Guifan Zeng’s research while affiliated with Xiamen University and other places

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Publications (19)


Unravelling the Oxygen Evolution Mechanism of Lithium‐Rich Antifluorite Prelithiation Agent Based on Anionic Oxidation
  • Article

March 2025

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9 Reads

Angewandte Chemie

Yuanlong Zhu

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Ruoyu Xu

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Yichun Zheng

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[...]

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Shi‐Gang Sun

Developing sacrificial cathode prelithiation technology to compensate for irreversible lithium loss is crucial for enhancing the energy density of lithium‐ion batteries. Antifluorite Li‐rich Li 5 FeO 4 (LFO) is a promising prelithiation agent due to its high theoretical capacity (867 mAh g ⁻¹ ) and superior decomposition dynamic (<4.0 V vs. Li/Li ⁺ ). However, the oxygen evolution mechanism in LFO remains unclear, limiting its application as an ideal prelithiation agent. Herein, we systematically track the full lifecycle oxygen footprint in LFO lattice, electrolyte and solid electrolyte interface (SEI). We demonstrate the lattice mismatch induced by the quasi‐disorder rocksalt intermediate phase can activate the lattice oxygen oxidation promoting the dimerization to O 2 . Specifically, in contrast to the O─O dimers formed within typical anionic‐redox active cathodes, the oxidation of lattice oxygen in LFO generates O ⁻ stabilized in Li 6 ‐O configuration. Significantly, a pair of edge‐sharing Li 6 ‐O configurations transforms into a superoxo dimer, which further evolves into O 2 via a ligand‐to‐metal charge transfer process. Moreover, we demonstrate that nucleophilic intermediates threaten the stability of electrolytes and SEI. Leveraging the insights above, we offer comprehensive perspectives for the modification of ideal prelithiation agents.


a) Galvanostatic charge profile of Li5FeO4 with 4.5 V cutoff voltage at a current density of 20 mA g⁻¹. Charging from OCV to 3.85 V and 3.85 V to 4.5 V are denoted as the stage I (SI) and stage II (SII), respectively. The structure of the Li5FeO4 unit cell is inserted. b) Rietveld refinements of sXRD patterns collected at OCV, 3.85 V, and 3.95 V. c) 2D model of sXRD patterns corresponding to the different states of charge in b.
a) Fe K‐edge EXAFS fitting results of Fe‐O shell in R‐space based on LFO collected at different states of charge. Corresponding coordination environment compositions are shown in pie charts, whose coordination number (C. N.) is 4.0 in the yellow region and is 6.0 in the red region. b) The mean square relative displacements (MSRD, σ²) of Fe‐O bonds based on LFO collected by fitting the corresponding EXAFS spectra. The delithiation amount from 0 to 4 corresponds to the charge state from OCV to 4.5 V by sequence. c) Fe K‐edge XANES based on LFO at different states of charge. d) Edge positions of Fe K‐edge XANES based on LFO collected at different states of charge. e) Diagram of LFO structure distribution during the entire phase transition process, where each color block represents a region with a long‐range order phase. Corresponding local atomic geometry configurations are attached next to the color blocks. The dotted circles around O atoms indicate the variations in interatomic distance induced by the deviations of the actual atomic positions from the equilibrium positions, which reflects the degree of local disorder under specific states of charge.
a) The top panel shows the galvanostatic charge curve for the initial charging process of the LFO at a current density of 40 mA g⁻¹. Five points are labelled in the charge curve: OCV, 3.5 V, 3.85 V, 3.95 V and 4.5 V, respectively. The middle panel shows quantitative TMS for O2 and CO2 collected from LFO at corresponding states of charge. The bottom panel shows DEMS results of corresponding time‐resolved evolution rates for O2 and CO2 during initial charging. b) O K‐edge SXAS spectra of the LFO at TFY modes collected at different states of charge showing the emergence of the peak at around 528 eV. c) O K‐edge RIXS maps of the LFO collected at OCV, 3.85 V, 3.95 V and 4.5 V, respectively. The anionic‐redox feature emerges at an excitation energy of around 528 eV and an emission energy of around 526 eV. d) Electrochemical in situ SERS of LFO during charging to 4.5 V. SERS peak intensities for carbonate (≈1080 cm⁻¹), and superoxide (O─O) (≈1108 cm⁻¹) are indicated, respectively. e) Delithiation amount‐dependent relative intensity of superoxide (red dots) and carbonate (blue dots) in SERS during charging.
pDOS of the O 2p orbitals and Fe 3d orbitals of O ions and first nearest Fe ions based on different local coordination environments in x = 2 (Li5‐xFeO4), including a) Li6–O configurations where hole polarons localize on oxygen (O⁻) to form in‐gap states, b) a pair of edge‐sharing Li6–O configurations exhibiting localized unpaired non‐bonding O‐p character on the Fermi level before relaxation, c) superoxo dimer after relaxation. d) Fe Bader charge change during delithiation process. The corresponding oxygen evolution process undergoes dimerization of lattice oxygen (O²⁻) to superoxo dimer (O2⁻) and further transforms into O2 through LMCT. e) Calculated O vacancy formation energy (red dots) and lattice mismatch (blue dots) as a function of Li removal in Li5FeO4.
a) Summary of phase transitions and Fe/O contribution forms in charge compensation process of LFO at different states of charge. b) The schematized rearrangement pattern of the electronic band structure during the charge process of LFO, where U and ΔCT represent coulombic interactions in the d shell and TM–O charge transfer, respectively. The pristine state is described by a partially filled anti‐(TM‐O) band, split by U into an empty upper Hubbard band (UHB) and a lower Hubbard band (LHB). A fully occupied O 2p lone pairs states (|O2p) band overlaps significantly with the LHB near the Fermi level (U/2 ∼ ΔCT), which allows simultaneous cationic and anionic oxidation. The oxidation of O generates hole polaron O⁻, which is stabilized by Li6‐O configuration. At SI, O⁻ species is stable as long as ΔCT > ΔO─Oσ*, and the anionic oxidation is reversible within the lattice. A pair of edge‐sharing Li6‐O configuration promotes O─O pairing out of lattice. Further charge from SI to SII, the narrow |O2p band splits into discrete σ, π, π*, and σ* bands. As a result of the depletion of electrons from the metallic d‐band and the concomitant U increase, the metallic band lies below the π* states of the oxidized species (ΔO─Oπ* > ΔCT), enabling the formation of O2⁻. In the meantime, a significant charge transfer can occur from oxygen to the metal center (LMCT process). The electron depletion from the |O2p finally leads to further evolution of superoxo dimer into O2 via a reductive elimination process.

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Unravelling the Oxygen Evolution Mechanism of Lithium‐Rich Antifluorite Prelithiation Agent Based on Anionic Oxidation
  • Article
  • Publisher preview available

March 2025

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22 Reads

Developing sacrificial cathode prelithiation technology to compensate for irreversible lithium loss is crucial for enhancing the energy density of lithium‐ion batteries. Antifluorite Li‐rich Li5FeO4 (LFO) is a promising prelithiation agent due to its high theoretical capacity (867 mAh g⁻¹) and superior decomposition dynamic (<4.0 V vs. Li/Li⁺). However, the oxygen evolution mechanism in LFO remains unclear, limiting its application as an ideal prelithiation agent. Herein, we systematically track the full lifecycle oxygen footprint in LFO lattice, electrolyte and solid electrolyte interface (SEI). We demonstrate the lattice mismatch induced by the quasi‐disorder rocksalt intermediate phase can activate the lattice oxygen oxidation promoting the dimerization to O2. Specifically, in contrast to the O─O dimers formed within typical anionic‐redox active cathodes, the oxidation of lattice oxygen in LFO generates O⁻ stabilized in Li6‐O configuration. Significantly, a pair of edge‐sharing Li6‐O configurations transforms into a superoxo dimer, which further evolves into O2 via a ligand‐to‐metal charge transfer process. Moreover, we demonstrate that nucleophilic intermediates threaten the stability of electrolytes and SEI. Leveraging the insights above, we offer comprehensive perspectives for the modification of ideal prelithiation agents.

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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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90 Reads

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12 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.


Sustainable layered cathode with suppressed phase transition for long-life sodium-ion batteries

February 2024

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600 Reads

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66 Citations

Nature Sustainability

Sodium-ion batteries are among the most promising alternatives to lithium-based technologies for grid and other energy storage applications due to their cost benefits and sustainable resource supply. For the cathode—the component that largely determines the energy density of a sodium-ion battery cell—one major category of materials is P2-type layered oxides. Unfortunately, at high state-of-charge, such materials tend to undergo a phase transition with a very large volume change and consequent structural degradation during long-term cycling. Here we address this issue by introducing vacancies into the transition metal layer of P2-Na0.7Fe0.1Mn0.75□0.15O2 (‘□’ represents a vacancy). The transition metal vacancy serves to suppress migration of neighbouring Na ions and therefore maintain structural and thermal stability in Na-depleted states. Moreover, the specific Na−O−□ configuration triggers a reversible anionic redox reaction and boosts the energy density. As a result, the cathode design here enables pouch cells with energy densities of 170 Wh kg⁻¹ and 120 Wh kg⁻¹ that can operate for over 600 and 1,000 cycles, respectively. Our work not only suggests a feasible strategy for cathode design but also confirms the possibility of developing a battery chemistry that features a reduced need for critical raw materials.


Achieving a high-performance sodium-ion pouch cell by regulating intergrowth structures in a layered oxide cathode with anionic redox

January 2024

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518 Reads

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90 Citations

Nature Energy

In P2-type layered transition metal (TM) oxides, which are typical cathode materials for Na-ion batteries, the presence of Li within the TM layer could lead to the formation of specific Na–O–Li configurations that trigger additional oxygen redox at high charging voltages. However, the prismatic-type (P-type) to octahedral-type (O-type) phase transition and irreversible TM migration could be simultaneously aggravated in high state of charge, resulting in structural distortion. Here we demonstrate that excessive desodiation of P2-Na0.67Li0.1Fe0.37Mn0.53O2 (NLFMO) induces the formation of neighbouring O-type stacking faults with an intergrowth structure (that is, interlacing of O- and P-type layers), which leads to out-of-lattice Li migration and irreversible oxygen loss. We show that, by controlling the depth of charge to tailor the intergrowth structure, a P-type stacking state can be uniformly interspersed between the O-type stacking state, thereby avoiding neighbouring O-type stacking faults. Adjusting the O/P intergrowth structure leads to both reversible migration of Li/TM ions and reversible anionic redox in the NLFMO cathode. We thereby achieve a high-performance pouch cell (with an energy density of 165 W h kg⁻¹ based on the entire weight of the cell) with both cationic and anionic redox activities.


a) Galvanostatic charge profile of Li2CO3 with 4.7 V cutoff voltage at a current density of 50 mA g⁻¹. Partial enlarged profile and thermodynamic decomposition pathway are inserted. b) Effect and route of structural design for Co‐Li2CO3@LCO through ball milling. Rietveld refinements of c) sXRD and d) NPD of Co‐Li2CO3@LCO. e) TEM image of Co‐Li2CO3@LCO at pristine state, the FFT and IFFT images representing BM‐LCO (blue rectangular area) and Co‐Li2CO3 (yellow rectangular area) are also listed in the figure. f) Galvanostatic charge profile of Li2CO3 and Co‐Li2CO3@LCO with 4.7 V cutoff voltage at a current density of 50 mA g⁻¹. The capacity contribution of BM‐LCO (green region) and Co‐Li2CO3 (blue region) are clarified in pie chart.
a) Total density of states (TDOS) and projected density of states (PDOS) of Li‐s, C‐p, O‐p, Co‐d based on Li2CO3 and Co‐Li2CO3. b) (negative integrated) Crystal occupation Hamiltonian population (COHP/‐ICOHP) of the Li1─O1 bonds based on Li2CO3 and Co‐Li2CO3. c) Wavelet transform (WT)‐EXAFS spectra of BM‐LCO and Co‐Li2CO3@LCO at pristine states. d) Chromatic 3D WT‐EXAFS differential spectrum of Co‐Li2CO3@LCO versus BM‐LCO at pristine states. e) The Co molar percentage pie chart of BM‐LCO (yellow region) and Co‐Li2CO3 (red region) in Co‐Li2CO3@LCO, whose coordination number (CN) of Co─O is 6.0 and 4.0, respectively. Co K‐edge EXAFS fitting results of Co─O shell in R‐space at pristine state based on BM‐LCO and Co‐Li2CO3@LCO are plotted below. f,g) Co K‐edge XANES and their first order derivative spectra with differential and first order derivative differential spectra (charge to 4.6 V vs OCV) based on f) BM‐LCO and g) Co‐Li2CO3@LCO, respectively.
a) Electrochemical in situ Raman (blue trace) and SERS (red trace) spectra of Co‐Li2CO3@LCO during charging to 4.7 V. In situ Raman peak intensity for Li2CO3 (≈1080 cm⁻¹), SERS peak intensities for Li2CO3 (≈1080 cm⁻¹), and superoxide (O─O) (≈1108 cm⁻¹) are indicated, respectively. b) Capacity‐dependent relative intensity of Li2CO3 in Raman (blue dots), Li2CO3 in SERS (red dots), and superoxide (O─O) in SERS (grey dots) during charging. c) In situ OEMS harvested from Co‐Li2CO3@LCO (blue trace) and BM‐LCO (orange trace) during initial cycle (2.8–4.7 V) and the second charging to 4.7 V at current density of 150 mA g⁻¹. CO2, CO, and O2 were collected simultaneously. The electron number (versus CO2 gas molecule) is marked with the dashed lines. d) Quantitative TMS for Li2CO3 at pristine and charged state (4.7 V). The TMS‐related cell unit is inserted for clarity. e) The schematic for the achievement of Co‐Li2CO3@LCO electrochemical decomposition through lattice engineering.
a) Cycling performance of NCM‐811 half‐cell with addition of 0, 3, 5 wt% Co‐Li2CO3@LCO at 20 mA g⁻¹ (2.8–4.7 V) during initial cycle and 50 mA g⁻¹ (2.8–4.3 V) in subsequent cycle. The bar chart corresponding to the charge and discharge capacity of the initial cycle is inserted. b) Full cell performance in two different scenarios. Voltage profiles during initial cycle of the SiO/C || Li half‐cell (at 40 mA g⁻¹), and the NCM‐811 || SiO/C full‐cell without/with 9 wt% (at 20 mA g⁻¹). c) Galvanostatic charge/discharge curves of NCM‐811 || SiO/C without/with 9 wt% coin‐type full‐cell at 20 mA g⁻¹ (2.0–4.65 V for 1st) and 50 mA g⁻¹ (2.0–4.2 V for 2nd–50th). Cycling performance of d) NCM‐811 || SiO/C and e) NCM‐811 || Gr coin‐type full cells without/with 9/5 wt%. f) Discharge capacity and coulombic efficiency during cycles of the NCM‐811 || Gr pouch‐type full‐cell with 5 wt%. Inset: a photograph of the pouch cell is shown for clarity. g) Galvanostatic charge curves of TM‐Li2CO3@TM source (LiFePO4, NCM‐333, LiCoO2, spent LiCoO2) with 4.7 V cutoff voltage at 50 mA g⁻¹. The spent LiCoO2 collected from waste cells is in the inset.
a) The schematic for the configuration of battery pack with pressure‐driven safety valve enlarged for clarity. b) In situ OEMS harvested from charge process of NCM‐811 half‐cell with 9 wt% Co‐Li2CO3@LCO (4.5 V, 20 mA g⁻¹). The normal working voltage of cycle is ≤ 4.2 V (green region) followed by overcharge (red region). Gas evolution rate (blue trace) and amount (red trace) of CO2 are plotted below. The accumulation of CO2 in the headspace leads to the increase in pressure, ultimately triggering the safety valve to release CO2 and cut off the power supply promptly, which is depicted in the inset.
Lattice Engineering on Li 2 CO 3 ‐Based Sacrificial Cathode Pre‐lithiation Agent for Improving The Energy Density of Li‐Ion Battery Full‐Cell

December 2023

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169 Reads

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20 Citations

Developing sacrificial cathode pre‐lithiation technology to compensate for active lithium loss is vital for improving the energy density of lithium‐ion battery full‐cells. Li 2 CO 3 owns high theoretical specific capacity, superior air stability, but poor conductivity as an insulator, acting as a promising but challenging pre‐lithiation agent candidate. Herein, extracting a trace amount of Co from LiCoO 2 (LCO), we develop a lattice engineering through substituting Li sites with Co and inducing Li defects to obtain Co‐Li 2 CO 3 @LCO, in which both the bandgap and Li‐O bond strength have essentially declined. Benefiting from the synergistic effect of Li defects and bulk phase catalytic regulation of Co, the potential of Li 2 CO 3 deep decomposition significantly decreases from typical >4.7 V to ∼4.25 V versus Li/Li ⁺ , presenting >600 mAh/g compensation capacity. Impressively, coupling 5 wt% Co‐Li 2 CO 3 @LCO within NCM‐811 cathode, 235 Wh/kg pouch‐type full‐cell is achieved, performing 88% capacity retention after 1000 cycles. This article is protected by copyright. All rights reserved


The typical design principles of the conventional modification strategies: coating, doping, and architecture engineering.
a) Refined ND patterns of pristine Nb@LCO. A schematic illustration of Nb occupying Li sites in Nb@LCO is shown in the inset. b) HR‐TEM image of Nb@LCO. The fast Fourier transform (FFT) image and corresponding inverse FFT (IFFT) image obtained from the Li3NbO4 surface layer are displayed on the right side. c) FIB‐SEM image of Nb@LCO and EDX mapping of Co and Nb. d) XPS spectra of Nb 3d collected from Nb@LCO. The results demonstrate the gradient distribution of Nb. e,f) Typical galvanostatic charge/discharge profiles curves of e) LCO and f) Nb@LCO under the current density of 0.2 C (1 C = 200 mA g⁻¹) for 3–4.6 V. g) Discharge capacity hysteresis against cycle numbers profiles of LCO and Nb@LCO half‐cells at the cut‐off voltage of 4.6 V. h) Discharge capacity hysteresis against cycle numbers profiles of Nb@LCO||graphite pouch cell with the energy density of 250 Wh kg⁻¹. i) Discharge capacity hysteresis against cycle numbers profiles of 550 Wh kg⁻¹ Nb@LCO pouch cell assembled with thin Li anode at the cut‐off voltage of 4.7 V.
a) Schematic drawing of sXAS technique with surface‐sensitive TEY and more bulk‐sensitive TFY detection modes. b,c) Co L3‐edge sXAS spectra of pristine sample, charged LCO, and charged Nb@LCO collected from b) TEY and c) TFY modes. d) Schematic drawing of EC and corresponding C═O stretching vibrations during oxidative dehydrogenation. e) DRIFT spectra of the C═O stretching region obtained from fresh electrolyte, charged LCO, and charged Nb@LCO electrode surface after long‐term cycling while maintaining the presence of the electrolyte. DFT simulated spectra of dehydrogenated EC (deH‐EC), Li⁺‐coordinated EC (Li⁺‐EC), and Li⁺‐coordinated dehydrogenated EC (Li⁺‐deH‐EC) are depicted on the right‐hand side. Additionally, simulated spectra of species derived from DEC are also provided. f) TOF‐SIMS depth profiles (normalized to maximum) of P‐bearing inorganic species (POF2⁻) and hybrid inorganic/organic electrolyte decomposition products (LiCO3⁻, C2HO⁻, C2H3O⁻) collected from cycled LCO and Nb@LCO cathodes. The 3D distribution of dissolved Co species (CoF3⁻) is also shown inset.
a,b) In situ XRD patterns and the corresponding galvanostatic charge/discharge curves of a) LCO and b) Nb@LCO cathodes during the initial cycling process. c) The typical XRD curves collected at the end of charge. The process involves the phase transition from O3 to H1‐3 (hybrid‐phase of O1 and O3), with the red line indicating the reduced H1‐3 peak in Nb@LCO. d) The typical XRD curves collected at the end of discharge. The red trace patterns highlight the distinct phase transition modes of LCO and Nb@LCO during Li insertion, with the former exhibiting a single‐phase solid solution and the latter displaying the coexistence of H1 and H2 phases. The proposed models of Li insertion are also depicted in the inset. e,f) The GITT results of LCO and Nb@LCO in the e) 10th and f) 30th cycles. The red dashed line represents a significantly higher Li⁺ diffusion coefficient in Nb@LCO compared to LCO at the end of charge and discharge in the 30th cycle.
a) Calculated formation energy of oxygen vacancy on the surface and in the bulk of LCO (represented by orange column) and Nb@LCO (green column) with 0.7 Li⁺ removal. The illustrations depict the surface (Li3NbO4 coating) and bulk (doped Nb occupying at Li sites) structures of Nb@LCO. b) Potential‐dependent in situ OEMS results of O2 evolution in LCO and Nb@LCO cathodes during the initial charging to 4.7 V. c) Calculated energy of Co ion along the migration path from octahedral site in the TM layer to tetrahedral site in the Li layer. The related microstructural degradation, including O loss and Co migration, is depicted in the schematic drawing. d) The k³‐weighted Co K‐edge EXAFS spectra of charged LCO and Nb@LCO. The inset displays the fitted Co–O coordination numbers, demonstrating that Nb@LCO retains more CoO6 layered plates compared to LCO. e,f) Co L‐edge EELS data acquired from the surface to the interior of e) LCO and f) Nb@LCO cathodes after long‐term cycling. The red lines indicate the formation of the spinel‐like phase on the surface of LCO. g,h) HR‐TEM images of cycled g) LCO and h) Nb@LCO. The FFT and IFFT images obtained from surface and bulk regions are displayed on the right‐hand side of the figure.
One-Step Surface-to-Bulk Modification of High-Voltage and Long-Life LiCoO2 Cathode with Concentration Gradient Architecture

November 2023

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125 Reads

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34 Citations

Raising the charging cut‐off voltage of layered oxide cathodes can improve their energy density. However, it inevitably introduces instabilities regarding both bulk structure and surface/interface. Herein, exploiting the unique characteristics of high‐valance Nb ⁵⁺ element, we achieved a synchronous surface‐to‐bulk modified LiCoO 2 featuring Li 3 NbO 4 surface coating layer, Nb‐doped bulk, and the desired concentration gradient architecture through one‐step calcination. Such a multifunctional structure facilitates the construction of high‐quality cathode/electrolyte interface, enhances Li ⁺ diffusion, and restrains lattice‐O loss, Co migration and associated layer‐to‐spinel phase distortion. Therefore, a stable operation of Nb‐modified LiCoO 2 half‐cell is achieved at 4.6 V (90.9% capacity retention after 200 cycles). Long‐life 250 Wh/kg and 4.7 V‐class 550 Wh/kg pouch‐cells assembled with graphite and thin Li anodes are harvested (both beyond 87% after 1600 and 200 cycles). This multifunctional one‐step modification strategy establishes a technological paradigm to pave the way for high‐energy density and long‐life lithium‐ion cathode materials. This article is protected by copyright. All rights reserved


Lattice‐Matched Interfacial Modulation Based on Olivine Enamel‐Like Front‐Face Fabrication for High‐Voltage LiCoO2

November 2023

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130 Reads

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13 Citations

The high‐voltage induced undesirable surface passivation bilayer (cathode/electrolyte interface and cation‐densified surface phase) of LiCoO2 inevitably leads to battery degradation. Herein, a continual/uniform enamel‐like olivine layer on LiCoO2 surface is fabricated by employing a high‐speed mechanical fusion method . The enamel‐like layer suppresses interfacial side reactions by tuning EC dehydrogenation, contributing to an ultrathin and stable cathode/electrolyte interface. The strong bonding affinity between LiCoO2 and enamel‐like layer restrains both lattice oxygen loss and associated layered‐to‐spinel structural distortion. Moreover, the thermal stability of highly delithiated LiCoO2 is improved, as both the onset temperatures of layered‐to‐spinel transition and O2 evolution are simultaneously postponed. Stable operation of LiCoO2 at 4.6 V high‐voltage and 55 °C elevated temperature (both >85% capacity retention after 200 cycles) is achieved. This facile and scalable high‐speed solid‐phase coating strategy establishes a technical paradigm to enhance surface/interface stability of high‐energy‐density cathode candidates by constructing an ideal enamel‐like surface layer.


Citations (15)


... 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

... At the end stage of delithiation, a rapid drop of D Li + for all the cathodes can be inspected, for which the contraction of lattice along c-axis should be responsible. [37,38] However, NM91 displays significantly dropped voltage decay compared to EL-N9-3 after the 200 th cycles ( Figure S15), accompanied by the pronouncedly reduced D Li + values, which is almost one orders of magnitude smaller than that of EL-N9-3 during the H2-H3 phase transition process. These findings powerfully demonstrate that NM91 undergoes more severe structural degradation to form surface Li-insulative rock-salt phase and thicker detrimental by-products layers, whereas EL-N9-3 maintains a more stable layered structure that enables better conduction of Li + while reducing detrimental side reactions. ...

Revealing Gliding-Induced Structural Distortion in High-Nickel Layered Oxide Cathodes for Lithium-Ion Batteries
  • Citing Article
  • September 2024

ACS Nano

... Furthermore, uneven contact can result in inconsistent pre-sodiation, affecting battery capacity retention. [14] Inorganic additives have been explored for pre-sodiation purposes, including NaN 3 , [17,18] Na 2 O, [19,20] Na 3 P, [21] and NaCrO 2 . [22] However, their application is complicated by issues such as gas production, residual "dead mass," toxicity, and explosion risk. ...

Achieving High‐Capacity Cathode Presodiation Agent Via Triggering Anionic Oxidation Activity in Sodium Oxide

... Meanwhile, cation migration contributes to the cumulative formation of spinel phases and severe voltage decay during cycling, and attempts have been made to suppress this behavior by modulating the coordination structure of TM in the Na layer. This has inspired efforts to optimize the overall coordination structure of the TMO 2 and NaO 2 slabs to address the phase change and cation migration 14,20 . ...

Sustainable layered cathode with suppressed phase transition for long-life sodium-ion batteries

Nature Sustainability

... In this work, we use O3-Na[Li 1/3 Mn 2/3 ]O 2 , a promising O3-type oxygen anionic redox (OAR) cathode material for sodium-ion batteries, to demonstrate the complex reaction mechanism in a ternary system featuring two alkaline metals, both of which can form various oxide species with manganese, and importantly, the pivotal role of the synthesis atmosphere in determining the reaction pathways during the synthesis. We highlight that, despite their attractive properties such as high capacity and good cycling stability demonstrated by Na[Li 1/3 Mn 2/3 ]O 2 24 , manganese-based O3-type OAR sodium cathodes are significantly scarcer 21,24 as compared to the P2 polymorphs [25][26][27][28][29][30][31][32][33][34][35][36][37][38][39][40][41][42][43][44] . The key issue lies in the lack of fundamental understanding into the synthesis reactions that leads to the inaccessibility of O3-type phase pure compounds. ...

Achieving a high-performance sodium-ion pouch cell by regulating intergrowth structures in a layered oxide cathode with anionic redox

Nature Energy

... 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

... 21 From these results, the chemical states of Ni and Mn in LNMO are not changed by annealing even at 450 C, indicating the high thermal stability of LNMO electrode in comparison with other positive electrodes such as LiCoO 2 . 22,23 Notably, the peak of P 2p is located at 133.8 eV in the XPS spectra of the films without and with annealing at 200 C [ Fig. 2(c)], which is consistent with the corresponding XPS peak position reported for asprepared LPO (134 eV). 24 However, the peak is shifted to 133.2 eV in the XPS spectrum of the film annealed at 450 C, indicating that hightemperature annealing reduces the P in LPO. ...

Lattice‐Matched Interfacial Modulation Based on Olivine Enamel‐Like Front‐Face Fabrication for High‐Voltage LiCoO2

... In recent years, numerous approaches have been developed to stabilize the lattice, including introducing a more stable structure to act as a scaffold. 116,117 As shown in Fig. 13A, researchers have incorporated the perovskite variant phase La 4 [LiTM]O 8 (LLMO) as a "rivet" into the layered structure, forming a mechanically stable crystal structure. 114 HAADF-STEM images display the coherent growth of the LLMO phase along the [100] direction within the layered NCM (Fig. 13B). ...

One-Step Surface-to-Bulk Modification of High-Voltage and Long-Life LiCoO2 Cathode with Concentration Gradient Architecture

... In comparison with the white line peak (I) of NFM, the decreased intensity for Fe K-edge and increased intensity of NFM-CZF indicate that electric-dipole-allowed Fe/Mn 1s-4p (t* 1u ) transition would be affected by heteroatom doping. [16] Meanwhile, both the near edge line (II) of Fe and Mn exhibit a blue shift toward the standard average electronic valence state, suggesting the formation of a more optimized local electronic structure. [4b] In addition, the pre-edge peak (III) is mainly originated from the TM 3d (e* g )-O 2p orbital, showing a slight decrease in intensity with Ca/Zr/F incorporation, reflecting mitigated lattice distortion and strengthened centrosymmetry structure. ...

Unveiling the Evolution of LiCoO 2 beyond 4.6 V
  • Citing Article
  • October 2023

ACS Energy Letters

... All of the microstructure, phase components, particle shape, particle size, and specific surface of NaFePO 4 /C cathode materials were resources constrains their application in energy storage systems. Sodium (Na) and lithium (Li) are in the same main group of the periodic table and share similar chemical properties, which suggests that NaFePO 4 can theoretically offer performance comparable to LiFePO 4 [7][8][9][10][11][12][13]. However, sodium resources are more abundant, NaFePO 4 cathode material attracts much attention. ...

From Li to Na: Exploratory Analysis of Fe‐Based Phosphates Polyanion‐Type Cathode Materials by Mn Substitution
  • Citing Article
  • August 2023