Engineering porous electrodes for next-generation redox flow batteries: recent progress and opportunities

Redox flow batteries are a promising electrochemical technology for energy-intensive grid storage applications, but further cost reductions are needed for universal adoption. As porous electrodes are responsible for functions within the flow cell that impact charge transfer, ohmics, and mass transport, improvements in electrode materials and design may yield significant performance and economic benefits. This mini-review summarizes recent developments in the design and characterization of porous electrodes with a focus on understanding and controlling both the microstructure and surface chemistry, which broadly align with mass transport and reaction kinetics. Key opportunities and challenges in the science and engineering of these materials are also presented with the goal of engaging the broader community and accelerating progress towards chemistry-specific flow battery electrodes.     

Kinetics of multiple electron transfer reactions at porous electrodes under stationary and flow conditions

The kinetics of consecutive two-electron transfer reactions at porous flooded electrodes are investigated under both stationary and flow conditions, where mass transfer is due respectively to diffusion and forced convection. The current-polarization relations were calculated for both modes of mass transfer as a function of the specific surface area of the electrode, the rates of the respective steps of the electron transfer reaction and the appropriate mass transfer coefficients. The computed solutions degenerate to the known limiting cases of single electron transfer control under conditions of very high or very low polarizations. Thus, at high anodic polarization, the electrochemical reaction is controlled by a single electron transfer step, the other step being too fast. Under conditions of 0.1<i/i_L<1, the overall reaction rate is controlled by both mass transfer and electrochemical activation. For flooded diffusion electrodes, the current-voltage curves follow the Tafel equation with a slope of double the normal value. This is attributed to mass transfer control in agreement with previous work. Experimental results, obtained on the porous flow-through electrode, agreed well with the theoretical predictions. The calculations presented here enable a quantitative evaluation of the relative influence of the rate of any step on the overall behaviour of the electrode under the appropriate experimental conditions.     

A Self‐Sampling‐and‐Flow Biosensor for Continuous Monitoring

A self‐sampling‐and‐flow biosensor was fabricated by sandwiching a nitrocellulose strip on the working electrode side of the double‐sided microporous gold electrodes and a wicking pad on the counter electrode side. The double‐sided microporous electrodes were formed by plasma sputtering of gold on a porous nylon substrate. Sample was taken up to the enzyme‐immobilized working electrode by the capillary action of the front nitrocellulose strip dipped into the sample solution, analyzed electrochemically at the enzyme‐immobilized electrode, and diffuses out to the backside wicking pad through the micropores of the electrodes, constituting a complete flow cell device with no mechanical liquid‐transporting device. Biosensor was formed by co‐immobilizing the glucose oxidase and electron transfer mediator (ferrocene acetic acid) on the thioctic acid self‐assembled monolayer‐modified working electrode. A typical response time of the biosensor was about 5 min with the sensitivity of 2.98 nA/mM glucose, providing linear response up to 22.5 mM. To demonstrate the use of self‐sampling‐and‐flow biosensor, the consumption rate of glucose in the presence of yeast was monitored for five days.     

Developments in plane parallel flow channel cells

Plane parallel electrodes are favoured, in laboratory studies and industry, for electrosynthesis, environmental treatment and energy conversion. This electrode geometry offers uniform current distribution, while a flow channel ensures a controlled reaction environment. Performance can be enhanced by the use of tailored electrode surfaces, porous, three-dimensional (3D) electrodes and bipolar electrical connections. Scale-up can be achieved by increasing the electrode size, the number of electrodes in a stack, or the number of stacks in a system. Recent trends include (a) 3D printing of fast prototype cell components, (b) use of porous 3D electrode supports and their decoration, (c) development of microflow cells for electrosynthesis, (d) anodic Fenton oxidations for wastewater treatment and (e) computational models to simulate and rationalise reaction environment and performance. Future research needs are highlighted.     

3D-printed porous electrodes for advanced electrochemical flow reactors: A Ni/stainless steel electrode and its mass transport characteristics

Porous electrodes have shown high performance in industrial electrochemical processes and redox flow batteries for energy storage. These materials offer great advantages over planar electrodes in terms of larger surface area, superior space time yield and enhanced mass transport. In this work, a highly ordered porous stainless steel structure was manufactured by 3D-printing and coated with nickel from an acidic bath by electrodeposition in a divided rectangular channel flow cell. Following the electrodeposition, the volumetric mass transport coefficient of this electrode was determined by the electrochemical reduction of 1.0×10⁻³ mol dm⁻³ of ferricyanide ions by linear sweep voltammetry and chronoamperometry. The convection diffusion characteristics are compared with other geometries to demonstrate the novelty and the advantages of 3D-printed porous electrodes in electrochemical flow reactors. Robust porous electrodes with tailored surface area, composition, volumetric porosity and flow properties are possible.     

Electrocatalytic oxidation of reduced nicotinamide adenine dinucleotide (NADH) at thick-film gold electrodes

Cyclic voltammetric and electrochemical impedance spectroscopic investigations of screen-printed, thick-film gold electrodes reveal significant differences when compared with conventional polished gold disk electrodes of comparable size. The rough and porous structure of the thick-film electrode surface leads to an actual electrode area which is increased six-fold compared to polished disk electrodes. Due to the catalytic properties of these surface structures it is possible to perform the electrochemical oxidation of reduced nicotinamide adenine dinucleotide (NADH) at relatively low overpotentials, i.e. +0.145 V vs. SCE. By operating electrodes at this potential, electrode fouling processes and interference from electroactive species, e.g. acetaminophen, are minimized. An amperometric glucose sensor based on polymer matrix-entrapped glucose dehydrogenase with a working potential of +0.145 V vs. SCE was successfully incorporated into a flow injection analysis (FIA) system.     

直接甲醇燃料电池纳米结构电催化材料及多孔电极研究

直接甲醇燃料电池(DMFC)因其燃料能量密度高,工作温度低,低污染排放等优点被认为是用作移动设备电源的最佳选择之一,至今已有美国的Oorja Protonics公司和丹麦的IRD公司等新能源相关企业相继发布了多款用于手机、电脑、通信基站、叉式装卸机或房车的商业产品.然而, DMFC内部的复杂情况造成的多种不同的电压损失仍旧使得其实际电压效率远低于理论值.其中从阳极渗透到阴极的甲醇造成的混合电位导致的电压损失尤为明显.目前,众多研究人员都致力于开发高稳定性、高耐久性、高性能且低成本的催化材料体系,以克服传统Pt催化剂存在的各种问题.除了催化剂本身之外, DMFC的问题还与其中膜电极的微结构和电化学特性息息相关.膜电极是化学能通过电催化氧化还原反应转化为电能的反应场所,通常由阳极扩散层、阳极催化层、质子交换膜、阴极催化层和阴极扩散层依序组合而成.通过对MEA中的各层进行优化,如传质管理和甲醇渗透等问题都能得到有效解决.
　　近年来,纳米技术常被用于改进DMFC性能的研究.具备纳米结构的金属-碳/金属氧化物载体类催化材料得到了广泛研究.这些电催化材料在制备方法、结构和组分上都有较大区别.结构方面,许多研究都证明制备纳米级多孔网络结构或者有序阵列结构的催化层有助于提高催化性能和Pt的利用率.组分方面,许多研究人员都开展了引入Pt以外金属成分或金属氧化物来改变Pt催化剂的表面电子状态的研究.引入这些组分导致的配位体效应可以通过弱化Pt与H+, OH-或COads等的相互作用来起到抗催化毒化和提高催化效率的作用.尽管对于DMFC领域的认知逐渐完善,但是仍有许多问题有待解决.因此,本文介绍了目前用于DMFC的纳米结构电催化材料和多孔电极的研究进展.重点介绍了纳米结构催化剂和载体材料的合成及表征.
　　通过对比不同催化材料的特性可以发现,在本文涉及到的催化材料中, In0.1SnO2-Pt和(MoO3)0.2SnO2-Pt/C表现出了最高的催化活性,但是它们高效催化甲醇电氧化所需的碱性环境与现在占绝对主流地位的Nafion质子交换膜所必须的酸性环境相冲突,所以其实际应用价值在碱性阴离子交换膜研究取得突破前都难以有效发挥.而另一类表现较好的采用溶致液晶模板法合成的纳米树枝状和纳米星形Pt催化剂则存在制备工艺难以商业规模化的问题.总的来说,采用溶剂热合成法制备的Pt-NRCeO2/GNs和Pt/Ti0.9Sn0.1O2-C等纳米结构金属氧化物、碳材料复合载体和Pt基贵金属催化剂组成的催化材料体系不仅催化性能相对于商业化Pt纳米颗粒有很大提高,而且制备方法易于商业规模化,值得进一步关注.此外,本文还介绍了如内部传质过程的理论建模计算和膜电极中功能结构的制备等优化DMFC中多孔电极内传质过程的方法.通过计算机模拟得到优化DMFC内部传质过程所需的扩散层、催化层的传质特性相关参数,再通过改进MEA制备工艺,有效控制各层的结构参数向模拟的优化值靠拢,能够实现DMFC性能的有效提升.综合模拟、实验研究及工艺研究结果,根据实际需要,设计和制备包含新功能层的MEA的相关研究也更进一步提高了DMFC的性能和实用性.就目前的研究情况而言,如果在性能提升的基础上,使用寿命再取得突破, DMFC一定会有很好的商业应用前景.     

Principles and Analytical Applications of Heated Electrodes

This article reviews the development of the various heated electrodes, heating devices and their analytical applications which have been published during the last decades. Generally spoken, electrode heating can provide different positive effects on electrochemical measurements: mass transport enhancement, reaction kinetics acceleration and the removal of deposited substances from the electrode surface. This often leads to remarkably improved signal-to-noise characteristics in electroanalytical chemistry. Short heat pulses or direct heating of very small electrolyte compartments allow for temperatures far above the boiling point of the solution. Major application fields include trace metal and nucleic acids analysis. Future development will result in miniaturized selectively heated electrode arrays.     

Dielectrophoretic cell trapping for improved surface plasmon resonance imaging sensing

The performance of conventional surface plasmon resonance (SPR) biosensors can be limited by the diffusion of the target analyte to the sensor surface. This work presents an SPR biosensor that incorporates an active mass‐transport mechanism based on dielectrophoresis and electroosmotic flow to enhance analyte transport to the sensor surface and reduce the time required for detection. Both these phenomena rely on the generation of AC electric fields that can be tailored by shaping the electrodes that also serve as the SPR sensing areas. Numerical simulations of electric field distribution and microparticle trajectories were performed to choose an optimal electrode design. The proposed design improves on previous work combining SPR with DEP by using face‐to‐face electrodes, rather than a planar interdigitated design. Two different top‐bottom electrode designs were experimentally tested to concentrate firstly latex beads and secondly biological cells onto the SPR sensing area. SPR measurements were then performed by varying the target concentrations. The electrohydrodynamic flow enabled efficient concentration of small objects (3 μm beads, yeasts) onto the SPR sensing area, which resulted in an order of magnitude increased SPR response. Negative dielectrophoresis was also used to concentrate HEK293 cells onto the metal electrodes surrounded by insulating areas, where the SPR response was improved by one order of magnitude.     

Comparison of temperature and work function measurements obtained with different GTA electrodes

This work was carried out on one standard electrode (W-ThO₂,) and other electrodes developed by additions of La₂O₃, CeO₂, and Y₂O₃,. The effect of rare-earth metal oxides on GTAW electrode phenomena, concerning electrode temperature, emissivity, and work function, was analyzed and compared from the point of view of those oxides' behavior during arcing. The experimental results indicate that the electrode temperature, emissivity, and work (unction .strongly depend on the behavior of the rare-earth metal oxides during arcing. The investigation demonstrates good stability of La₂O₃ during arcing compared with the other oxides. The temperature distributions along the electrode axis of these electrodes were measured by using infrared pyrometer and grooved electrodes. The W-La₂O₃ electrode showed the lowest temperature values, followed by W-CeO₂ and W-ThO₂ electrodes in that order. Also W-La₂O₃ electrodes have a higher emissivity and lower work Junction, followed by W-CeO₂ and W-ThO₂ electrodes in that order.     

Modeling of electrochemical process in flow 3D electrode with account for distribution of flow velocity of electrolyte in electrode

A mathematical model of the electrochemical metal deposition process in a flow 3D electrode is developed with account for dynamic distribution of the flow velocity of electrolyte, metal mass, potential, porosity, conductivity, specific electrode surface area, and other characteristics in the local volume of the electrode. These characteristics of the process and electrode are considered as functions of time and coordinate within the electrode. The results of experimental studies and calculations of copper electrodeposition process from ammonium sulfate electrolyte onto cathodes of graphitized carbon fibrous materials with different conductivity are presented at different initial flow velocities of electrolyte.     

Insightful understanding of three-phase interface behaviors in 1T-2H MoS2/CFP electrode for hydrogen evolution improvement

Hydrogen evolution reaction (HER) catalytic electrodes under actual working conditions show interesting mass transfer behaviors at solid (electrode)/liquid (electrolyte)/gas (hydrogen) three-phase interfaces. These behaviors are essential for forming a continuous and effective physical contact region between the electrolyte and the electrode and require further detailed understanding. Here, a case study on 1T-2H phase molybdenum disulfide (MoS₂)/carbon fiber paper (CFP) catalytic electrodes is performed. Rapid gas-liquid mass transfer at the interface for enhancing the working area stability and capillarity for increasing the electrode working area is found. The real scenario, wherein the energy utilization efficiency of the as-prepared non-noble metal catalytic electrode exceeds that of the noble metal catalytic electrode, is disclosed. Specifically, a fluid dynamics model is developed to investigate the behavior mechanism of hydrogen bubbles from generation to desorption on the catalytic electrode surface with different hydrophilic and hydrophobic properties. These new insights and theoretical evidence on the non-negligible three-phase interface behaviors will identify opportunities and motivate future research in high-efficiency, stability, and low-cost HER catalytic electrode development.     

A copper ion-selective electrode with high selectivity prepared by sol-gel and coated wire techniques

A sol-gel electrode and a coated wire ion-selective poly(vinyl chloride) membrane, based on thiosemicarbazone as a neutral carrier, were successfully developed for the detection of Cu (II) in aqueous solutions. The sol-gel electrode and coated electrode exhibited linear response with Nernstian slopes of 29.2 and 28.1 mV per decade respectively, within the copper ion concentration ranges 1.0×10^–5–1.0×10^–1 M and 6.0×10^–6–1.0×10^–1 M for coated and sol-gel sensors. The coated and sol-gel electrodes show detection limits of 3.0×10^–6 and 6.0×10^–6 M respectively. The electrodes exhibited good selectivities for a number of alkali, alkaline earth, transition and heavy metal ions. The proposed electrodes have response times ranging from 10–50 s to achieve a 95% steady potential for Cu²⁺ concentration. The electrodes are suitable for use in aqueous solutions over a wide pH range (4–7.5). Applications of these electrodes for the determination of copper in real samples, and as an indicator electrode for potentiometric titration of Cu²⁺ ion using EDTA, are reported. The lifetimes of the electrodes were tested over a period of six months to investigate their stability. No significant change in the performance of the sol-gel electrode was observed over this period, but after two months the coated wire copper-selective electrode exhibited a gradual decrease in the slope. The selectivity of the sol-gel electrode was found to be better than that of the coated wire copper-selective electrode. Based on these results, a novel sol-gel copper-selective electrode is proposed for the determination of copper, and applied to real sample assays.     

Insights into analyte electrolysis in an electrospray emitter from chronopotentiometry experiments and mass transport calculations

Insights into the electrolysis of analytes at the electrode surface of an electrospray (ES) emitter capillary are realized through an examination of the results from off-line chronopotentiometry experiments and from mass transport calculations for flow through tubular electrodes. The expected magnitudes and trends in the interfacial potential in an ES emitter under different solution conditions and current densities, using different metal electrodes, are revealed by the chronopotentiometry data. The mass transport calculations reveal the electrode area required for complete analyte electrolysis at a given volumetric flow rate. On the basis of these two pieces of information, the design of ES emitters that may maximize and those that may minimize analyte electrolysis during ES mass spectrometry are discussed.     

Microband electrodes of ideal and nonideal geometries: AC impedance spectroscopy

The AC impedance behavior of microband electrode geometries which deviate from the ideal is derived via numerical modelling of the chronoamperometric response under diffusion-only conditions. Specifically attention is given to four electrode shapes in addition to the ideal microband geometry: elevated microband electrodes (with conducting supporting sides), recessed microband electrodes (with insulating pit walls), platform electrodes (with insulating supporting sides) and, for the purposes of comparison, a hypothetical line electrode without any support which permits diffusional mass transport to both sides of the infinitesimally thin electrode. Simple analytical expressions are established for the frequency dependence of the AC impedance in each case.     

Electrochemical Studies of Chemically Modified Nanometer‐Sized Electrodes

Self‐assembled monolayers (SAMs) of 4‐aminothiophenol (4‐ATP) has been successfully deposited onto nanometer‐sized gold (Au) electrodes. The cyclic voltammograms obtained on a 4‐ATP SAMs modified electrode show peaks and the peak height is proportional to the scan rate, which is similar to that on an electroactive SAMs modified macro electrode. The electrochemical behavior and mechanism of outer‐sphere electron transfer reaction on the 4‐ATP SAMs modified nanometer‐sized electrode has also been studied. The 4‐ATP SAMs modified electrode is further modified with platinum (Pt) nanoparticles. Electrochemical behaviors show that there is electrical communication between Pt nanoparticles and Au metal on the Pt nanoparticles/4‐ATP SAMs/Au electrode. However, scanning electron microscopic image shows that the Pt nanoparticles are not evenly covered the electrode.     

Enhancement of Anodic Response for DMSO at Ruthenium Oxide Film Electrodes as a Result of Doping with Iron(III)

The oxidation of dimethyl sulfoxide (DMSO) to dimethyl sulfone (DMSO₂) is representative of numerous anodic oxygen‐transfer reactions of organosulfur compounds that suffer from slow kinetics at noble metal electrodes. Anodic voltammetric data for DMSO are examined at various RuO₂‐film electrodes prepared by thermal deposition on titanium substrates. The response for DMSO is slightly larger at RuO₂ films prepared in a flame as compared with films prepared in a furnace; however, temperature is more easily controlled in the furnace. Doping of the RuO₂ films with Fe(III) further improves the sensitivity of anodic response for DMSO. Optimal response is obtained at an Fe(III)‐doped RuO₂‐film electrode prepared using a deposition solution of 50 mM RuCl₃ and 10 mM FeCl₃ in a 1 : 1 mixture of isopropanol and 12 M HCl at an annealing temperature of 450 °C. The Levich plot (i vs. ω^1/2) and Koutecky‐Levich plot (1/i vs. 1/ω^1/2) of amperometric data for the oxidation of DMSO at an Fe(III)‐doped RuO₂‐film electrode configured as a rotated disk are consistent with an anodic response controlled by mass‐transport processes at low rotational velocities. Flow injection data demonstrate that Fe(III)‐doped RuO₂‐film electrodes exhibit detection capability for methionine and cysteine in addition to DMSO. Detection limits for 100‐μL injections of the three compounds are ca. 3.2×10^?4 mM, i.e., ca. 32 pmol.     

Dynamics of the filling of a porous cathode by the deposited metal: Modeling the process and analyzing the case of high cathode conductance and low solution depletion degree

A dynamic model for a porous electrode is designed on the basis of a one-dimensional representation of the electrode in the form of parallel filaments. The method takes into account the alterations in the local values of the filament diameter (and, correspondingly, in the effective conductances of phases), porosity, the velocity of a linear flow, and the mass transfer coefficient for the deposited metal ions, which occur in the course of the metal electrodeposition. For the simplest version of dynamics, at a high initial conductance of the electrode and a small solution depletion degree, the method predicts the following specific features: (i) the development of the working surface area and an increase in the current efficiency for the metal associated with it, (ii) a decrease in the metal penetration depth into the electrode with time and the metal localization near the most loaded end, and (iii) an irregular change in the current efficiency and concentration of the metal at the exit out of the electrode.Translated from Elektrokhimiya, Vol. 41, No. 3, 2005, pp. 333–342.Original Russian Text Copyright © 2005 by Maslii, Poddubnyi, Medvedev.     

Tungsten electrode for urea

Tungsten electrodes for urea were prepared via covalent linking of urease on oxidized metal surfaces in different ways. The most stable electrodes were obtained when tungsten was silanized and activated by glutaraldehyde or hexamethylene diisocyanate. The electrode with urease coupled via glutaraldehyde was tested for optimum conditions of use. The nature of the buffer and its concentration and ionic strength are particularly important.     

An Air‐breathing Carbon Cloth‐based Screen‐printed Electrode for Applications in Enzymatic Biofuel Cells

We report a prototype air‐breathing carbon cloth‐based electrode that was fabricated starting from a commercially available screen‐printed electrode equipped with a transparent ITO working electrode (DropSens, ref. ITO10). The fabrication of the air‐breathing electrodes is straightforward, shows satisfactory reproducibility and a good electrochemical response as evaluated by means of [Fe(CN)₆]^3?/4? voltammetry. The gas‐diffusion electrodes were successfully modified with the O₂ reducing enzyme bilirubin oxidase from Myrothecium verrucaria in a direct electron transfer regime. The enzyme modified electrodes showed a remarkable high current density for O₂ reduction in passive air‐breathing mode of up to 5 mA cm^?2. Moreover, the enzyme modified electrodes were applied as O₂ reducing biocathodes in a glucose/air enzymatic biofuel cell in combination with a high current density glucose oxidase/redox polymer bioanode. The biofuel cell provides a high maximum power density of (0.34±0.02) mW cm^?2 at 0.25 V. The straightforward design, low cost and the high reproducibility of these electrodes are considered as basis for standardized measurements under gas‐breathing conditions and for high throughput screening of gas converting (bio‐)catalysts.