In operando synchrotron X-ray radiography studies of polymer electrolyte membrane water electrolyzers

Polymer electrolyte membrane water electrolysis (PEL) cells are studied in-operando by synchrotron X-ray radiography. Two-phase flow phenomena associated with the evolution of oxygen and hydrogen in the surrounding water are investigated on a running electrolyzer cell. We examine the gas bubble discharge from the porous transport layer (PTL) into the flow channel and discuss the transport of bubbles in the flow channel. The transport of gas inside the PTL and the number of gas bubble discharge sites is examined and correlated with current density.     

电池电极反应的新应用：分步法电解制氢气

可再生能源与电解水制氢技术的结合是实现可持续制氢的最佳途径. 然而,传统电解水技术中解决氢-氧同时、同步、同地产生的问题必须依赖于膜分离技术,大幅限制了氢-氧分离和氢气异地运输的灵活性,并阻碍了可再生能源(如风能、太阳能)与电解水技术的直接结合. 针对上述问题,作者课题组在近期提出了基于电池电极反应的分步法电解水制氢技术,即通过电池电极的可逆电化学反应将现有电解水过程拆分为制氢和制氧分立步骤,实现在无膜条件下氢气和氧气的分时、分地交替制备,提升了电解水制氢的灵活性,促进了可再生能源向氢能的直接转化. 本文将介绍这一新技术的研究进展,并分析这一技术的优点和面临的挑战.     

不同浸润性多孔电极表面的气泡行为

采用氢气模板法制备了具有多孔结构的电极; 通过改变电镀电流密度和电镀时间实现了电极表面多孔结构孔径和分布的控制; 通过改变表面化学组成有效调控了电极表面的浸润性质. 比较了具有不同微观结构和表面化学组成的电极在给定条件下电解水过程中气泡的产生及行为机制. 实验结果表明: 相对于亲水的多孔电极, 疏水的多孔电极表面能够黏附气泡, 更易倾向于形成稳定的气膜; 多孔结构对于亲水电极表面气泡行为的影响比对疏水电极表面气泡行为的影响更为显著; 与没有多孔结构的亲水电极相比, 具有多孔结构的亲水电极表面产生的气泡数量多, 速率快; 与较小孔径的多孔亲水电极相比, 较大孔径的多孔亲水电极表面产生气泡速率快且黏附气泡数量少. 该研究结果为微气泡减阻电极的设计提供了理论依据.     

Advances,opportunities, and challenges of hydrogen and oxygen production from seawater electrolysis: An electrocatalysis perspective

With increasing energy consumption and greenhouse gas emissions, the importance of developing renewable energy sources to replace fossil fuels has become a vital global task. Hydrogen produced via water electrolysis powered by renewable energy systems at a large scale is an essential measure to reduce greenhouse gas and particulate emissions. Electrolysers use a substantial amount of water (mainly freshwater) to produce hydrogen and oxygen at the cathode, and anode, respectively. However, seawater is preferred because it is the most abundant water resource. Although many R&D efforts on seawater electrolysis have been carried out since the 1970s, the barriers are the undesired chlorine gas evolution reaction at the anode, and corrosion induced by chloride ions. Unlike the available data for electrocatalyst materials based upon platinum group metals in pure solutions, limited data is available for electrocatalysts in seawater. Therefore, there is an urgent need to develop new electrocatalysts for seawater electrolysis.     

The potential of proton exchange membrane–based electrolysis technology

Hydrogen is an important chemical feedstock for many industrial applications, and today, more than 95% of this feedstock is generated from fossil fuel sources such as reforming of natural gas. In addition, the production of hydrogen from fossil fuels represents most carbon dioxide emissions from large chemical processes such as ammonia generation. Renewable sources of hydrogen such as hydrogen from water electrolysis need to be driven to similar production costs as methane reforming to address global greenhouse gas emission concerns. Water electrolysis has begun to show scalability to relevant capacities to address this need, but materials and manufacturing advancements need to be made to meet the cost targets. This article describes specific needs for one pathway based on proton exchange membrane electrolysis technology.     

An alternative approach to selective sea water oxidation for hydrogen production

Sea water electrolysis is one of the promising ways to produce hydrogen since it is available in plentiful supply on the earth. However, in sea water electrolysis toxic chlorine evolution is the preferred reaction over oxygen evolution at the anode. In this work, research has been focused on the development of electrode materials with a high selectivity for oxygen evolution over chlorine evolution. Selective oxidation in sea water electrolysis has been demonstrated by using a cation-selective polymer. We have used a perm-selective membrane (Nafion^®), which electrostatically repels chloride ions (Cl⁻) to the electrode surface and thereby enhances oxygen evolution at the anode. The efficiency and behaviour of the electrode have been characterized by means of anode current efficiency and polarization studies. The surface morphology of the electrode has been characterized by using a scanning electron microscope (SEM). The results suggest that nearly 100% oxygen evolution efficiency could be achieved when using an IrO₂/Ti electrode surface-modified by a perm-selective polymer.     

Bubble‐free electrokinetic flow with propylene carbonate

For electroosmotic pumping, a large direct‐current (DC) electric field (10+ V/cm) is applied across a liquid, typically an aqueous electrolyte. At these high voltages, water undergoes electrolysis to form hydrogen and oxygen, generating bubbles that can block the electrodes, cause pressure fluctuations, and lead to pump failure. The requirement to manage these gases constrains system designs. This article presents an alternative polar liquid for DC electrokinetic pumping, propylene carbonate (PC), which remains free of bubbles up to at least 10 kV/cm. This offers the opportunity to create electrokinetic devices in closed configurations, which we demonstrate with a fully sealed microfluidic hydraulic actuator. Furthermore, the electroosmotic velocity of PC is similar to that of water in PDMS microchannels. Thus, water could be substituted by PC in existing electroosmotic pumps.     

A miniature, nongassing electroosmotic pump operating at 0.5 V

Electroosmotic pumps are arguably the simplest of all pumps, consisting merely of two flow-through electrodes separated by a porous membrane. Most use platinum electrodes and operate at high voltages, electrolyzing water. Because evolved gas bubbles adhere and block parts of the electrodes and the membrane, steady pumping rates are difficult to sustain. Here we show that when the platinum electrodes are replaced by consumed Ag/Ag(2)O electrodes, the pumps operate well below 1.23 V, the thermodynamic threshold for electrolysis of water at 25 °C, where neither H(2) nor O(2) is produced. The pumping of water is efficient: 13?000 water molecules are pumped per reacted electron and 4.8 mL of water are pumped per joule at a flow rate of 0.13 mL min(-1) V(-1) cm(-2), and a flow rate per unit of power is 290 mL min(-1) W(-1). The water is driven by protons produced in the anode reaction 2Ag(s) + H(2)O → Ag(2)O(s) + 2H(+) + 2e(-), traveling through the porous membrane, consumed by hydroxide ions generated in the cathode reaction Ag(2)O(s) + 2 H(2)O + 2e(-) → 2Ag(s) + 2 OH(-). A pump of 2 mm thickness and 0.3 cm(2) cross-sectional area produces flow of 5-30 μL min(-1) when operating at 0.2-0.8 V and 0.04-0.2 mA. Its flow rate can be either voltage or current controlled. The flow rate suffices for the delivery of drugs, such as a meal-associated boli of insulin.     

Electrolysis of ammonia for hydrogen production catalyzed by Pt and Pt-Ir deposited on nickel foam

Electrolysis of ammonia in alkaline electrolyte solution was applied for the production of hydrogen. Both Pt-loaded Ni foam and Pt-Ir loaded Ni foam electrodes were prepared by electrodeposition and served as anode and cathode in ammonia electrolytic cell, respectively. The electrochemical behaviors of ammonia in KOH solution were individually investigated via cyclic voltammetry on three electrodes, i.e. bare Ni foam electrode, Pt-loaded Ni foam electrode and Pt-Ir loaded Ni foam electrode. The morphology and composition of the prepared Ni foam electrode were analyzed by scanning electron microscopy (SEM) and X-ray diffraction (XRD). Effects of the concentration of electrolyte solution and temperature of electrolytic cell on the electrolysis reaction were examined in order to enhance the efficiency of ammonia electrolysis. The competition of ammonia electrolysis and water electrolysis in the same alkaline solution was firstly proposed to explain the changes of cell voltage with the electrolysis proceeding. At varying current densities, different cell voltages could be obtained from galvanostatic curves. The low cell voltage of 0.58 V, which is less than the practical electrolysis voltage of water (1.6 V), can be obtained at a current density of 2.5 mA/cm². Based on some experimental parameters, such as the applied current, the resulting cell voltage and output of hydrogen gas, the power consumption per gram of H₂ produced can be estimated.     

“绿氢”工业化碱性催化剂研究现状及未来展望

电解水制氢技术的发展对于加快实现全球碳中和目标具有重要意义。然而,碱性介质中缓慢的析氢/析氧反应动力学过程目前是阻碍该技术发展的瓶颈问题。基于此,本文首先综述了碱性环境下析氢反应与析氧反应不同的动力学理论机制,总结了针对改善动力学反应过程的理论设计策略。随后,介绍了目前电解水催化剂的设计理念及方向。对新兴的“绿氢”技术而言,探索在高电流密度下高性能电催化剂对这项技术在工业化应用推广中起着核心作用。同时,大规模合成策略是辅助合成工业电极的关键技术。进一步,我们在推进“绿氢”工业化应用的基础上总结了目前常用三种电解槽,介绍了目前电解槽设计的局限性及对应解决方案。总之,深入研究适用于碱性环境中的工业电催化剂、商业膜或电解槽的设计,提高对工业设计原则的理解,对于获得效率更高、安全性更高、实用性更强的工业电解槽具有重要意义。     

High purity oxygen production with a polymer electrolyte membrane electrolyser

Oxygen is required for treatment of patients in hospitals and at home, in industrial processes and for fuel combustion. Most commonly oxygen is produced by cryogenic or pressure swing adsorption routes. Other techniques include oxygen-ion conducting ceramic membranes, polymer membranes and chemical processes used mainly in civil aviation to reduce the condition of hypoxia at high altitudes. Water electrolysis is used mainly for the production of hydrogen with oxygen as a by-product. In order to use this system only for oxygen production, hydrogen must be utilised and disposed off safely. This, however, is not practical in many instances where there is no use for hydrogen and it poses an explosion hazard. In this paper, an electrolyser system based on polymer electrolyte membrane is described in which hydrogen produced on one side of the electrochemical cell is consumed by combining it with atmospheric oxygen, through operating the cell in a carefully configured fuel cell mode. This reduces the power consumed in the electrolysis operation by more than 35% and eliminates hydrogen in exit gases. Oxygen generated is of high quality and can be used for human consumption (portable and plug-in home care oxygen therapy devices, in hospitals, defence or aerospace requirements) and for many other industrial applications.     

Reversible Solid Oxide Fuel Cell for Power Accumulation and Generation

The anodic and cathodic polarization dependences for the oxygen electrode based on lanthanum-strontium manganite and the fuel Ni-cermet electrode are studied in the temperature range of 700–900°С in gas media that correspond to working conditions of a reversible fuel cell. The temporal behavior of these electrodes is studied in the course of periodic polarity changes of current with the density of 0.5 A/cm². The electrode overvoltage is shown to be about 0.1 V in modes of power generation and water electrolysis at 900°С and the current density of 0.5 A/cm². A single electrolyte supported tubular solid-oxide fuel cell was fabricated and tested in the fuel-cell and hydrogen-generation modes. It is found that at 900°С and overvoltage of 0.7 V, the cell generates the specific electric power of 0.4 W/cm² when the 50% H2 + 50% H₂O gas mixture is used as the fuel and air is used as the oxidizer. At the water electrolysis with the current density of 0.5 A/cm², which under normal conditions corresponds to generation of about 0.2 and 0.1 L/h of hydrogen and oxygen, respectively, the consumed power is about 0.55 W/cm². The efficiency of the conversion cycle electric power–hydrogen–electric power is 70–75%.     

Phenazine-based Compound Realizing Separate Hydrogen and Oxygen Production in Electrolytic Water Splitting

Electrocatalytic water splitting powered by renewable energy is a sustainable approach for hydrogen production. However, conventional water electrolysis may suffer from gas mixing, and the different kinetics between hydrogen evolution reaction (HER) and oxygen evolution reaction (OER) will limit the direct use of unstable renewable energies, leading to increased cost of H₂ production. Herein, a novel phenazine-based compound is synthesized to develop the solid-state redox mediator associated water splititng process, and thus decoupling the H₂ and O₂ production in acid solution without the use of membrane. Excitingly, this organic redox mediator exhibits high specific capacity (290 mAh g⁻¹ at 0.5 A g⁻¹), excellent rate performance (186 mAh g⁻¹ at 30 A g⁻¹) and long cycle life (3000 cycles) due to its π-conjugated aromatic structure and the fast kinetics of H⁺ storage/release process. Furthermore, a membrane-free decoupled water electrolysis architecture driven by solar energy is achieved, demonstrating high-purity H₂ production at different times.     

Stable Potential Windows for Long‐Term Electrocatalysis by Manganese Oxides Under Acidic Conditions

Efficient, earth‐abundant, and acid‐stable catalysts for the oxygen evolution reaction (OER) are missing pieces for the production of hydrogen via water electrolysis. Here, we report how the limitations on the stability of 3d‐metal materials can be overcome by the spectroscopic identification of stable potential windows in which the OER can be catalyzed efficiently while simultaneously suppressing deactivation pathways. We demonstrate the benefits of this approach using gamma manganese oxide (γ‐MnO₂), which shows no signs of deactivation even after 8000 h of electrolysis at a pH of 2. This stability is vastly superior to existing acid‐stable 3d‐metal OER catalysts, but cannot be realized if there is a deviation as small as 50‐mV from the stable potential window. A stable voltage efficiency of over 70 % in a polymer–electrolyte membrane (PEM) electrolyzer further verifies the availability of this approach and showcases how materials previously perceived to be unstable may have potential application for water electrolysis in an acidic environment.     

Use of iridium oxide films as hydrogen gas evolution cathodes in aqueous media

Hydrous iridium oxide films are highly resistant to reduction under cathodic, hydrogen gas evolution, conditions in aqueous acid or base. Such behavior is not in agreement with simple thermodynamic (Pourbaix) data based on the assumption that the system behaves in a reversible manner. The barrier to reduction is attributed, as discussed earlier for RuO₂, to the involvement of high-energy intermediates (iridium atoms or microclusters of same) which can only be generated at unusually negative overpotential values evidently far into the hydrogen gas evolution region. Thermally prepared IrO₂/Ti electrodes are possible candidates for hydrogen gas evolution cathodes in water electrolysis cells; however, under extended operating conditions, the performance of these cathodes was found to deteriorate due to gradual shedding of the active oxide layer.     

Gas and liquid permeation properties of modified interfacial composite reverse osmosis membranes

Gas permeation tests using nitrogen, oxygen, hydrogen, helium and carbon dioxide were performed to assess how membrane modification procedures affect the separating layer morphology of thin-film composite reverse osmosis membranes. Gas selectivity data provided evidence for the presence of nanoscale separating layer defects in dry samples of six commercial membrane types. These defects were eliminated when the membrane surface was coated with a polyether–polyamide block copolymer (PEBAX 1657), as indicated by a 25-fold decrease in gas permeance and at least a 2-fold increase in most selectivity values. Treatment with n-butanol followed by drying reduced water flux and gas flux by 30% and 75%, respectively, suggesting that using n-butanol as a solvent for applying coatings negatively affects membrane performance. The results of this study demonstrate that gas permeation measurements can be used to detect morphological features that impact gas and water membrane flux.     

氧分压对固体氧化物电解池性能的影响

High-temperature (700–900 ℃) steam electrolysis based on solid oxide electrolysis cells (SOECs) is valuable as an efficient and clean path for large-scale hydrogen production with nearly zero carbon emissions, compared with the traditional paths of steam methane reforming or coal gasification. The operation parameters, in particular the feeding gas composition and pressure, significantly affect the performance of the electrolysis cell. In this study, a computational fluid dynamics model of an SOEC is built to predict the electrochemical performance of the cell with different sweep gases on the oxygen electrode. Sweep gases with different oxygen partial pressures between 1.01 × 10³ and 1.0 × 10⁵ Pa are fed to the oxygen electrode of the cell, and the influence of the oxygen partial pressure on the chemical equilibrium and kinetic reactions of the SOECs is analyzed. It is shown that the rate of increase of the reversible potential is inversely proportional to the oxygen partial pressure. Regarding the overpotentials caused by the ohmic, activation, and concentration polarization, the results vary with the reversible potential. The Ohmic overpotential is constant under different operating conditions. The activation and concentration overpotentials at the hydrogen electrode are also steady over the entire oxygen partial pressure range. The oxygen partial pressure has the largest effect on the activation and concentration overpotentials on the oxygen electrode side, both of which decrease sharply with increasing oxygen partial pressure. Owing to the combined effects of the reversible potential and polarization overpotentials, the total electrolysis voltage is nonlinear. At low current density, the electrolysis cell shows better performance at low oxygen partial pressure, whereas the performance improves with increasing oxygen partial pressure at high current density. Thus, at low current density, the best sweep gas should be an oxygen-deficient gas such as nitrogen, CO₂, or steam. Steam is the most promising because it is easy to separate the steam from the by-product oxygen in the tail gas, provided that the oxygen electrode is humidity-tolerant. However, at high current density, it is best to use pure oxygen as the sweep gas to reduce the electric energy consumption in the steam electrolysis process. The effects of the oxygen partial pressure on the power density and coefficient of performance of the SOEC are also discussed. At low current density, the electrical power demand is constant, and the efficiency decreases with growing oxygen partial pressure, whereas at high current density, the electrical power demand drops, and the efficiency increases.     

Self-supported ultrathin Co3O4 nanoarray enabling efficient paired electrolysis of 5-hydroxymethylfurfural for simultaneous dihydroxymethylfuran (DHMF) and furandicarboxylic acid (FDCA) production

Production of value-added chemicals and fuels from biomass via electrochemical methods has been of emerging interest in light of the increasing environmental, economic, and political challenges. Paired electrolysis, with anodic oxidation and cathodic reduction reactions pairing in a single electrochemical cell, offers an effective way to produce desired products in both electrodes, thus achieving complete electron economy. In this work, an efficient 5-hydroxymethylfurfural (HMF) paired electrolysis system is developed over a self-supported ultrathin Co₃O₄ nanoarray electrocatalyst for simultaneous production of value-added 2,5-dihydroxymethylfuran (DHMF) and 2,5-furandicarboxylic acid (FDCA). The as-designed paired electrolysis cell achieves a high HMF conversion and DHMF/FDCA selectivity at both anode and cathode without external hydrogen and oxygen input. A near-quantitative yield (95.7%) of FDCA and 78.8% yield of DHMF can be achieved in the paired electrolysis system, with a total Faradaic efficiency of 127%. This work will open up new opportunities in designing efficient electrochemical devices to simultaneously produce building-block chemicals from biomass-derived molecules in both anode and cathode.     

Composite liquid membrane for enzyme electrode construction

Microporous polycarbonate membranes were treated with a lipid, isopropyl myristate. The resulting composites were used as external membranes for the construction of hydrogen peroxide-based glucose-detecting enzyme electrodes. The linearity of glucose electrodes was increased to well above the substrate physiological range; for treated membranes of pore size 0.015 μm, linearity was up to 100 mM of glucose. The electrode system had a greatly decreased dependence on temperature, solution pH and background oxygen levels. It also showed reduced interference from electrochemically active species in blood and eliminated the need for sample stirring. Use with whole blood indicated that the treated membrane also had good haemocompatibility, and blood measurements showed an acceptable correlation with a routine spectrophotometric method (y = 0.739x + 1.153; r = 0.969).