][BF₄] ionic liquid, and choline chloride-urea deep eutectic solvent at 298 K are 72.57, 100.66, and 748.09 mPa·s, respectively [28-30].

Fig. 3 Viscosities (η) of DMI solvent and DMI-LiNO₃ solvated ionic liquid at different temperatures (a) and relationship between ln η and T ^-1 for DMI-LiNO₃ solvated ionic liquid (b)

Furthermore, the viscosity of the DMI-LiNO₃ solvated ionic liquid decreases from 69.59 to 14.89 mPa·s upon an increase in temperature from 298 to 348 K owing to the effect of temperature on hydrogen bonds and van der Waals forces. As described in Eq. (4), the viscosities at various temperatures can be fitted to the Arrhenius  equation [21,31].

ln η=ln η_∞-E_η/(RT)                       (4)

where η_∞ is the viscosity at infinite temperature (mPa·s), and E_η is the apparent activation energy (J/mol). As shown in Fig. 3(b), the logarithmic viscosity (ln η) is linearly related to the reciprocal of temperature (T ^-1). The fitting parameters η_∞  and E_η are determined to be 1.86×10^-4 mPa·s and 31.81 kJ/mol, respectively. Therefore, the viscosity can be described by ln η=-8.59+3825.7/T

3.2 Cyclic voltammetry

The cyclic voltammetry curves of the DMI-LiNO₃ solvated ionic liquid in the absence and presence of Nd(CF₃SO₃)₃ were obtained using a tungsten electrode (Fig. 4). The scan rate was 80 mV/s, and the experimental temperature was 303 K. As shown in Fig. 4(a), during the sweep from 0 to -5 V (vs Ag), the cyclic voltammetry curve of DMI is very stable, indicating its high stability. After the addition of 0.5 mol/L LiNO₃ to DMI, a pair of reduction and oxidation signals are observed, as shown in Fig. 4(b). Based on the results of our previous study, the current waves P-P' are due to the reduction and oxidation of Li, and the appearance of the cathodic current loop indicates the nucleation of Li on the tungsten working electrode [19]. The shoulders in the cathodic scan at approximately -2.6 V (vs Ag) and anodic scan at -1.1 V (vs Ag) are observed, which may be related to the underpotential deposition of Li and its oxidation on the working electrode [32]. In addition, no noticeable impurity peak is observed in the cyclic voltammetry curve of the DMI-LiNO₃ solvated ionic liquid from 0 to -2.8 V (vs Ag), indicating that the ionic liquid is stable within this potential range.

Fig. 4 Cyclic voltammetry curves of DMI (a), DMI-LiNO₃ (b), and DMI-LiNO₃-Nd(CF₃SO₃)₃ (c) solvated ionic liquid at 303 K and scan rate of 80 mV/s

Figure 4(c) shows the cyclic voltammetry curve of the DMI-LiNO₃ solvated ionic liquid containing 0.05 mol/L Nd(CF₃SO₃)₃. Two pairs of reduction and oxidation peaks (M-M' and N-N') are observed. Considering the cyclic voltammetry curve in the absence of Nd(CF₃SO₃)₃, the current density increase at approximately -1.0 V (vs Ag) and the subsequent reduction peak at -2.5 V (Point N) are attributed to the electrodeposition of Nd. The second reduction peak M (-3.5 V) is due to the reduction of Li⁺ ions to metallic Li. During the reverse potential sweep, the oxidation peaks M' (-3.2 V) and N' (-1.7 V) are related to the anodic stripping of Li and Nd from the surface of the working electrode, respectively.

To investigate the kinetics of Nd electro- deposition, cyclic voltammetry tests were performed at different scan rates (20, 40, 60, 80, and 120 mV/s). As shown in Fig. 5, the potentials of the reduction peaks gradually shift toward more negative values with increasing the scan rate. For the reversible electrode reaction, the peak potential (φ_p) is independent of the scan rate (v). Therefore, the electrochemical reduction of Nd(III) on tungsten electrode in DMI-LiNO₃-Nd(CF₃SO₃)₃ solvated ionic liquid can be considered an irreversible process.

Fig. 5 Cyclic voltammetry curves of DMI-LiNO₃- Nd(CF₃SO₃)₃ solvated ionic liquid at 303 K and scan rates of 20, 40, 60, 80, and 120 mV/s

For an irreversible electrochemical reaction, the number of electrons transferred can be calculated using the following equation [33]:

φ=B-[RT/(nF)]ln[I/(I_p-I)]                  (5)

where φ is the potential (V), B is the half-wave potential (V), n is the number of transferred electrons, F is the Faraday constant (96485 C/mol), I is the current (A), and I_p is the current of the reduction peak (A). The relationship between potential (φ) and ln[I/(I_p-I)] at 303 K is plotted based on the data derived from Fig. 5. As shown in Fig. 6(a), there is a linear relationship between φ and ln[I/(I_p-I)]. Combining the slopes of the plot in Fig. 6(a) and Eq. (5), the number of transferred electrons is 3.2, which is close to the theoretical number of transferred electrons in the reduction of Nd(III) to metallic Nd. Therefore, the reduction of Nd(III) in the DMI-LiNO₃-Nd(CF₃SO₃)₃ solvated ionic liquid proceeds via one-step three-electron transfer, and the electrochemical reaction can be described by Eq. (6):

Nd(III)+3e=Nd                                (6)

Fig. 6 Relationships between φ and ln[I/(I_p-I)] (a), and I_p and v^1/2 (b)

For an irreversible electrode process, there is a linear relationship between |φ_p-φ_p/2| and the charge transfer coefficient (α) [33]. Based on the data derived from Fig. 5 and Eq. (7), the charge transfer coefficient α at different scan rates can be calculated, and the average value of α for Nd(III) reduction in DMI-LiNO₃-Nd(CF₃SO₃)₃ solvated ionic liquid is 0.087.

|φ_p-φ_p/2|=1.857RT/(αnF)                    (7)

where φ_p is the peak potential of Nd(III) reduction (V), and φ_p/2 is the half-peak potential of Nd(III) reduction (V).

Furthermore, the peak current density of Nd(III) reduction in Fig. 5 gradually changes from -0.40 to -1.48 mA/cm² with an increase in the scan rate from 20 to 120 mV/s. As shown in Fig. 6(b), a linear relationship is observed between the peak current (I_p) and square root of the scan rate (v^1/2), indicating that Nd electrodeposition is controlled by diffusion [17]. According to the Randles-Sevcik equation (Eq. (8)) and the slope of the plot in Fig. 6(b), the diffusion coefficient for Nd(III) reduction on tungsten electrode in the DMI- LiNO₃-Nd(CF₃SO₃)₃ solvated ionic liquid is calculated to be 5.08×10^-8 cm²/s [33].

I_p=0.4958nFAc₀D^1/2v^1/2[αnF/(RT)]^1/2          (8)

where A is the immersion area of the working electrode (0.8 cm²), c₀ is the bulk concentration of Nd(III) ions (5×10^-5 mol/L), and D is the diffusion coefficient (cm²/s).

3.3 Characterization of electrodeposits

Owing to the pre-deposition of metals on the reactive Al substrate, Al-Nd intermetallic compounds can be easily formed by electro- deposition on Al electrode [18,19]. Therefore, electrodeposition experiments in the DMI-LiNO₃-Nd(CF₃SO₃)₃ solvated ionic liquid were carried out on an Al substrate to ensure the electrochemical extraction of metallic Nd. The applied potential was -4 V (vs Ag), and the deposition time was 2 h.

The phase composition of the electrodeposit was determined by XRD. As shown in Fig. 7(c), the XRD pattern indicates that the cathode product is composed of Al, Li, and LiAl phases. Among these, the Al phase is attributed to the cathode, while the Li and LiAl phases are formed because the applied potential is sufficiently negative for the electro- chemical reduction of Li⁺ ions. The SEM image and EDS spectrum of the coating are shown in Figs. 7(a) and (b), respectively. The Li particles are distributed on the coating surface. The EDS data show that the electrodeposit mainly contains Al and O, and Li is not detected within the resolution of  the EDS detector because the atomic number and energy of Li are small. In addition, the electrodeposit was analyzed by XPS, and the results are shown in Fig. 7(d). According to the fine scan of the Li peak, zero-valent Li with a mass fraction of 24.77% was detected [34], indicating that metallic Li is obtained by electrodeposition at -4 V (vs Ag) in the DMI-LiNO₃ solvated ionic liquid.

Furthermore, the electrodeposition experiment was performed in the DMI-LiNO₃ solvated ionic liquid containing 0.05 mol/L Nd(CF₃SO₃)₃ on an Al substrate with an applied potential of -4 V (vs Ag). The SEM image and EDS spectrum of the electrodeposit are shown in Fig. 8. The EDS spectra show that the particles with agglomerated structures mainly contain Al, O, and Nd. The presence of Al is attributed to the cathode substrate, while 21.91 wt.% Nd is derived from the reduction of Nd(III) in the solvated ionic liquid. In addition, the presence of O is mainly due to the high activity and small particle size of metallic Nd, which causes the oxidation of the electrodeposit upon exposure to air. However, within the resolution of the XRD  detector, no Nd was detected, suggesting that the Nd deposit was non-crystalline [14-16]. In addition to SEM-EDS analysis, the electrodeposit was analyzed by XPS. In the fine scan of the Nd peak (Fig. 8(b)), 67.51 wt.% Nd was detected [35,36], revealing that metallic Nd was obtained by electrodeposition at -4 V (vs Ag) in the DMI- LiNO₃-Nd(CF₃SO₃)₃ solvated ionic liquid.

Fig. 7 SEM image (a), EDS spectrum (b), XRD pattern (c) and XPS data (d) of electrodeposits obtained from DMI- LiNO₃ solvated ionic liquid on Al substrate after electrodeposition at -4 V (vs Ag) for 2 h

Fig. 8 SEM image (a), XPS spectrum (b), and EDS data (c, d) of electrodeposit obtained from DMI-LiNO₃- Nd(CF₃SO₃)₃ solvate ionic liquid after electrodeposition at 323 K and -4 V (vs Ag) for 2 h

4 Conclusions

(1) The solvated ionic liquid comprising DMI and 0.5 mol/L LiNO₃ is suitable for the electro- chemical preparation of Nd films from the Nd(CF₃SO₃)₃ precursor at room temperature.

(2) The density of the DMI-LiNO₃ solvated ionic liquid is 1.087-1.133 g/cm³ at 298-358 K, which can be described by ρ=-7.64×10^-4T+1.36.

(3) The conductivities and viscosities of the DMI-LiNO₃ solvated ionic liquid are equal to 1.02-6.14 mS/cm at 301-350 K and 14.89- 69.59 mPa·s at 298-348 K, respectively, which can be described by the following equations: σ= 611530.43exp(-4032.58/T); ln η=-8.59+3825.7/T.

(4) The electrochemical reduction of Nd(III) is an irreversible diffusion-controlled process with a diffusion coefficient of 5.08×10^-8 cm²/s, which can be described as Nd(Ⅲ)+3e=Nd. EDS and XPS analyses of the electrodeposit at -4 V (vs Ag) confirm the presence of metallic Nd.

Acknowledgments

The authors are grateful for the financial supports from the National Natural Science Foundation of China (Nos. 52004062, 52074084, 51804070), the Natural Science Foundation of Liaoning Province of China (No. 2020-MS-084), and the Guangxi Innovation-Driven Development Program, China (No. GUIKE AA18118030).

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DMI-LiNO₃溶剂化离子液体的物理化学性质及其在室温电沉积钕中的应用

刘爱民¹，姚 宇¹，郭梦霞¹，刘玉宝²，石忠宁³，刘风国¹，胡宪伟¹，何文才¹，王兆文¹

1. 东北大学 多金属共生矿生态化冶金教育部重点实验室，沈阳 110819；

2. 包头稀土研究院 白云鄂博稀土资源研究与综合利用国家重点实验室，包头 014030；

3. 东北大学 轧制技术及连轧自动化国家重点实验室，沈阳 110819

摘  要：测定1,3-二甲基-2-咪唑啉酮和硝酸锂(DMI-LiNO₃)溶剂化离子液体在不同温度下的密度、电导率和黏度，并研究DMI-LiNO₃溶剂化离子液体中电沉积钕及其电化学机理。循环伏安结果表明，Nd(III)的电化学还原为不可逆的一步转移3个电子的过程，且受扩散控制，其扩散系数为5.08×10^-8 cm²/s。能量分散X射线光谱和X射线光电子能谱分析表明，在DMI-LiNO₃-Nd(CF₃SO₃)₃溶剂化离子液体及-4 V(vs Ag)条件下的电沉积产物包括金属钕。

关键词：电沉积；钕；离子液体；物理化学性质；循环伏安法

(Edited by Wei-ping CHEN)

Corresponding author: Zhong-ning SHI, Tel: +86-24-83686381, E-mail: znshi@mail.neu.edu.cn

DOI: 10.1016/S1003-6326(21)65672-8

1003-6326/ 2021 The Nonferrous Metals Society of China. Published by Elsevier Ltd & Science Press