中国有色金属学报(英文版)

Trans. Nonferrous Met. Soc. China 24(2014) 2883-2889

Preparation of ZrMn2 hydrogen storage alloy by electro-deoxidation in molten calcium chloride

Lei DAI1,2, Shuo WANG1, Ling WANG1, Yao YU 1, Guang-jie SHAO2

1. College of Chemical Engineering, Hebei United University, Tangshan 063009, China;

2. State Key Laboratory of Metastable Materials Science and Technology, Yanshan University, Qinhuangdao 066004, China

Received 27 August 2013; accepted 27 November 2013

Abstract:

ZrMn2 alloy was electro-synthesized directly from cathode pellets compacted with powdered mixture of MnO2 and ZrO2 in molten calcium chloride. Sintering temperature, cell voltage and electrolysis time were the dominant factors that affected the characteristics of the final product. The results confirmed the formation of pure ZrMn2 alloy through the electro-deoxidation of the mixed oxide pellets at 3.1 V for 12 h in 900 °C CaCl2 melt. The X-ray diffraction (XRD) and cyclic voltammetry analysis suggested that the electro-deoxidation proceeded from the reduction of manganese oxides to Mn, followed by ZrO2 or CaZrO3 reduction on the pre-formed Mn to ZrMn2 alloy. The cyclic voltammetry measurements using powder microelectrode showed that the prepared ZrMn2 alloy has a good electrochemical hydrogen storage property.

Key words:

electro-deoxidation; ZrMn2 alloy; CaCl2 melt; oxides; hydrogen storage property;

1 Introduction

The Zr-based AB2 type Laves phase alloys have been extensively investigated as promising hydrogen storage materials and metal hydride electrodes due to their fast kinetics, high storage capacity, easy activation and moderate working conditions [1-3]. A significant number of laboratory studies have been focused on their composition, structures, physicochemical properties and alloying effects [4-7]. Meanwhile, due to the continuous large scale use of the hydrogen storage alloys, some attentions have been paid to developing new preparation methods with low energy consumption and simple operation to cope with challenge from the soaring market prices of metals in recent years [8-10]. The dominant extractive metallurgy is focused on separately extracting and refining the individual metals, followed by melting, alloying and casting under vacuum. Such processes are high in energy consumption but low in production efficiency, contributing to the relatively high costs of the hydrogen storage materials.

The recent demonstration of direct electro- deoxidation of solid metal oxides in molten salts promises a novel generic technology, known as the FFC-Cambridge process, for the extraction of reactive metals in situ during electrolysis without going through any melting step [11-15]. Meanwhile, the other perceived advantages of the electro-deoxidation method include low energy consumption, simple operation, and the capability to directly reduce a combination of different metal oxides together to form alloys [16-19]. Some hydrogen storage alloys, such as LaNi5 [20], CeNi5 [21], TbNi5 [22], CeCo5 [23] and ZrCr2 [24], have been successfully prepared by the electro-deoxidation method. Compared with hydrogen storage alloys prepared by other methods, the ones prepared by the FFC-Cambridge process exhibit comparable or better electro-hydrogen storage properties, and have easy preparation and low cost.

This work reported the success of applying the FFC-Cambridge process to preparation of ZrMn2 alloy from their oxides. The influence of process parameters, such as sintering temperature, cell voltage and electrolysis time on the electrolysis process were investigated. The mechanism of the electro-deoxidation was proposed based on cyclic voltammetry curve using metallic cavity electrode in conjunction with X-ray diffraction (XRD) analysis.

2 Experimental

2.1 Preparation of cathode pellet

The oxide pellets were prepared by mixing commercial available powders of ZrO2 and MnO2 according to the stoichiometry of ZrMn2. PVB (1%) and absolute alcohol were added to the mixture and thoroughly milled in a ball-milling container for 3 h. After drying, the mixture was pressed into pellets of 10 mm in diameter and 3 mm in thickness. And then the pellets were sintered at 900, 1050 and 1250 °C for 5 h, respectively. The composition and morphology of the sintered pellets were analyzed by XRD (Vantage 4.0) and SEM (S-4800), respectively.

2.2 Constant voltage electrolysis

The experimental apparatus used here was similar to that described in Ref. [21]. An alumina crucible was filled with about 800 g of a dehydrated CaCl2 and placed at the bottom of a stainless steel reactor in a vertical furnace. Subsequently, argon gas was introduced into the reactor continuously. After the temperature increased to pre-set temperature, electrolysis of the oxide cathode with one or two pellets wrapped with Kanthal wire mesh proceeded at a constant voltage with high purity graphite used as the counter electrode. After electrolysis, the sample was lifted from the molten salt and cooled naturally in a stream of argon before removal from the steel reactor, and then was immediately washed in distilled water. The composition and morphology of the products were analyzed by XRD and SEM, respectively.

2.3 Cyclic voltammetry

Foil of molybdenum (width of 10 mm, thickness of 0.5 mm, length of 20 mm, purity of 99.9%) with one circular hole (diameter of 1.0 mm) was used for making the metallic cavity electrodes (MCE). The oxide powders manually filled into the MCE cavity by repeatedly finger-pressing were used as the working electrode on which cyclic voltammetry (CV) was then carried out in CaCl2 melt at 900 °C. High purity graphite and Kanthal wire were used as the counter electrode and the pseudo- reference electrode, respectively. All electrochemical experiments were operated under the protection of an argon flow. The CVs were then recorded by ZAHNER IM6e electrochemical station.

2.4 Measurement of electrochemical hydrogen storage property

The electrochemical hydrogen storage property of ZrMn2 alloy was investigated by CV experiments in a classical three-electrode cell. The powder microelectrode loading ZrMn2 alloy was used as working electrode. A Pt plate and a Hg/HgO electrode were used as a counter electrode and a reference electrode, respectively.

3 Results and discussion

3.1 Influence of sintering temperatures

The cathode pellets sintered at different temperatures were analyzed using XRD. Figure 1 shows the variation of phases present in the precursor pellets after sintering at various temperatures. It was apparent that ZrO2 kept stable and some change occurred to MnO2 after sintering over the temperature range of 900-1250 °C. MnO2 sintered at 900 °C was changed into Mn2O3 due to reaction (1). With the increase of sintering temperature, Mn2O3 was further reduced and Mn3O4 was formed at 1050 and 1250 °C, following reaction (2). Based on Gibbs free energy (ΔGΘ) values for reactions (1) and (2) at the sintering temperatures, the two reactions could take place.

2MnO2=Mn2O3+1/2O2,

DGΘ=-40.646 kJ mol-1, 900 °C            (1)

3/2Mn2O3=Mn3O4+1/4O2,

           (2)

Fig. 1 XRD patterns of mixed oxide pellets sintered at various temperatures

Pellet sintering involves both increase of sample strength and shrinkage of volume, which can avoid powdering of the pellets in molten salt. Compared with the as-pressed ones, the sintered pellets became slightly smaller but much stronger. Figure 2 displays the SEM images of the mixed oxide pellets sintered at different temperatures. As shown in Fig. 2, the pellet porosity decreased with elevating sintering temperature and the particles grew up. The pellet had uniform small pores after being sintered at 900 °C. The pellet sintered at 1050 °C was more compact than the one sintered at 900 °C. At sintering temperature up to 1250 °C, it was clearly seen that a few of big pores appeared and particle size was quite big. The relatively large particle size meant a longer distance for oxygen ion transportation from particle inner to surface and hence a lower electro- deoxidation rate [21,25].

Fig. 2 SEM images of mixed oxide pellets sintered at 900 °C (a), 1050 °C (b) and 1250 °C (c) for 5 h, respectively

Figure 3 shows the typical current–time plots recorded during electrolysis of the oxide pellets sintered at different temperatures in 900 °C CaCl2 melt. All current–time plots exhibited three steps. 1) In the first few minutes, electrolysis current increased along with time. When a constant cell voltage of 3.1 V was applied, the oxide in contact with the Kanthal wire began to reduce into metal, and then the new three-phase interlines (3PIs, metal/oxide/electrolyte) formed on pellet surface due to newly formed metal. With such processes continuing, the 3PIs expanded from the initial metal-oxide contact points along the pellet’s surface, which increased the contact area of the metallic current collector and resulted in the increase of current [26]. 2) The current quickly declined in the 20-150 min. In this step, the 3PIs moving from surface into the interior of the oxide pellet and particles along the depth direction resulted in current decrease due to mass transfer difficulties [27]. 3) The current slowly declined to background value. In this step, the reduction reaction occurred in 3PIs of particles interior, so the electrolysis current slowly decreased down to background value. Due to electronic conduction through CaCl2 melt, which resulted from the residue of the graphite particles and the impurity of the molten salt, the background current was zero [18,19]. The electrolysis current of the sample was dependent on sample sintering temperature. It was understood that the electro-deoxidization involved metal ion reduction and oxygen ion diffusion through the 3PIs. When the pellets were sintered at higher temperatures, the density and particle size increased, meaning the decrease of 3PIs length and oxygen ion transportation difficulty, and resulted in lower electro-deoxidation rate.

Fig. 3 Current–time plots of electrolysis of pellets sintered at different temperatures in 900 °C CaCl2 melt at 3.1 V for12 h

Figure 4 shows the XRD patterns of the products from the mixed oxide pellets sintered at 900, 1050 and 1250 °C. It was clearly seen that after being electrolyzed at 3.1 V for 12 h, the pellet sintered at 900 °C was completely reduced to pure ZrMn2 alloy. The reduced pellet could easily be ground into powder with pestle and mortar. As shown by the SEM image in Fig. 5, the product obtained after electrolysis for 12 h showed spongy and porous structure with the nodular particles, in agreement with previous findings in most metallized products from electro-reduction of solid metal oxides in CaCl2 melt. As to the pellets sintered at 1050 and 1250 °C, XRD spectra showed that the electrolysis products were a mixture of ZrMn2, Mn and CaZrO3. The results further demonstrated that the sintering temperature increase does lead to lower reduction rate.

Fig. 4 XRD patterns of products from electrolysis of pellets sintered at different temperatures (3.1 V, 900 °C CaCl2 melt,  12 h)

Fig. 5 SEM image of product from electrolysis of pellets sintered at 900 °C (3.1 V, 900 °C CaCl2 melt, 12 h)

3.2 Influence of cell voltage

The principle for the choice of cell voltages is to avoid salt decomposition but achieve relatively high electro-deoxidation speed [22]. According to thermo- dynamic data, the decomposition voltages of ZrO2, Mn2O3, Mn3O4 and CaCl2 at 900 °C can be calculated.

Ca2++2e-=Ca, DE=3.23 V                     (3)

ZrO2=Zr+O2, DE=2.37 V                     (4)

Mn2O3=2Mn+3/2O2, DE=1.13 V                (5)

Mn3O4=3Mn+2O2, DE=1.27 V                  (6)

Based on above theoretical calculation, in this work, the cell voltages of 2.5, 2.8 and 3.1 V were chosen for the electro-deoxidation of the mixture oxide pellets. The XRD patterns of electrolysis products at different applied voltages are shown in Fig. 6. When 2.5 V was applied, the XRD spectrum of the product exhibited the Mn and CaZrO3 phases, but no ZrMn2 phase formed. At 2.8 V, the XRD spectrum of the product appeared to be ZrMn2 phase. Meanwhile, there were still Mn, CaZrO3 and traces of ZrO2 phases, which meant that higher cell voltage was needed for the formation of pure ZrMn2 phase. The XRD spectrum of the product after electrolysis at 3.1 V showed that pure ZrMn2 phase was formed.

Fig. 6 XRD patterns of products from electrolysis of pellets sintered at 900 °C at different cell voltages for 12 h in 900 °C CaCl2 melt

3.3 Analysis of electro-deoxidation process

To investigate the electrochemical reduction process of the mixed oxide pellets, the electrolysis of the pellets sintered at 900 °C was carried out at 3.1 V for different time and then the obtained products were analyzed by XRD.

Figure 7 shows the XRD patterns of the products that were electrolyzed at 3.1 V for 1, 4, 7, 10 and 12 h. In the first 1 h of electrolysis, the products were a mixture of ZrO2, CaZrO3, Mn2O3, Mn3O4 and Mn, but no ZrMn2 was detected, which suggested that only Mn2O3 was reduced to Mn3O4 and Mn. After 4 h electrolysis, the ZrMn2 phase began to appear. With a further increase in the electrolysis time, especially after 7 h, the ZrMn2 phase dominated in the product. After 12 h electrolysis, pure ZrMn2 phase was detected. These results gave an indication of the formation of ZrMn2 from the reduction of ZrO2 or CaZrO3 on the pre-formed Mn directly.

Fig. 7 XRD patterns of products from electrolysis of pellets sintered at 900 °C at 3.1 V for different time in 900 °C CaCl2 melt

Based on the XRD results and previous studies on the mechanisms of the electro-reduction of solid metal oxides [21,28], the electro-deoxidation of ZrO2-Mn2O3 to ZrMn2 in CaCl2 melt should have proceeded through the following steps.

3Mn2O3+2e=2Mn3O4+O2-     (7)

Mn3O4+8e=3Mn+4O2-      (8)

ZrO2+Ca2++O2-=CaZrO3      (9)

ZrO2+2Mn+4e=ZrMn2+2O2-      (10)

CaZrO3+2Mn+4e=ZrMn2+Ca2++3O2-      (11)

To further understand the electro-deoxidation process mechanism, the cyclic voltammograms of samples on the MCE were measured in CaCl2melt at 900 °C. Figure 8 shows the CVs of pure ZrO2 powder, pure Mn2O3 powder and mixed ZrO2 and Mn2O3 powders recorded in CaCl2 melt at 900 °C. In the absence of oxide, the CV of the bare MCE showed a reduction peak c1 formed at -1.5 V until the potential scan was reversed which could be attributed to the reduction of CaCl2 [22]. The voltammetric features of the pure ZrO2 powders in the range from 0 to -0.65 V were similar to the ones of the bare MCE. Then the current became large, which suggested that the ZrO2 or CaZrO3 was reduced [29]. Compared with the bare MCE and ZrO2 powders, the CV of the pure Mn2O3 powders exhibited larger current at potentials more negative than -0.1 V and a reduction peak c2 was formed at -0.8 V which could be attributed to the reduction of Mn2O3 into Mn metal. The voltammetric features of the mixed ZrO2 and Mn2O3 powders were similar to those observed on the CV of the pure Mn2O3 powder in the range from 0 to -0.65 V and then the current became large and a peak, c3, was seen at -1.25 V which was absent on the CVs of the others. It was likely caused by the formation of the ZrMn2 compound resulting from the reduction of ZrO2 or CaZrO3 on the newly formed Mn metal particles.

Fig. 8 Cyclic voltammograms of MCE without and with ZrO2 powder, Mn2O3 powder and mixed ZrO2 and Mn2O3 powders in 900 °C CaCl2 melt (potential scanning rate: 10 mV/s)

3.4 Electrochemical hydrogen storage property

CV measurements were done at the potential ranging from -1200 to 0 mV (versus Hg/HgO electrode) to investigate the electrochemical hydrogen storage property of ZrMn2 powders. Figure 9(a) illustrates the CV curves of the ZrMn2 alloy powder microelectrode. The anodic peak (at -0.65 V) observed was due to the oxidation of the desorbed hydrogen atoms on the surface, which was used for evaluating the discharge processes of the ZrMn2 alloy. The discharge capacities for sample can be calculated from the cyclic voltammograms based on previously reported method [30]. Figure 9(b) shows that discharge capacities depended on cycle number. The activation of ZrMn2 was needed and almost completed after 20 cycles. The prepared ZrMn2 had the best hydrogen storage property between 40 and 55 cycles. After 120 cycles the discharge capacity retention was approximately 96.7%.

Fig. 9 Cyclic voltammograms of ZrMn2 alloy powder microelectrode in 6 mol/L KOH solution (a) and discharge capacity versus cycle number (b) (potential scanning rate: 50 mV/s)

Compared with previously reported Zr-based hydrogen storage alloys [24,31,32], the electrolytic ZrMn2 alloy exhibited comparable or better cycling stability, which might be attributed to the unique nodule-based porous structures with a large metal surface area for an enhanced interaction with H+.

4 Conclusions

1) This work demonstrated a facile method for the fabrication of ZrMn2 alloy powder from mixed oxides using the FFC-Cambridge process. Higher sintering temperature resulted in lower electro-deoxidation rate. The higher cell voltage favored the electro-deoxidation process. The pure ZrMn2 alloy was obtained by electrolyzing a mixture of ZrO2/MnO2 in 900 °C CaCl2 melt when 3.1V was applied for 12 h.

2) According to XRD and CVs analyses, the mechanism of the electro-deoxidation process could be divided into two steps: the reduction of mixed oxide started from manganese oxides to Mn, followed by ZrO2 or CaZrO3 reduction on the pre-formed Mn to form ZrMn2 alloy.

3) The ZrMn2 alloy powder for hydrogen storage showed good activity and cycling stability and the capacity retention was approximately 96.7% after 120 cycles.

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熔盐电脱氧法制备ZrMn2储氢合金

戴 磊1,2,王 硕1,王 岭1,余 瑶1,邵光杰2

1. 河北联合大学 化学工程学院,唐山 063009;

2. 燕山大学 亚稳材料制备技术与科学国家重点实验室,秦皇岛 066004

摘  要:采用熔盐电脱氧法,由MnO2和ZrO2混合氧化物直接合成ZrMn2合金。研究烧结温度、电解电压及电解时间等工艺参数对产物组成的影响。在900 °C的CaCl2熔盐中,经900 °C烧结的混合氧化物阴极在3.1 V恒电压下电解12 h,可制备出纯相的ZrMn2合金。XRD和循环伏安结果表明,在电解过程中,Mn-O化合物首先还原成单质Mn, ZrO2和CaZrO3再在单质Mn表面还原,并与其合金化,形成ZrMn2合金。以粉末微电极为工作电极,循环伏安测试结果表明,所制备的ZrMn2合金表现出良好的电化学储氢性能。

关键词:电脱氧;ZrMn2合金;CaCl2熔盐;氧化物;储氢性能

(Edited by Hua YANG)

Foundation item: Project (51201058) supported by the National Natural Science Foundation of China; Projects (E2010000941, E2014209009) supported by Hebei Provincial Natural Science Foundation of China

Corresponding author: Ling WANG; Tel/Fax: +86-315-2592170; E-mail: tswling@126.com

DOI: 10.1016/S1003-6326(14)63422-1

Abstract: ZrMn2 alloy was electro-synthesized directly from cathode pellets compacted with powdered mixture of MnO2 and ZrO2 in molten calcium chloride. Sintering temperature, cell voltage and electrolysis time were the dominant factors that affected the characteristics of the final product. The results confirmed the formation of pure ZrMn2 alloy through the electro-deoxidation of the mixed oxide pellets at 3.1 V for 12 h in 900 °C CaCl2 melt. The X-ray diffraction (XRD) and cyclic voltammetry analysis suggested that the electro-deoxidation proceeded from the reduction of manganese oxides to Mn, followed by ZrO2 or CaZrO3 reduction on the pre-formed Mn to ZrMn2 alloy. The cyclic voltammetry measurements using powder microelectrode showed that the prepared ZrMn2 alloy has a good electrochemical hydrogen storage property.

[1] CUI X Y, LI Q, CHOU K C, CHEN S L, LIN G W, XU K D. A comparative study on the hydriding kinetics of Zr-based AB2 hydrogen storage alloys [J]. Intermetallics, 2008, 16: 662-667.

[2] ANIKINA E Y, VERBETSKY V N. Investigation of ZrMn2+x-H2 by means of calorimetric method [J]. Journal of Alloys and Compounds, 2007, 446-447: 443-446.

[3] KIM J H, LEE H, HWANGA K T, HAN J S. Hydriding behavior in Zr-based AB2 alloy by gas atomization process [J]. International Journal of Hydrogen Energy, 2009, 34: 9424-9430.

[4] HARA M, YUDOU K, KINOSHITA E, OKAZAKI K, ICHINOSE K, WATANABE K, MATSUYAMA M. Alloying effects on the hydride formation of Zr(Mn1-xCox)2 [J]. International Journal of Hydrogen Energy, 2011, 36: 2333-2337.

[5] KANDAVEL M, BHAT V V, ROUGIER A, AYMARD L, NAZRI G A, TARASCON J M. Improvement of hydrogen storage properties of the AB2 Laves phase alloys for automotive application [J]. International Journal of Hydrogen Energy, 2008, 33: 3754-3761.

[6] PHILIPOSE S M, MANI N, KESAVAN T R, RAMAPRABHU S. Investigations of hydrogen storage properties in certain Zr-based AB2 alloys [J]. International Journal of Hydrogen Energy, 2002, 27: 419-424.

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