effect of chloride ions in electrowinning solutions on

9
Effect of Chloride Ions in Electrowinning Solutions on Zinc Deposition Behavior and Crystal Texture Keisuke Kashida 1,* , Satoshi Oue 2 and Hiroaki Nakano 2 1 Department of Materials Science & Engineering, School of Engineering, Kyushu University, Fukuoka 819–0395, Japan 2 Department of Materials Science & Engineering, Kyushu University, Fukuoka 819–0395, Japan To clarify the effect of chloride ions on Zn electrowinning in terms of deposition behavior and crystal texture, the partial polarization curve, current efficiency, and AC impedance for Zn deposition as well as its morphology and crystal orientation were investigated. In solutions containing chloride ions, the partial polarization curve for Zn deposition was evidently depolarized, and the degree of depolarization increased when increasing the concentration of chloride ions from 300 to 6,000 mg/L. The exchange current density i 0 for Zn deposition also increased with increasing chloride ion concentration, which indicates that the chloride ions promote the charge-transfer process during Zn deposition. The polarization resistance for Zn deposition measured by AC impedance decreased with increasing chloride ion concentration. Conversely, the capacity of the electric double layer increased with increasing chloride ion concentration from 300 to 1,200 mg/L; however, from 3,000 to 6,000 mg/L, the capacity decreased and approached that obtained from a chloride ion-free solution. On the other hand, the partial polarization curve for hydrogen evolution was almost unchanged by the presence of chloride ions. As a result, the current efficiency of Zn deposition in- creased by 5–7% and 1.7% in the initial stage of deposition (up until the thickness of Zn reached approximately 2.1 μm) and at 500 A/m 2 for 6 hours (482 μm), respectively. With the addition of 300 to 1,200 mg/L of chloride ions, the deposited Zn exhibited a preferred orientation of {0001} plane, and it increased with increasing chloride ion concentration, which is attributed to a decrease in the overpotential for Zn deposi- tion; however, no preferred orientation of a specific plane was shown in the deposits when increasing the concentration of chloride ions above 3,000 mg/L. Some spherical concavities resulting from traces of evolved hydrogen gas were observed on the surface of deposited Zn, and the size of the concavities increased with increasing chloride ion concentration. The size of platelet crystals of the deposited Zn decreased with in- creasing chloride ion concentration, which indicates that the chloride ions possibly promote the nucleation rate of Zn crystals due to specific adsorption onto the cathode. [doi:10.2320/matertrans.M-M2017827] (Received April 27, 2017; Accepted June 28, 2017; Published August 4, 2017) Keywords: zinc, electrowinning, chloride ions, current efficiency, polarization, depolarization 1. Introduction During electrodeposition of Zn from an electrowinning solution containing a large amount of sulfuric acid, hydro- gen evolution occurs on the cathode only at low current den- sities. With an increase in the current density, Zn deposition commences when the cathode is polarized to reach the equi- librium potential of Zn. The minimum current density re- quired for initiating Zn deposition has been named the criti- cal current density. For Zn electrowinning from highly concentrated sulfuric acid solution, the critical current densi- ty for Zn deposition increases due to impurities contaminat- ing the solution, resulting in a significant decrease in current efficiency of the deposition. Therefore, there are many stud- ies concerning the effect of impurities on the critical current density and current efficiency of Zn deposition. 1–9) Fukushi- ma et al. previously classified the impurities into four groups by comparing the critical current density reported by Ohya- ma 2) with that by Tainton, 1) and reported the effects of the impurities of each group on the critical current density for Zn deposition. 10,11) The critical current density reported by Tainton is the current density at which Zn begins to deposit onto an impurity metal cathode from an impurity-free elec- trowinning solution, 1) and the critical current density by Ohyama is the minimum current density needed to initiate Zn deposition on a pure Zn cathode from an impurity- containing solution. 2) These impurities are metal ions such as Co, Ni, Fe, Cu, Cd, Al, Pb and Ag, and semimetal ions such as Sb, As and Ge, which derive from the ore; however, there have been few reports on the effect of nonmetallic ions. Therefore, Nakano et al. selected chloride ions as non- metallic ions and investigated the effect of chloride ions on the deposition behavior and surface morphology of Zn. 12) As a result, it was reported that the partial polarization curve for Zn deposition shifted to noble potential direction upon the addition of small amounts of chloride ions, and the current efficiency of Zn deposition in the initial stage of deposition increased with increasing chloride ions. 12) The shift of cath- ode potential for reduction reaction to noble potential direc- tion is referred to as depolarization. However, only two con- centrations of chloride ions, 600 and 6,000 mg/L, were investigated, and the effect of chloride ions on the Zn depo- sition behavior was examined only in the initial stage of deposition (up until the thickness of Zn reached approxi- mately 10 μm). There are many ambiguities regarding the effect of chloride ions on the current efficiency and crystal texture of Zn deposited by long-term electrolysis. Therefore, in this study, to elucidate this effect, the partial polarization curve, current efficiency, and AC impedance for Zn deposi- tion were investigated in the solutions containing five differ- ent concentrations of chloride ions from 300 to 6,000 mg/L, and the morphology and crystal orientation of Zn deposited with thicknesses of approximately 2.1 and 482 μm were ana- lyzed. 2. Experimental Table 1 shows the electrolyte compositions and electroly- sis conditions for the short-time electrolysis used to investi- * Graduate Student, Kyushu University. Present address: Toho Zinc Corpo- ration, Fujioka 375–0005, Japan Materials Transactions, Vol. 58, No. 10 (2017) pp. 1418 to 1426 ©2017 The Mining and Materials Processing Institute of Japan

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Page 1: Effect of Chloride Ions in Electrowinning Solutions on

Effect of Chloride Ions in Electrowinning Solutions on Zinc Deposition Behavior and Crystal Texture

Keisuke Kashida1,*, Satoshi Oue2 and Hiroaki Nakano2

1Department of Materials Science & Engineering, School of Engineering, Kyushu University, Fukuoka 819–0395, Japan2Department of Materials Science & Engineering, Kyushu University, Fukuoka 819–0395, Japan

To clarify the effect of chloride ions on Zn electrowinning in terms of deposition behavior and crystal texture, the partial polarization curve, current ef�ciency, and AC impedance for Zn deposition as well as its morphology and crystal orientation were investigated. In solutions containing chloride ions, the partial polarization curve for Zn deposition was evidently depolarized, and the degree of depolarization increased when increasing the concentration of chloride ions from 300 to 6,000 mg/L. The exchange current density i0 for Zn deposition also increased with increasing chloride ion concentration, which indicates that the chloride ions promote the charge-transfer process during Zn deposition. The polarization resistance for Zn deposition measured by AC impedance decreased with increasing chloride ion concentration. Conversely, the capacity of the electric double layer increased with increasing chloride ion concentration from 300 to 1,200 mg/L; however, from 3,000 to 6,000 mg/L, the capacity decreased and approached that obtained from a chloride ion-free solution. On the other hand, the partial polarization curve for hydrogen evolution was almost unchanged by the presence of chloride ions. As a result, the current ef�ciency of Zn deposition in-creased by 5–7% and 1.7% in the initial stage of deposition (up until the thickness of Zn reached approximately 2.1 μm) and at 500 A/m2 for 6 hours (482 μm), respectively. With the addition of 300 to 1,200 mg/L of chloride ions, the deposited Zn exhibited a preferred orientation of {0001} plane, and it increased with increasing chloride ion concentration, which is attributed to a decrease in the overpotential for Zn deposi-tion; however, no preferred orientation of a speci�c plane was shown in the deposits when increasing the concentration of chloride ions above 3,000 mg/L. Some spherical concavities resulting from traces of evolved hydrogen gas were observed on the surface of deposited Zn, and the size of the concavities increased with increasing chloride ion concentration. The size of platelet crystals of the deposited Zn decreased with in-creasing chloride ion concentration, which indicates that the chloride ions possibly promote the nucleation rate of Zn crystals due to speci�c adsorption onto the cathode. [doi:10.2320/matertrans.M-M2017827]

(Received April 27, 2017; Accepted June 28, 2017; Published August 4, 2017)

Keywords:  zinc, electrowinning, chloride ions, current ef�ciency, polarization, depolarization

1.  Introduction

During electrodeposition of Zn from an electrowinning solution containing a large amount of sulfuric acid, hydro-gen evolution occurs on the cathode only at low current den-sities. With an increase in the current density, Zn deposition commences when the cathode is polarized to reach the equi-librium potential of Zn. The minimum current density re-quired for initiating Zn deposition has been named the criti-cal current density. For Zn electrowinning from highly concentrated sulfuric acid solution, the critical current densi-ty for Zn deposition increases due to impurities contaminat-ing the solution, resulting in a signi�cant decrease in current ef�ciency of the deposition. Therefore, there are many stud-ies concerning the effect of impurities on the critical current density and current ef�ciency of Zn deposition.1–9) Fukushi-ma et al. previously classi�ed the impurities into four groups by comparing the critical current density reported by Ohya-ma2) with that by Tainton,1) and reported the effects of the impurities of each group on the critical current density for Zn deposition.10,11) The critical current density reported by Tainton is the current density at which Zn begins to deposit onto an impurity metal cathode from an impurity-free elec-trowinning solution,1) and the critical current density by Ohyama is the minimum current density needed to initiate Zn deposition on a pure Zn cathode from an impurity- containing solution.2) These impurities are metal ions such as Co, Ni, Fe, Cu, Cd, Al, Pb and Ag, and semimetal ions

such as Sb, As and Ge, which derive from the ore; however, there have been few reports on the effect of nonmetallic ions. Therefore, Nakano et al. selected chloride ions as non-metallic ions and investigated the effect of chloride ions on the deposition behavior and surface morphology of Zn.12) As a result, it was reported that the partial polarization curve for Zn deposition shifted to noble potential direction upon the addition of small amounts of chloride ions, and the current ef�ciency of Zn deposition in the initial stage of deposition increased with increasing chloride ions.12) The shift of cath-ode potential for reduction reaction to noble potential direc-tion is referred to as depolarization. However, only two con-centrations of chloride ions, 600 and 6,000 mg/L, were investigated, and the effect of chloride ions on the Zn depo-sition behavior was examined only in the initial stage of deposition (up until the thickness of Zn reached approxi-mately 10 μm). There are many ambiguities regarding the effect of chloride ions on the current ef�ciency and crystal texture of Zn deposited by long-term electrolysis. Therefore, in this study, to elucidate this effect, the partial polarization curve, current ef�ciency, and AC impedance for Zn deposi-tion were investigated in the solutions containing �ve differ-ent concentrations of chloride ions from 300 to 6,000 mg/L, and the morphology and crystal orientation of Zn deposited with thicknesses of approximately 2.1 and 482 μm were ana-lyzed.

2.  Experimental

Table 1 shows the electrolyte compositions and electroly-sis conditions for the short-time electrolysis used to investi-

* Graduate Student, Kyushu University. Present address: Toho Zinc Corpo-ration, Fujioka 375–0005, Japan

Materials Transactions, Vol. 58, No. 10 (2017) pp. 1418 to 1426 ©2017 The Mining and Materials Processing Institute of Japan

Page 2: Effect of Chloride Ions in Electrowinning Solutions on

gate the deposition behavior and crystal morphology of Zn in the initial stages of deposition. An electrolytic solution was prepared by dissolving ZnO with purity of 99.999% (0.765 mol/L) in distilled and ion-exchanged water contain-ing sulfuric acid. The concentration of free sulfuric acid was 1.53 mol/L. Chloride ions were added in the form of HCl, at concentrations of 300, 600, 1,200, 3,000, and 6,000 mg/L (0.00846, 0.0169, 0.0338, 0.0846, and 0.169 mol/L). Al-though the chloride ions were reported to be present in an amount of 41 to 350 mg/L into the practical electrolyte,13) in this study, a larger amount of chloride ions were added to make their effect on the deposition behavior and crystal tex-ture of Zn clear. An Al sheet and a Pt sheet with the same area of 1 cm ×  2 cm were used as the cathode and anode, re-spectively. Prior to electrodeposition, the working electrode was carefully polished and buffed with Nos. 600, 1,500, and 2,000 emery paper before acid pickling and electrolytic degreasing were performed. The electrodeposition was per-formed in 0.5 L of a non-agitated solution at 40°C. The total polarization curve was obtained by measuring the corre-sponding cathode potential while changing the current den-sity every 3 min in a range from 0.01 to 2,000 A/m2. The partial polarization curves were obtained via electrodeposi-tion under coulostatic (50 kC/m2) and galvanostatic condi-tions for a current density range from 50 to 2,000 A/m2. The deposits were dissolved from the cathode using nitric acid, and Zn was quantitatively analyzed using inductively cou-pled plasma spectroscopy to calculate the current ef�ciency of Zn deposition. The partial current densities for Zn and H2 evolutions were calculated in each case by multiplying the total current density by the current ef�ciency. The current ef�ciency of the H2 evolution was calculated by subtracting the current ef�ciency of the Zn deposition from 100%. The cathode potentials were measured using a saturated KCl and Ag/AgCl reference electrode (0.199 V vs. a normal hydro-gen electrode, at 25°C). The potentials were plotted with ref-erence to the normal hydrogen electrode. The exchange cur-rent density i0 for Zn deposition was measured from the equilibrium potential of Zn and the extrapolation line in the Tafel plot of Zn partial polarization curve.

The AC impedance was measured at 200 A/m2 during Zn deposition. To obtain Nyquist plots, the frequency depen-dence of the AC impedance and the phase difference were measured for 1,600 s using a frequency-response analyzer at 50 A/m2 (±10 mA sine wave, 10  ×  10−3 to 105 Hz, 10

points/decade).To investigate the effect of chloride ions on the current ef-

�ciency and crystal texture of Zn deposited by long-term electrolysis, Zn electrodeposition was performed by circulat-ing 3.0 L of solution under galvanostatic conditions of 500 A/m2 at 40°C for 6 h. An Al sheet and a Zn sheet with the same area of 6 cm ×  8 cm were used as the cathode and anode, respectively. Zn sheet was used to prevent chloride ions from oxidizing at anode. The size of the electrolytic cell was 8.5 cm (length) ×  13 cm (width) ×  9.5 cm (depth), and the capacity of the electrolyte and the anode–cathode dis-tance were 1.05 L and 3 cm, respectively. Table 2 lists the conditions used for long-term electrolysis. 2.52 mol/L of Zn2+ ions were continuously supplied into the circulation tank at a rate of 0.26 mL/min, and the in�ow from the circu-lation tank to the electrolysis tank was 150 mL/min. The current ef�ciency of Zn deposition was calculated from the mass difference of the cathode before and after electrolysis. The surface and cross-sectional morphologies of the deposit-ed Zn were observed using a scanning electron microscope (SEM). The crystal orientation of the deposited Zn was de-termined using the method introduced by Wilson and Rog-ers14) with an X-ray diffraction intensity of 0002 to 112̄2 re-�ection. The crystallite size of the deposited Zn was calculated using the Scherrer equation15) from the half-width of the X-ray diffraction peak corresponding to the 0002 re-�ection. The cross-sectional texture of the deposited Zn was investigated by electron backscatter diffraction (EBSD). Pri-or to obtaining EBSD, the sample was embedded in a con-ductive resin, and the cross section was polished to a mirror �nish using aluminum powders with grain sizes of 1, 0.3, and 0.1 μm, after which etching was performed by Ar ion milling. Using EBSD, the crystallographic orientations of the reference direction (RD, i.e., the direction normal to the surface of the deposited Zn) were examined.

3.  Results and Discussion

3.1  Effect of chloride ions on Zn deposition behavior during the initial stage of deposition

Figure 1 shows the effect of chloride ions on the total po-larization curve for Zn deposition. In total polarization, the current for hydrogen evolution was detected at the potential region more noble than the equilibrium potential of Zn, EZn

eq (−0.766 V), regardless of whether chloride ions were present or not, whereas Zn deposition began near the equi-

Table 1 Electrolyte compositions and electrolysis conditions for short-time electrolysis.

Bath composition

Zn2+ (mol/L) 0.765

H2SO4 (mol/L) 1.53

Cl− (mg/L) 300~6000

Operating conditions

Current density (A/m2) 0.01~2000

Temperature (°C) 40

Amount of charge (C/m2) 5 ×  104

Cathode Al (1 ×  2 cm2)

Anode Pt (1 ×  2 cm2)

Electrolyte volume Quiescent bath

(L) 0.5

Table 2 Conditions used for long-term electrolysis.

Bath composition

Zn2+ (mol/L) 0.765

H2SO4 (mol/L) 1.53

Cl− (mg/L) 300~6000

Operating conditions

Current density (A/m2) 500

Temperature (°C) 40

Cathode Al (6 ×  8 cm2)

Anode Zn (6 ×  8 cm2)

Electrolyte duration (h) 6

Electrolyte volume (L) 3.0

Circulated electrolyte (mL/min) 150

1419Effect of Chloride Ions in Electrowinning Solutions on Zinc Deposition Behavior and Crystal Texture

Page 3: Effect of Chloride Ions in Electrowinning Solutions on

librium potential of Zn. Although the effect of chloride ions on the polarization curve in the region of hydrogen evolution was not observed, the polarization curve in the region of Zn deposition evidently shifted to noble potential direction with the coexistence of chloride ions. Therefore, the effect of chloride ions on the partial polarization curves for Zn depo-sition and hydrogen evolution in the potential region less no-ble than the equilibrium potential of Zn was also investigat-ed.

Figure 2 shows the partial polarization curves for Zn deposition in solutions containing various amounts of chlo-ride ions. The partial polarization curves signi�cantly shifted to noble potential direction with 300 mg/L of chloride ions compared with chloride ion-free solution. When increasing the chloride ions to more than 300 mg/L, the degree of de-polarization increased with increasing chloride ion concen-tration. The partial polarization curve curved greatly at Zn partial current densities of 500 to 700 A/m2 regardless of whether chloride ions were present or not. The depolariza-tion effect increased with increasing chloride ion concentra-tion in both regions where the charge-transfer overpotential occurred at current densities less than 500 A/m2 and the dif-fusion overpotential increased at current densities more than 700 A/m2. The exchange current density i0 for Zn deposition was measured at the equilibrium potential of Zn (−0.766 V) by extrapolation of the Tafel plot of the Zn partial polariza-tion curve at current densities less than 200 A/m2.

Figure 3 shows the relationship between the exchange

current density for Zn deposition and the concentration of chloride ions in solution. The exchange current density with 300 mg/L of chloride ions was two times larger than that without chloride ions, and increased signi�cantly with the concentration of chloride ions above 300 mg/L. This indi-cates that chloride ions promote the charge-transfer process for Zn deposition.

Figure 4 shows the partial polarization curves for hydro-gen evolution in solutions containing various amounts of chloride ions. The partial polarization curve for hydrogen evolution was almost linear at potentials from −0.8 to −0.88 V, and rarely changed despite the coexistence of 300 to 6,000 mg/L of chloride ions.

Figure 5 shows the current ef�ciency of Zn deposition at each current density in solutions containing various amounts of chloride ions. Whether chloride ions were present or not, the current ef�ciency increased with increasing current den-sity in a range less than 1000 A/m2, reached maximum at 1,000 A/m2, and then decreased somewhat at 2,000 A/m2. The current ef�ciencies at all measured current densities were higher with chloride ions than without. The current ef-�ciency increased with increasing chloride ion concentra-tion. When increasing the concentration of chloride ions to 6,000 mg/L, the current ef�ciency was 5–7% higher than that without chloride ions at all measured current densities. The current ef�ciency of Zn deposition increased with the coexistence of chloride ions, which is expected from the po-larization curves for Zn deposition and hydrogen evolution shown in Figs. 2 and 4. That is, with the coexistence of chlo-

Fig. 1 Effect of chloride ions in electrowinning solutions on the total po-larization curve for Zn deposition.

Fig. 2 Partial polarization curves for Zn deposition in solutions containing various amounts of chloride ions.

Fig. 3 Relationship between the exchange current density for Zn deposi-tion and the concentration of chloride ions in solution.

Fig. 4 Partial polarization curves for hydrogen evolution in solutions con-taining various amounts of chloride ions.

1420 K. Kashida, S. Oue and H. Nakano

Page 4: Effect of Chloride Ions in Electrowinning Solutions on

ride ions, hydrogen evolution rarely changed but Zn deposi-tion was depolarized, resulting in an increase in the current ef�ciency of Zn deposition. Since the degree of depolariza-tion for Zn deposition increased with increasing chloride ion concentration (Fig. 2), the current ef�ciency of Zn deposi-tion also increased with chloride ion concentration.

To elucidate the effect of chloride ions on the polarization resistance for Zn deposition, the AC impedance was mea-sured during Zn deposition at 200 A/m2 in solutions con-taining various amounts of chloride ions. At 200 A/m2, the charge-transfer process is rate-determining and the Tafel equation is completed, as can be seen from Fig. 2. The ob-tained Nyquist plots are shown in Fig. 6. The diameter of the semicircle in the Nyquist plots was larger without chloride ions than that with chloride ions and decreased with increas-ing chloride ion concentration. The polarization resistance for Zn deposition was measured from the diameter of the semicircle, and the capacity of the electric double layer was calculated from both the frequency at the peak of the semi-circle and the polarization resistance for Zn deposition. Fig-ure 7 shows the polarization resistance for Zn deposition and the capacity of the electric double layer in solutions contain-ing various amounts of chloride ions. The polarization resis-tance signi�cantly decreased upon the addition of 300 mg/L of chloride ions and further decreased with increasing chlo-ride ion concentration. Conversely, the capacity of the elec-tric double layer increased with increasing chloride ion con-centration from 300 to 1,200 mg/L; however, from 3,000 to 6,000 mg/L, the capacity decreased and approached that ob-tained from a chloride ion-free solution. It has been reported

that the speci�c adsorption of chloride ions increases the ca-pacity of the electric double layer.16) The increase in the ca-pacity of the electric double layer with chloride ion concen-tration from 300 to 1,200 mg/L demonstrated by this study can be attributed to the speci�c adsorption of the chloride ions. The reason for the decrease in the capacity of the elec-tric double layer with chloride ion concentration from 3,000 to 6,000 mg/L is unknown and should be investigated fur-ther in future.

It has been reported that the exchange current density of a reaction at a metal electrode is affected by the anion in the solution.17,18) The electron shell of ions becomes a dipole due to polarization which shows the forming regions of posi-tive and negative charge. It is known that there is a correla-tion between the polarizability and the exchange current density of the metal electrode in the reaction, and the ex-change current density of the reaction increases with in-creasing polarizability of the anion in solution.17,18) The po-larizability of chloride ions is larger than that of other anions; as a result, the chloride ions promote the deposition of most metal.19,20) For example, it was reported that the po-larizability of chloride ions (8.9 cm3/mol) is larger than that of sulfate ions (3.9 cm3/mol); the exchange current density for Zn deposition in a sulfate solution is 3 ×  10−5 A/cm2, and it is 3 ×  10−4 A/cm2 in chloride solutions.17,18) On the other hand, it has been reported that the overpotential for a cathode reaction decreases due to a decrease in the potential at the inner Helmholtz plane by the speci�c adsorption of anions on the cathode, according to the model of electrode potential distribution in Helmholtz double layers.17) By in-creasing the polarizability of the anions, both the adsorption ability of the anions onto the cathode and complexation abil-ity with the metal ions increase. In this study, the depolariza-tion of the Zn deposition potential observed in the presence of chloride ions is possibly caused by a decrease in the po-tential at the inner Helmholtz plane due to the speci�c ad-sorption of chloride ions or by a promoting effect on deposi-tion due to the formation of weak complexes or reaction intermediates involving chloride and Zn2+ ions.

Figure 8 shows the surface morphology of Zn deposited at different current densities in solutions containing various amounts of chloride ions. The size of blocks comprising crystal grains became larger with the coexistence of chloride ions. This tendency is more evident upon increasing the con-centration of chloride ions to 6,000 mg/L. The surface of Fig. 5 Current ef�ciency of Zn deposition at each current density in solu-

tions containing various amounts of chloride ions.

Fig. 6 Nyquist plots obtained at 200 A/m2 in solutions containing various amounts of chloride ions. [Cl− concentration (mg/L), ○0, △300, □1200, ◆6000].

Fig. 7 Polarization resistance for Zn deposition and the capacity of the electric double layer in solutions containing various amounts of chloride ions.

1421Effect of Chloride Ions in Electrowinning Solutions on Zinc Deposition Behavior and Crystal Texture

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blocks comprising crystal grains became smoother with the coexistence of chloride ions. On the other hand, the block size of crystals decreased with increasing current density.

3.2  Effect of chloride ions on the crystal texture of Zn obtained by long-term electrolysis

Figure 9 shows the current ef�ciency of Zn deposition at 500 A/m2 for 6 hours in solutions containing various amounts of chloride ions. The current ef�ciency increased by 1.1% upon the addition of 300 mg/L of chloride ions and further increased with increasing chloride ion concentration above 300 mg/L. The current ef�ciency with 6,000 mg/L of chloride ions was 1.7% higher than that without chloride ions.

Figure 10 shows the surface morphology of Zn deposited at 500 A/m2 for 6 hours in solutions containing various amounts of chloride ions. Some spherical concavities were observed on the surface of deposited Zn regardless of wheth-er chloride ions were present or not. This concavity may re-sult from traces of evolved hydrogen gas. The size of spheri-cal concavities increased with increasing chloride ion concentration. In particular, when increasing the concentra-tion of chloride ions to 6,000 mg/L, numerous layered spherical concavities were observed all over the surface of deposited Zn. The amount of hydrogen evolution seems to decrease with increasing chloride ion concentration because the current ef�ciency of Zn deposition increased with in-creasing chloride ion concentration. The increase in the number of spherical concavities suggests a decrease in the desorption capability of hydrogen gas from the deposited Zn or an increase in the nonuniformity of Zn crystal growth, with increasing chloride ion concentration.

Figure 11 shows the surface morphology of areas without the concavities of deposited Zn, which was observed at a higher magni�cation. Zn deposited from the chloride ion-

free solution comprised platelet crystals which signi�cantly inclined to the substrate. On the contrary, with 300 to 1,200 mg/L of chloride ions, Zn platelet crystals became parallel to the substrate, and the {0001} Zn basal plane of the hcp structure was observed on the outermost surface. Upon increasing the concentration of chloride ions to 3,000 mg/L, Zn platelet crystals became smaller and layered inclining to the substrate. With further increasing the chloride ions to 6,000 mg/L, the clear Zn platelet crystals disappeared and the grain size became smaller.

Figure 12 shows the crystal orientation of Zn deposited at 500 A/m2 for 6 hours in solutions containing various amounts of chloride ions. Zn deposited from the chloride ion-free solution showed somewhat preferred orientation of the {101̄3} plane. On the contrary, with 300 to 1,200 mg/L of chloride ions, the preferred orientation of {0001} plane was signi�cantly observed. Upon increasing the concentration of chloride ions to 3,000 mg/L, the preferred orientation of {0001} plane disappeared, and the orientation of {101̄3} plane increased somewhat, which was almost the same trend

Fig. 8 Surface morphology of Zn deposited at different current densities in solutions containing various amounts of chloride ions.

Fig. 9 Current ef�ciency of Zn deposition at 500 A/m2 for 6 hours in solutions containing various amounts of chloride ions.

1422 K. Kashida, S. Oue and H. Nakano

Page 6: Effect of Chloride Ions in Electrowinning Solutions on

as that from the chloride ions-free solution. With further in-creasing the concentration of chloride ions to 6,000 mg/L, the deposited Zn showed a texture close to a non-oriented dispersed type without the preferred orientation of a speci�c plane. Comparing the surface morphology of deposited Zn (Fig. 11) with the crystal orientation (Fig. 12), the angle of inclination of Zn platelet crystals to the substrate decreased upon increasing the orientation index of the {0001} plane, suggesting that the crystal orientation of deposited Zn corre-sponds to the macro surface morphology.

Figure 13 shows the cross-sectional SEM images of Zn deposited at 500 A/m2 for 6 hours in solutions containing various amounts of chloride ions. The top of Zn deposited

Fig. 12 Crystal orientation of Zn deposited at 500 A/m2 for 6 hours in solutions containing various amounts of chloride ions.

Fig. 10 Surface morphology of Zn deposited at 500 A/m2 for 6 hours in solutions containing various amounts of chloride ions. [Cl− concentration (mg/L), (a) 0, (b) 300, (c) 600, (d) 1200, (e) 3000, (f) 6000].

Fig. 11 Surface morphology of areas except for the concavities of deposited Zn. [Cl− concentration (mg/L), (a) 0, (b) 300, (c) 600, (d) 1200, (e) 3000, (f) 6000].

1423Effect of Chloride Ions in Electrowinning Solutions on Zinc Deposition Behavior and Crystal Texture

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from the chloride ion-free solution was slightly rough, but it became smoother with 300 to 1,200 mg/L of chloride ions, probably because the Zn platelet crystals became parallel to the substrate due to the preferred orientation of {0001} plane at these chloride ion concentrations. When increasing the concentration of chloride ions to 6,000 mg/L, voids were observed at the surface and inside the deposited Zn, as shown in Fig. 10. These voids probably result from traces of evolved hydrogen gas.

Figures 14 and 15 shows the crystal orientation mapping images by EBSD of Zn deposited at 500 A/m2 for 6 hours in solutions containing various amounts of chloride ions. For the EBSD, the crystallographic orientations of the RD, i.e., the direction normal to the surface of the deposited Zn, are shown. In the solution without chloride ions, as shown in Fig. 14 (a), the deposited Zn exhibited a non-oriented dis-persed type of �ne crystals in the initial stage of deposition, and at a thickness above 10 μm, the deposited Zn shifted to epitaxial growth that the deposits succeed the crystallo-graphic orientation of substrate, resulting in large grains. At a thickness over 50 μm, the deposited Zn comprised both in-clined �brous type crystals with the <101̄3>, <101̄2> and <101̄1> orientations and crystals re�ecting the epitaxial growth. On the contrary, with 300 to 1,200 mg/L of chloride ions, as shown in Figs. 14 (b), (c), Fig. 15(d), the deposits exhibited �brous type crystals with the <0001> orientation from the initial stage of deposition. With 1200 mg/L of chloride ions, as shown in Fig. 15(d), although the deposits showed epitaxial growth with orientations besides <0001> from the middle of the deposition onward, the deposits mostly comprised crystals with the <0001> orientation. Upon increasing the concentration of chloride ions to 3,000 mg/L, as shown in Fig. 15(e), the �brous type crystals with the <0001> orientation disappeared, and the deposits

exhibited a non-oriented dispersed type of �ne crystals from the initial stage to the outermost surface. Upon further in-creasing the concentration of chloride ions to 6,000 mg/L,

Fig. 13 Cross-sectional SEM images of Zn deposited at 500 A/m2 for 6 hours in solutions containing various amounts of chloride ions. [Cl− con-centration (mg/L), (a) 0, (b) 300, (c) 600, (d) 1200, (e) 3000, (f) 6000].

Fig. 14 Crystal orientation mapping images by EBSD of Zn deposited at 500 A/m2 for 6 hours in solutions containing various amounts of chlo-ride ions. [Cl− concentration (mg/L), (a) 0, (b) 300, (c) 600].

Fig. 15 Crystal orientation mapping images by EBSD of Zn deposited at 500 A/m2 for 6 hours in solutions containing various amounts of chlo-ride ions. [Cl− concentration (mg/L), (d) 1200, (e) 3000, (f) 6000].

1424 K. Kashida, S. Oue and H. Nakano

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as shown in Fig. 15(f), although the deposits had voids re-sulting from traces of evolved hydrogen at the surface and inside the deposited Zn, the deposits exhibited a non-orient-ed dispersed type of �ne crystals from the initial stage to the outermost surface. The crystal orientation of deposited Zn examined by mapping images of EBSD is almost consistent with the surface orientation of Zn shown in Fig. 12.

Pangarov calculated the relative values of two-dimension-al nucleation work for various crystal planes. By assuming that two-dimensional nuclei with the smallest nucleation work were formed at a given crystallization overpotential, he examined the overpotential dependence of the preferred ori-entation of the various metals deposited from aqueous solu-tions.21,22) According to Pangarov, the preferred orientations of hcp Zn shifted from the {0001} plane to the {101̄1}, {112̄0}, and {101̄0} planes (in that order) with increasing Zn deposition overpotential. In this study, the increase in the {0001} plane of the deposits obtained at 500 A/m2 with the coexistence of 300 to 1,200 mg/L of chloride ions is at-tributed to a decrease in the overpotential for Zn deposition with chloride ions (Fig. 2). However, although the overpo-tential for Zn deposition at 500 A/m2 decreased with 3,000 and 6,000 mg/L of chloride ions, the preferred orientation of the {0001} plane disappeared, which cannot be explained by the overpotential theory. Pangarov also suggested that the work of two-dimensional nucleation on the various crystal planes could change regardless of the overpotential when certain foreign additives were adsorbed onto the cath-ode.21,22) When increasing the concentration of chloride ions above 3,000 mg/L, the chloride ions in this study possibly affected the nucleation and growth rate of speci�c crystal planes.

Figure 16 shows the crystallite size of Zn deposited at 500 A/m2 for 6 hours in solutions containing various amounts of chloride ions. The crystallite size of deposited Zn decreased with increasing chloride ion concentration. When the overpotential for metal deposition decreases, the nucleation rate of the deposited metal generally becomes smaller than the growth rate of the metal, thereby resulting in an increase in the crystallite size.23) However, in this study, although the overpotential for Zn deposition de-creased with increasing chloride ion concentration, the crys-tallite size of Zn decreased, which cannot be explained by the overpotential theory. The reason for this is unknown, but

the chloride ions possibly promote the nucleation rate of Zn crystals due to the speci�c adsorption onto the cathode. The measured crystallite size of Zn was approximately 34 to 92 nm, and the size of the platelet crystals was several tens of micrometers, as shown in Fig. 11. It was reported that the hexagonal platelets of deposited Zn comprise many particles that are several tens of nanometers in size.24) In this study, the crystallite size was determined using the half-width of the X-ray diffraction peaks, and it appears to correspond to the size of each particle that formed the platelet crystals of Zn. Upon increasing the concentration of chloride ions, the sizes of both platelet crystals and crystallites of the deposit-ed Zn decreased, which suggests that there is a correlation between the sizes of platelet crystals and crystallites of Zn in this study.

From the above results, the existence of chloride ions in solution is favorable for an increase in current ef�ciency for Zn deposition from the electrowinning solution. However, the higher concentration of chloride ions cause the voids at the surface and inside of deposited Zn as shown in Figs. 10 and 13, and are known to originate the pitting corrosion of Al cathode and the dissolution of Pb-Ag alloy anode. There-fore, the proper concentration of chloride ions in solution should be hereafter investigated from the perspective of ad-vantages and disadvantages.

4.  Conclusion

The partial polarization curve, current ef�ciency, and AC impedance for Zn deposition and the morphology and crys-tal orientation of the deposited Zn were investigated to clari-fy the effect of chloride ions in electrowinning solutions on the deposition behavior and crystal texture of Zn. With the coexistence of chloride ions in solution, the partial polariza-tion curve for Zn deposition was evidently depolarized, and the degree of depolarization increased with increasing chlo-ride ion concentration from 300 to 6,000 mg/L. The ex-change current density i0 for Zn deposition increased with increasing chloride ion concentration, which indicates that the chloride ions promote the charge-transfer process for Zn deposition. The polarization resistance for Zn deposition measured by AC impedance decreased with increasing chlo-ride ion concentration. Conversely, the capacity of the elec-tric double layer increased with increasing chloride ion con-centration from 300 to 1,200 mg/L; however, from 3,000 to 6,000 mg/L, the capacity decreased and approached that ob-tained from a chloride ion-free solution. On the other hand, the partial polarization curve for hydrogen evolution was al-most unchanged with the coexistence of chloride ions. As a result, the current ef�ciency of Zn deposition increased by 5–7% and 1.7% in the initial stage of deposition (up until the thickness of Zn reached approximately 2.1 μm) and at 500 A/m2 for 6 hours (482 μm), respectively.

With the addition of 300 to 1,200 mg/L of chloride ions, the deposited Zn exhibited a preferred orientation of {0001} plane, which is attributed to a decrease in the overpotential for Zn deposition; however, no preferred orientation of a speci�c plane was shown in the deposits when increasing the concentration of chloride ions above 3,000 mg/L. Some spherical concavities resulting from traces of evolved hydro-

Fig. 16 Crystallite size of Zn deposited at 500 A/m2 for 6 hours in solu-tions containing various amounts of chloride ions.

1425Effect of Chloride Ions in Electrowinning Solutions on Zinc Deposition Behavior and Crystal Texture

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gen gas were observed on the surface of deposited Zn, and the size of the concavities increased with increasing chloride ion concentration. The size of platelet crystals of the depos-ited Zn decreased with increasing chloride ion concentra-tion, which indicates that the chloride ions possibly promote the nucleation rate of Zn crystals due to speci�c adsorption onto the cathode.

REFERENCES

1) U.C. Tainton: Trans. Am. Electrochem. Soc. 41 (1922) 389–410. 2) S. Ohyama and S. Morioka: Proc. Int. Symp. Extractive Metallurgy of

Zn, (Tokyo, 1985) pp.219–234. 3) S. Morioka: Journal of MMIJ 85 (1969) 631–633. 4) Y. Ogawa: Journal of MMIJ 49 (1933) 571–579. 5) T. Ohgai, T. Akiyama and H. Fukushima:Proc. Int. Symp. on the Ex-

traction and Applications of Zinc & Lead, (Sendai, 1995) pp.352–359. 6) D.R. Fosnacht and T.J. O’keefe: J. Appl. Electrochem. 10 (1980) 495–

504. 7) D.R. Fosnacht and T.J. O’keefe: Metall. Trans. B, 14 (1983) 645–655. 8) D.J. MacKinnon: Hydrometallurgy 35 (1994) 11–26. 9) A.R. Ault and E.J. Frazer: J. Appl. Electrochem. 18 (1988) 583–589. 10) H. Fukushima, T. Akiyama and T. Ohgai: Journal of MMIJ 110 (1994)

967–972.

11) H. Nakano, S. Oue, T. Noguchi, T. Akiyama and H. Fukushima: Jour-nal of MMIJ 120 (2004) 39–42.

12) H. Nakamura, S. Oue, N. Sogabe and H. Nakano: Journal of MMIJ 131 (2015) 164–169.

13) M. Sakata, T. Imai, A. Horiuchi, K. Morita, Y. Kondo and M. Kusano: Proc. Int. Symp. on the Zinc & Lead, (Kyoto, 2005) pp.139–151.

14) K.S. Willson and J.A. Rogers: Tech. Proc. Amer. Electroplaters Soc. 51 (1964) 92–95.

15) T. Watanabe: J. Finish. Soc. Jpn. 40 (1989) 280–286. 16) K. Higashi and H. Fukushima: J. Jpn. Inst. Metals 40 (1976) 765–769. 17) J. M. West, translated by T. Ishikawa and T. Shibata: Electrodeposi-

tion and Corrosion Processes, (Sangyo Tosho, Tokyo, 1970)p.33, pp.107–109.

18) S. Haruyama: Hyomen Gizyutsusya no tameno Denkikagaku, (Maruzen, Tokyo, 2006) pp.75–76.

19) M. Yasuda, I. Ohno and S. Haruyama: J. Surf. Finish. Soc. Jpn. 41 (1990) 312–317.

20) Z. Nagy, J.P. Blaudeau, N.C. Hung, L.A. Curtiss and D.J. Zurawski: J. Electrochem. Soc. 142 (1995) L87–L89.

21) N.A. Pangarov: J. Electroanal. Chem. 9 (1965) 70–85. 22) N.A. Pangarov: Electrochim. Acta 9 (1964) 721–726. 23) S. Haruyama: Hakumaku Zairyo no Kiso to Ohyo, (Jpn. Inst. Met.,

Sendai, 1987) p.37. 24) K. Kondo, T. Murakami, F. Cerwinski and K. Shinohara: ISIJ Int. 37

(1997) 140–145.

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