Huan Huang’s research while affiliated with Institute of High Energy Physics, Chinese Academy of Sciences and other places

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Publications (70)


In Situ Observation of How Pt Catalyst Evolves in Pulsed Electrolysis
  • Article

March 2025

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2 Reads

The Journal of Physical Chemistry C

Wenchao Liu

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Yinghao Xia

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Guikai Zhang

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Approach to Automated In-situ X-Ray Absorption Fine Structure Spectroscopy Characterization

February 2025

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7 Reads

Chemical Research in Chinese Universities

In order to expand the range of synchrotron radiation structural characterization modes, an automated in-situ X-ray absorption fine structure (XAFS) spectroscopy characterization for electrochemical research has been established. An in-situ control system equipped with an automatic trigger capability facilitates automated acquisition of XAFS and electrochemical data. Furthermore, the quick scanning XAFS (QXAFS) terminal, in-situ server and data storage were all controlled by remote users, enabling remote measurement to be achieved. Using this system, the evolution of the local structure near Fe atoms during the charging and discharging of lithium-sulfur battery (LSB) cathode materials was observed, which provides deep insights into the sulfur reaction pathway in LSBs by leveraging structural information. The system established here paves the way for fully automated and intelligent in-situ XAFS experiments.


Scheme of ROS scavenging. (a) A diagram illustrating the role of selenoenzymes in the reduction of ROS, such as H2O2, to H2O. (b) A schematic representation of the catalytic cycle, wherein the Se site within the enzyme facilitates the capture of one O atom from H2O2. GSH denotes an abbreviation for a functional group within glutathione peroxidase.
Structural characterizations of Se/C‐600. (a) Raman spectra of Se/C‐x catalysts synthesized at various temperatures. (b) HAADF‐STEM image of a single Se site (bright dots) in the Se/C‐600 catalyst. (c) Se K‐edge XANES and (d) high‐resolution Se 3d XPS spectra of the Se/C‐600 catalyst, with Se powder (or Se foil) and SeO2 used as reference samples. (e) Se K‐edge k³‐weighted FT‐EXAFS of Se/C‐600 with Se foil and SeO2 as references, the C−Se−OH pathway was used to calculate the experimental spectra. (f) Simulation of XANES spectra of Se/C‐600 with a proposed C−Se−OH structure.
Direct 4‐electron selectivity in Se/C‐600 (a) ORR polarization curves (bottom) and H2O2 yields (top) of Se/C‐600 and N/C catalysts in O2‐saturated 0.1 M H2SO4 electrolyte, with a catalyst loading of 0.6 mg cm⁻², at 900 rpm and a temperature of 30 °C. (b, c) Interruption current methods used to accurately measure the H2O2 yields of Se/C‐600 and commercial Pt/C catalysts at 0.5 V. (d) Comparison of H2O2 yields of Se/C‐600 catalyst with those of previously reported ORR catalysts, including non‐metals, non‐noble metals, and noble metal catalysts.
Theoretical calculation. (a) Six optimized potential atomic structures for Se/C‐600. (b) The volcano curve of ORR limiting potential versus ▵GOH. (c) Gibbs free energy diagrams of ORR reaction pathways on Arm‐C1SeOH. (d) Schematic of the Arm‐C1SeOH catalyzing the ORR, in which the C−Se−OH site captures an O atom from H2O2. The behavior of Se observed in Arm‐C1SeOH is consistent with that observed in glutathione peroxidase.
In situ XAS measurement. (a) In situ XAS spectra at a potential of 0.1 and 0.4 V under N2 and O2 atmospheres. (b) Comparison of FT‐EXAFS spectra at different atmospheres and potentials. (c) Coordination bond length and charge of the Se site in non‐reactive state. (d) Coordination bond length and charge of the Se site in intermediate II.

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Enzyme‐Inspired Single Selenium Site for Selective Oxygen Reduction
  • Article
  • Publisher preview available

January 2025

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17 Reads

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1 Citation

Learning from nature has garnered significant attention in the scientific community for its potential to inspire creative solutions in material or catalyst design. The study highlights the design of a biomimetic single selenium (Se) site‐modified carbon (C) moiety that retains the unique reactivity of selenoenzyme with peroxides, which plays crucial roles in selectively catalyzing the oxygen reduction reaction (ORR). The as‐designed Se−C demonstrates nearly 100 % 4‐electron selectivity, evidenced by 0.039 % of H2O2 yield at 0.5 V versus reversible hydrogen electrode, outperforming commercial platinum (Pt) by 65 times. In situ X‐ray absorption spectroscopy and theoretical calculations attribute this exceptional selectivity to the enzyme‐like behaviors of the Se site to steal an O atom from peroxide intermediates. The second achievement is the significantly increased consecutive 2+2 electron selectivity. Benefiting from the enzyme‐like H2O2 reduction activity with a higher onset potential of 0.915 V compared to Pt at 0.875 V, the Se−C as a secondary catalytic site reduced the H2O2 yields of the Co−N−C, Fe−N−C, and N−C catalysts by 96 %, 67 %, and 98 %, respectively, via a consecutive 2+2 electron pathway. This also leads to more stable catalysts via protecting the active sites from oxidative attacks. This work establishes new pathways for precise tuning of reaction selectivity in ORR and beyond.

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Enzyme‐Inspired Single Selenium Site for Selective Oxygen Reduction

January 2025

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8 Reads

Angewandte Chemie

Learning from nature has garnered significant attention in the scientific community for its potential to inspire creative solutions in material or catalyst design. The study reports a biomimetic single selenium (Se) site‐modified carbon (C) moiety that retains the unique reactivity of selenoenzyme with peroxides, aiming to selectively catalyze the oxygen reduction reaction (ORR). The as‐designed Se‐C demonstrates nearly 100% 4‐electron selectivity, evidenced by 0.039% of H2O2 yield at 0.5 V versus reversible hydrogen electrode, outperforming commercial platinum (Pt) by 65 times. In‐situ X‐ray absorption spectroscopy and theoretical calculations attribute this exceptional selectivity to the enzyme‐like behaviors of the Se site to steal an O atom from peroxide intermediates. The second achievement is the significantly increased consecutive 2+2 electron selectivity. Benefiting from the enzyme‐like H2O2 reduction activity with a higher onset potential of 0.915 V compared to Pt at 0.875 V, the Se‐C as a secondary catalytic site reduced the H2O2 yields of the Co‐N‐C, Fe‐N‐C, and N‐C catalysts by 96%, 67%, and 98%, respectively, via a consecutive 2+2 electron pathway. This also leads to more stable catalysts via protecting the active sites from oxidative attacks. This work establishes new pathways for precise tuning of reaction selectivity in ORR and beyond.



Depth‐of‐Discharge Dependent Capacity Decay Induced by the Accumulation of Oxidized Lattice Oxygen in Li‐Rich Layered Oxide Cathode

December 2024

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61 Reads

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1 Citation

More and more basic practical application scenarios have been gradually ignored/disregarded, in fundamental research on rechargeable batteries, e.g. assessing cycle life under various depths‐of‐discharge (DODs). Herein, although benefit from the additional energy density introduced by anionic redox, we critically revealed that lithium‐rich layered oxide (LRLO) cathodes present anomalously poor capacity retention at low‐DOD cycling, which is essentially different from typical layered cathodes (e.g. NCM), and pose a formidable impediment to the practical application of LRLO. We systemically demonstrated that DOD‐dependent capacity decay is induced by the anionic redox and accumulation of oxidized lattice oxygen (Oⁿ⁻). Upon low‐DOD cycling, the accumulation of Oⁿ⁻ and the persistent presence of vacancies in the transition metal (TM) layer intensified the in‐plane migration of TM, exacerbating the expansion of vacancy clusters, which further facilitated detrimental out‐of‐plane TM migration. As a result, the aggravated structural degradation of LRLO at low‐DOD impeded reversible Li⁺ intercalation, resulting in rapid capacity decay. Furthermore, prolonged accumulation of Oⁿ⁻ persistently corroded the electrode‐electrolyte interface, especially negative for pouch‐type full‐cells with the shuttle effect. Once the “double‐edged sword” effect of anionic redox being elucidated under practical condition, corresponding modification strategies/routes would become distinct for accelerating the practical application of LRLO.


Depth‐of‐Discharge Dependent Capacity Decay Induced by the Accumulation of Oxidized Lattice Oxygen in Li‐Rich Layered Oxide Cathode

November 2024

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26 Reads

Angewandte Chemie

More and more basic practical application scenarios have been gradually ignored/disregarded, in fundamental research on rechargeable batteries, e.g. assessing cycle life under various depths‐of‐discharge (DODs). Herein, although benefit from the additional energy density introduced by anionic redox, we critically revealed that lithium‐rich layered oxide (LRLO) cathodes present anomalously poor capacity retention at low‐DOD cycling, which is essentially different from typical layered cathodes (e.g. NCM), and pose a formidable impediment to the practical application of LRLO. We systemically demonstrated that DOD‐dependent capacity decay is induced by the anionic redox and accumulation of oxidized lattice oxygen (On‐). Upon low‐DOD cycling, the accumulation of On‐ and the persistent presence of vacancies in the transition metal (TM) layer intensified the in‐plane migration of TM, exacerbating the expansion of vacancy clusters, which further facilitated detrimental out‐of‐plane TM migration. As a result, the aggravated structural degradation of LRLO at low‐DOD impeded reversible Li+ intercalation, resulting in rapid capacity decay. Furthermore, prolonged accumulation of On‐ persistently corroded the electrode‐electrolyte interface, especially negative for pouch‐type full‐cells with the shuttle effect. Once the “double‐edged sword” effect of anionic redox being elucidated under practical condition, corresponding modification strategies/routes would become distinct for accelerating the practical application of LRLO.



(a) Refined synchrotron radiation XRD patterns of the pristine layered LCO and lithiated spinel LCO. Corresponding schematic illustrations of structures are shown in the inset. (b) Selected 2θ regions and component analysis. (c) Typical galvanostatic charge–discharge profiles curves of layered LCO and lithiated spinel LCO at a current density of 0.1C (1C = 200 mA g⁻¹) for 3–4.2 V (vs. Li/Li⁺). The inset depicts a schematic diagram of the reversible phase transition between Li0.5CoO2 and LiCoO2 within the spinel structure. (d) Main peaks of the in situ XRD patterns for layered LCO (left) and lithiated spinel LCO (right), along with the galvanostatic charge–discharge curve from 3 to 4.6 V (vs. Li/Li⁺). The peak shift is denoted as ΔDE when the d-spacing reaches its maximum expansion and as ΔDs when the d-spacing reaches its minimum shrinkage. (e) The design principle of the layered-spinel heterostructure modification strategies for LCO
(a) Refined synchrotron radiation XRD pattern of the pristine layered-spinel LCO. The inset displays selected 2θ regions and component analysis. (b) Charge–discharge profiles and the corresponding dQ/dV chart during discharge of the layered-spinel LCO at a current density of 0.1C for 3–4.2 V (vs. Li/Li⁺). (c) HR-TEM image of the layered-spinel LCO. The FFT and IFFT images obtained from the corresponding regions of the cathode are displayed on the right side. (d) Main peaks of the in situ XRD patterns for the layered-spinel LCO and galvanostatic charge–discharge curve from 3 to 4.6 V (vs. Li/Li⁺). The c lattice parameters of the layered (yellow) and spinel (purple) phases, obtained from the refinement, are shown in the right panel
Electrochemical performance of different LCO batteries. (a and e) Charge–discharge profiles of layered LCO and layered-spinel LCO at 0.1C, in a voltage range of (a) 3–4.2 V and (e) 3–4.6 V (vs. Li/Li⁺). (b–d) Cycle performance of different cell configurations: (b) layered-spinel LCO, (c) 600 °C 1 h- LCO (spinel ratio > 10%), and (d) 700 °C 1 h- LCO (spinel ratio < 10%), compared to the layered LCO at a current density of 0.1C for 3–4.2 V (vs. Li/Li⁺). (f) Cycle performance comparison of the layered-spinel LCO and the layered LCO at 0.1C for 3–4.6 V (vs. Li/Li⁺)
(a–c) Normalized ex situ Co K-edge XANES spectra at states of pristine, 4.2 V and 4.6 V (vs. Li/Li⁺) for (a) layered LCO, (b) layered-spinel LCO and (c) spinel LCO. (d–f) Co K-edge EXAFS spectra at states of pristine, 4.2 V and 4.6 V (vs. Li/Li⁺) for (d) layered LCO, (e) layered-spinel LCO and (f) spinel LCO
(a and b) Refined NPD pattern of pristine LT-LCO with two different main phases: (a) spinel and (b) cubic-layered. (c and d) HR-TEM images and corresponding FFT/IFFT images of (c) pristine LT-LCO and (d) LT-LCO after the 1st cycle. (e) A schematic illustration of the lithium diffusion pathway within the spinel structure. (f) A schematic illustration of lithium diffusion and deterioration analysis for LT-LCO
Does “zero-strain” lithiated spinel serve as a strain retardant and an irreversible phase transition regulator for layered oxide cathodes?

September 2024

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64 Reads

Layered oxide cathodes encounter structural challenges during cycling, prompting the exploration of an ingenious heterostructure strategy, which incorporates stable components into the layered structure as strain regulators to enhance materials cycle stability. Despite considerable research efforts, identifying suitable, convenient, and cost-effective materials and methods remains elusive. Herein, focused on lithium cobalt oxide (LiCoO2), we utilized its low-temperature polymorph as a strain-retardant embedded within a cathode. Our findings reveal that the low-temperature component, exhibiting zero-strain characteristic, adopts a complex configuration with a predominant lithiated spinel structure, also featuring both cubic-layered and typical-layered configurations. But this composite cathode exhibits a sluggish lithium-ion transport rate, attributed to Co&Li dislocation at the dual structural boundaries and the formation of cobalt(iii) oxide. This investigation presents a pioneering endeavor in employing heterostructure strategies, underscoring the critical role of such strategies in component selection, which ultimately propels the advancement of layered oxide cathode candidates for Li-ion battery technology.


Structure analysis of Fe–NC and Fe–NCBrCl catalysts
a Aberration-corrected atomic resolution HAADF-STEM micrograph of Fe–NCBrCl. b, c HAADF-STEM images and corresponding EDS mapping. d XAS spectra collected at N K-edge. e The deconvoluted high-resolution N 1s XPS. f The hysteresis curves. g Normalized Fe K-edge XANES spectra. h Fourier transform of k³-weighted EXAFS spectra. i FT-EXAFS fitting curve, gray ball represents C atom, blue ball represents N atom, red ball represents Fe atom, yellow ball represents Br atom.
ORR activity, SD and TOF measurements of Fe–NCs
a RDE ORR curves measured in O2-saturated 0.1 M H2SO4 at 10 mV s⁻¹ with a rotation speed of 900 rpm. The catalyst loading was 0.6 mg cm⁻². b The kinetic ORR activities of Fe–NCs. c Comparison of SD values determined by nitrite stripping method for Fe–NC and Fe–NCBrCl catalysts. d Comparison of TOF at 0.80 and 0.85 VRHE for Fe–NC and Fe–NCBrCl catalysts. Error bars represent the standard deviation for three separate measurements.
Performance tests with Fe–NC and Fe–NCBrCl as the cathode catalysts in a single-cell PEMFCs
a H2-O2 PEMFCs polarization curves. Cathode, ~3.5 mgcat cm⁻² for Fe–NC and 0.2 mgPt cm⁻² for Pt/C; anode, 0.4 mgPt cm⁻² Pt/C; GORE-SELECT® membrane (15 μm thickness); 0.3 L H2 min⁻¹ and 0.4 L O2 min⁻¹ feed, 100% relative humidity (RH), 250 kPa absolute partial pressure H2 and O2, 80 °C, electrode area 1.21 cm². The cell voltage and power density are not iR corrected. b The polarization curves without (solid line) and with (dotted line) iR-correction and HFR under 250 kPaabs H2-O2 PEMFCs. c Current densities at 0.8 ViR-free and 0.7 ViR-free. d Tafel plots derived from the ORR polarization curves displayed in (c).
The polarization curves obtained by DOE MEA test protocol of PGM-free electrocatalyst
a H2–O2 polarization curves, acquired from OCV to 0.70 V in 25 mV steps and 0.70 V to 0.25 V in 50 mV steps, with a hold time of 45 s per point. 0.3 L H2 min⁻¹ and 0.4 L O2 min⁻¹ feed, 100% relative humidity (RH), 150 kPa absolute partial pressure H2 and O2, 80 °C. b H2–O2 polarization curve with iR-correction. c H2–air polarization curves. d Tafel plots derived from the ORR polarization curves displayed in (c).
The interface effect of MEA
a, b The secondary ion two-dimensional imaging from ToF-SIMS, a Fe–NC, b Fe–NCBrCl. The green is S⁻, the red is Fe⁺. c Integral SO3⁻ distribution in cathode catalyst layer shows intensity gradients from both Fe–NC (blue) and Fe–NCBrCl (red) catalysts. d Relationship between Rtotal and absolute gas pressure obtained by the limiting current method. Insets were Rnp and Rp. e An Arrhenius plot of i0 obtained from the Nyquist plots shown in Supplementary Fig. 37. f Nyquist plots for PEMFCs of indicated cathode catalysts at the current density of 1.0 A cm–2, the inset shows the equivalent circuit model, Rct and Rmt of Fe–NC and Fe–NCBrCl obtained by EIS fitting. Error bars represent the standard deviation of the fitting results.
A Fe-NC electrocatalyst boosted by trace bromide ions with high performance in proton exchange membrane fuel cells

August 2024

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61 Reads

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11 Citations

Replacement of expensive and rare platinum with metal–nitrogen–carbon catalysts for oxygen reduction reactions in proton exchange membrane fuel cells is hindered by their inferior activity. Herein, we report a highly active iron-nitrogen-carbon catalyst by optimizing the carbon structure and coordination environments of Fe-N4 sites. A critical high-temperature treatment with ammonium chloride and ammonium bromide not only enhances the intrinsic activity and density of Fe-N4 sites, but also introduces numerous defects, trace Br ions and creates mesopores in the carbon framework. Notably, surface Br ions significantly improve the interaction between the ionomer and catalyst particles, promoting ionomer infiltration and optimizing the O2 transport and charge transfer at triple-phase boundary. This catalyst delivers a high peak power density of 1.86 W cm⁻² and 54 mA cm⁻² at 0.9 ViR-free in a H2-O2 fuel cells at 80 °C. Our findings highlight the critical role of interface microenvironment regulation.


Citations (40)


... Reproduced with permission. [13] Copyright 2024, American Chemical Society. f) Operating and average (red dot) voltage comparison of different cathode materials with LSV results of electrolytes in LIBs and SIBs. ...

Reference:

A Perspective on Pathways Toward Commercial Sodium‐Ion Batteries
Elucidating the Structural Evolution of O3-type NaNi 1/3 Fe 1/3 Mn 1/3 O 2 : A Prototype Cathode for Na-Ion Battery
  • Citing Article
  • November 2024

Journal of the American Chemical Society

... This not only enhances the interaction between metal atoms and the support but also effectively suppresses the aggregation of single atoms. As a result, halogen doping offers new opportunities for improving the stability and optimizing the performance of SACs [44][45][46]. ...

A Fe-NC electrocatalyst boosted by trace bromide ions with high performance in proton exchange membrane fuel cells

... This approach is crucial for advancing theoretical descriptions of electrochemical interface structures and catalytic process evolution, thereby providing valuable guidance for the precise control of complex, multifaceted interfaces under operational conditions [129]. In recent years, progress has been made in understanding the mechanisms of oxygen reduction catalysts through the application of computational simulations and in situ spectroscopic techniques [130][131][132][133]. ...

An in situ exploration of how Fe/N/C oxygen reduction catalysts evolve during synthesis under pyrolytic conditions

... This mechanism is particularly important in certain metal oxide electrocatalysts with specific lattice structures. The reaction steps can be given in more detail as [54,55] : ...

Selective Activation of Lattice Oxygen Site Through Coordination Engineering to Boost the Activity and Stability of Oxygen Evolution Reaction

... Over the past decade, researchers have introduced a multitude of optimization strategies to forestall metal agglomeration during the synthesis of M-N-C materials. These strategies encompass complexation protection, impregnation adsorption, the use of sacrificial templates, and the spatially restricted domain approach, collectively surmounting the limitations associated with high metal loading in M-N-C [53][54][55][56] . In recent years, the low-temperature reduction of M-N-C has also been developed. ...

Unveiling Low Temperature Assembly of Dense Fe‐N4 Active Sites via Hydrogenation in Advanced Oxygen Reduction Catalysts

... More information on NN architectures, such as activation functions, gradient descent, convolutional NN, feedforward NN, and recurrent NN, can be found in these works [60,61]. NN models are wellsuited for pattern matching, especially with large and complex training datasets, making them promising tools for classification and prediction tasks [62]. Nevertheless, a significant drawback is that NN are often viewed as black-box models, offering little insight into their internal mappings and requiring extensive trial and error for hyperparameter tuning. ...

Artificial neural network for deciphering the structural transformation of condensed ZnO by extended X-ray absorption fine structure spectroscopy

... Yun et al synthesized ultra-low Pt-loaded PtFe-FeNC catalysts through stepwise vapor deposition, which significantly reduced the Pt usage. But the yield of FeNC precursor was relatively low [13]. Niu et al developed an integrated catalyst by embedding PtFe alloys into FeNC supports, effectively suppressing the negative impact of the Fenton reaction. ...

FeN 4 Active Sites Electronically Coupled with PtFe Alloys for Ultralow Pt Loading Hybrid Electrocatalysts in Proton Exchange Membrane Fuel Cells
  • Citing Article
  • December 2023

ACS Nano

... [32] Typically, the intensity ratio of the (003) to (104) peaks is used to assess the degree of Li/Ni mixing, the higher value meaning a higher hexagonal ordering. [33] The I (003) /I (104) values for the different LRM-NS-X samples are 2.05, 2.12, 2.04, and 2.03, respectively. As the (NH 4 ) 2 S 2 O 8 concentration increases, the (003) and (104) peaks shift to lower angles (Figure 3b,c), indicating an increase in interlayer spacing, which facilitates the insertion and extraction of Li + . ...

Does single-crystallization a feasible direction for designing Li-rich layered cathodes?
  • Citing Article
  • August 2023

Energy Storage Materials

... Alternatively, the electronic interaction is constructed by combining SSCs with other materials, thereby enhancing catalytic stability. [174,175] In addition, the structure-stability relationship of SSCs under reaction conditions should be evaluated. [174] This helps to reveal the key factors affecting the stability of single site catalysts and provides a universal approach for designing stable SSCs. ...

Mechanism of Particle-Mediated Inhibition of Demetalation for Single-Atom Catalytic Sites in Acidic Electrochemical Environments
  • Citing Article
  • July 2023

Journal of the American Chemical Society

... [82] Through the innovative approach of lattice-matched layered/olivine composite-structure fabrication, the electrochemical characteristic of LiCoO 2 cathode at 4.65 V could be sustained, ensuring both feasibility and costeffectiveness. [60] Moreover, the enamel-like interfacial layer can be developed through rapid mechanical fusion and subsequent heating processes, effectively curbing side reactions and minimizing by-products at the interfacial. [81d] This protective layer significantly reduced the risk of detrimental phase evolution and O 2 loss, showcasing the effectiveness of straightforward solidstate mechanical approaches in CSOG strategies that enhance interfacial chemistry among active components. ...

Blending Layered Cathode with Olivine: An Economic Strategy for Enhancing the Structural and Thermal Stability of 4.65 V LiCoO2