Yuanlong Zhu’s research while affiliated with Xiamen University and other places

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Publications (10)


(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
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December 2024

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96 Reads

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2 Citations

Haiyan Luo

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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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45 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.


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.


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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152 Reads

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14 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


(a) Schematic illustration of the preparation procedure of CLO prelithiation agent by high‐energy ball milling. (b) sXRD pattern and (c) NPD pattern of CLO prelithiation agent and the results of fitting via Rietveld refinement. (d) Voltage profile for CLO prelithiation agent cathode at 50 mA/g with a 4.3 V upper cutoff potential, the inset showing the pure Li2O cathode prelithiation capacity (<20mAh/g) above 4.5 V. (e) The density of states (DOS) of Li2O (top) and CLO (bottom). (f) Crystal orbital Hamilton populations (COHP) analysis of Li−O1 and Li−O2 bonds in the Li2O (left) and CLO (right). The energy coordinate is relative to the Fermi level (Ef), so the Fermi level is set at 0 eV.
(a) Capacity‐dependent in situ Raman spectra and (b) in situ SERS spectra recorded from the CLO prelithiation agent cathode recorded during initial galvanostatic charging of a half cell. (c) Capacity dependence of the Raman peak intensities at 523 cm⁻¹ (Li2O), ≈788 cm⁻¹ (O−O stretch, Li2O2) and ≈1080 cm⁻¹ (Li2CO3), ≈1110 cm⁻¹ (O−O stretch, adsorbed O2⁻) collected from (a) the in situ Raman spectra and (b) the in situ SERS spectra. (d) The top panel shows the galvanostatic charge curve for the initial charging process of the CLO prelithiation agent cathode at a current density of 50 mA/g. Five points are labeled in the charge curve: C1: pristine; C2: 200 mAh/g (≈3.25 V); C3: 400 mAh/g (≈3.45 V); C4: 500 mAh/g (≈3.6 V); C5: end of initial charging at 4.3 V. (e) The middle panel shows OEMS results of gas evolution rates for O2 and CO2 during initial charging. (f) TMS result: amounts of O2 collected from the CLO prelithiation agent plates with different specific voltages at C1−C5, respectively.
(a) The initial charge–discharge curves of CLO prelithiation agent cathode at 50 mA/g in the 0.2 to 4.3 V range. The short discharge platform (≈2.75 V) corresponds to the O2 oxidation reaction. The discharge platform (≈1.1 V) corresponds to the phase conversion reaction of Co3O4. Insert: corresponding the in situ sXRD patterns. The sXRD peak intensities of CLO prelithiation agent cathode at 2θ=9.1° and 10.7° (PTFE), 2θ=9.4° and 10.3° (CLO), 2θ=10.4° (Co3O4), respectively. (b) TEM images of charged CLO prelithiation agent cathode at 4.3 V. Insets present the corresponding SEAD patterns. (c) Co K‐edge X‐ray absorption near‐edge structure (XANES) spectra at different voltage states and corresponding difference spectrum. (d) Co K‐edge FT‐EXAFS spectra of collected at different charge/discharge states and corresponding difference spectrum. (e) The corresponding Wavelet‐transformed Co K‐edge EXAFS. Color 3D WT EXAFS spectra showing the difference between the WT‐EXAFS spectra of the Co−O shell and Co−Co shell (initial charge to 4.3 V vs. OCV (f) and discharge to 1.5 V vs. initial charge to 4.3 V (g)).
(a) Cycling performance of NCM811 and NCM811 with P wt % (P=3 %, 5 %, and 7 %) CLO prelithiation agent cathodes at 50 mA/g in the range of 2.8–4.3 V. Inset: the bar chart is corresponding to the charge and discharge capacity of the initial cycle at 20 mA/g. (b) Galvanostatic charge/discharge curves of SiO/C||NCM without/with 7 wt % CLO prelithiation agent coin‐type full‐cell at 20 mA/g (1 st) and 50 mA/g (5–50 th) in the range of 2.0–4.2 V. (c) Cycling performance of SiO/C||NCM without/with 7 wt % CLO prelithiation agent (left) and Graphite||NCM without/with 3 wt % CLO prelithiation agent (right) coin‐type full‐cell in the range of 2.0–4.2 V. (d) The photograph of the SiO/C||LCO pouch cell‐A (capacity: 2.11 Ah, energy density: 250 Wh/kg) and pouch cell‐B (LCO with 6.5 wt % CLO, capacity: 2.50 Ah, energy density: 270 Wh/kg). (e) Discharge capacity and coulombic efficiency during different cycles for the pouch cell‐A and cell‐B. (f) The initial charge profiles of Li2O@cathode (cathode: fresh LCO, fresh NCM811 and spent LCO, respectively) at 50 mA/g with a 4.3 V upper cutoff potential. Insert: comparison of charging capacity of main prelithiation agent materials (based on the mass of the entire prelithiation agent).
Implanting Transition Metal into Li2O‐Based Cathode Prelithiation Agent for High‐Energy‐Density and Long‐Life Li‐Ion Batteries

December 2023

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86 Reads

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16 Citations

Compensating the irreversible loss of limited active lithium (Li) is essentially important for improving the energy‐density and cycle‐life of practical Li‐ion battery full‐cell, especially after employing high‐capacity but low initial coulombic efficiency anode candidates. Introducing prelithiation agent can provide additional Li source for such compensation. Herein, we precisely implant trace Co (extracted from transition metal oxide) into the Li site of Li2O, obtaining (Li0.66Co0.11□0.23)2O (CLO) cathode prelithiation agent. The synergistic formation of Li vacancies and Co‐derived catalysis efficiently enhance the inherent conductivity and weaken the Li−O interaction of Li2O, which facilitates its anionic oxidation to peroxo/superoxo species and gaseous O2, achieving 1642.7 mAh/g~Li2O prelithiation capacity (≈980 mAh/g for prelithiation agent). Coupled 6.5 wt % CLO‐based prelithiation agent with LiCoO2 cathode, substantial additional Li source stored within CLO is efficiently released to compensate the Li consumption on the SiO/C anode, achieving 270 Wh/kg pouch‐type full‐cell with 92 % capacity retention after 1000 cycles.


Implanting Transition Metal into Li2O‐Based Cathode Prelithiation Agent for High‐Energy‐Density and Long‐Life Li‐Ion Batteries

December 2023

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42 Reads

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3 Citations

Angewandte Chemie

Compensating the irreversible loss of limited active lithium (Li) is essentially important for improving the energy‐density and cycle‐life of practical Li‐ion battery full‐cell, especially after employing high‐capacity but low initial coulombic efficiency anode candidates. Introducing prelithiation agent can provide additional Li source for such compensation. Herein, we precisely implant trace Co (extracted from transition metal oxide) into the Li site of Li2O, obtaining (Li0.66Co0.11□0.23)2O (CLO) cathode prelithiation agent. The synergistic formation of Li vacancies and Co‐derived catalysis efficiently enhance the inherent conductivity and weaken the Li‐O interaction of Li2O, which facilitates its anionic oxidation to peroxo/superoxo species and gaseous O2, achieving 1642.7 mAh/g~Li2O prelithiation capacity (~980 mAh/g for prelithiation agent). Coupled 6.5 wt% CLO‐based prelithiation agent with LiCoO2 cathode, substantial additional Li source stored within CLO is efficiently released to compensate the Li consumption on the SiO/C anode, achieving 270 Wh/kg pouch‐type full‐cell with 92% capacity retention after 1000 cycles.


XRD patterns of a) LFP, b) LF0.5M0.5P, c) LF0.3M0.7P, d) NFP, e) NF0.7M0.3P, f) NF0.5M0.5P. Inset: the corresponding SEM images.
a) Galvanostatic charge–discharge profiles of LFP, LF0.5M0.5P, and LF0.3M0.7P cathodes at a current rate of 0.1 C (1 C = 170 mA g⁻¹). b) Rate performances of LFP, LF0.5M0.5P, and LF0.3M0.7P cathodes. c) Cycling performances of LFP, LF0.5M0.5P, and LF0.3M0.7P cathodes at 1 C. d) The initial cycle galvanostatic charge–discharge profiles of NFP, NF0.7M0.3P, and NF0.5M0.5P cathodes at a current rate of 0.1 C (charging under constant current‐constant voltage (CC–CV) chagre mode and 5 h holding at 4.5 V 1 C = 155 mA g⁻¹). e) Rate performances of NFP, NF0.7M0.3P, and NF0.5M0.5P cathodes. f) Cycling performances of NFP, NF0.7M0.3P, and NF0.5M0.5P cathodes at 1 C.
a) GITT potential curves and chemical diffusion coefficient [log(DLi⁺)] of LFP, and LF0.5M0.5P cathodes at the first cycle. b) GITT potential curves and chemical diffusion coefficient [log(DNa⁺)] of NFP, and NF0.7M0.3P cathodes at the first cycle. c) In situ XRD patterns of LFP and LF0.5M0.5P. The diffraction peaks of (002), (131), and (112) marked by blue or red dashed lines are attributed to LiFePO4 (LFP) and FePO4 (FP), respectively. d) Ex situ XRD patterns of NFP and NF0.7M0.3P in different voltages. The diffraction peaks marked by blue dashed lines (220), (121), and (131) are attributed to the NaFePO4.
a) Average output voltage, real specific capacity, and energy density for the LFP, LFMP, NFP, and NFMP cathodes. Herein, real capacity indicates that the specific capacity is normalized by the entire cathode mass, including inactive components (binder, carbon, and so on). Structural sketching diagrams of b) olivine‐type LiFe(Mn)PO4 and c) maricite‐type NaFe(Mn)PO4. The radar map covers five aspects for evaluating materials performance.
From Li to Na: Exploratory Analysis of Fe‐Based Phosphates Polyanion‐Type Cathode Materials by Mn Substitution

August 2023

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8 Citations

Both LiFePO4 (LFP) and NaFePO4 (NFP) are phosphate polyanion‐type cathode materials, which have received much attention due to their low cost and high theoretical capacity. Substitution of manganese (Mn) elements for LFP/NFP materials can improve the electrochemical properties, but the connection between local structural changes and electrochemical behaviors after Mn substitution is still not clear. This study not only achieves improvements in energy density of LFP and cyclic stability of NFP through Mn substitution, but also provides an in‐depth analysis of the structural evolutions induced by the substitution. Among them, the substitution of Mn enables LiFe0.5Mn0.5PO4 to achieve a high energy density of 535.3 Wh kg⁻¹, while NaFe0.7Mn0.3PO4 exhibits outstanding cyclability with 89.6% capacity retention after 250 cycles. Specifically, Mn substitution broadens the ion‐transport channels, improving the ion diffusion coefficient. Moreover, LiFe0.5Mn0.5PO4 maintains a more stable single‐phase transition during the charge/discharge process. The transition of NaFe0.7Mn0.3PO4 to the amorphous phase is avoided, which can maintain structural stability and achieve better electrochemical performance. With systematic analysis, this research provides valuable guidance for the subsequent design of high‐performance polyanion‐type cathodes.

Citations (2)


... 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. ...

Reference:

Interface Engineering of MOF Nanosheets for Accelerated Redox Kinetics in Lithium‐Sulfur Batteries
Lattice Engineering on Li 2 CO 3 ‐Based Sacrificial Cathode Pre‐lithiation Agent for Improving The Energy Density of Li‐Ion Battery Full‐Cell

... 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