Haiyan Luo’s research while affiliated with Xiamen University and other places

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Publications (25)


(a) Ex/in situ ATR‐FTIR spectroscopy reveals the essence of concentration changes in both the bulk and interface. a) Ex situ ATR‐FTIR spectra of EC/EMC electrolytes with different concentrations. The upper part displays the original infrared absorption spectra, while the lower part shows the subtracted spectrum of the three electrolytes, and the 1.0 M as the background to be deducted. b) Schematic diagram of the ATR‐FTIR spectroscopy. c) (I) In situ ATR‐FTIR spectra of the LFP/electrolyte interface collected during the first cycle with the colors of the spectra varying from red in charge to blue in discharge. The in situ cell was cycled at a current density of 25 mA g⁻¹, with infrared spectra collected every 5 minutes. To highlight the detailed changes in the spectra, one spectrum was selected out of every four for plotting. There are no obvious changes in the original spectra because the main signals originate from the thin‐layer bulk. (II) The A(n)‐A(OCV) relative absorbance evolution during charging and discharging, and the spectrum collected at OCV as background to be deducted. (III) The A(n+1)‐A(n) relative absorbance evolution during charging, in which each spectrum has subtracted its corresponding preceding spectrum. d) Schematic illustration of the electrolyte solvation configuration at the LFP‐electrolyte interface during Li⁺‐(de)solvation (i. e., charging/discharging) process. The interface transitions from a solvent‐rich state to a Li⁺‐solvent/anion‐rich state during charging, while the reverse applies in the discharging process.
In situ ATR‐FTIR spectroscopy reveals the inflection point of interfacial Li⁺‐solvent/anion concentration caused by the anti‐synergy effect. a) A snapshot of the LiCoO2‐electrolyte interface in the simulation system. b). The potential of mean force (PMF) of interfacial solvated‐Li⁺ as a function of distance from the electrode under different voltages. c) In situ ATR‐FTIR spectra of the LCO/electrolyte interface collected during initial charging. The current density is 25 mA g⁻¹. The spectrum collected at inflection voltage is colored in red. d) Schematic illustration of the electrolyte solvation configuration at the LCO/electrolyte interface during the Li⁺‐solvation (charging) process at different voltages.
CEI architecture analysis from the influence of inflection point and protocol optimization method. (a) TOF‐SIMS characterization of the 4.1 V and 4.2 V‐cycled LCO cathodes (below/above the inflection voltage) retrieved from the coin cells after 5 cycles. Normalized depth profiles of representative inorganic and organic fragments illustrate the CEI architecture. (b) Schematic illustration of CEI structure formed at charge cut‐off voltages below/above inflection voltage. (c) The ToF‐SIMS chemical mapping (size: 150×150 μm²) of CHO2⁻ corresponding to different sputtering times in Figure 3a. (d) Charge curves of typical CC‐cycled and special CV‐holding mode. (f) Comparison of cycling performance of Li||LCO cells with different pre‐cycle modes.
Electrolyte engineering in regulating the CEI architecture. a) Schematic diagram illustrating the electrolyte design principle of reducing electropositivity of solvated‐Li⁺. b) ¹⁹F NMR of EC/EMC37 and EC/EMC11 electrolyte. c) The A(n+1)‐A(n) relative absorbance evolution on LCO surfaces upon charging to 4.5 V in EC/EMC37 and EC/EMC11 electrolyte. The spectrum collected at inflection voltage is colored in red. The middle part represents the corresponding voltage profile (red for EC/EMC37 and blue for EC/EMC11). d) ATR‐FTIR absorbance evolution of the O−C−O bands of EC and P−F band of CIP during the charging in the first cycle. e) Normalized depth profiles of CH2⁻ fragment of LCO surfaces upon charging to 4.5 V in EC/EMC37 and EC/EMC11 electrolyte. f) Cycling performance of LCO cathode in two electrolytes.
Revealing the Dynamic Evolution of Electrolyte Configuration on the Cathode‐Electrolyte Interface by Visualizing (De) Solvation Processes
  • Article
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December 2024

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98 Reads

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2 Citations

Haiyan Luo

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[...]

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Shi‐Gang Sun

Electrolyte engineering is crucial for improving cathode electrolyte interphase (CEI) to enhance the performance of lithium‐ion batteries, especially at high charging cut‐off voltages. However, typical electrolyte modification strategies always focus on the solvation structure in the bulk region, but consistently neglect the dynamic evolution of electrolyte solvation configuration at the cathode‐electrolyte interface, which directly influences the CEI construction. Herein, we reveal an anti‐synergy effect between Li⁺‐solvation and interfacial electric field by visualizing the dynamic evolution of electrolyte solvation configuration at the cathode‐electrolyte interface, which determines the concentration of interfacial solvated‐Li⁺. The Li⁺ solvation in the charging process facilitates the construction of a concentrated (Li⁺‐solvent/anion‐rich) interface and anion‐derived CEI, while the repulsive force derived from interfacial electric field induces the formation of a diluted (solvent‐rich) interface and solvent‐derived CEI. Modifying the electrochemical protocols and electrolyte formulation, we regulate the “inflection voltage” arising from the anti‐synergy effect and prolong the lifetime of the concentrated interface, which further improves the functionality of CEI architecture.

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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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46 Reads

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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25 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.



Decoupling the Failure Mechanism of Li‐Rich Layered Oxide Cathode During High‐Temperature Storage in Pouch‐Type Full‐Cell: A Practical Concern on Anionic Redox Reaction

In addressing the global climate crisis, the energy storage performance of Li‐ion batteries (LIBs) under extreme conditions, particularly for high‐energy‐density Li‐rich layered oxide (LRLO) cathode, is of the essence. Despite numerous researches into the mechanisms and optimization of LRLO cathodes under ideal moderate environment, there is a dearth of case studies on their practical/harsh working environments (e.g., pouch‐type full‐cell, high‐temperature storage), which is a critical aspect for the safety and commercial application. In this study, using pouch‐type full‐cells as prototype investigation target, the study finds the cell assembled with LRLO cathode present severer voltage decay than typical NCM layered cathode after high‐temperature storage. Further decoupling elucidates the primary failure mechanism is the over‐activation of lattice oxidized oxygen (aggravate by high‐temperature storage) and subsequent escape of oxidized oxygen species (Oⁿ⁻), which disrupts transition metal (TM) coordination and exacerbates electrolyte decomposition, leading to severe TM dissolution, interfacial film reconstruction, and harmful shuttle effects. These chain behaviors upon high‐temperature storage significantly influence the stability of both electrodes, causing substantial voltage decay and lithium loss, which accelerates full‐cell failure. Although the anionic redox reaction can bring additional energy, but the escape of metastable Oⁿ⁻ species would introduce new concerns in practical cell working conditions.


Electrolyte Solvation Engineering Stabilizing Anode‐Free Sodium Metal Battery With 4.0 V‐Class Layered Oxide Cathode

September 2024

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89 Reads

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1 Citation

Anode‐free sodium metal batteries (AFSMBs) are regarded as the “ceiling” for current sodium‐based batteries. However, their practical application is hindered by the unstable electrolyte and interfacial chemistry at the high‐voltage cathode and anode‐free side, especially under extreme temperature conditions. Here, an advanced electrolyte design strategy based on electrolyte solvation engineering is presented, which shapes a weakly solvating anion‐stabilized (WSAS) electrolyte by balancing the interaction between the Na⁺‐solvent and Na⁺‐anion. The special interaction constructs rich contact ion pairs (CIPs) /aggregates (AGGs) clusters at the electrode/electrolyte interface during the dynamic solvation process which facilitates the formation of a uniform and stable interfacial layer, enabling highly stable cycling of 4.0 V‐class layered oxide cathode from −40 °C to 60 °C and excellent reversibility of Na plating/stripping with an ultrahigh average CE of 99.89%. Ultimately, industrial multi‐layer anode‐free pouch cells using the WSAS electrolyte achieve 80% capacity remaining after 50 cycles and even deliver 74.3% capacity at −30 °C. This work takes a pivotal step for the further development of high‐energy‐density Na batteries.


Revealing the Dynamic Evolution of Electrolyte Configuration on the Cathode‐Electrolyte Interface by Visualizing (De)Solvation Processes

August 2024

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34 Reads

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1 Citation

Angewandte Chemie

Electrolyte engineering is crucial for improving cathode electrolyte interphase (CEI) to enhance the performance of lithium‐ion batteries, especially at high charging cut‐off voltages. However, typical electrolyte modification strategies always focus on the solvation structure in the bulk region, but consistently neglect the dynamic evolution of electrolyte solvation configuration at the cathode‐electrolyte interface, which directly influences the CEI construction. Herein, we reveal an anti‐synergy effect between Li+‐solvation and interfacial electric field by visualizing the dynamic evolution of electrolyte solvation configuration at the cathode‐electrolyte interface, which determines the concentration of interfacial solvated‐Li+. The Li+ solvation in the charging process facilitates the construction of a concentrated (Li+‐solvent/anion‐rich) interface and anion‐derived CEI, while the repulsive force derived from interfacial electric field induces the formation of a diluted (solvent‐rich) interface and solvent‐derived CEI. Modifying the electrochemical protocols and electrolyte formulation, we regulate the “inflection voltage” arising from the anti‐synergy effect and prolong the lifetime of the concentrated interface, which further improves the functionality of CEI architecture.


Characterization of Na2O‐based high capacity presodiation agent. a) Voltage profile for (Na2O + NiO) composite cathode at 10 mA g⁻¹ with a 4.5 V upper cutoff potential; the inset shows the pure Na2O cathode capacity (<15 mAh g⁻¹) at cutoff 4.5 V. b) Schematic illustration of the preparation procedure of NNO composite presodiation agent by high‐energy ball milling. c) sXRD pattern and d) NPD pattern of NNO presodiation agent and the results of fitting via Rietveld refinement. e) The density of states (DOS) of Na2O (top) and Ni–Na2O (bottom). f) Gibbs free energy diagrams during the pure Na2O and Ni–Na2O decomposition process.
The structural and local covalent environment evolution during NNO decomposition. a) Ex situ sXRD patterns and the results of fitting via Rietveld refinement of NNO presodiation agent in different voltages. The sXRD peak intensities of Ni–Na2O presodiation agent at 2θ = 14.0°, 19.8°, 23.3°, 24.3°, and 28.3° (Ni–Na2O), 2θ = 16.4°, 18.9°, and 26.9° (NiO), respectively. b–d) TEM images of charged NNO presodiation agent cathode at pristine, charge 4.3 V, and discharge 1.5 V. Insets present the corresponding SEAD patterns. The red and yellow marker lines represent the NiO and Ni–Na2O phases, respectively, and the white ones represent the amorphous phase. e) Ni K‐edge X‐ray absorption near‐edge structure (XANES) spectra at different voltage states. Upper left inset: enlarged pre‐edge of Ni K‐edge XANES spectra and a schematic illustration of Ni–O tetrahedral (tetra.) configuration (Ni in Na2O) and octahedral (octa.) configuration (Ni in NiO). Inset below right: edge positions of Ni K‐edge at different voltage states. f) Ni K‐edge EXAFS spectra (weighted by k³) of pristine and charged 4.5 V NNO presodiation agent. The Ni molar percentage pie chart of Ni–Na2O (green region) and NiO (purple region) in NNO presodiation agent. The fitted Ni–O coordination numbers (C.N.) are shown in the inset.
Analysis of oxygen behavior upon Na2O oxidation in NNO. a) The top panel shows the galvanostatic charge curve for the initial charging process of the NNO presodiation agent cathode at a current density of 50 mA g⁻¹. Five points are labeled in the charge curve: OCV, 3.25 V,3.45 V, 3.65 V, and 4.5 V, respectively. b) The middle panel shows OEMS results of corresponding time‐resolved evolution rates for O2 and CO2 during initial charging. c) TMS result: amounts of O2 and CO2 collected from the NNO presodiation agent plates with different specific voltages. d) O K‐edge XANES spectra of the NNO presodiation agent cathode and standard samples at TEY modes. The peak at 533 eV represents oxygen in the antifluorite structure of Na2O; the peak at 531.4 eV represents σ* (O─O) peroxide species; and the peak at 531.2 eV represents the hybridized state of O 2p and Ni 3d orbitals in NiO. e) The schematic diagram illustrating the dynamics of electrochemical transfer oxidation process during the charging of Ni–Na2O. The electronic structure of Na2O exhibits a charge transfer electronic ground state in the reduced phase (left). The O (2p) lone pairs denote |O2p. The splitting of the O 2p narrow band into distinct σ, π, π*, and σ* states is illustrated by the red (ΔσO─O) and green (ΔπO─O) arrows, with respect to the conversion of O─O dimer species (bottom horizontal axis).
Electrochemical performance after presodiation. a) Initial charge profiles of Na3V2(PO4)3 (NVP) and Na2/3Ni2/3Mn1/3O2 (NNMO) with n wt % (n = 0%, 5%, and 10%) NNO presodiation agent cathodes at 10 mA g⁻¹ in the range from 2.5 to 4.3 V and from 2.0 to 4.15 V, respectively. b) Cycling performance of NVP without or with NNO presodiation agent cathodes at 50 mA g⁻¹ in the range from 2.5 to 4.3 V. Inset: the bar chart corresponds to the charge and discharge capacity of the initial cycle at 10 mA g⁻¹. c) Galvanostatic charge/discharge curves of HC||NVP without or with 10 wt% NNO presodiation agent coin‐type full‐cell at 10 mA g⁻¹ (1 st) and 50 mA g⁻¹ (5–50 th) in the range from 1.0 to 4.2 V. d) Cycling performance of HC||NVP without or with 10 wt% NNO presodiation agent coin‐type full‐cell in the range from 1.0 to 4.2 V. e) Galvanostatic charge/discharge curves of HC||NNMO without or with 10 wt% NNO presodiation agent coin‐type full‐cell at 10 mA g⁻¹ (1st) and 50 mA g⁻¹ (5–50 th) in the range from 0.5 to 4.0 V. f) Cycling performance of HC||NNMO without or with 10 wt% NNO presodiation agent coin‐type full‐cell in the range from 0.5 to 4.0 V.
The impact of NNO on the electrode–electrolyte interface and associated perspective on presodiation agent. a) TOF‐SIMS characterization of pure NVP and NVP‐NNO cycled cathode electrodes after 150 cycles. The normalized depth profiles of the interface and bulk fragments illustrate the structure of CEI. b) 3D renderings of selected secondary ion fragments of different CEI. The sputtered volume is 100 µm (length) × 100 µm (width) × 150 nm (height). c) TEM images of NVP‐NNP after 200 cycles. The IFFT results for the surface and bulk regions are also listed in the figure. The light green‐dashed ground state region is identified as NVP structure, white is defined as carbon layer region, and yellow is assessed as a CEI architecture. d) Scheme of CEI formation and changes on NVP and NVP‐NNO cathodes summarized from characterization data in FEC‐containing electrolytes. e) Perspectives for cathode presodiation agent.
Achieving High‐Capacity Cathode Presodiation Agent Via Triggering Anionic Oxidation Activity in Sodium Oxide

July 2024

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86 Reads

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5 Citations

Compensating for the irreversible loss of limited active sodium (Na) is crucial for enhancing the energy density of practical sodium‐ion batteries (SIBs) full‐cell, especially when employing hard carbon anode with initially lower coulombic efficiency. Introducing sacrificial cathode presodiation agents, particularly those that own potential anionic oxidation activity with a high theoretical capacity, can provide additional sodium sources for compensating Na loss. Herein, Ni atoms are precisely implanted at the Na sites within Na2O framework, obtaining a (Na0.89Ni0.05□0.06)2O (Ni–Na2O) presodiation agent. The synergistic interaction between Na vacancies and Ni catalyst effectively tunes the band structure, forming moderate Ni–O covalent bonds, activating the oxidation activity of oxygen anion, reducing the decomposition overpotential to 2.8 V (vs Na/Na⁺), and achieving a high presodiation capacity of 710 mAh/g≈Na2O (Na2O decomposition rate >80%). Incorporating currently‐modified presodiation agent with Na3V2(PO4)3 and Na2/3Ni2/3Mn1/3O2 cathodes, the energy density of corresponding Na‐ion full‐cells presents an essential improvement of 23.9% and 19.3%, respectively. Further, not limited to Ni–Na2O, the structure–function relationship between the anionic oxidation mechanism and electrode–electrolyte interface fabrication is revealed as a paradigm for the development of sacrificial cathode presodiation agent.


Capturing the variation of interfacial electrolyte configuration during (de−)solvation process via IR spectroscopy. (a) Ex situ FTIR spectra of EC: DMC (volume ratio=1 : 1) with different LiPF6 concentrations of 0 M, 1 M, and 3 M, respectively. The differential spectrum between 1 M and 3 M reveals the amount of conversion of free solvents and coordinated solvents when changing salt concentration, demonstrating a bipolar “peak‐dip” pattern. (b) The schematic of the ATR‐IR that in situ monitoring electrolyte configuration at electrode/electrolyte interface. (c) In situ raw FTIR spectra and corresponding differential spectrum of electrolyte during potentiostatic plating and stripping processes. The bipolar “peak‐dip” pattern in differential spectra reveals the dynamic variation of interfacial electrolyte configuration. Schematic diagram of (d) the anion‐lean solvent‐rich interface and (e) the anion‐rich solvent‐lean interface involving the interfacial evolution of Li⁺‐solvent species and anions during the de‐solvation/solvation process.
Visualizing anion distribution during plating/stripping processes via in situ MRI. The schematic of (a) in situ MRI that in situ monitoring ¹⁹F to present concentration distribution of PF6⁻ anion and (b) the symmetric sealed cell for In situ MRI. (c) Original 2D‐MRI sagittal plane image. (d) In situ subtractive 2D‐MRI images (image acquisition every 30 minutes (I–IX)).
A pulse cycling protocol for regulating interfacial electrolyte configuration to modify SEI architecture. (a) The schematic of interfacial electrolyte configuration variation from typical galvanostatic and pulse protocol. For both protocols, the anion‐lean solvent‐rich interface is formed as the anodic current passes. For typical galvanostatic protocol, the anion is repelled when a cathodic current is applied. For pulse protocol, the gradient of concentration promotes anion diffusion towards the electrode in Toff. Thus, the concentration of anion in the interfacial region is restored leading to forming anion‐derived SEI. (b) Cycle performances of Li/Li symmetric cells with typical galvanostatic protocol (gray) and pulse protocol (blue) at a fixed capacity of 1 mAh cm⁻² at the current density of 3 mA cm⁻². Note: Ton=1 s; Ton: Toff=1 : 5. The rest time (Toff) has been subtracted.
Characterizations of SEIs formation in the 1 M LiPF6/EC: DMC (volume ratio=1 : 1) on the cycled Lithium foils with different protocols. (a) XPS spectra of SEIs formation with a pulse (upper) protocol and galvanostatic protocol (lower). (b) The atomic ratio of F, C, O, and P elements as a function of Ar⁺ etching depth. (c) 3D‐rendering images of LiF2⁻ (I and II) (indicating LiF component generated from anion decomposition), C2HO⁻ (III and IV), and LiCO3⁻ (V and VI) (indicating organic species especially carboxylates generated from carbonate decomposition). (d) The intuitive XZ‐2D plane reconstructed images of the relevant ion fragments.
Visualizing and Regulating Dynamic Evolution of Interfacial Electrolyte Configuration during De‐solvation Process on Lithium‐Metal Anode

March 2024

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66 Reads

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23 Citations

Acting as a passive protective layer, solid‐electrolyte interphase (SEI) plays a crucial role in maintaining the stability of the Li‐metal anode. Derived from the reductive decomposition of electrolytes (e.g., anion and solvent), the SEI construction presents as an interfacial process accompanied by the dynamic de‐solvation process during Li‐metal plating. However, typical electrolyte engineering and related SEI modification strategies always ignore the dynamic evolution of electrolyte configuration at the Li/electrolyte interface, which essentially determines the SEI architecture. Herein, by employing advanced electrochemical in situ FT‐IR and MRI technologies, we directly visualize the dynamic variations of solvation environments involving Li⁺‐solvent/anion. Remarkably, a weakened Li⁺‐solvent interaction and anion‐lean interfacial electrolyte configuration have been synchronously revealed, which is difficult for the fabrication of anion‐derived SEI layer. Moreover, as a simple electrochemical regulation strategy, pulse protocol was introduced to effectively restore the interfacial anion concentration, resulting in an enhanced LiF‐rich SEI layer and improved Li‐metal plating/stripping reversibility.


Visualizing and Regulating Dynamic Evolution of Interfacial Electrolyte Configuration during De‐solvation Process on Lithium‐Metal Anode

March 2024

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17 Reads

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4 Citations

Angewandte Chemie

Acting as a passive protective layer, solid‐electrolyte interphase (SEI) plays a crucial role in maintaining the stability of the Li‐metal anode. Derived from the reductive decomposition of electrolytes (e.g., anion and solvent), the SEI construction presents as an interfacial process accompanied by the dynamic de‐solvation process during Li‐metal plating. However, typical electrolyte engineering and related SEI modification strategies always ignore the dynamic evolution of electrolyte configuration at the Li/electrolyte interface, which essentially determines the SEI architecture. Herein, by employing advanced electrochemical in‐situ FT‐IR and MRI technologies, we directly visualize the dynamic variations of solvation environments involving Li+‐solvent/anion. Remarkably, a weakened Li+‐solvent interaction and anion‐lean interfacial electrolyte configuration have been synchronously revealed, which is difficult for the fabrication of anion‐derived SEI layer. Moreover, as a simple electrochemical regulation strategy, pulse protocol was introduced to effectively restore the interfacial anion concentration, resulting in an enhanced LiF‐rich SEI layer and improved Li‐metal plating/stripping reversibility.


Citations (10)


... To further clarify the principles behind the discrepancy of fast charging performance, we then studied the solvation structures of electrolytes, which usually result from the competition between different interactions. [48][49][50][51][52] The solvation structure can be generally classied into three types according to the coordination number of Li + with TFSI − , namely AGGs (>1 Li + ), CIPs (contact ion pairs = 1 Li + ), and SSIPs (solvent-separated ion pairs, no Li + and free TFSI − ). Symmetric S-N-S stretching vibration in TFSI − , located at around 750 cm −1 in Raman and Fourier Transform Infrared (FTIR) spectra, is sensitive to the coordination of Li + . ...

Reference:

Solvation structure dependent ion transport and desolvation mechanism for fast-charging Li-ion batteries
Visualizing and Regulating Dynamic Evolution of Interfacial Electrolyte Configuration during De‐solvation Process on Lithium‐Metal Anode

... As displayed in Figure 5i, Figure S43 and Figure S44, the multi-component nature of SEI is demonstrated by the observed amorphous and crystalized region with thickness of around 120 nm. A mixture of crystalline lattice fringes of ZnO (100), Zn 5 -(OH) 8 Cl 2 · H 2 O (101) are identified in the SEI, which may possess high interfacial energy to suppress the detrimental side reactions [45] (Figure 5j-5l). Compared to HAE, the poly-inorganic composite aggregates and larger crystal lattice area can be detected with numerous non-uniform protrusions in Aqua, which may irreversibly block ion transport and cause accumulation of by products in the stripping/plating processes. ...

Gradient Interphase Engineering Enabled by Anionic Redox for High-Voltage and Long-Life Li-Ion Batteries
  • Citing Article
  • February 2024

Journal of the American Chemical Society

... With the widespread adoption of new energy vehicles and large-scale energy storage devices, traditional Li + batteries are approaching their limits in the energy storage capacity. [1][2][3][4] Lithium-sulfur (Li-S) batteries, with their high theoretical energy density (2600 W h kg À 1 ) and low cost, are emerging as promising candidates for the next generation of energy storage system. [5] However, the real-world application of LiÀ S batteries has encountered significant obstacles, primarily due to limited practical energy density, low coulombic efficiency, and poor cycling stability. ...

Lattice Engineering on Li 2 CO 3 ‐Based Sacrificial Cathode Pre‐lithiation Agent for Improving The Energy Density of Li‐Ion Battery Full‐Cell

... [14] However, lithium salt additives, such as LiF, LiNO 3 , and LiDFOB, are costly and limited in variety. [15] Inorganic compound additives may lead to cycling instability due to subtle changes in size, morphology, and crystal phase. In contrast, ionic liquids (ILs), particularly pyrrole-and imidazolyl-based ones, have gained extensive attentions as organic additives due to their low cost, renewability, and self-repairing properties. ...

Protecting Li-metal in O2 atmosphere by sacrificial polymer additive for Li-O2 Battery
  • Citing Article
  • November 2023

Nanoscale

... Subsequently, in 1991, Sony commercialized the first lithium-ion batteries (LIBs) product [9][10][11][12][13] . With the continued strong demand in the new energy market and the release of production capacity in the industry, new batteries such as zinc ions [14] , sodium ions [15] , and lithium-sulfur [16] have appeared dramatically. During this period, scientific researchers conducted continuous research on the battery efficiency and found that it largely depended on the characteristics of the cathode materials [17] . ...

Recognition and Application of Catalysis in Secondary Rechargeable Batteries
  • Citing Article
  • July 2023

ACS Catalysis

... 当聚焦在"料-材-器-用"的"器"和"用"的层次时, [57,58] (图7b), 更加适用于穿透商业 图 5 针对二次电池产气的工况表征 [47] (网络版彩图) 图 7 针对二次电池工况的显微计算机断层扫描表征(a)和 中子成像表征(b) [58] (网络版彩图) Figure 7 Operando microcomputed tomography (a) and neutron imaging (b) [58] characterization for rechargeable batteries (color online). ...

Tracking gassing behavior in pouch cell by operando on-line electrochemical mass spectrometry
  • Citing Article
  • May 2023

Journal of Energy Chemistry

... As shown in part I of Figure 1a, the raw spectra are mainly divided into three regions: the region with the maximum wavenumber (1830-1680 cm À 1 ) falls within the range of the stretching vibration absorption of the carbonyl group (C=O) in carbonate solvent, while the absorption peak around 1350-1040 cm À 1 is grouped as the vibrational absorption of the OÀ CÀ O group in the solvent; [33] and the region with the minimum wavenumber (880-790 cm À 1 ) corresponds to the stretching vibration region of the PÀ F bond in PF 6 À -associated species. [35] The assignments of the infrared absorption of the electrolyte are summarized in Table S1. ...

Full-Dimensional Analysis of Electrolyte Decomposition on Cathode-Electrolyte Interface: Establishing Characterization Paradigm on LiNi0.6Co0.2Mn0.2O2 Cathode with Potential Dependence
  • Citing Article
  • May 2023

The Journal of Physical Chemistry Letters

... Both the VF-NFMO and VC-NFMO cathodes were charged to 4.5 V and then disassembled immediately in the glove box, and the obtained cathode plates (with electrolyte) were placed into a well-designed airtight container for testing. Next, the airtight container was transferred from the glove box and connected to an advanced gas analysis system (previously reported) 55 . To ensure a stable background, the total gas line was purged by Ar carrier for about 20 min. ...

Titration Mass Spectroscopy (TMS): A Quantitative Analytical Technology for Rechargeable Batteries
  • Citing Article
  • December 2022

Nano Letters

... 9 Besides, the constantly generated SEI forms a thick and porous surface layer on lithium metal, resulting in largely increased interfacial resistance. 10 Numerous efforts have been devoted to inhibiting lithium dendrite growth and enhancing the stability of anodes, such as using modified separators, 11 nanostructured anodes, 12 electrolyte additives, 13 surface coating, 14 and so on. Among these approaches, developing appropriate electrolyte additives is one of the most effective and economical strategies to improve the electrochemical performance and energy efficiency of lithium-oxygen batteries. ...

Enhancing the Reaction Kinetics and Reversibility of Li–O2 Batteries by Multifunctional Polymer Additive

... Fifth, for Li 1s peaks, it is noted that, more LiF and ROCO 2 Li, Li 3 PO 4 species exist in the FEC-DFEC electrolyte, locating at binding energies of 56.0 and 55.4 eV, respectively. [ 15 ] 1.3 M LiPF 6 in EC/PC/EB + 7% FEC + 1% LiFMDFB + 3% HTCN + 0.2% TMSP LCO||graphite coin cell: 3.0-4.55 V charge at 1.5 C and discharge at 0.5 C 500 th 51.8%. ...

Tailoring Electrolyte Dehydrogenation with Trace Additives: Stabilizing the LiCoO 2 Cathode beyond 4.6 V
  • Citing Article
  • July 2022

ACS Energy Letters