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        <p>JES is the flagship journal of The Electrochemical Society. Published continuously from 1902 to the present, JES remains one of the most highly-cited journals in electrochemistry and solid-state science and technology.</p>
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Mark Wightman and Christian Amatore</option><option value="/collections/1945-7111_focus_issue_165_15_Y15">Focus Issue on Electrocatalysis – In Honor of Radoslav Adzic</option><option value="/collections/1945-7111_focus_issue_165_4_Y5">Focus Issue on Processes at the Semiconductor–Solution Interface</option><option value="/collections/1945-7111_focus_issue_165_6_Y7">Focus Issue on Proton Exchange Membrane Fuel Cell (PEMFC) Durability</option><option value="/collections/1945-7111_focus_issue_165_8_Y9">Focus Issue on Ubiquitous Sensors and Systems for IoT</option><option value="/collections/1945-7111_focus_issue_164_1_Y1">Focus Issue of Selected Papers from IMLB 2016 with Invited Papers Celebrating 25
      Years of Lithium Ion Batteries</option><option value="/collections/1945-7111_focus_issue_164_10_Y11">Focus Issue on Oxygen Reduction and Evolution Reactions for High Temperature Energy Conversion and Storage</option><option value="/collections/1945-7111_focus_issue_164_3_Y3">Focus Issue on Biological Fuel Cells</option><option value="/collections/1945-7111_focus_issue_164_8_Y9">Focus Issue on Progress in Molten Salts and Ionic Liquids</option><option value="/collections/focus-issue_1945-7111_164_5_Y5">Focus Issue on Biosensors and Micro–Nano Fabricated Electromechanical Systems</option><option value="/collections/1945-7111_focus_issue_163_1_Y1">Focus Issue on Redox Flow Batteries–Reversible Fuel Cells</option><option value="/collections/1945-7111_focus_issue_163_11_Y19">Focus Issue on Electrolysis for Increased Renewable Energy Penetration</option><option value="/collections/1945-7111_focus_issue_163_12_Y21">Focus Issue on Electrochemical Deposition as Surface Controlled Phenomenon</option><option value="/collections/1945-7111_focus_issue_163_4_Y13">Focus Issue Honoring Allen J. Bard</option><option value="/collections/1945-7111_focus_issue_electrochemical_capacitors_fundamentals_to_applications">Electrochemical Capacitors: Fundamentals to Applications</option><option value="/collections/1945-7111_focus_issue_focus_issue_of_selected_presentations_from_IMLB_2014">Focus Issue of Selected Presentations from the International Meeting on Lithium Batteries (IMLB 2014)</option><option value="/collections/1945-7111_focus_issue_microfluidics_MEMS_NEMS_sensors_and_devices">Microfluidics, MEMS/NEMS, Sensors and Devices</option><option value="/collections/1945-7111_focus_issue_162_11_Y9">Focus Issue on Electrophoretic Deposition</option><option value="/collections/1945-7111_focus_issue_162_13_Y13">Focus Issue on Electrochemical Interfaces in Energy Storage Systems</option><option value="/collections/1945-7111_focus_issue_in_recognition_of_adam_heller_and_his_enduring_contributions_to_electrochemistry">In Recognition of Adam Heller and His Enduring Contributions to Electrochemistry</option><option value="/collections/1945-7111_focus_issue_mechano-electro-chemical_coupling_in_energy_related_materials_and_devices">Mechano-Electro-Chemical Coupling in Energy Related Materials and Devices</option><option value="/collections/1945-7111_focus_issue_mathematical_modeling_of_electrochemical_systems_at_multiple_scales">Mathematical Modeling of Electrochemical Systems at Multiple Scales</option><option value="/collections/1945-7111_focus_issue_electrochemical_processing_and_materials_tailoring_for_advanced_energy_technology">Electrochemical Processing and Materials Tailoring for Advanced Energy
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                    Open all abstracts<span class="offscreen-hidden">,&nbsp;in this tab</span></button></p><!--    articleEntryList start--><ul class="art-list"><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/2.0411609jes" class="art-list-item-title event_main-link">Calendar Aging of Lithium-Ion Batteries</a><p class="small art-list-item-meta">Peter Keil <em>et al</em> 2016 <em>J. Electrochem. Soc.</em> <b>163</b> A1872 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/2.0411609jes/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Calendar Aging of Lithium-Ion Batteries</span></a><a href="/article/10.1149/2.0411609jes/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Calendar Aging of Lithium-Ion Batteries</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Calendar Aging of Lithium-Ion Batteries" data-link-purpose-append-open="Calendar Aging of Lithium-Ion Batteries">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>In this study, the calendar aging of lithium-ion batteries is investigated at different temperatures for 16 states of charge (SoCs) from 0 to 100%. Three types of 18650 lithium-ion cells, containing different cathode materials, have been examined. Our study demonstrates that calendar aging does not increase steadily with the SoC. Instead, plateau regions, covering SoC intervals of more than 20%–30% of the cell capacity, are observed wherein the capacity fade is similar. Differential voltage analyses confirm that the capacity fade is mainly caused by a shift in the electrode balancing. Furthermore, our study reveals the high impact of the graphite electrode on calendar aging. Lower anode potentials, which aggravate electrolyte reduction and thus promote solid electrolyte interphase growth, have been identified as the main driver of capacity fade during storage. In the high SoC regime where the graphite anode is lithiated more than 50%, the low anode potential accelerates the loss of cyclable lithium, which in turn distorts the electrode balancing. Aging mechanisms induced by high cell potential, such as electrolyte oxidation or transition-metal dissolution, seem to play only a minor role. To maximize battery life, high storage SoCs corresponding to low anode potential should be avoided.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/2.0411609jes">https://doi.org/10.1149/2.0411609jes</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/abae37" class="art-list-item-title event_main-link">Degradation of Commercial Lithium-Ion Cells as a Function of Chemistry and Cycling Conditions</a><p class="small art-list-item-meta">Yuliya Preger <em>et al</em> 2020 <em>J. Electrochem. Soc.</em> <b>167</b> 120532 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/abae37/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Degradation of Commercial Lithium-Ion Cells as a Function of Chemistry and Cycling Conditions</span></a><a href="/article/10.1149/1945-7111/abae37/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Degradation of Commercial Lithium-Ion Cells as a Function of Chemistry and Cycling Conditions</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Degradation of Commercial Lithium-Ion Cells as a Function of Chemistry and Cycling Conditions" data-link-purpose-append-open="Degradation of Commercial Lithium-Ion Cells as a Function of Chemistry and Cycling Conditions">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Energy storage systems with Li-ion batteries are increasingly deployed to maintain a robust and resilient grid and facilitate the integration of renewable energy resources. However, appropriate selection of cells for different applications is difficult due to limited public data comparing the most commonly used off-the-shelf Li-ion chemistries under the same operating conditions. This article details a multi-year cycling study of commercial LiFePO<sub>4</sub> (LFP), LiNi<sub>x</sub>Co<sub>y</sub>Al<sub>1−x−y</sub>O<sub>2</sub> (NCA), and LiNi<sub>x</sub>Mn<sub>y</sub>Co<sub>1−x−y</sub>O<sub>2</sub> (NMC) cells, varying the discharge rate, depth of discharge (DOD), and environment temperature. The capacity and discharge energy retention, as well as the round-trip efficiency, were compared. Even when operated within manufacturer specifications, the range of cycling conditions had a profound effect on cell degradation, with time to reach 80% capacity varying by thousands of hours and cycle counts among cells of each chemistry. The degradation of cells in this study was compared to that of similar cells in previous studies to identify universal trends and to provide a standard deviation for performance. All cycling files have been made publicly available at batteryarchive.org, a recently developed repository for visualization and comparison of battery data, to facilitate future experimental and modeling efforts.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/abae37">https://doi.org/10.1149/1945-7111/abae37</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ad6cbd" class="art-list-item-title event_main-link">The Operation Window of Lithium Iron Phosphate/Graphite Cells Affects their Lifetime</a><p class="small art-list-item-meta">Eniko S. Zsoldos <em>et al</em> 2024 <em>J. Electrochem. Soc.</em> <b>171</b> 080527 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ad6cbd/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;The Operation Window of Lithium Iron Phosphate/Graphite Cells Affects their Lifetime</span></a><a href="/article/10.1149/1945-7111/ad6cbd/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;The Operation Window of Lithium Iron Phosphate/Graphite Cells Affects their Lifetime</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="The Operation Window of Lithium Iron Phosphate/Graphite Cells Affects their Lifetime" data-link-purpose-append-open="The Operation Window of Lithium Iron Phosphate/Graphite Cells Affects their Lifetime">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Lithium iron phosphate (LFP) battery cells are ubiquitous in electric vehicles and stationary energy storage because they are cheap and have a long lifetime. This work compares LFP/graphite pouch cells undergoing charge-discharge cycles over five state of charge (SOC) windows (0%–25%, 0%–60%, 0%–80%, 0%–100%, and 75%–100%). Cycling LFP cells across a lower average SOC results in less capacity fade than cycling across a higher average SOC, regardless of depth of discharge. The primary capacity fade mechanism is lithium inventory loss due to: lithiated graphite reactivity with electrolyte, which increases incrementally with SOC, and lithium alkoxide species causing iron dissolution and deposition on the negative electrode at high SOC which further accelerates lithium inventory loss. Our results show that even low voltage LFP systems (3.65 V) have a tradeoff between average SOC and lifetime. Operating LFP cells at lower average SOC can extend their lifetime substantially in both EV and grid storage applications.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ad6cbd">https://doi.org/10.1149/1945-7111/ad6cbd</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ab9050" class="art-list-item-title event_main-link">Development of Experimental Techniques for Parameterization of Multi-scale Lithium-ion Battery Models</a><p class="small art-list-item-meta">Chang-Hui Chen <em>et al</em> 2020 <em>J. Electrochem. Soc.</em> <b>167</b> 080534 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ab9050/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Development of Experimental Techniques for Parameterization of Multi-scale Lithium-ion Battery Models</span></a><a href="/article/10.1149/1945-7111/ab9050/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Development of Experimental Techniques for Parameterization of Multi-scale Lithium-ion Battery Models</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Development of Experimental Techniques for Parameterization of Multi-scale Lithium-ion Battery Models" data-link-purpose-append-open="Development of Experimental Techniques for Parameterization of Multi-scale Lithium-ion Battery Models">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Presented here, is an extensive 35 parameter experimental data set of a cylindrical 21700 commercial cell (LGM50), for an electrochemical pseudo-two-dimensional (P2D) model. The experimental methodologies for tear-down and subsequent chemical, physical, electrochemical kinetics and thermodynamic analysis, and their accuracy and validity are discussed. Chemical analysis of the LGM50 cell shows that it is comprised of a NMC 811 positive electrode and bi-component Graphite-SiO<sub>x</sub> negative electrode. The thermodynamic open circuit voltages (OCV) and lithium stoichiometry in the electrode are obtained using galvanostatic intermittent titration technique (GITT) in half cell and three-electrode full cell configurations. The activation energy and exchange current coefficient through electrochemical impedance spectroscopy (EIS) measurements. Apparent diffusion coefficients are estimated using the Sand equation on the voltage transient during the current pulse; an expansion factor was applied to the bi-component negative electrode data to reflect the average change in effective surface area during lithiation. The 35 parameters are applied within a P2D model to show the fit to experimental validation LGM50 cell discharge and relaxation voltage profiles at room temperature. The accuracy and validity of the processes and the techniques in the determination of these parameters are discussed, including opportunities for further modelling and data analysis improvements.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ab9050">https://doi.org/10.1149/1945-7111/ab9050</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/2.0191808jes" class="art-list-item-title event_main-link">Review—Organic-Inorganic Hybrid Functional Materials: An Integrated Platform for Applied Technologies</a><p class="small art-list-item-meta">Sajjad Husain Mir <em>et al</em> 2018 <em>J. Electrochem. Soc.</em> <b>165</b> B3137 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/2.0191808jes/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Review—Organic-Inorganic Hybrid Functional Materials: An Integrated Platform for Applied Technologies</span></a><a href="/article/10.1149/2.0191808jes/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Review—Organic-Inorganic Hybrid Functional Materials: An Integrated Platform for Applied Technologies</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Review—Organic-Inorganic Hybrid Functional Materials: An Integrated Platform for Applied Technologies" data-link-purpose-append-open="Review—Organic-Inorganic Hybrid Functional Materials: An Integrated Platform for Applied Technologies">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Hybrid functional materials, constituting both inorganic and organic components, are considered potential platforms for applications in extremely diverse fields such as optics, micro-electronics, transportation, health, energy, energy storage, diagnosis, housing, environment and the highly relevant area is Internet of Things (IoT). Material properties of hybrid materials can be tuned by modification of the composition on the molecular scale to produce smart materials. Cross-cutting approaches, to synergistically couple molecular engineering and processing allows to tailor complex hybrid systems of various shapes with perfect control over size, composition, functionality, and morphology. The detailed description and discussion of variety of hybrid functional organic-inorganic materials and their contribution in the designing of specific modern technologies is the prime focus of this review.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/2.0191808jes">https://doi.org/10.1149/2.0191808jes</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ad14d0" class="art-list-item-title event_main-link">Lithium-Ion Cells in Automotive Applications: Tesla 4680 Cylindrical Cell Teardown and Characterization</a><p class="small art-list-item-meta">Manuel Ank <em>et al</em> 2023 <em>J. Electrochem. Soc.</em> <b>170</b> 120536 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ad14d0/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Lithium-Ion Cells in Automotive Applications: Tesla 4680 Cylindrical Cell Teardown and Characterization</span></a><a href="/article/10.1149/1945-7111/ad14d0/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Lithium-Ion Cells in Automotive Applications: Tesla 4680 Cylindrical Cell Teardown and Characterization</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Lithium-Ion Cells in Automotive Applications: Tesla 4680 Cylindrical Cell Teardown and Characterization" data-link-purpose-append-open="Lithium-Ion Cells in Automotive Applications: Tesla 4680 Cylindrical Cell Teardown and Characterization">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Battery research depends upon up-to-date information on the cell characteristics found in current electric vehicles, which is exacerbated by the deployment of novel formats and architectures. This necessitates open access to cell characterization data. Therefore, this study examines the architecture and performance of first-generation Tesla 4680 cells in detail, both by electrical characterization and thermal investigations at cell-level and by disassembling one cell down to the material level including a three-electrode analysis. The cell teardown reveals the complex cell architecture with electrode disks of hexagonal symmetry as well as an electrode winding consisting of a double-sided and homogeneously coated cathode and anode, two separators and no mandrel. A solvent-free anode fabrication and coating process can be derived. Energy-dispersive X-ray spectroscopy as well as differential voltage, incremental capacity and three-electrode analysis confirm a NMC811 cathode and a pure graphite anode without silicon. On cell-level, energy densities of 622.4 Wh/L and 232.5 Wh/kg were determined while characteristic state-of-charge dependencies regarding resistance and impedance behavior are revealed using hybrid pulse power characterization and electrochemical impedance spectroscopy. A comparatively high surface temperature of ∼70 °C is observed when charging at 2C without active cooling. All measurement data of this characterization study are provided as open source.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ad14d0">https://doi.org/10.1149/1945-7111/ad14d0</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/2.1441707jes" class="art-list-item-title event_main-link">Review—SEI: Past, Present and Future</a><p class="small art-list-item-meta">E. Peled and S. Menkin 2017 <em>J. Electrochem. Soc.</em> <b>164</b> A1703 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/2.1441707jes/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Review—SEI: Past, Present and Future</span></a><a href="/article/10.1149/2.1441707jes/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Review—SEI: Past, Present and Future</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Review—SEI: Past, Present and Future" data-link-purpose-append-open="Review—SEI: Past, Present and Future">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>The Solid-Electrolyte-Interphase (SEI) model for non-aqueous alkali-metal batteries constitutes a paradigm change in the understanding of lithium batteries and has thus enabled the development of safer, durable, higher-power and lower-cost lithium batteries for portable and EV applications. Prior to the publication of the SEI model (1979), researchers used the Butler-Volmer equation, in which a direct electron transfer from the electrode to lithium cations in the solution is assumed. The SEI model proved that this is a mistaken concept and that, in practice, the transfer of electrons from the electrode to the solution in a lithium battery, must be prevented, since it will result in fast self-discharge of the active materials and poor battery performance. This model provides [E. Peled, in “Lithium Batteries,” J.P. Gabano (ed), Academic Press, (1983), E. Peled, <i>J. Electrochem. Soc.</i>, <b>126</b>, 2047 (1979).] new equations for: electrode kinetics (i<sub>o</sub> and b), anode corrosion, SEI resistivity and growth rate and irreversible capacity loss of lithium-ion batteries. This model became a cornerstone in the science and technology of lithium batteries. This paper reviews the past, present and the future of SEI batteries.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/2.1441707jes">https://doi.org/10.1149/2.1441707jes</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ac6d13" class="art-list-item-title event_main-link">Review—“Knees” in Lithium-Ion Battery Aging Trajectories</a><p class="small art-list-item-meta">Peter M. Attia <em>et al</em> 2022 <em>J. Electrochem. Soc.</em> <b>169</b> 060517 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ac6d13/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Review—“Knees” in Lithium-Ion Battery Aging Trajectories</span></a><a href="/article/10.1149/1945-7111/ac6d13/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Review—“Knees” in Lithium-Ion Battery Aging Trajectories</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Review—“Knees” in Lithium-Ion Battery Aging Trajectories" data-link-purpose-append-open="Review—“Knees” in Lithium-Ion Battery Aging Trajectories">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Lithium-ion batteries can last many years but sometimes exhibit rapid, nonlinear degradation that severely limits battery lifetime. In this work, we review prior work on “knees” in lithium-ion battery aging trajectories. We first review definitions for knees and three classes of “internal state trajectories” (termed snowball, hidden, and threshold trajectories) that can cause a knee. We then discuss six knee “pathways”, including lithium plating, electrode saturation, resistance growth, electrolyte and additive depletion, percolation-limited connectivity, and mechanical deformation—some of which have internal state trajectories with signals that are electrochemically undetectable. We also identify key design and usage sensitivities for knees. Finally, we discuss challenges and opportunities for knee modeling and prediction. Our findings illustrate the complexity and subtlety of lithium-ion battery degradation and can aid both academic and industrial efforts to improve battery lifetime.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ac6d13">https://doi.org/10.1149/1945-7111/ac6d13</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae3b18" class="art-list-item-title event_main-link">Erratum: Advanced LiTFSI-LiPF<sub>6</sub> Dual-Salt Electrolyte for High-Power and Wide-Temperature Operation of Lithium-Ion Batteries [<i>J. Electrochem. Soc.,</i> <b>172</b>, 120530 (2025)]</a><p class="small art-list-item-meta">David J. Kautz <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 039001 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae3b18/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Erratum: Advanced LiTFSI-LiPF6 Dual-Salt Electrolyte for High-Power and Wide-Temperature Operation of Lithium-Ion Batteries [J. Electrochem. Soc., 172, 120530 (2025)]</span></a><a href="/article/10.1149/1945-7111/ae3b18/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Erratum: Advanced LiTFSI-LiPF6 Dual-Salt Electrolyte for High-Power and Wide-Temperature Operation of Lithium-Ion Batteries [J. Electrochem. Soc., 172, 120530 (2025)]</span></a></div><div class="reveal-content"><div class="article-text view-text-small"></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae3b18">https://doi.org/10.1149/1945-7111/ae3b18</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae8e62" class="art-list-item-title event_main-link">Cations Make the Difference: Stabilizing Forward-Bias Bipolar Membrane CO<sub>2</sub> Electrolysis</a><p class="small art-list-item-meta">Valerio Fagnini <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 153502 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae8e62/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Cations Make the Difference: Stabilizing Forward-Bias Bipolar Membrane CO2 Electrolysis</span></a><a href="/article/10.1149/1945-7111/ae8e62/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Cations Make the Difference: Stabilizing Forward-Bias Bipolar Membrane CO2 Electrolysis</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Cations Make the Difference: Stabilizing Forward-Bias Bipolar Membrane CO2 Electrolysis" data-link-purpose-append-open="Cations Make the Difference: Stabilizing Forward-Bias Bipolar Membrane CO2 Electrolysis">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Zero-gap CO<sub>2</sub> electrolyzers employing Anion Exchange Membranes (AEMs) ensure beneficial cathodic alkalinity. However, (bi)carbonates formed at the cathode from CO<sub>2</sub> feed gas migrate through the AEM to the anode, releasing gaseous CO<sub>2</sub>. They also react with metal cations translocated from the anolyte, causing malfunction through blocking of the Gas Diffusion Electrode (GDE) by salt precipitation. Forward-bias Bipolar Membranes (BPMs) mitigate anodic CO<sub>2</sub> loss, but cation management remains crucial to avoid salt deposition. In this work, the performance of an electrolysis process employing a forward-bias BPM is optimized and compared to AEM- and reverse-bias BPM-based systems, achieving remarkable Energy Efficiency for CO (<i>EE</i><sub>CO</sub>)≈35%, Faradaic Efficiency for CO (<i>FE</i><sub>CO</sub>) &gt; 80% and reduced CO<sub>2</sub> loss. An innovative cation management comprising intermittent cation supply to the anolyte is performed, avoiding process failure through salt deposition. Na<sup>+</sup>-, K<sup>+</sup>- and Cs<sup>+</sup>- based electrolytes are investigated, highlighting the influence of metal cation identity on selectivity and stability of the electrolysis process.</p><h2 id="artAbst2" class="collapse-blocked">Highlights</h2><p>
<ul><li><p>Forward-bias membranes mitigate (bi)carbonate transport to the anode and CO<sub>2</sub> loss</p></li><li><p>Dynamic cation management reduces salt deposition in zero-gap electrolyzers</p></li><li><p>Stable CO formation achieved at near pure-water anolyte molarity</p></li><li><p>Metal cation identity influences product selectivity and process stability</p></li><li><p>Anolyte control within the experiment improves long-term carbon utilization</p></li></ul></p><h2 id="artAbst3" class="collapse-blocked"></h2><p>
<span style="display: none;">figure placeholder</span>
</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae8e62">https://doi.org/10.1149/1945-7111/ae8e62</a></div></div></li></ul><!--    articleEntryList end--></div></div></div><!-- End Most read tabpanel --><!-- Start Latest tabpanel --><div tabindex="0"
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                    Open all abstracts<span class="offscreen-hidden">,&nbsp;in this tab</span></button></p><!--    articleEntryList start--><ul class="art-list"><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae94f1" class="art-list-item-title event_main-link">Chromium Electrodeposition from Hydrate Melts: Formation of Metastable δ-Cr Phase in Conjunction with Hydrogen Incorporation</a><p class="small art-list-item-meta">Haruki Katori <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 162503 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae94f1/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Chromium Electrodeposition from Hydrate Melts: Formation of Metastable δ-Cr Phase in Conjunction with Hydrogen Incorporation</span></a><a href="/article/10.1149/1945-7111/ae94f1/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Chromium Electrodeposition from Hydrate Melts: Formation of Metastable δ-Cr Phase in Conjunction with Hydrogen Incorporation</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Chromium Electrodeposition from Hydrate Melts: Formation of Metastable δ-Cr Phase in Conjunction with Hydrogen Incorporation" data-link-purpose-append-open="Chromium Electrodeposition from Hydrate Melts: Formation of Metastable δ-Cr Phase in Conjunction with Hydrogen Incorporation">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>As an alternative to hexavalent chromium plating, chloride-based hydrate melts enable crystalline chromium electrodeposition from trivalent chromium without the use of organic complexing agents. Cr films deposited from these hydrate melt-based baths uniquely contain a metastable <i>δ</i>-Cr phase absent in conventional baths. Achieving hard coatings with adequate mechanical properties requires a systematic understanding of the crystallographic features including phase formation. In this study, the deposition of <i>δ</i>-Cr and its subsequent phase transformation to <i>α</i>-Cr were systematically investigated from the perspectives of crystal growth mode and hydrogen incorporation. The results indicate that <i>δ</i>-Cr preferentially forms during the initial nucleation and coalescence stage, where isotropic fine grains are generated. As electrodeposition proceeds, the crystal growth mode transitions to columnar growth, in which <i>α</i>-Cr becomes the dominant phase. The obtained <i>δ</i>-Cr was confirmed to transform into <i>α</i>-Cr at relatively low temperatures ranging from room temperature to 250 °C. The thermal desorption spectrum of hydrogen and time-of-flight secondary-ion mass spectrometry (ToF-SIMS) experiments using deuterium as a stable isotope label suggest that the formation and stability of the electrodeposited <i>δ</i>-Cr phase may well be attributed to incorporated hydrogen. These findings provide a fundamental basis for microstructural control of electrodeposited Cr from chloride-based hydrate melts.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae94f1">https://doi.org/10.1149/1945-7111/ae94f1</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/ae9647" class="art-list-item-title event_main-link">Wearable Electrochemical Sensors for Cortisol Monitoring in Body Fluids: From Materials to Applications</a><p class="small art-list-item-meta">Zeda Zhou and Yixuan Bian 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 167503 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9647/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Wearable Electrochemical Sensors for Cortisol Monitoring in Body Fluids: From Materials to Applications</span></a><a href="/article/10.1149/1945-7111/ae9647/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Wearable Electrochemical Sensors for Cortisol Monitoring in Body Fluids: From Materials to Applications</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Wearable Electrochemical Sensors for Cortisol Monitoring in Body Fluids: From Materials to Applications" data-link-purpose-append-open="Wearable Electrochemical Sensors for Cortisol Monitoring in Body Fluids: From Materials to Applications">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Cortisol, a steroid hormone, is critical in regulating the stress response, metabolic homeostasis, and immune balance in the human body. Since cortisol is widely distributed in body fluids, the use of easily accessible fluids, such as sweat, makes continuous health assessment possible. Wearable sensors support the non-invasive and <i>in situ</i> collection of biomarkers, while electrochemical sensing methods have been widely used for the analysis of biomarkers due to their low cost, easy operation, high sensitivity, and fast response. The development and application of wearable electrochemical sensors provide essential support for non-invasive, real-time, and continuous monitoring of cortisol. This review systematically covers the recent progress in wearable electrochemical sensors, focusing particularly on sensing strategies of different recognition elements and critically evaluating their performance and limitations in complex biological fluids. Additionally, this review introduces the innovative applications of graphene, MXene, metal nanoparticles, and other functional materials in wearable electrochemical sensors, systematically comparing the sensing abilities of each material. Subsequently, in view of the challenges encountered in practical applications, this work discusses microfluidic integration strategies, multilayer interference-resistant interface designs, and machine learning-based data calibration methods. Finally, future prospects for interdisciplinary approaches in advancing precision medicine and real-time health monitoring are reviewed.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9647">https://doi.org/10.1149/1945-7111/ae9647</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae959d" class="art-list-item-title event_main-link">Time and Temperature Dependent Aging Mechanisms in Commercial Lithium-Ion Cells with SiO<i><sub>x</sub></i>/Graphite Anodes</a><p class="small art-list-item-meta">Jihed Ayari <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 160510 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae959d/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Time and Temperature Dependent Aging Mechanisms in Commercial Lithium-Ion Cells with SiOx/Graphite Anodes</span></a><a href="/article/10.1149/1945-7111/ae959d/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Time and Temperature Dependent Aging Mechanisms in Commercial Lithium-Ion Cells with SiOx/Graphite Anodes</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Time and Temperature Dependent Aging Mechanisms in Commercial Lithium-Ion Cells with SiOx/Graphite Anodes" data-link-purpose-append-open="Time and Temperature Dependent Aging Mechanisms in Commercial Lithium-Ion Cells with SiOx/Graphite Anodes">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>This work addresses the limited understanding of how changes in SiO<sub><i>x</i></sub>/graphite anodes and the N/P ratio induced by aging influence the temperature-dependent transition between degradation mechanisms. It provides insight into the potentially evolving risk of lithium plating and its implications for the safe and durable operation of batteries. Commercial 3.5 Ah Li-ion 18 650 cells with SiO<i><sub>x</sub></i>/graphite anodes (∼2.5 wt.% Si) and Ni-rich LiNi<sub>1−<i>x</i>−<i>y</i></sub>Mn<i><sub>x</sub></i>Co<i><sub>y</sub></i>O<sub>2</sub> cathodes were systematically aged in the temperature range from −10 °C to +45 °C at 0.5 C and 0.85 C. Aging rates were evaluated at both beginning-of-life, i.e. 100%–95% state-of-health and mid-of-life (92.5%–87.5% state-of-health) using Arrhenius plots. The <i>V</i>-shaped Arrhenius plots at beginning-of-life exhibited minima, while the minima of the mid-of-life aged cells were either shifted to higher temperatures or even vanished in the investigated temperature range, indicating an increased susceptibility to lithium plating in the aged cells. Post-mortem analyses using FIB-SEM/EDX mapping revealed that SiO<i><sub>x</sub></i> degradation and related side reactions are more pronounced at high temperatures, while most likely lithium plating predominates at low temperatures. Loss of anode active material in the form of SiO<i><sub>x</sub></i> degradation and the resulting decrease in the N/P ratio is most likely the cause of the observed changes in the Arrhenius plots after cycling.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p><h2 id="artAbst3" class="collapse-blocked">Highlights</h2><p><ul><li><p>Aging of commercial 18650 Li-ion cells investigated from -10°C to 45°C</p></li><li><p>V-shaped Arrhenius plots for new cells indicate Li plating at low temperatures</p></li><li><p>Post-Mortem analysis and FIB-SEM/EDX show degradation of SiO<sub><i>x</i></sub></p></li><li><p>Degradation of SiO<sub><i>x</i></sub> in anode decreases N/P ratio and changes Arrhenius plot</p></li><li><p>High temperature aging most likely increases later susceptibility to Li plating</p></li></ul></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae959d">https://doi.org/10.1149/1945-7111/ae959d</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/ae95a0" class="art-list-item-title event_main-link">Deep Learning for Lithium-Ion Battery State of Health Estimation via Explainable Feature Screening</a><p class="small art-list-item-meta">Zhijun Gao <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 160509 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae95a0/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Deep Learning for Lithium-Ion Battery State of Health Estimation via Explainable Feature Screening</span></a><a href="/article/10.1149/1945-7111/ae95a0/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Deep Learning for Lithium-Ion Battery State of Health Estimation via Explainable Feature Screening</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Deep Learning for Lithium-Ion Battery State of Health Estimation via Explainable Feature Screening" data-link-purpose-append-open="Deep Learning for Lithium-Ion Battery State of Health Estimation via Explainable Feature Screening">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Accurate state of health estimation is essential for the safe and reliable operation of lithium-ion battery management systems, yet practical prediction remains difficult because battery degradation involves strong nonlinearity, local capacity regeneration, and long-range temporal dependence. This study proposes an Informer encoder and Newton–Raphson-optimized extreme learning machine framework (InE-NRBO-ELM) that integrates random forest and SHapley Additive exPlanations feature screening (RF-SHAP) with an Informer encoder and a Newton–Raphson optimizer for extreme learning machine regression. Nineteen candidate health features are first evaluated to retain the most informative inputs and suppress redundant interference. The Informer encoder then learns long-range degradation representations, while the Newton–Raphson optimizer jointly optimizes the extreme learning machine regularization coefficient and hidden node number to improve regression stability. Experiments on the NASA and CALCE datasets show that the proposed method accurately tracks both gradual degradation and local regeneration behavior. Under a 60% training ratio, the model achieved mean absolute percentage error of 0.4801%, mean absolute error of 0.00342, and root mean square error of 0.00460 across eight batteries. Within the controlled NASA and CALCE test conditions, benchmark, robustness and ablation studies demonstrate stable performance and the complementary roles of input screening, temporal representation, and adaptive regression optimization.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p><h2 id="artAbst3" class="collapse-blocked">Highlights</h2><p><ul><li><p>A new deep learning framework improves lithium-ion battery health estimation.</p></li><li><p>Explainable feature screening keeps the most useful aging signals from charge data.</p></li><li><p>Long-range sequence learning captures gradual degradation and local recovery trends.</p></li><li><p>Tests on two public datasets showed accurate and stable predictions across batteries.</p></li><li><p>Average error stayed below 0.5%, supporting reliable battery management decisions.</p></li></ul></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae95a0">https://doi.org/10.1149/1945-7111/ae95a0</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/ae9649" class="art-list-item-title event_main-link">Ti<sub>3</sub>C<sub>2</sub>T<sub>x</sub> MXene/CeO<sub>2</sub>-Integrated Graphite Conductive Ink Based Flexible Electrode for Norepinephrine Detection</a><p class="small art-list-item-meta">Selen Uruc <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 167502 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9649/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Ti3C2Tx MXene/CeO2-Integrated Graphite Conductive Ink Based Flexible Electrode for Norepinephrine Detection</span></a><a href="/article/10.1149/1945-7111/ae9649/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Ti3C2Tx MXene/CeO2-Integrated Graphite Conductive Ink Based Flexible Electrode for Norepinephrine Detection</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Ti3C2Tx MXene/CeO2-Integrated Graphite Conductive Ink Based Flexible Electrode for Norepinephrine Detection" data-link-purpose-append-open="Ti3C2Tx MXene/CeO2-Integrated Graphite Conductive Ink Based Flexible Electrode for Norepinephrine Detection">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>The development of conductive and sustainable materials with high electrochemical performance remains an important goal for next-generation sensing platforms. In this study, a flexible electrochemical sensor was fabricated on a low-cost cellulose-based paper substrate using an MXene/cerium oxide/graphite (MXene/CeO<sub>2</sub>/G) composite conductive ink. The conductive ink was formulated by dispersing MXene, CeO<sub>2</sub>, and graphite as individual components within the same matrix, forming a composite structure. This combination improved both the electrical conductivity and the electrocatalytic activity toward norepinephrine (NE) oxidation. The electrochemical behavior of the MXene/CeO<sub>2</sub>/G screen-printed electrode (SPE) was investigated, and the oxidation process was found to be diffusion and adsorption-controlled. The electroactive surface area of the electrodes was also determined, indicating an increased number of active sites. The effect of pH was examined, and the highest current response was obtained at pH 6.4. Under optimized conditions, the sensor exhibited a detection limit (LOD) of 77.29 nM and a linear range of 0.25–25 µM using differential pulse voltammetry (DPV). The sensor showed good selectivity in the presence of common interfering species. Recovery values ranged between 95.1% and 107.0%, with low relative standard deviation (RSD), confirming the reliability of the method. The applicability of the sensor was demonstrated in artificial urine samples. These results demonstrate that MXene/CeO<sub>2</sub>/G-based conductive inks provide a promising approach for the development of flexible and cost-effective electrochemical sensors.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p><h2 id="artAbst3" class="collapse-blocked">Highlights</h2><p><ul><li><p>MXene/CeO<sub>2</sub>/graphite ink was developed for SPE fabrication.</p></li><li><p>Flexible and low-cost SPEs were fabricated on paper substrates.</p></li><li><p>NE was detected using a non-enzymatic approach with DPV.</p></li><li><p>The sensor demonstrated successful applicability in artificial urine samples.</p></li></ul></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9649">https://doi.org/10.1149/1945-7111/ae9649</a></div></div></li></ul><!--    articleEntryList end--></div></div></div><!-- End Latest tabpanel --><!-- Express Letters tabpanel --><!-- Express Letters tabpanel --><!-- Start Review tabpanel --><div tabindex="0"
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                    Open all abstracts<span class="offscreen-hidden">,&nbsp;in this tab</span></button></p><!--    articleEntryList start--><ul class="art-list"><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/ae9647" class="art-list-item-title event_main-link">Wearable Electrochemical Sensors for Cortisol Monitoring in Body Fluids: From Materials to Applications</a><p class="small art-list-item-meta">Zeda Zhou and Yixuan Bian 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 167503 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9647/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Wearable Electrochemical Sensors for Cortisol Monitoring in Body Fluids: From Materials to Applications</span></a><a href="/article/10.1149/1945-7111/ae9647/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Wearable Electrochemical Sensors for Cortisol Monitoring in Body Fluids: From Materials to Applications</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Wearable Electrochemical Sensors for Cortisol Monitoring in Body Fluids: From Materials to Applications" data-link-purpose-append-open="Wearable Electrochemical Sensors for Cortisol Monitoring in Body Fluids: From Materials to Applications">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Cortisol, a steroid hormone, is critical in regulating the stress response, metabolic homeostasis, and immune balance in the human body. Since cortisol is widely distributed in body fluids, the use of easily accessible fluids, such as sweat, makes continuous health assessment possible. Wearable sensors support the non-invasive and <i>in situ</i> collection of biomarkers, while electrochemical sensing methods have been widely used for the analysis of biomarkers due to their low cost, easy operation, high sensitivity, and fast response. The development and application of wearable electrochemical sensors provide essential support for non-invasive, real-time, and continuous monitoring of cortisol. This review systematically covers the recent progress in wearable electrochemical sensors, focusing particularly on sensing strategies of different recognition elements and critically evaluating their performance and limitations in complex biological fluids. Additionally, this review introduces the innovative applications of graphene, MXene, metal nanoparticles, and other functional materials in wearable electrochemical sensors, systematically comparing the sensing abilities of each material. Subsequently, in view of the challenges encountered in practical applications, this work discusses microfluidic integration strategies, multilayer interference-resistant interface designs, and machine learning-based data calibration methods. Finally, future prospects for interdisciplinary approaches in advancing precision medicine and real-time health monitoring are reviewed.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9647">https://doi.org/10.1149/1945-7111/ae9647</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae9406" class="art-list-item-title event_main-link">From Task-Specific AI to Battery Foundation Models</a><p class="small art-list-item-meta">Jingyuan Zhao <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 150520 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9406/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;From Task-Specific AI to Battery Foundation Models</span></a><a href="/article/10.1149/1945-7111/ae9406/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;From Task-Specific AI to Battery Foundation Models</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="From Task-Specific AI to Battery Foundation Models" data-link-purpose-append-open="From Task-Specific AI to Battery Foundation Models">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Artificial intelligence (AI) is influencing battery research and life-cycle management, spanning materials discovery, electrode and cell design, manufacturing optimization, diagnostics, safety monitoring, recycling, and certification. These advances are enabled by growing battery datasets and learning methods that extract patterns from complex electrochemical systems. Yet most current models remain task-specific and are trained on fragmented datasets, limiting transferability across chemistries, cell formats, operating conditions, and life-cycle stages. Battery foundation models (BFMs) offer a promising but emerging paradigm for battery intelligence. They may be formulated as large, pre-trained, and adaptable architectures that integrate multimodal battery data with physics-informed priors to represent electrochemical structures, states, and dynamics. Unlike direct analogues of general large language models, BFMs should be understood as physics-aware foundation models designed for scientific reasoning under multiscale physical constraints, heterogeneous and incomplete data, and stringent safety and reliability requirements. By combining self-supervised learning with mechanistic electrochemical models, BFMs may learn more interpretable and transferable representations across materials, formats, and duty cycles. If sufficiently validated, such representations could support materials discovery, manufacturing, diagnostics, recycling, and certification. This Review discusses challenges in data fragmentation, validation, interpretability, and computational sustainability, and outlines a roadmap toward responsible BFMs and integrated battery-domain ecosystems across the lifecycle.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p><h2 id="artAbst3" class="collapse-blocked">Highlights:</h2><p><ul><li><p>Trace the shift from general LLMs toward physics-aware foundation models for battery science.</p></li><li><p>Integrate multimodal data with physics-informed priors to enable robust and transferable models.</p></li><li><p>Discuss lifecycle-wide applications from materials discovery to recycling and certification.</p></li><li><p>Frame challenges in data fragmentation, interpretability, and computational sustainability.</p></li><li><p>Outline a roadmap toward lifecycle-responsible BFMs and integrated domain ecosystems.</p></li></ul></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9406">https://doi.org/10.1149/1945-7111/ae9406</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/ae888c" class="art-list-item-title event_main-link">Isothermal Microcalorimetry for Battery Characterization</a><p class="small art-list-item-meta">David J. Arnot <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 150515 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae888c/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Isothermal Microcalorimetry for Battery Characterization</span></a><a href="/article/10.1149/1945-7111/ae888c/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Isothermal Microcalorimetry for Battery Characterization</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Isothermal Microcalorimetry for Battery Characterization" data-link-purpose-append-open="Isothermal Microcalorimetry for Battery Characterization">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>As battery function has improved over the past decades, so too has our ability to interrogate the underlying electrochemical processes. Thermal energy generation is a key aspect of batteries affecting electrochemical function, safety, and lifespan. The heat generated by a battery is related to thermodynamics, kinetics, structural changes, and side reactions; measurements of heat production can therefore provide insight into any of these subjects. Isothermal microcalorimetry (IMC) can quantify heat flow within functioning systems with microwatt (or better) accuracy and precision. The ability to simultaneously measure heat production and electrochemical properties allows for fundamental scientific investigations as well as practical measurements on laboratory scale and commercial cells with different form factors. Herein, we review the use of isothermal microcalorimetry for probing battery thermal effects associated with the (dis)charge reaction, phase changes, and parasitic reactions. This work serves as an introduction for unfamiliar readers and summarizes the research that has been done over the years. We begin with a brief history of IMC as it relates to battery research, followed by an overview of the applicable theory, and highlight extensive examples from the literature. Opportunities for future research directions involving application and advances for the use of IMC are also presented.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p><h2 id="artAbst3" class="collapse-blocked">Highlights</h2><p><ul><li><p>Battery energy content is released as either usable work or unwanted heat</p></li><li><p>Isothermal microcalorimetry measures thermal energy exchange with <i>μ</i>W accuracy and precision</p></li><li><p>Battery thermal processes can be a signature of degradation processes</p></li><li><p>Thermodynamic properties can be derived from calorimetric measurements</p></li></ul></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae888c">https://doi.org/10.1149/1945-7111/ae888c</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae8eb9" class="art-list-item-title event_main-link">The Use of Adsorptive Stripping Voltammetry for the Determination of Ti(IV): Advantages, Limitations, Applications—A Review</a><p class="small art-list-item-meta">Edyta Sobczak and Malgorzata Grabarczyk 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 156503 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae8eb9/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;The Use of Adsorptive Stripping Voltammetry for the Determination of Ti(IV): Advantages, Limitations, Applications—A Review</span></a><a href="/article/10.1149/1945-7111/ae8eb9/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;The Use of Adsorptive Stripping Voltammetry for the Determination of Ti(IV): Advantages, Limitations, Applications—A Review</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="The Use of Adsorptive Stripping Voltammetry for the Determination of Ti(IV): Advantages, Limitations, Applications—A Review" data-link-purpose-append-open="The Use of Adsorptive Stripping Voltammetry for the Determination of Ti(IV): Advantages, Limitations, Applications—A Review">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>This review discusses methods of determining the presence of titanium using adsorptive stripping voltammetry (AdSV) and catalytic adsorptive voltammetry (CAdSV). The work centers on the key factors that influence the sensitivity and selectivity of the proposed analytical procedures. Particular attention was paid to the role of the complexing agents used and the presence of oxidizing agents. The influence of the type of working electrode and the most commonly used electrode modifiers was also considered. The possibility of determining titanium and other elements simultaneously during a single voltammetric measurement was also discussed. The following sections describe the potential for interference from components of the inorganic and organic matrices. The review also provides examples of how the described voltammetric procedures can be used to determine titanium in real samples with diverse matrices. The most important analytical parameters of the methods described are presented in tabular form to allow comparison of their usefulness for analysis.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae8eb9">https://doi.org/10.1149/1945-7111/ae8eb9</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/ae8d5d" class="art-list-item-title event_main-link">Corrosion of Candidate Cladding and Structural Materials for Sodium-Cooled Fast Reactor Applications</a><p class="small art-list-item-meta">Tolin Skov-Black and Dev Chidambaram 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 151502 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae8d5d/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Corrosion of Candidate Cladding and Structural Materials for Sodium-Cooled Fast Reactor Applications</span></a><a href="/article/10.1149/1945-7111/ae8d5d/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Corrosion of Candidate Cladding and Structural Materials for Sodium-Cooled Fast Reactor Applications</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Corrosion of Candidate Cladding and Structural Materials for Sodium-Cooled Fast Reactor Applications" data-link-purpose-append-open="Corrosion of Candidate Cladding and Structural Materials for Sodium-Cooled Fast Reactor Applications">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Generation IV reactors aim for more efficient, cheaper, safer nuclear power with less waste generation. Sodium-cooled fast reactors (SFRs) are expected to be among the first GenIV designs to operate. SFR structural and cladding materials must withstand high‐temperature liquid sodium, where degradation is driven by selective dissolution and impurity‐mediated reactions rather than electrochemistry. This review focuses on corrosion and mass transfer in sodium, highlighting the coupled role of temperature gradients, flow velocity, and impurities (notably oxygen and carbon) in driving elemental leaching and redistribution, carburization/decarburization, and formation of stable ternary oxides such as Na–Cr–O compounds. Corrosion behavior is then assessed for major candidate classes: austenitic stainless steels as a performance baseline; ferritic–martensitic steels and the role of carbon activity and chromium content; ODS steels and chemistry-dependent oxide development; nickel-based alloys with comparatively high sodium solubility; and SiC/SiC composites with impurity-sensitive intergranular attack. A database of recent experiments (temperature, impurity level, flow, exposure time) is used to map existing data and expose gaps for advanced cladding deployment. Key gaps are the limited parametric studies spanning oxygen/carbon activity, velocity, and irradiation damage, and the lack of long-duration datasets and validated mechanistic models for SFR deployment.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae8d5d">https://doi.org/10.1149/1945-7111/ae8d5d</a></div></div></li></ul><!--    articleEntryList end--></div></div></div><!-- End Review tabpanel --><!-- Start Featured tabpanel --><!-- End Featured tabpanel --><!-- Start Editor's chocie tabpanel --><div tabindex="0"
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                    Open all abstracts<span class="offscreen-hidden">,&nbsp;in this tab</span></button></p><!--    articleEntryList start--><ul class="art-list"><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae60a9" class="art-list-item-title event_main-link">Editors’ Choice—Understanding the Role of Multivalency in Chloride-Based Electrolytes for Efficient Iron Electrosynthesis</a><p class="small art-list-item-meta">William Lvovich <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 082502 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae60a9/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Understanding the Role of Multivalency in Chloride-Based Electrolytes for Efficient Iron Electrosynthesis</span></a><a href="/article/10.1149/1945-7111/ae60a9/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Understanding the Role of Multivalency in Chloride-Based Electrolytes for Efficient Iron Electrosynthesis</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Editors’ Choice—Understanding the Role of Multivalency in Chloride-Based Electrolytes for Efficient Iron Electrosynthesis" data-link-purpose-append-open="Editors’ Choice—Understanding the Role of Multivalency in Chloride-Based Electrolytes for Efficient Iron Electrosynthesis">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>This study investigates aqueous electrolytes for efficient iron electrodeposition directly from Fe<sup>3+</sup> at ambient temperature. Concentrated lithium chloride (LiCl) based electrolytes were found to stabilize the Fe<sup>3+</sup> in the electrolyte, suppress parasitic hydrogen evolution and suppress redox shuttling of intermediate Fe<sup>2+</sup>, thus promoting efficient iron electrodeposition. These attributes collectively enabled high Coulombic efficiencies (&gt;75%) at high current densities (&gt;200 mA cm<sup>−2</sup>). Furthermore, detailed investigation revealed that increasing the LiCl concentration increased the electrolyte viscosity and decreased the Fe<sup>2+</sup> out-diffusion rate while also suppressing the activity of water. Sufficiently high LiCl concentrations (&gt;7 M) thus provide a window of current densities in which elevated Coulombic efficiencies can be achieved. Overall, this paper develops an understanding of the effects of electrolyte composition on the competition between Fe electrodeposition, hydrogen co-evolution, and intermediate Fe<sup>2+</sup> out-diffusion for efficient Fe metal electrosynthesis.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae60a9">https://doi.org/10.1149/1945-7111/ae60a9</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae17eb" class="art-list-item-title event_main-link">Editors’ Choice—Modeling of Multistage Redox-Mediated Electrodialysis for Volatile Fatty Acids Fractionation</a><p class="small art-list-item-meta">Riccardo Candeago <em>et al</em> 2025 <em>J. Electrochem. Soc.</em> <b>172</b> 113503 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae17eb/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Modeling of Multistage Redox-Mediated Electrodialysis for Volatile Fatty Acids Fractionation</span></a><a href="/article/10.1149/1945-7111/ae17eb/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Modeling of Multistage Redox-Mediated Electrodialysis for Volatile Fatty Acids Fractionation</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Editors’ Choice—Modeling of Multistage Redox-Mediated Electrodialysis for Volatile Fatty Acids Fractionation" data-link-purpose-append-open="Editors’ Choice—Modeling of Multistage Redox-Mediated Electrodialysis for Volatile Fatty Acids Fractionation">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Production of volatile fatty acids (VFAs) from biomass fermentation is a promising pathway for sustainable chemical production. A central challenge is cost-effective recovery and fractionation of VFAs from fermentation broths. Redox-mediated electrodialysis (redox-ED) can be an energy efficient technique for VFA separation, replacing water splitting with redox-reactions. However, the low selectivity between VFAs of different lengths (separation factors &lt;3) obtained using commercially-available anion-exchange membranes limits the final product purity for industrial use. Cascaded operation can overcome these material limitations and increase product purity, yet multistage redox-ED can be complex and has not been extensively explored for selective ion separations. Here, we developed a physics-based model of redox-ED using finite elements to simulate the separation of a ternary carboxylic acid feed (propionic, butyric, and hexanoic) and evaluated five different multistage architectures including series, parallel, co-current, and counter-current setups. The single-stage, two-dimensional steady-state model captured the effect of the flow-field, concentration, and potential gradients, yielding reasonable agreement with experimental data. We then investigated the tradeoff between number of stages, product purity, and productivity, and assessed the impact of membrane selectivity. In sum, cascaded redox-ED with reflux simultaneously improved product purity and productivity, while series or equivalent single-stage architectures presented a tradeoff between VFA purity and productivity.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae17eb">https://doi.org/10.1149/1945-7111/ae17eb</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/adc553" class="art-list-item-title event_main-link">Editors’ Choice—Rapid Deactivation Convolutes Electrochemical CO<sub>2</sub> Reduction Selectivity Measurements on Gold Rotating Ring Disk Electrodes</a><p class="small art-list-item-meta">Maria Kelly <em>et al</em> 2025 <em>J. Electrochem. Soc.</em> <b>172</b> 046503 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/adc553/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Rapid Deactivation Convolutes Electrochemical CO2 Reduction Selectivity Measurements on Gold Rotating Ring Disk Electrodes</span></a><a href="/article/10.1149/1945-7111/adc553/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Rapid Deactivation Convolutes Electrochemical CO2 Reduction Selectivity Measurements on Gold Rotating Ring Disk Electrodes</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Editors’ Choice—Rapid Deactivation Convolutes Electrochemical CO2 Reduction Selectivity Measurements on Gold Rotating Ring Disk Electrodes" data-link-purpose-append-open="Editors’ Choice—Rapid Deactivation Convolutes Electrochemical CO2 Reduction Selectivity Measurements on Gold Rotating Ring Disk Electrodes">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Voltammetric measurements of electrochemical CO<sub>2</sub> reduction reaction (CO<sub>2</sub>RR) selectivity on rotating ring disk electrodes (RRDE) are a rapid and sensitive method for quantifying an electrocatalyst’s selectivity, i.e. faradaic efficiency (FE). This method has been applied to polycrystalline Au electrocatalysts where a Au disk electrode catalyzes both the CO<sub>2</sub>RR and hydrogen evolution reaction while the concentric Au ring electrode selectively senses CO by oxidizing CO back to CO<sub>2</sub>. Such measurements enabled fundamental mechanistic studies but suffer from poor inter-laboratory reproducibility. This work identifies causes of variability in RRDE selectivity measurements by comparing protocols with different electrochemical methods, reagent purities, and glassware cleaning procedures. We observed FE<sub>CO</sub> decrease by 56% during 5 min chronoamperometry measurements, a phenomenon that is not readily apparent in voltammetric scans due to their dynamic nature. Electroplating of electrolyte impurities onto the disk and ring surfaces were identified as a major contributor to Au deactivation. Additionally, the oxygen reduction reaction may lead to higher disk currents in inadequately purged electrolytes, causing an apparent underestimation of FE<sub>CO</sub> at low overpotentials. Lastly, we propose operational bounds for CO<sub>2</sub>RR selectivity measurements on Au using the RRDE method and provide suggestions on steps for improving the accuracy of this technique.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/adc553">https://doi.org/10.1149/1945-7111/adc553</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/adbd7d" class="art-list-item-title event_main-link">Editors’ Choice—Molten Salt Electrolysis in Chloride Melts for Energy-Efficient Iron Metal Production</a><p class="small art-list-item-meta">Anar Badalbayli <em>et al</em> 2025 <em>J. Electrochem. Soc.</em> <b>172</b> 032508 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/adbd7d/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Molten Salt Electrolysis in Chloride Melts for Energy-Efficient Iron Metal Production</span></a><a href="/article/10.1149/1945-7111/adbd7d/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Molten Salt Electrolysis in Chloride Melts for Energy-Efficient Iron Metal Production</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Editors’ Choice—Molten Salt Electrolysis in Chloride Melts for Energy-Efficient Iron Metal Production" data-link-purpose-append-open="Editors’ Choice—Molten Salt Electrolysis in Chloride Melts for Energy-Efficient Iron Metal Production">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>This study explores chloride molten salt electrolysis (CMSE) as a promising route for energy-efficient iron metal (Fe) production. Moderate temperature (500 °C) LiCl-KCl molten salts offer excellent thermodynamic stability, high ionic conductivity and diffusivity, and high solubility for FeCl<sub>3</sub>, thereby enabling efficient Fe metal extraction at high electrowinning rates. Here, we demonstrate the two essential steps for converting taconite ore into Fe metal. First, Fe<sub>2</sub>O<sub>3</sub> from taconite pellets was selectively leached in HCl yielding a high-purity FeCl<sub>3</sub> aqueous solution, while the gangue components settled at the bottom. Then, anhydrous FeCl<sub>3</sub> was electrolyzed in a LiCl-KCl eutectic molten salt at 500 °C at high current density (1 A cm<sup>−2</sup>) and at high Coulombic efficiency (&gt;85%). Analysis of the electrowon Fe deposits revealed dendritic structures with purity of &gt;99 wt%, which could be further improved to nearly 100 wt% through arc re-melting. CMSE offers low specific energy consumption (3.7 kWhr kg<sup>−1</sup>), competitive with H<sub>2</sub>-DRI and other electrolytic approaches being pursued globally. Our findings underscore the potential of CMSE as an energy-efficient route for electrosynthesis of Fe metal.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/adbd7d">https://doi.org/10.1149/1945-7111/adbd7d</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/adaf5b" class="art-list-item-title event_main-link">Editors’ Choice—Investigation of the Dynamic Evolution of the Cathode-Electrolyte Interphase Using Scanning Electrochemical Microscopy</a><p class="small art-list-item-meta">Guoxin Li <em>et al</em> 2025 <em>J. Electrochem. Soc.</em> <b>172</b> 026501 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/adaf5b/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Investigation of the Dynamic Evolution of the Cathode-Electrolyte Interphase Using Scanning Electrochemical Microscopy</span></a><a href="/article/10.1149/1945-7111/adaf5b/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Editors’ Choice—Investigation of the Dynamic Evolution of the Cathode-Electrolyte Interphase Using Scanning Electrochemical Microscopy</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Editors’ Choice—Investigation of the Dynamic Evolution of the Cathode-Electrolyte Interphase Using Scanning Electrochemical Microscopy" data-link-purpose-append-open="Editors’ Choice—Investigation of the Dynamic Evolution of the Cathode-Electrolyte Interphase Using Scanning Electrochemical Microscopy">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Cathode-electrolyte interphase (CEI) is critical for inhibiting the cathode degradation to maintain cell life. However, the evolution of the CEI is still unclear due to its complex and slow dynamic process. Here we used scanning electrochemical microscopy (SECM) for in situ investigation of CEI formation process on LiFePO<sub>4</sub> cathode. Feedback images and probe scan curves showed a heterogeneous passivation that was gently generated on the LiFePO<sub>4</sub> particles during both charging and discharging. Besides, a LiFePO<sub>4</sub> composited electrode was also used to investigate the CEI formation to simulate the condition of real battery system. The composited cathode does not show obvious CEI formation within first two cycles. The SECM results between the pristine LiFePO<sub>4</sub> particles and the composited LiFePO<sub>4</sub> indicated the dynamic accumulation of CEI, which is influenced by the ability to charge transfer kinetics of cathode materials. This approach provided a feasible consideration for the connections between the dynamic evolution of the CEI and changes in charge transfer capability of cathode during cycling.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p><h2 id="artAbst3" class="collapse-blocked">Highlights</h2><p><ul><li><p>In-situ investigation of cathode-electrolyte interphase formation.</p></li><li><p>The evolution of native active material and composite slurry were compared.</p></li><li><p>The electrochemical activity change upon cathode cycling are analysed in situ.</p></li><li><p>The influence of the charge transfer capability upon CEI generation is revealed.</p></li></ul></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/adaf5b">https://doi.org/10.1149/1945-7111/adaf5b</a></div></div></li></ul><!--    articleEntryList end--></div></div></div><!-- End Editor's chocie tabpanel --><!-- Start AM tabpanel --><div tabindex="0"
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                         style="display: none;"><!--    accepted manuscript listing start--><p id="jnl-issue-disp-links" class="cf"><button data-reveal-label-alt="Close all abstracts" class="reveal-all-trigger mr-2 small"
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               data-link-purpose-append-open="in this tab">Open all abstracts<span class="offscreen-hidden">,&nbsp;in this tab</span></button></p><!-- Start AM list content --><ul class="art-list" id="wd-jnl-issue-art-list"><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/ae9ce1" class="art-list-item-title event_main-link">Study on the Preparation of Polysilicon from Fluorine-Containing Silicon Slag by Molten Salt Electrolysis and the Performance of Lithium-Ion Battery Anodes</a><p class="small art-list-item-meta">Zhou et al&nbsp;</p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9ce1/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View accepted manuscript<span class="offscreen-hidden">,&nbsp;Study on the Preparation of Polysilicon from Fluorine-Containing Silicon Slag by Molten Salt Electrolysis and the Performance of Lithium-Ion Battery Anodes</span></a><a href="/article/10.1149/1945-7111/ae9ce1/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Study on the Preparation of Polysilicon from Fluorine-Containing Silicon Slag by Molten Salt Electrolysis and the Performance of Lithium-Ion Battery Anodes</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Study on the Preparation of Polysilicon from Fluorine-Containing Silicon Slag by Molten Salt Electrolysis and the Performance of Lithium-Ion Battery Anodes" data-link-purpose-append-open="Study on the Preparation of Polysilicon from Fluorine-Containing Silicon Slag by Molten Salt Electrolysis and the Performance of Lithium-Ion Battery Anodes">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small">
						<p>Aiming at the problems of difficult treatment and low resource utilization rate of fluorine-containing silicon slag (mainly composed of SiO2 and F), an industrial solid waste generated from the wet-process phosphoric acid industry, this study adopts the molten salt electrolysis method and uses fluorine-containing silicon slag as precursor to directly prepare polysilicon via electrolytic deoxidation in molten CaCl2. The effects of tableting pressure, electrolytic voltage and time, the obtained product were systematically investigated. The results demonstrate that under the 30 MPa, 3.2 V, and 12 h of electrolysis at 900 ℃, polysilicon can be successfully obtained. Characterizations via SEM and TEM confirm that the product is silicon nanowires with a diameter of 20-50 nm, growing along the [111] crystallographic orientation. The electrolysis process follows a dual-path reduction mechanism: direct reduction of SiO2, and reduction of the CaSiO3 intermediate generated from the reaction between SiO2 and CaO. The as-prepared polysilicon as an anode material for lithium-ion batteries exhibits outstanding electrochemical performance. After 1000 cycles at a current density of 1 A/g, the Coulombic efficiency still remains at 97%, proving the application potential of this solid waste resource utilization route in the field of new energy material preparation.</p>
					</div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9ce1">https://doi.org/10.1149/1945-7111/ae9ce1</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/ae9ce2" class="art-list-item-title event_main-link">Electrolytic Recovery of Spent Indium Zinc Oxide Targets in Aqueous Solution</a><p class="small art-list-item-meta">Zhou et al&nbsp;</p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9ce2/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View accepted manuscript<span class="offscreen-hidden">,&nbsp;Electrolytic Recovery of Spent Indium Zinc Oxide Targets in Aqueous Solution</span></a><a href="/article/10.1149/1945-7111/ae9ce2/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Electrolytic Recovery of Spent Indium Zinc Oxide Targets in Aqueous Solution</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Electrolytic Recovery of Spent Indium Zinc Oxide Targets in Aqueous Solution" data-link-purpose-append-open="Electrolytic Recovery of Spent Indium Zinc Oxide Targets in Aqueous Solution">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small">
						<p>Indium zinc oxide (IZO, typical mass ratio of indium oxide to zinc oxide is 9:1) is widely employed in advanced electronic devices. During the preparation and application of IZO, a large amount of spent IZO is generated. However, the recycling of spent IZO commonly confronts significant challenges, including high energy consumption, severe environmental pollution, and complex pretreatment requirements, which impede the sustainable utilization of strategic metal resources. To address these issues, this study proposes a green electrochemical method for recycling In and Zn from spent IZO at room temperature. Operating in an environmentally benign sodium salt aqueous electrolyte, this process achieves efficient and continuous electro-deoxidation of IZO. It demonstrated that the method enables highly efficient recovery of metallic indium and zinc while effectively removing impurities including Al, Si, and Fe. The entire process is characterized by low carbon emissions, absence of toxic reagents, and a less environmental burden.</p>
					</div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9ce2">https://doi.org/10.1149/1945-7111/ae9ce2</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/ae9ce3" class="art-list-item-title event_main-link">Core-Shell Technology Assisted Graphite-Silicon Composite Anode for NCA-based Li-ion Battery</a><p class="small art-list-item-meta">Gupta et al&nbsp;</p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9ce3/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View accepted manuscript<span class="offscreen-hidden">,&nbsp;Core-Shell Technology Assisted Graphite-Silicon Composite Anode for NCA-based Li-ion Battery</span></a><a href="/article/10.1149/1945-7111/ae9ce3/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Core-Shell Technology Assisted Graphite-Silicon Composite Anode for NCA-based Li-ion Battery</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Core-Shell Technology Assisted Graphite-Silicon Composite Anode for NCA-based Li-ion Battery" data-link-purpose-append-open="Core-Shell Technology Assisted Graphite-Silicon Composite Anode for NCA-based Li-ion Battery">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small">
						<p>This study demonstrates the development of surface engineered silicon nanoparticles with TiO2 coating (Si@TiO₂) and its reinforcement into pristine MCMB graphite (Gr) matrix, forming a composite (GST) electrode for high-energy LIBs. The study further delves into structural characterization and electrochemical performance of the developed GST composite, which is benchmarked against Gr-silicon composite (GS). Comprehensive structural analysis of GS and GST reveals uniform dispersion and successful integration of Si within the Gr matrix and the formation of a well-defined TiO2 shell (≈ 10 nm thickness) over Si nanoparticles. Electrochemical analysis shows superior performance for GST. In full-cell, GST-NCA composite delivers ≈ 144 mAhg-1anode and retains ≈ 81 % of its initial capacity after 100 cycles at C/3, outperforming the GS-NCA counterpart, while also exhibiting excellent rate capability up to 8C and stable long-term cycling over 300 cycles at C/3, maintaining ≈ 99 % coulombic efficiency. EIS shows lower impedance for GST, suggesting improved charge transfer kinetics. Post-cycling characterizations reveal improved SEI deposition with fewer cracks and a lower thickness growth for GST compared to GS after cycling, confirming its superior mechanical integrity. These results demonstrate that TiO2-based core-shell architecture effectively suppresses Si-induced degradation, enabling stable, high-performance full-cells for future LIBs.</p>
					</div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9ce3">https://doi.org/10.1149/1945-7111/ae9ce3</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/ae9ce4" class="art-list-item-title event_main-link">Exact Electrochemical Impedance of Heterogeneous Electrodes Modeled as Coupled Finite $RC$ Transmission Lines</a><p class="small art-list-item-meta">Allagui et al&nbsp;</p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9ce4/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View accepted manuscript<span class="offscreen-hidden">,&nbsp;Exact Electrochemical Impedance of Heterogeneous Electrodes Modeled as Coupled Finite $RC$ Transmission Lines</span></a><a href="/article/10.1149/1945-7111/ae9ce4/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Exact Electrochemical Impedance of Heterogeneous Electrodes Modeled as Coupled Finite $RC$ Transmission Lines</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Exact Electrochemical Impedance of Heterogeneous Electrodes Modeled as Coupled Finite $RC$ Transmission Lines" data-link-purpose-append-open="Exact Electrochemical Impedance of Heterogeneous Electrodes Modeled as Coupled Finite $RC$ Transmission Lines">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small">
						<p>In this work, we investigate the electrical response of a heterogeneous porous electrode/electrolyte system, modeled as two $RC$ transmission line (TL) subdomains of different lengths and with distinct electrical properties, coupled through an ideal interface that enforces the continuity of both voltage and current, thus giving rise to a shared flux between the two diffusion problems. This is different combining the impedances of the $RC$ TL segments in series, which implicitly imposes a blocking condition at the interface, and thereby discards any dynamic coupling between the subdomains. We derive the exact input impedance of the overall composite system, and demonstrate that it does not reduce to the sum of two independent $Z_{\mathrm{n}}= p^{-1} {\coth p} $ ($p =  \sqrt{j\omega\tau}$) impedances except in the limit where both subdomains share identical characteristic electrical and propagation properties. We analyze how variations in downstream subdomain's electrical and geometrical properties affect the overall impedance response, and show that the internal coupling induces characteristic signatures in the impedance spectrum, most pronounced in the low and intermediate frequency regimes. The results provide a simple, yet physically grounded picture for interpreting the impedance spectra of electrochemical energy storage and conversion devices with spatially heterogeneous porous structures</p>
					</div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9ce4">https://doi.org/10.1149/1945-7111/ae9ce4</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1945-7111/ae9c71" class="art-list-item-title event_main-link">Mass Transport and Transmembrane Electric Potential in Multi-Ionic Systems: From Entropy and Nernst-Planck to Hodgkin-Huxley.</a><p class="small art-list-item-meta">Kocherginsky&nbsp;</p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9c71/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View accepted manuscript<span class="offscreen-hidden">,&nbsp;Mass Transport and Transmembrane Electric Potential in Multi-Ionic Systems: From Entropy and Nernst-Planck to Hodgkin-Huxley.</span></a><a href="/article/10.1149/1945-7111/ae9c71/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Mass Transport and Transmembrane Electric Potential in Multi-Ionic Systems: From Entropy and Nernst-Planck to Hodgkin-Huxley.</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Mass Transport and Transmembrane Electric Potential in Multi-Ionic Systems: From Entropy and Nernst-Planck to Hodgkin-Huxley." data-link-purpose-append-open="Mass Transport and Transmembrane Electric Potential in Multi-Ionic Systems: From Entropy and Nernst-Planck to Hodgkin-Huxley.">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small">
						<p>A new equation for transmembrane electric potential for several ions with different charges is suggested. This potential is determined by a system of Nernst-Planck equations for each of ions. We explain why the experimental slope of   may change from  to 0 and even change its sign for multicomponent systems. Ohm’s law for electric current of each ion is not valid anymore. Problems with Nikolsky-Eisenman equation for experiments with solid membranes and multivalent ions disappear. Cl- concentrations in the donor and acceptor solutions change their places in the nominator and denominator of final equation. At zero total current a gradient of one ion concentration may lead to coupled co- or counter-transport of another ion in a membrane, leading to both electrogenic and electrically silent transport. Instead of Hodgkin-Huxley a new model describes mutual influence of transported K+ and Na+ ions, important in explanation of an action potential. Our theory describes many phenomena, and it will be useful in new experimental situations. One of the examples is spontaneous oscillations of both voltage and current at temperature-induced phase transitions in biomimetic membranes without any proteins.</p>
					</div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9c71">https://doi.org/10.1149/1945-7111/ae9c71</a></div></div></li></ul><!-- End AM list content --><p><a href="/journal/1945-7111/acceptedmanuscripts/1">More Accepted manuscripts</a></p><!--    accepted manuscript listing end--></div></div></div><!-- End AM tabpanel --><!-- Start Trending tabpanel --><div tabindex="0"
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                    Open all abstracts<span class="offscreen-hidden">,&nbsp;in this tab</span></button></p><!--    articleEntryList start--><ul class="art-list"><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae94f1" class="art-list-item-title event_main-link">Chromium Electrodeposition from Hydrate Melts: Formation of Metastable δ-Cr Phase in Conjunction with Hydrogen Incorporation</a><p class="small art-list-item-meta">Haruki Katori <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 162503 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae94f1/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Chromium Electrodeposition from Hydrate Melts: Formation of Metastable δ-Cr Phase in Conjunction with Hydrogen Incorporation</span></a><a href="/article/10.1149/1945-7111/ae94f1/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Chromium Electrodeposition from Hydrate Melts: Formation of Metastable δ-Cr Phase in Conjunction with Hydrogen Incorporation</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Chromium Electrodeposition from Hydrate Melts: Formation of Metastable δ-Cr Phase in Conjunction with Hydrogen Incorporation" data-link-purpose-append-open="Chromium Electrodeposition from Hydrate Melts: Formation of Metastable δ-Cr Phase in Conjunction with Hydrogen Incorporation">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>As an alternative to hexavalent chromium plating, chloride-based hydrate melts enable crystalline chromium electrodeposition from trivalent chromium without the use of organic complexing agents. Cr films deposited from these hydrate melt-based baths uniquely contain a metastable <i>δ</i>-Cr phase absent in conventional baths. Achieving hard coatings with adequate mechanical properties requires a systematic understanding of the crystallographic features including phase formation. In this study, the deposition of <i>δ</i>-Cr and its subsequent phase transformation to <i>α</i>-Cr were systematically investigated from the perspectives of crystal growth mode and hydrogen incorporation. The results indicate that <i>δ</i>-Cr preferentially forms during the initial nucleation and coalescence stage, where isotropic fine grains are generated. As electrodeposition proceeds, the crystal growth mode transitions to columnar growth, in which <i>α</i>-Cr becomes the dominant phase. The obtained <i>δ</i>-Cr was confirmed to transform into <i>α</i>-Cr at relatively low temperatures ranging from room temperature to 250 °C. The thermal desorption spectrum of hydrogen and time-of-flight secondary-ion mass spectrometry (ToF-SIMS) experiments using deuterium as a stable isotope label suggest that the formation and stability of the electrodeposited <i>δ</i>-Cr phase may well be attributed to incorporated hydrogen. These findings provide a fundamental basis for microstructural control of electrodeposited Cr from chloride-based hydrate melts.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae94f1">https://doi.org/10.1149/1945-7111/ae94f1</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae959d" class="art-list-item-title event_main-link">Time and Temperature Dependent Aging Mechanisms in Commercial Lithium-Ion Cells with SiO<i><sub>x</sub></i>/Graphite Anodes</a><p class="small art-list-item-meta">Jihed Ayari <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 160510 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae959d/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Time and Temperature Dependent Aging Mechanisms in Commercial Lithium-Ion Cells with SiOx/Graphite Anodes</span></a><a href="/article/10.1149/1945-7111/ae959d/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Time and Temperature Dependent Aging Mechanisms in Commercial Lithium-Ion Cells with SiOx/Graphite Anodes</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Time and Temperature Dependent Aging Mechanisms in Commercial Lithium-Ion Cells with SiOx/Graphite Anodes" data-link-purpose-append-open="Time and Temperature Dependent Aging Mechanisms in Commercial Lithium-Ion Cells with SiOx/Graphite Anodes">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>This work addresses the limited understanding of how changes in SiO<sub><i>x</i></sub>/graphite anodes and the N/P ratio induced by aging influence the temperature-dependent transition between degradation mechanisms. It provides insight into the potentially evolving risk of lithium plating and its implications for the safe and durable operation of batteries. Commercial 3.5 Ah Li-ion 18 650 cells with SiO<i><sub>x</sub></i>/graphite anodes (∼2.5 wt.% Si) and Ni-rich LiNi<sub>1−<i>x</i>−<i>y</i></sub>Mn<i><sub>x</sub></i>Co<i><sub>y</sub></i>O<sub>2</sub> cathodes were systematically aged in the temperature range from −10 °C to +45 °C at 0.5 C and 0.85 C. Aging rates were evaluated at both beginning-of-life, i.e. 100%–95% state-of-health and mid-of-life (92.5%–87.5% state-of-health) using Arrhenius plots. The <i>V</i>-shaped Arrhenius plots at beginning-of-life exhibited minima, while the minima of the mid-of-life aged cells were either shifted to higher temperatures or even vanished in the investigated temperature range, indicating an increased susceptibility to lithium plating in the aged cells. Post-mortem analyses using FIB-SEM/EDX mapping revealed that SiO<i><sub>x</sub></i> degradation and related side reactions are more pronounced at high temperatures, while most likely lithium plating predominates at low temperatures. Loss of anode active material in the form of SiO<i><sub>x</sub></i> degradation and the resulting decrease in the N/P ratio is most likely the cause of the observed changes in the Arrhenius plots after cycling.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p><h2 id="artAbst3" class="collapse-blocked">Highlights</h2><p><ul><li><p>Aging of commercial 18650 Li-ion cells investigated from -10°C to 45°C</p></li><li><p>V-shaped Arrhenius plots for new cells indicate Li plating at low temperatures</p></li><li><p>Post-Mortem analysis and FIB-SEM/EDX show degradation of SiO<sub><i>x</i></sub></p></li><li><p>Degradation of SiO<sub><i>x</i></sub> in anode decreases N/P ratio and changes Arrhenius plot</p></li><li><p>High temperature aging most likely increases later susceptibility to Li plating</p></li></ul></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae959d">https://doi.org/10.1149/1945-7111/ae959d</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae9c72" class="art-list-item-title event_main-link">The Impact of Cobalt Substitution in Lithiated Spinel/Layered Li<sub>2</sub>(MnNi)<sub>1-δ</sub>Co<sub>δ</sub>O<sub>4</sub> (0≤δ≤0.667) Cathodes for Li-Ion Batteries</a><p class="small art-list-item-meta">Subhadip Mallick <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b></b>  </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9c72/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;The Impact of Cobalt Substitution in Lithiated Spinel/Layered Li2(MnNi)1-δCoδO4 (0≤δ≤0.667) Cathodes for Li-Ion Batteries</span></a><a href="/article/10.1149/1945-7111/ae9c72/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;The Impact of Cobalt Substitution in Lithiated Spinel/Layered Li2(MnNi)1-δCoδO4 (0≤δ≤0.667) Cathodes for Li-Ion Batteries</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="The Impact of Cobalt Substitution in Lithiated Spinel/Layered Li2(MnNi)1-δCoδO4 (0≤δ≤0.667) Cathodes for Li-Ion Batteries" data-link-purpose-append-open="The Impact of Cobalt Substitution in Lithiated Spinel/Layered Li2(MnNi)1-δCoδO4 (0≤δ≤0.667) Cathodes for Li-Ion Batteries">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>In 2020, the discovery of the lithiated spinel Li2MnNiO4 opened the door to the design of a new class of cathode materials for the lithium-ion battery industry.  This compound is typically prepared in air at 400 °C and co-exists with a disordered layered structure of the same composition (LiMn0.5Ni0.5O2), delivering most of its capacity (~200 mAh/g) between 4.8 and 3.0 V with essentially no redox on the manganese ions.  This communication reports the effects of cobalt substitution on the structural and electrochemical properties of lithiated-spinel/layered Li2(MnNi)1-δCoδO4 composite electrodes over the compositional range 0≤δ≤0.667.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9c72">https://doi.org/10.1149/1945-7111/ae9c72</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae9c73" class="art-list-item-title event_main-link">The Role of Nitrates in Pitting Corrosion of Stainless Steel in Concentrated Salt Solutions: Understanding Critical Ratios in Fully Immersed and Atmospheric Environments</a><p class="small art-list-item-meta">Daria Bentley <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b></b>  </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9c73/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;The Role of Nitrates in Pitting Corrosion of Stainless Steel in Concentrated Salt Solutions: Understanding Critical Ratios in Fully Immersed and Atmospheric Environments</span></a><a href="/article/10.1149/1945-7111/ae9c73/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;The Role of Nitrates in Pitting Corrosion of Stainless Steel in Concentrated Salt Solutions: Understanding Critical Ratios in Fully Immersed and Atmospheric Environments</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="The Role of Nitrates in Pitting Corrosion of Stainless Steel in Concentrated Salt Solutions: Understanding Critical Ratios in Fully Immersed and Atmospheric Environments" data-link-purpose-append-open="The Role of Nitrates in Pitting Corrosion of Stainless Steel in Concentrated Salt Solutions: Understanding Critical Ratios in Fully Immersed and Atmospheric Environments">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Nitrates, common atmospheric compounds, have been observed in atmospheric environments where they can deposit on metal surfaces along with seawater aerosols.  In many cases, nitrates have been shown to inhibit localized corrosion of stainless steels, a common infrastructure material component, at various nitrate:chloride ratios. In this study, full immersion polarization scans were performed on 304 Stainless Steel (SS304) coupons at a variety of scan rates, temperatures, and nitrate:chloride ratios to further examine the inhibitory influences. Additionally, atmospheric exposures were performed with droplet experiments in an atmospheric chamber under both static and diurnal relative humidity cycles.  Atmospheric exposures examined the same initial nitrate:chloride ratios as explored in full immersion but also looked at influences of droplet size effects as well as dynamic conditions. Pit frequency and pit area calculations to quantify the effects of nitrates in these solutions were completed. It was found that the inhibition ratios for nitrates to chloride in full immersion do not translate directly to atmospheric conditions.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9c73">https://doi.org/10.1149/1945-7111/ae9c73</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae96d3" class="art-list-item-title event_main-link">Selective Electrochemical Recovery of Valuable Metals from Spent Lithium-Ion Batteries Using a Betaine-Based Deep Eutectic Solvent</a><p class="small art-list-item-meta">Kazem Mohammadzadeh <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 162502 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae96d3/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Selective Electrochemical Recovery of Valuable Metals from Spent Lithium-Ion Batteries Using a Betaine-Based Deep Eutectic Solvent</span></a><a href="/article/10.1149/1945-7111/ae96d3/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Selective Electrochemical Recovery of Valuable Metals from Spent Lithium-Ion Batteries Using a Betaine-Based Deep Eutectic Solvent</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Selective Electrochemical Recovery of Valuable Metals from Spent Lithium-Ion Batteries Using a Betaine-Based Deep Eutectic Solvent" data-link-purpose-append-open="Selective Electrochemical Recovery of Valuable Metals from Spent Lithium-Ion Batteries Using a Betaine-Based Deep Eutectic Solvent">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>The rapid growth in lithium-ion battery (LIB) deployment has led to increasing volumes of end-of-life batteries, creating an urgent need for sustainable recycling technologies capable of recovering critical metals from complex waste streams. Although leaching has been successfully shown in various DES systems, selective recovery of metals/metal oxides still remain a challenge. In this study, a deep eutectic solvent (DES) of betaine hydrochloride and ethylene glycol is employed as a green medium for both dissolution of valuable metals and selective electrochemical recovery from LIB black mass. Rapid dissolution of Li, Ni, Co, and Mn together with 86% Cu was achieved within 30 min at 100 °C. Based on electrochemical studies, it was observed that temperature and potential/ current can be adjusted for selective metal recovery. Copper was selectively deposited at 40 °C, while increasing the deposition temperature to 60 and 80 °C enabled deposition of Ni–Co alloys. Manganese was recovered from the remaining electrolyte via carbonate precipitation. The integrated process achieved overall recovery efficiencies of approximately 98% for Cu, ∼90% for Ni and Co, and ∼80% for Mn. Thus, this work demonstrates a selective and environmentally benign strategy for recovering valuable metals from complex LIB waste streams, providing a promising pathway toward circular battery recycling.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae96d3">https://doi.org/10.1149/1945-7111/ae96d3</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae8b2d" class="art-list-item-title event_main-link">Modelling Intermediate-Current Transitions in Asymmetric-Valence Binary Electrolytes</a><p class="small art-list-item-meta">Georgina C. Ryan <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 166502 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae8b2d/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Modelling Intermediate-Current Transitions in Asymmetric-Valence Binary Electrolytes</span></a><a href="/article/10.1149/1945-7111/ae8b2d/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Modelling Intermediate-Current Transitions in Asymmetric-Valence Binary Electrolytes</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Modelling Intermediate-Current Transitions in Asymmetric-Valence Binary Electrolytes" data-link-purpose-append-open="Modelling Intermediate-Current Transitions in Asymmetric-Valence Binary Electrolytes">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Asymmetric valences in a binary electrolyte can significantly affect the performance of systems such as reverse electrodialysis cells, batteries, and supercapacitors. To generate a theoretical understanding of this effect, we consider a steady one-dimensional Poisson Nernst Planck model of an electrolytic cell with imposed constant ionic fluxes, focusing on varying ion valences in a general asymmetric binary electrolyte. Numerical simulations reveal a smooth transition between the qualitatively distinct near-equilibrium and strongly non-equilibrium steady-state regimes. These regimes are distinguished by a valence-dependent transition point at an intermediate current where the classical Debye-scale boundary layer vanishes. We characterize this transition using asymptotic analysis, recovering the Gouy Chapman and limiting-current results in the appropriate limits, and determining the correct transition results when neither is appropriate. We provide implicit solutions for the potential and ion concentrations of general asymmetric binary electrolytes and, notably, we provide explicit analytic expressions for the asymptotic composite solutions for <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="tex"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/173/16/166502/revision3/jesae8b2dieqn1.gif" style="max-width: 100%;" alt="$2z\hspace{-0.8 mm}:\hspace{-0.8 mm}z$" align="top" role="math"></img></span><script type="math/tex">2z\hspace{-0.8 mm}:\hspace{-0.8 mm}z</script></span></span>, <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="tex"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/173/16/166502/revision3/jesae8b2dieqn2.gif" style="max-width: 100%;" alt="$z\hspace{-0.8 mm}:\hspace{-0.8 mm}2z$" align="top" role="math"></img></span><script type="math/tex">z\hspace{-0.8 mm}:\hspace{-0.8 mm}2z</script></span></span>, and <span xmlns:xlink="http://www.w3.org/1999/xlink" class="inline-eqn"><span class="tex"><span class="texImage"><img src="data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAAEAAAABCAQAAAC1HAwCAAAAC0lEQVR42mNkYAAAAAYAAjCB0C8AAAAASUVORK5CYII=" data-src="https://content.cld.iop.org/journals/1945-7111/173/16/166502/revision3/jesae8b2dieqn3.gif" style="max-width: 100%;" alt="$z\hspace{-0.8 mm}:\hspace{-0.8 mm}z$" align="top" role="math"></img></span><script type="math/tex">z\hspace{-0.8 mm}:\hspace{-0.8 mm}z</script></span></span> electrolytes. We show how the results can be presented in a collapsed phase diagram that can be used to predict qualitative intermediate-current steady-state behavior in terms of ion valences and fluxes.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p><h2 id="artAbst3" class="collapse-blocked">Highlights</h2><p><ul><li><p>Valence ratio controls behavior in steady-state electrolytes with current.</p></li><li><p>Asymptotic analysis of Poisson Nernst Planck equations produces mathematical model.</p></li><li><p>Analytic solutions derived with asymmetric valences for concentrations and potential.</p></li><li><p>Smooth transition between Gouy Chapman theory and limiting current regime.</p></li><li><p>Diffuse layer vanishes at a critical current.</p></li></ul></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae8b2d">https://doi.org/10.1149/1945-7111/ae8b2d</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae92d6" class="art-list-item-title event_main-link">Direct Electrochemical Recovery of Rhodium from Spent Hydroformylation Catalyst Streams</a><p class="small art-list-item-meta">Ching-Hsiu Chung <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 163501 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae92d6/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Direct Electrochemical Recovery of Rhodium from Spent Hydroformylation Catalyst Streams</span></a><a href="/article/10.1149/1945-7111/ae92d6/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Direct Electrochemical Recovery of Rhodium from Spent Hydroformylation Catalyst Streams</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Direct Electrochemical Recovery of Rhodium from Spent Hydroformylation Catalyst Streams" data-link-purpose-append-open="Direct Electrochemical Recovery of Rhodium from Spent Hydroformylation Catalyst Streams">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Homogeneous Rhodium-based catalysts are essential for hydroformylation because of their high activity, but recovering these valuable critical metals from spent reaction streams remains difficult using conventional energy- and chemical-intensive methods. Here, the direct recovery of the spent Rh from a post-reaction hydroformylation stream is achieved via electrowinning at both cathode and anode, followed by electro-stripping in diluted acid. Under optimized conditions, a single electrowinning stage recovered 37.6% of the spent Rh catalyst (19.3% from the cathode and 18.3% from the anode). Three cascade electrowinning stages increase cumulative Rh recovery to 77.6%, and subsequent electro-stripping yielded an overall Rh recovery of 24.0%. Reticulated Vitreous Carbon (RVC) and activated carbon cloth (ACC) electrodes were selected to maximize Rh recovery, and dichloromethane (DCM) containing tetrabutylammonium hexafluorophosphate (TBAPF<sub>6</sub>) served as a conductive reaction medium that maintained hydroformylation catalytic performance. X-ray photoelectron spectroscopy (XPS) revealed reduction of the spent Rh catalyst to Rh(0) at the working electrode and oxidation to Rh(III) at the counter electrode. Mass spectrometry confirmed that the stripped Rh in the acidic solution existed as chloride- or nitrate- ligated complexes. A techno-economic analysis indicates that the process achieves cost savings of more than 100 000 USD per kilogram of Rh recovered, corresponding to approximately 40% of the average Rh market value from recent years. This work uniquely demonstrates the direct electrochemical recovery of spent homogeneous hydroformylation catalysts from an industrially relevant reaction medium.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae92d6">https://doi.org/10.1149/1945-7111/ae92d6</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae940b" class="art-list-item-title event_main-link">Anion Effects on Manganese Dioxide Charge Storage in Electrochemical Capacitor Systems</a><p class="small art-list-item-meta">Fahad J. Mujammami and Scott W. Donne 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 160506 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae940b/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Anion Effects on Manganese Dioxide Charge Storage in Electrochemical Capacitor Systems</span></a><a href="/article/10.1149/1945-7111/ae940b/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Anion Effects on Manganese Dioxide Charge Storage in Electrochemical Capacitor Systems</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Anion Effects on Manganese Dioxide Charge Storage in Electrochemical Capacitor Systems" data-link-purpose-append-open="Anion Effects on Manganese Dioxide Charge Storage in Electrochemical Capacitor Systems">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Herein the behavior of electrodeposited manganese dioxide is examined in different aqueous electrolytes to demonstrate the impact the electrolyte anion has on its performance as an electrochemical capacitor electrode. Potassium salts of sulfate, chloride, perchlorate and nitrate were used. A double pulse chronoamperometric technique is used to deposit the manganese dioxide onto a platinum coated quartz EQCM electrode. These confirm manganese dioxide as the electrodeposition product, as well as enable determination of the manganese dioxide electrochemically active surface area. Performance and mechanistic analyses were conducted using cyclic voltammetry in which case the sulfate system performed best (217 F·g<sup>−1</sup> at 0.01 V·s<sup>−1</sup>). The rate of capacitance fade (d<i>C</i>/dlog(<i>v</i>)) decreased as the Coulombic efficiency tended to unity. EQCM data show that the sulfate system is unique in that sulfate adsorption and desorption contribute to charge storage. This was not the case for the other systems, in which case only cation (de)intercalation processes were apparent. It is demonstrated that K<sup>+</sup> (de)intercalation is a relatively facile process, albeit with limited capacity, compared to H<sup>+</sup> (de)intercalation, which has access to greater charge because of diffusion within the manganese dioxide structure. In the sulfate system, anion adsorption and desorption was also a relatively slow process.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae940b">https://doi.org/10.1149/1945-7111/ae940b</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae94ee" class="art-list-item-title event_main-link">Multiscale Modeling of Lithium-Ion Batteries: Integrating P4D Analysis with Microstructure-Resolved DEM Simulations</a><p class="small art-list-item-meta">Timothy Carlson <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b>173</b> 160505 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae94ee/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Multiscale Modeling of Lithium-Ion Batteries: Integrating P4D Analysis with Microstructure-Resolved DEM Simulations</span></a><a href="/article/10.1149/1945-7111/ae94ee/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Multiscale Modeling of Lithium-Ion Batteries: Integrating P4D Analysis with Microstructure-Resolved DEM Simulations</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Multiscale Modeling of Lithium-Ion Batteries: Integrating P4D Analysis with Microstructure-Resolved DEM Simulations" data-link-purpose-append-open="Multiscale Modeling of Lithium-Ion Batteries: Integrating P4D Analysis with Microstructure-Resolved DEM Simulations">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Incorporating electrode microstructure design and manufacturing variability remains a major barrier to developing predictive digital twins of practical batteries. This work presents an integrated simulation workflow that upscales manufacturing-induced microstructural features to cell-level electrochemical behavior and validates predictions against published experimental data. The workflow begins with discrete element method (DEM) mixing simulations of active material particles stochastically generated from particle size distributions. The resulting microstructure is then compressed using Finite Element (FE) calendering simulations to match experimentally observed mass loading and porosity. Spatially resolved continuum properties, including local particle radii, specific surface area, and porosity, are extracted from the calendered microstructure. Tortuosity is further quantified through effective diffusivity and solid conductivity simulations to determine Bruggeman coefficients. These parameters are mapped into an inhomogeneous, anisotropic pseudo-4D (P4D) electrochemical model and compared with conventional P4D simulations assuming uniform electrode properties. The integrated workflow shows that realistic manufacturing-induced heterogeneity modifies cell-scale transport behavior and predicted rate capability. Two representative electrode cases from Wood et al. [Journal of Power Sources 515, 230,429 (2021)] are simulated and compared with experimental performance data.</p><h2 id="artAbst2" class="collapse-blocked"></h2><p><span style="display: none;">figure placeholder</span></p><h2 id="artAbst3" class="collapse-blocked">Highlights</h2><p><ul><li><p>Enables efficient analysis and optimization of structured electrodes.</p></li><li><p>Creates heterogeneous battery cell virtual twins from manufacturing simulation.</p></li><li><p>Captures microstructure effects on performance and aging via homogenization.</p></li><li><p>Enables efficient multiphysics simulation of heterogeneous energy materials.</p></li><li><p>Validates predicted trends against published experimental results.</p></li></ul></p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae94ee">https://doi.org/10.1149/1945-7111/ae94ee</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ae9b72" class="art-list-item-title event_main-link">Assessment of Power-Limiting Processes in LiFePO4-Based Composite Electrodes Linking Design and Electrochemical Performance</a><p class="small art-list-item-meta">Mohamed Raghibi <em>et al</em> 2026 <em>J. Electrochem. Soc.</em> <b></b>  </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ae9b72/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Assessment of Power-Limiting Processes in LiFePO4-Based Composite Electrodes Linking Design and Electrochemical Performance</span></a><a href="/article/10.1149/1945-7111/ae9b72/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Assessment of Power-Limiting Processes in LiFePO4-Based Composite Electrodes Linking Design and Electrochemical Performance</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Assessment of Power-Limiting Processes in LiFePO4-Based Composite Electrodes Linking Design and Electrochemical Performance" data-link-purpose-append-open="Assessment of Power-Limiting Processes in LiFePO4-Based Composite Electrodes Linking Design and Electrochemical Performance">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Optimizing electrode design represents a key strategy for improving Li-ion batteries to meet the requirements of electric mobility. Here, we investigate the effects of composition, porosity, and loading on the electrochemical response of LiFePO4 (LFP)-based electrode using galvanostatic cycling (determination of the limiting current density, Jlim) and Impedance Spectroscopy. A complete characterization by electron microscopy, laser granulometry, and gas adsorption, allows microstructure characterization and defines both active material and composite electrodes' surface. Subsequently, the limiting processes are identified and correlated to the evolution of Jlim and the effective diffusion coefficient (Deff). The impedance spectra exhibit a strong dependence with porosity and carbon content with a dominant contribution ascribed to the electronic contact resistance (Rc). Once Rc is minimized at an optimal porosity of 20%, the effect of low carbon content is partially mitigated, leading to a four- to nine-fold increase in Jlim across all compositions. Increasing the LFP loading (0.8 to 2.9 mAh·cm⁻²) results in a twofold drop in performance. Variations in Jlim and Deff indicate a shift from active material-driven to electrolyte-driven limitations. No charge transfer contribution is observed in the impedance spectra, and it is considered negligible, as confirmed by low-temperature measurements.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ae9b72">https://doi.org/10.1149/1945-7111/ae9b72</a></div></div></li></ul><!--    articleEntryList end--><p><a href="/nsearch?currentPage=1&amp;terms=&amp;nextPage=2&amp;previousPage=-1&amp;searchDatePeriod=anytime&amp;journals=1945-7111&amp;accessType=open-access&amp;orderBy=newest&amp;pageLength=20">More Open Access articles</a></p></div></div></div><!-- End Open Access tabpanel --><!-- Start Spotlights tabpanel --><!-- End Spotlights tabpanel --><!-- MostCited tabpanel --><div tabindex="0"
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                    Open all abstracts<span class="offscreen-hidden">,&nbsp;in this tab</span></button></p><!--    articleEntryList start--><ul class="art-list"><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1.1856988" class="art-list-item-title event_main-link">Trends in the Exchange Current for Hydrogen Evolution</a><p class="small art-list-item-meta">J. K. Nørskov <em>et al</em> 2005 <em>J. Electrochem. Soc.</em> <b>152</b> J23 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1.1856988/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Trends in the Exchange Current for Hydrogen Evolution</span></a><a href="/article/10.1149/1.1856988/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Trends in the Exchange Current for Hydrogen Evolution</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Trends in the Exchange Current for Hydrogen Evolution" data-link-purpose-append-open="Trends in the Exchange Current for Hydrogen Evolution">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>A density functional theory database of hydrogen chemisorption energies on close packed surfaces of a number of transition and noble metals is presented. The bond energies are used to understand the trends in the exchange current for hydrogen evolution. A volcano curve is obtained when measured exchange currents are plotted as a function of the calculated hydrogen adsorption energies and a simple kinetic model is developed to understand the origin of the volcano. The volcano curve is also consistent with Pt being the most efficient electrocatalyst for hydrogen evolution. © 2005 The Electrochemical Society. All rights reserved.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1.1856988">https://doi.org/10.1149/1.1856988</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1.2358294" class="art-list-item-title event_main-link">Comment on “Trends in the Exchange Current for Hydrogen Evolution” [<i>J. Electrochem. Soc.</i>, 152, J23 (2005)]</a><p class="small art-list-item-meta">Wolfgang Schmickler and Sergio Trasatti 2006 <em>J. Electrochem. Soc.</em> <b>153</b> L31 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1.2358294/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Comment on “Trends in the Exchange Current for Hydrogen Evolution” [J. Electrochem. Soc., 152, J23 (2005)]</span></a><a href="/article/10.1149/1.2358294/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Comment on “Trends in the Exchange Current for Hydrogen Evolution” [J. Electrochem. Soc., 152, J23 (2005)]</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Comment on “Trends in the Exchange Current for Hydrogen Evolution” [J. Electrochem. Soc., 152, J23 (2005)]" data-link-purpose-append-open="Comment on “Trends in the Exchange Current for Hydrogen Evolution” [J. Electrochem. Soc., 152, J23 (2005)]">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>We compare the adsorption energies calculated by Nørskov  et al. with data derived from experimental values; except for Ni and Co, which absorb hydrogen strongly, there is a linear relation. We discuss the model proposed by these authors in the light of extensive previous work and of experimental data and find it overly simplistic.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1.2358294">https://doi.org/10.1149/1.2358294</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/2.1441707jes" class="art-list-item-title event_main-link">Review—SEI: Past, Present and Future</a><p class="small art-list-item-meta">E. Peled and S. Menkin 2017 <em>J. Electrochem. Soc.</em> <b>164</b> A1703 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/2.1441707jes/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Review—SEI: Past, Present and Future</span></a><a href="/article/10.1149/2.1441707jes/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Review—SEI: Past, Present and Future</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Review—SEI: Past, Present and Future" data-link-purpose-append-open="Review—SEI: Past, Present and Future">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>The Solid-Electrolyte-Interphase (SEI) model for non-aqueous alkali-metal batteries constitutes a paradigm change in the understanding of lithium batteries and has thus enabled the development of safer, durable, higher-power and lower-cost lithium batteries for portable and EV applications. Prior to the publication of the SEI model (1979), researchers used the Butler-Volmer equation, in which a direct electron transfer from the electrode to lithium cations in the solution is assumed. The SEI model proved that this is a mistaken concept and that, in practice, the transfer of electrons from the electrode to the solution in a lithium battery, must be prevented, since it will result in fast self-discharge of the active materials and poor battery performance. This model provides [E. Peled, in “Lithium Batteries,” J.P. Gabano (ed), Academic Press, (1983), E. Peled, <i>J. Electrochem. Soc.</i>, <b>126</b>, 2047 (1979).] new equations for: electrode kinetics (i<sub>o</sub> and b), anode corrosion, SEI resistivity and growth rate and irreversible capacity loss of lithium-ion batteries. This model became a cornerstone in the science and technology of lithium batteries. This paper reviews the past, present and the future of SEI batteries.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/2.1441707jes">https://doi.org/10.1149/2.1441707jes</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/2.0021707jes" class="art-list-item-title event_main-link">Oxygen Release and Its Effect on the Cycling Stability of LiNi<sub>x</sub>Mn<sub>y</sub>Co<sub>z</sub>O<sub>2</sub> (NMC) Cathode Materials for Li-Ion Batteries</a><p class="small art-list-item-meta">Roland Jung <em>et al</em> 2017 <em>J. Electrochem. Soc.</em> <b>164</b> A1361 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/2.0021707jes/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Oxygen Release and Its Effect on the Cycling Stability of LiNixMnyCozO2 (NMC) Cathode Materials for Li-Ion Batteries</span></a><a href="/article/10.1149/2.0021707jes/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Oxygen Release and Its Effect on the Cycling Stability of LiNixMnyCozO2 (NMC) Cathode Materials for Li-Ion Batteries</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Oxygen Release and Its Effect on the Cycling Stability of LiNixMnyCozO2 (NMC) Cathode Materials for Li-Ion Batteries" data-link-purpose-append-open="Oxygen Release and Its Effect on the Cycling Stability of LiNixMnyCozO2 (NMC) Cathode Materials for Li-Ion Batteries">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Layered LiNi<sub>x</sub>Mn<sub>y</sub>Co<sub>z</sub>O<sub>2</sub> (NMC) is a widely used class of cathode materials with LiNi<sub>1/3</sub>Mn<sub>1/3</sub>Co<sub>1/3</sub>O<sub>2</sub> (NMC111) being the most common representative. However, Ni-rich NMCs are more and more in the focus of current research due to their higher specific capacity and energy. In this work we will compare LiNi<sub>1/3</sub>Mn<sub>1/3</sub>Co<sub>1/3</sub>O<sub>2</sub> (NMC111), LiNi<sub>0.6</sub>Mn<sub>0.2</sub>Co<sub>0.2</sub>O<sub>2</sub> (NMC622), and LiNi<sub>0.8</sub>Mn<sub>0.1</sub>Co<sub>0.1</sub>O<sub>2</sub> (NMC811) with respect to their cycling stability in NMC-graphite full-cells at different end-of-charge potentials. It will be shown that stable cycling is possible up to 4.4 V for NMC111 and NMC622 and only up to 4.0 V for NMC811. At higher potentials, significant capacity fading was observed, which was traced back to an increase in the polarization of the NMC electrode, contrary to the nearly constant polarization of the graphite electrode. Furthermore, we show that the increase in the polarization occurs when the NMC materials are cycled up to a high-voltage feature in the dq/dV plot, which occurs at ∼4.7 V vs. Li/Li<sup>+</sup> for NMC111 and NMC622 and at ∼4.3 V vs. Li/Li<sup>+</sup> for NMC811. For the latter material, this feature corresponds to the H2 → H3 phase transition. Contrary to the common understanding that the electrochemical oxidation of carbonate electrolytes causes the CO<sub>2</sub> and CO evolution at potentials above 4.7 V vs. Li/Li<sup>+</sup>, we believe that the observed CO<sub>2</sub> and CO are mainly due to the chemical reaction of reactive lattice oxygen with the electrolyte. This hypothesis is based on gas analysis using On-line Electrochemical Mass Spectrometry (OEMS), by which we prove that all three materials release oxygen from the particle surface and that the oxygen evolution coincides with the onset of CO<sub>2</sub> and CO evolution. Interestingly, the onsets of oxygen evolution for the different NMCs correlate well with the high-voltage redox feature at ∼4.7 V vs. Li/Li<sup>+</sup> for NMC111 and NMC622 as well as at ∼4.3 V vs. Li/Li<sup>+</sup> for NMC811. To support this hypothesis, we show that no CO<sub>2</sub> or CO is evolved for the LiNi<sub>0.43</sub>Mn<sub>1.57</sub>O<sub>4</sub> (LNMO) spinel up to 5 V vs. Li/Li<sup>+</sup>, consistent with the absence of oxygen release. Lastly, we demonstrate by the use of <sup>13</sup>C labeled conductive carbon that it is the electrolyte rather than the conductive carbon which is oxidized by the released lattice oxygen. Taking these findings into consideration, a mechanism is proposed for the reaction of released lattice oxygen with ethylene carbonate yielding CO<sub>2</sub>, CO, and H<sub>2</sub>O.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/2.0021707jes">https://doi.org/10.1149/2.0021707jes</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1.1393348" class="art-list-item-title event_main-link">High Capacity Anode Materials for Rechargeable Sodium‐Ion Batteries</a><p class="small art-list-item-meta">D. A. Stevens and J. R. Dahn 2000 <em>J. Electrochem. Soc.</em> <b>147</b> 1271 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1.1393348/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;High Capacity Anode Materials for Rechargeable Sodium‐Ion Batteries</span></a><a href="/article/10.1149/1.1393348/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;High Capacity Anode Materials for Rechargeable Sodium‐Ion Batteries</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="High Capacity Anode Materials for Rechargeable Sodium‐Ion Batteries" data-link-purpose-append-open="High Capacity Anode Materials for Rechargeable Sodium‐Ion Batteries">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Electrochemical techniques have been used to study the reversible insertion of sodium into hard‐carbon host structures at room temperature. In this paper we compare these results with those for lithium insertion in the same materials and demonstrate the presence of similar alkali metal insertion mechanisms in both cases. Despite the gravimetric capacities being lower for sodium than lithium insertion, we have achieved a reversible sodium capacity of 300 mAh/g, close to that for lithium insertion in graphitic carbon anode materials. Such materials may therefore be useful as anodes in rechargeable sodium‐ion batteries. © 2000 The Electrochemical Society. All rights reserved.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1.1393348">https://doi.org/10.1149/1.1393348</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1.3515880" class="art-list-item-title event_main-link">A Critical Review of Thermal Issues in Lithium-Ion Batteries</a><p class="small art-list-item-meta">Todd M. Bandhauer <em>et al</em> 2011 <em>J. Electrochem. Soc.</em> <b>158</b> R1 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1.3515880/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;A Critical Review of Thermal Issues in Lithium-Ion Batteries</span></a><a href="/article/10.1149/1.3515880/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;A Critical Review of Thermal Issues in Lithium-Ion Batteries</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="A Critical Review of Thermal Issues in Lithium-Ion Batteries" data-link-purpose-append-open="A Critical Review of Thermal Issues in Lithium-Ion Batteries">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Lithium-ion batteries are well-suited for fully electric and hybrid electric vehicles due to their high specific energy and energy density relative to other rechargeable cell chemistries. However, these batteries have not been widely deployed commercially in these vehicles yet due to safety, cost, and poor low temperature performance, which are all challenges related to battery thermal management. In this paper, a critical review of the available literature on the major thermal issues for lithium-ion batteries is presented. Specific attention is paid to the effects of temperature and thermal management on capacity/power fade, thermal runaway, and pack electrical imbalance and to the performance of lithium-ion cells at cold temperatures. Furthermore, insights gained from previous experimental and modeling investigations are elucidated. These include the need for more accurate heat generation measurements, improved modeling of the heat generation rate, and clarity in the relative magnitudes of the various thermal effects observed at high charge and discharge rates seen in electric vehicle applications. From an analysis of the literature, the requirements for lithium-ion thermal management systems for optimal performance in these applications are suggested, and it is clear that no existing thermal management strategy or technology meets all these requirements.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1.3515880">https://doi.org/10.1149/1.3515880</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1.1850854" class="art-list-item-title event_main-link">The Impact of Elastic Deformation on Deposition Kinetics at Lithium/Polymer Interfaces</a><p class="small art-list-item-meta">Charles Monroe and John Newman 2005 <em>J. Electrochem. Soc.</em> <b>152</b> A396 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1.1850854/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;The Impact of Elastic Deformation on Deposition Kinetics at Lithium/Polymer Interfaces</span></a><a href="/article/10.1149/1.1850854/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;The Impact of Elastic Deformation on Deposition Kinetics at Lithium/Polymer Interfaces</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="The Impact of Elastic Deformation on Deposition Kinetics at Lithium/Polymer Interfaces" data-link-purpose-append-open="The Impact of Elastic Deformation on Deposition Kinetics at Lithium/Polymer Interfaces">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Past theories of electrode stability assume that the surface tension resists the amplification of surface roughness at cathodes and show that instability at lithium/liquid interfaces cannot be prevented by surface forces alone [Electrochim. Acta, <b>40</b>, 599 (1995)]. This work treats interfacial stability in lithium/polymer systems where the electrolyte is solid. Linear elasticity theory is employed to compute the additional effect of bulk mechanical forces on electrode stability. The lithium and polymer are treated as Hookean elastic materials, characterized by their shear moduli and Poisson’s ratios. Two-dimensional displacement distributions that satisfy force balances across a periodically deforming interface are derived; these allow computation of the stress and surface-tension forces. The incorporation of elastic effects into a kinetic model demonstrates regimes of electrolyte mechanical properties where amplification of surface roughness can be inhibited. For a polymer material with Poisson’s ratio similar to poly(ethylene oxide), interfacial roughening is mechanically suppressed when the separator shear modulus is about twice that of lithium. © 2005 The Electrochemical Society. All rights reserved.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1.1850854">https://doi.org/10.1149/1.1850854</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><a href="/article/10.1149/1.1379565" class="art-list-item-title event_main-link">The Mechanisms of Lithium and Sodium Insertion in Carbon Materials</a><p class="small art-list-item-meta">D. A. Stevens and J. R. Dahn 2001 <em>J. Electrochem. Soc.</em> <b>148</b> A803 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1.1379565/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;The Mechanisms of Lithium and Sodium Insertion in Carbon Materials</span></a><a href="/article/10.1149/1.1379565/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;The Mechanisms of Lithium and Sodium Insertion in Carbon Materials</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="The Mechanisms of Lithium and Sodium Insertion in Carbon Materials" data-link-purpose-append-open="The Mechanisms of Lithium and Sodium Insertion in Carbon Materials">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>In this paper, we compare the interactions of lithium and sodium with a range of carbon materials in electrochemical cells. Through wide angle <i>in situ</i> X-ray scattering studies, we demonstrate that both lithium and sodium can be inserted into the interlayer space in disordered carbon materials. This insertion process is accompanied by an increase in the interlayer spacing in these materials. Small-angle <i>in situ</i> scattering studies are presented to clearly show the insertion of lithium and sodium into nanopores within disordered hard carbons. We also show that very little, if any, sodium can be inserted into graphitic materials in contrast to the large capacity seen for lithium insertion. © 2001 The Electrochemical Society. All rights reserved.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1.1379565">https://doi.org/10.1149/1.1379565</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/2.0251701jes" class="art-list-item-title event_main-link">The Development and Future of Lithium Ion Batteries</a><p class="small art-list-item-meta">George E. Blomgren 2017 <em>J. Electrochem. Soc.</em> <b>164</b> A5019 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/2.0251701jes/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;The Development and Future of Lithium Ion Batteries</span></a><a href="/article/10.1149/2.0251701jes/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;The Development and Future of Lithium Ion Batteries</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="The Development and Future of Lithium Ion Batteries" data-link-purpose-append-open="The Development and Future of Lithium Ion Batteries">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>This year, the battery industry celebrates the 25<sup>th</sup> anniversary of the introduction of the lithium ion rechargeable battery by Sony Corporation. The discovery of the system dates back to earlier work by Asahi Kasei in Japan, which used a combination of lower temperature carbons for the negative electrode to prevent solvent degradation and lithium cobalt dioxide modified somewhat from Goodenough's earlier work. The development by Sony was carried out within a few years by bringing together technology in film coating from their magnetic tape division and electrochemical technology from their battery division. The past 25 years has shown rapid growth in the sales and in the benefits of lithium ion in comparison to all the earlier rechargeable battery systems. Recent work on new materials shows that there is a good likelihood that the lithium ion battery will continue to improve in cost, energy, safety and power capability and will be a formidable competitor for some years to come.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/2.0251701jes">https://doi.org/10.1149/2.0251701jes</a></div></div></li><li class="art-list-item reveal-container reveal-closed"><div class="eyebrow"><span class="offscreen-hidden">The following article is </span><span class="red">Open access</span></div><a href="/article/10.1149/1945-7111/ab9050" class="art-list-item-title event_main-link">Development of Experimental Techniques for Parameterization of Multi-scale Lithium-ion Battery Models</a><p class="small art-list-item-meta">Chang-Hui Chen <em>et al</em> 2020 <em>J. Electrochem. Soc.</em> <b>167</b> 080534 </p><div class="art-list-item-tools small wd-abstr-upper"><a href="/article/10.1149/1945-7111/ab9050/meta" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="View article"><span class="icon-article"></span>View article<span class="offscreen-hidden">,&nbsp;Development of Experimental Techniques for Parameterization of Multi-scale Lithium-ion Battery Models</span></a><a href="/article/10.1149/1945-7111/ab9050/pdf" class="mr-2 mb-0 nowrap event_mini-link" data-event-action="PDF"><span class="icon-file-pdf"></span>PDF<span class="offscreen-hidden">,&nbsp;Development of Experimental Techniques for Parameterization of Multi-scale Lithium-ion Battery Models</span></a><button type="button" class="reveal-trigger mr-2 nowrap"><svg aria-hidden="true" class="fa-icon fa-icon--left fa-icon--flip" role="img" focusable="false" xmlns="http://www.w3.org/2000/svg" viewBox="0 0 320 512"><!--caret-down--><!--!Font Awesome Free 6.5.1 by @fontawesome - https://fontawesome.com License - https://fontawesome.com/license/free Copyright 2024 Fonticons, Inc.--><path d="M137.4 374.6c12.5 12.5 32.8 12.5 45.3 0l128-128c9.2-9.2 11.9-22.9 6.9-34.9s-16.6-19.8-29.6-19.8L32 192c-12.9 0-24.6 7.8-29.6 19.8s-2.2 25.7 6.9 34.9l128 128z"/></svg><span class="reveal-trigger-label" data-reveal-text="Open abstract" data-reveal-label-alt="Close abstract" data-link-purpose-append="Development of Experimental Techniques for Parameterization of Multi-scale Lithium-ion Battery Models" data-link-purpose-append-open="Development of Experimental Techniques for Parameterization of Multi-scale Lithium-ion Battery Models">Open abstract</span></button></div><div class="reveal-content"><div class="article-text view-text-small"><p>Presented here, is an extensive 35 parameter experimental data set of a cylindrical 21700 commercial cell (LGM50), for an electrochemical pseudo-two-dimensional (P2D) model. The experimental methodologies for tear-down and subsequent chemical, physical, electrochemical kinetics and thermodynamic analysis, and their accuracy and validity are discussed. Chemical analysis of the LGM50 cell shows that it is comprised of a NMC 811 positive electrode and bi-component Graphite-SiO<sub>x</sub> negative electrode. The thermodynamic open circuit voltages (OCV) and lithium stoichiometry in the electrode are obtained using galvanostatic intermittent titration technique (GITT) in half cell and three-electrode full cell configurations. The activation energy and exchange current coefficient through electrochemical impedance spectroscopy (EIS) measurements. Apparent diffusion coefficients are estimated using the Sand equation on the voltage transient during the current pulse; an expansion factor was applied to the bi-component negative electrode data to reflect the average change in effective surface area during lithiation. The 35 parameters are applied within a P2D model to show the fit to experimental validation LGM50 cell discharge and relaxation voltage profiles at room temperature. The accuracy and validity of the processes and the techniques in the determination of these parameters are discussed, including opportunities for further modelling and data analysis improvements.</p></div><div class="art-list-item-tools small wd-abstr-lower"><a class="mr-2" href="https://doi.org/10.1149/1945-7111/ab9050">https://doi.org/10.1149/1945-7111/ab9050</a></div></div></li></ul><!--    articleEntryList end--></div></div></div><!-- End Featured tabpanel --></div><!-- End Article listing tabs --><!--  Start of google banners in the middle.  --><section aria-label="Main column advert"><div class="ad-iframe-wrap"><div id='div-gpt-ad-1562594774007-0' style='width: 728px; height: 90px; display: block;'><script>
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