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Systematic Investigation of the Physical and Electrochemical Characteristics of the Vanadium

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Systematic Investigation of the Physical and Electrochemical Characteristics of the Vanadium ORIGINAL RESEARCH published: 14 July 2020 doi: 10.3389/fchem.2020.00502 Systematic Investigation of the Physical and Electrochemical Characteristics of the Vanadium (III) Acidic Electrolyte With Different Concentrations and Related Diffusion Kinetics Minghua Jing 1,3, Chengjie Li 2, Xinyu An 3, Zeyu Xu 1, Jianguo Liu 1, Chuanwei Yan 1, Dawei Fang 3 and Xinzhuang Fan 1,4* 1 Liaoning Engineering Research Center for Advanced Battery Materials, Institute of Metal Research, Chinese Academy of Edited by: Sciences, Shenyang, China, 2 Shandong Engineering Research Center of Green and High-Value Marine Fine Chemical, Du Yuan, Weifang University of Science and Technology, Shouguang, China, 3 Institute of Rare and Scattered Elements, College of Nanyang Technological Chemistry, Liaoning University, Shenyang, China, 4 Building Energy Research Center, Guangzhou HKUST Fok Ying Tung University, Singapore Research Institute, Guangzhou, China Reviewed by: Jingyu Xi, Tsinghua University, China Owing to the lack of systematic kinetic theory about the redox reaction of V(III)/V(II), the Yunguang Zhu, poor electrochemical performance of the negative process in vanadium flow batteries Massachusetts Institute of limits the overall battery performance to a great extent. As the key factors that influence Technology, United States Binyu Xiong, electrode/electrolyte interfacial reactivity, the physicochemical properties of the V(III) Wuhan University of acidic electrolyte play an important role in the redox reaction of V(III)/V(II), hence a Technology, China systematic investigation of the physical and electrochemical characteristics of V(III) acidic *Correspondence: Xinzhuang Fan electrolytes with different concentrations and related diffusion kinetics was conducted [email protected] in this work. It was found that the surface tension and viscosity of the electrolyte increase with increasing V(III) concentration, while the corresponding conductivity shows Specialty section: This article was submitted to an opposite trend. Both the surface tension and viscosity change slightly with increasing Electrochemistry, concentration of H2SO4, but the conductivity increases significantly, indicating that a section of the journal a lower V(III) concentration and a higher H2SO4 concentration are conducive to the Frontiers in Chemistry ion transfer process. The electrochemical measurements further show that a higher Received: 15 April 2020 Accepted: 15 May 2020 V(III) concentration will facilitate the redox reaction of V(III)/V(II), while the increase in Published: 14 July 2020 H2SO4 concentration only improves the ion transmission and has little effect on the Citation: electron transfer process. Furthermore, the diffusion kinetics of V(III) have been further Jing M, Li C, An X, Xu Z, Liu J, Yan C, Fang D and Fan X (2020) Systematic studied with cyclic voltammetry and chronopotentiometry. The results show that an Investigation of the Physical and elevated temperature facilitates the V(III)/V(II) redox reaction and gives rise to an increased Electrochemical Characteristics of the electrode reaction rate constant (ks) and diffusion coefficient [DV(III)]. On this basis, the Vanadium (III) Acidic Electrolyte With −1 Different Concentrations and Related diffusion activation energy (13.7 kJ·mol ) and the diffusion equation of V(III) are provided Diffusion Kinetics. to integrate kinetic theory in the redox reaction of V(III)/V(II). Front. Chem. 8:502. doi: 10.3389/fchem.2020.00502 Keywords: temperature, concentration, diffusion equation, trivalent vanadium ion, vanadium flow battery (VFB) Frontiers in Chemistry | www.frontiersin.org 1 July 2020 | Volume 8 | Article 502 Jing et al. Diffusion Kinetics of V(III) INTRODUCTION investigation into the physical and electrochemical characteristics of V(III) acidic electrolytes using different concentrations and Vanadium flow batteries (VFBs) have been widely developed as diffusion kinetics. a green energy storage technology because of their high energy In our previous work (Wang et al., 2014), the temperature- efficiency, flexible design, long life cycle, high safety, and low cost related reaction kinetics of the V(IV)/V(V) redox couple on a (Rychcik and Skyllas-Kazacos, 1988; Sun and Skyllas-Kazacos, graphite electrode in sulfuric acid solutions was investigated. 1992; Joerissen et al., 2004; Sukkar and Skyllas-Kazacos, 2004; Herein, we will investigate the physicochemical properties of Zhao et al., 2006; Rahman and Skyllas-Kazacos, 2009; Ding et al., the electrolytes with different concentrations of V(III) and 2013; Chakrabarti et al., 2014; Zheng et al., 2016). In general, sulfuric acid and conduct a systematic study of the diffusion VFBs are mainly composed of the electrolyte, electrode, ion kinetics of V(III). Our aim is to clarify the kinetic rules exchange membrane, and a bipolar plate. They store energy of the diffusion behavior of V(III) and further establish through the chemical changes in electroactive species, which are a diffusion equation, providing a better understanding of separated by the ion exchange membrane (Wang et al., 2014; the V(III)/V(II) redox reaction in the negative half-cell Xia et al., 2019; Ye et al., 2019, 2020a,b; Yu et al., 2019; Lou of VFBs. et al., 2020). The V(V)/V(IV) and V(III)/V(II) redox couples are used as the catholyte and the anolyte, respectively, and the sulfuric acid solution acts as the supporting electrolyte. The EXPERIMENTAL concentrations of vanadium and H+ ions play an important role in the determination of the electrochemical reaction processes Preparations of the Electrode and and the battery performance. Electrolyte The most commonly used electrolyte in VFBs is an equivalent A spectroscopically pure graphite rod (SPGR) (Sinosteel volume mixture of V(III) and V(IV) sulfuric acid solution. Shanghai Advanced Graphite Material Co. Ltd, China) was used Previous studies have noted that the concentration of V(IV) and as the working electrode. The working area of the SPGR was acid as well as the operating temperature have important effects ∼0.28 cm2. This was ground with silicon carbide papers (down on the physicochemical properties and electrochemical activity to 2,000 grit in grain size) and thoroughly rinsed with deionized of the positive electrode reaction (Sum et al., 1985; Kazacos water and alcohol before use. et al., 1990; Zhong and Skyllas-Kazacos, 1992; Iwasa et al., 2003; All chemicals used in this work were analytically pure Yi et al., 2003; Liu et al., 2011). However, few studies have agents and all solutions were prepared with deionized reported on the negative process. Sun and Skyllas-Kazacos (Sum water. V(III) acidic solutions were initially prepared by the and Skyllas-Kazacos, 1982) investigated the electrochemical electrochemical reduction of VOSO4 with an electrolytic behavior of the V(III)/V(II) redox couple at glassy carbon cell and then diluted to produce solutions with the electrodes using cyclic voltammetry (CV). They found that required H+ and V(III) concentrations. In addition, the the oxidation/reduction reaction is electrochemically irreversible concentration of the electrolytes was measured with a ultraviolet and the surface preparation is very critical in determining the spectrometer (TU-1900; Persee General Instrument Co. Ltd, electrochemical behavior. Yamamura et al. (2005) determined the Beijing, China). standard rate constants of the electrode reactions of vanadium on different carbon electrodes. Most studies (Sum and Skyllas- Kazacos, 1982; Oriji et al., 2005; Lee et al., 2012; Aaron Physical Characterization of the Electrolyte et al., 2013; Sun et al., 2016) found that the electrode reaction The viscosity was measured by means of an Ubbelohde rate of V(III)/V(II) is much less than that of V(IV)/V(V); viscometer. The electrical conductivity was determined using however, systematic investigations into the detailed mechanism a conductivity meter (Mettler Toledo) at 293K. The surface remain scarce. tensions of the solutions were measured by the bubble- Owing to the sluggish kinetics of V(III)/V(II) and the pressure method. significant hydrogen evolution reaction, the negative process contributes almost 80% polarization during the discharging process (Sun et al., 2016). Agar et al. (2013) further verified Electrochemical Measurements that the negative electrode process was the limiting factor in The electrochemical measurements were performed using a VFB performance by using an asymmetric cell configuration. Reference 600 electrochemical workstation (Gamry Instruments, As the key factors influencing electrode/electrolyte interfacial USA) with a conventional three-electrode cell with an SPGR reactivity, the concentration and physicochemical properties of as the working electrode, a platinum plate as the counter the V(III) acidic electrolyte as well as the temperature play electrode, and a saturated calomel electrode as the reference an important role in the redox reaction of V(III)/V(II) (Xiao electrode. A salt bridge was used to eliminate the liquid junction et al., 2016). For instance, the viscosity of the electrolyte potential between the Luggin capillary and the working electrode. affects the mass transfer kinetics and the conductivity directly The electrolyte was purged with nitrogen for 10 min before the influences the reversibility of the electrochemical reaction, which electrochemical test to reduce the influence of oxygen on the both depend on the concentration of vanadium and H2SO4 electrochemical oxidation of V(II). Temperature was controlled (Zhang, 2014). In
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