Open Access Article
Dat Le Thanh
abc,
Claire Villevieille
d,
Romain Berthelot
*be and
Emmanuelle Suard
*a
aInstitut Laue-Langevin (ILL), 38042, Grenoble, France. E-mail: suard@ill.fr
bICGM, Université de Montpellier, CNRS, ENSCM, 34095, Montpellier, France. E-mail: romain.berthelot@umontpellier.fr
cAlistore-European Research Institute, CNRS FR 3104, 80039, Amiens, France
dUniv. Grenoble Alpes, Univ. Savoie Mont Blanc, CNRS, Grenoble INP, LEPMI, Grenoble, 38000, France
eRéseau sur le Stockage Électrochimique de l'Énergie (RS2E), CNRS, 80039, Amiens, France
First published on 6th March 2026
Neutron powder diffraction is a powerful method for probing structural changes and localizing and quantifying lithium in battery electrode materials, but acquiring high-quality patterns during operando type measurement remains challenging due to the need for both good electrochemistry and a large active material amount for an optimal signal-to-noise ratio. However, this technique is rarely applied during fast cycling of high-rate electrode materials despite the growing demands of high-power batteries. Herein, we benchmarked two cell designs for operando measurement, coin-type and cylindrical cells, on two different diffractometers (high-resolution and high-flux instruments) using high-rate Wadsley–Roth FeNb11O29 as a model electrode material. The coin-type cell provides an excellent signal-to-noise ratio and ease of assembly, yet it relies on deuterated electrolytes. In contrast, a cylindrical cell delivers reliable electrochemistry at fast cycling rates while still providing neutron diffraction data of sufficient quality for structural analysis even when using conventional organic electrolyte. The two diffractometers also exhibit complementary capability: the high-flux instrument enabled fast data acquisitions in only a few minutes, while the high-resolution one was successfully employed in in situ mode for the first time with clearer peak separation. These results validate the cylindrical cell as a promising setup for realistic, high-rate cycling, paving the way towards more accessible and cost-effective operando neutron studies in battery research.
Among different characterisation methods, neutron powder diffraction (NPD) is a powerful technique in battery research owing to several advantages presented hereafter. First, it is particularly sensitive to light elements (e.g. lithium and oxygen) and can distinguish neighbouring elements (e.g. nickel, manganese, and cobalt in layered oxides), thanks to the irregular variations in neutron scattering lengths across the periodic table. Besides, due to their weak interaction with atom nuclei, neutrons are non-destructive and exhibit penetration depths that are much larger than those of X-rays, allowing for the bulk analysis of entire electrodes or even full batteries. Additionally, neutron scattering lengths are independent of the scattering vector Q, providing strong signal intensity even in high Q regions for accurate determination of structural parameters such as site occupancies and Debye–Waller factors. These advantages have motivated the development of in situ and operando NPD over the past three decades to address its stringent experimental requirements. Reliable measurements require both homogeneous electrochemical reactions and a large amount of active material to achieve an adequate diffraction signal while minimizing parasitic scattering from other cell components. Lithium-ion batteries contain several elements problematic for NPD: metallic parts such as current collectors or casings contribute intense Bragg peaks, while natural lithium strongly absorbs neutrons. Additionally, conventional organic-based electrolytes and separators are usually rich in hydrogens, whose incoherent cross section far exceeds its coherent value (σinc = 80.27 barns vs. σcoh = 1.75 barns), resulting in a featureless background that substantially lowers the diffraction pattern's signal-to-noise ratio. Although this can be mitigated by using deuterated electrolytes and low-hydrogen materials, deuteration is costly. Furthermore, the flux of neutron sources is several orders of magnitude lower than that of X-ray facilities, and neutron scattering cross-sections are smaller, necessitating large sample quantity and long acquisition times for good counting statistics. Consequently, only a few neutron facilities worldwide currently provide the flux and resolution required for operando NPD investigations of battery materials.
The development of custom-designed electrochemical cells became essential for in situ and operando NPD experiments. The central challenge in such designs has always been balancing the two conflicting requirements: ensuring sufficient loading for proper neutron signals while maintaining good electrochemical performance. Since the first custom-made cells were introduced in 1998,7,8 several cell designs have been developed and can be divided into three main categories: coin-type, pouch-type, and cylindrical roll-over cells9–29 (Note S1 and Fig. S1).
Despite these advances, further progress is challenging due to the trade-off between data quality and electrochemical performance. Existing cylindrical cells are based on costly deuterated electrolytes and long acquisition times, while coin-type cells suffer from thick electrodes and slow kinetics. To overcome these challenges, in this work a custom-designed cylindrical cell was developed combining advantages of several features such as (i) a neutron transparent body based on a Ti–Zr alloy (∼Ti2.08Zr)30 used as a cell casing, (ii) a rolling approach ensuring high loaded electrodes, ideal for temporal resolution, and (iii) a double coated electrode ensuring good electrochemical performance even at fast cycling rates. Niobium-based oxide FeNb11O29 was chosen as a model electrode material to validate this cell configuration. Indeed, FeNb11O29 belongs to the family of Wadsley–Roth oxides, known to exhibit excellent rate capability, and is currently intensively investigated as a promising alternative to negative electrodes in future LIBs.31–43
In this work, we aim to benchmark complementary instruments and cell designs for in situ/operando NPD: (i) two diffractometers at the Institut Laue-Langevin (high-resolution D2B and high-flux D20) and (ii) two NPD cell designs, the reported coin-type cell and a newly developed cylindrical cell. Overall, this work explores three key opportunities: (i) extending the D2B diffractometer's capabilities to perform in situ experiments, (ii) enabling reliable electrochemical cell cycling at higher rates while collecting neutron diffraction patterns, and (iii) demonstrating the practicality of using standard electrolytes. The study begins by introducing the two cell designs and component choices, then compares their electrochemical performance and evaluates how each component contributes to NPD data and finally focuses on operando data analyses on both cells and diffractometers. Together, these objectives aim to identify the prospects and challenges for making in situ and operando NPD studies more accessible, cost-effective, and closer to routine application in battery research, while still retaining good electrochemical cycling and sufficient data quality.
For the coin-type cell, a self-standing electrode was prepared by grinding FeNb11O29, carbon super P (Alfa Aesar) and a poly(tetrafluoroethene) (PTFE, Sigma-Aldrich) binder in an 80
:
10
:
10 weight ratio, followed by pressing the mixture into a ∼1 mm thick pellet (∼400 mg in total, ∼127 mg cm−2).
For the cylindrical cell, a double-coated electrode on Cu foil with a high mass loading (∼20 mg cm−2) was prepared from FeNb11O29, carbon Super P (Alfa Aesar), and a PVDF binder (Solef® 5130) in a 90
:
5
:
5 weight ratio. Around 3 g of dry mixture was mixed, dispersed in ∼3.5 mL of N-methyl-2-pyrrolidone (NMP, Sigma-Aldrich, 99.5%) (∼45% dry mass), homogenized in a Kakuhunter planetary centrifugal mixer (SK-300SII) and then coated onto 20 µm Cu foil (Goodfellow) using a 0.4 mm doctor-blade gap. The coated foil was air-dried for 2 hours to prevent cracking and adhesion issues, followed by vacuum drying at 80 °C for 12 hours before coating the opposite side. The composite electrode was then calendared to a targeted porosity of ∼44% to optimize porosity and ensure uniform thickness and lastly cut to 5.5 × 20 cm. The total mass of active material FeN11O29 is estimated to be ∼4 g.
:
1 by volume, Solvionic).
The cylindrical cell was assembled as illustrated in Note S2 and Fig. S3. The double-coated FeN11O29 electrode was paired with Li foil supported on a Cu grid as the counter/reference electrode, separated by two layers of a Celgard separator. The complete stack (electrode/separator/Li/separator) was carefully and tightly rolled around the central Ti2.08Zr rod, ensuring proper alignment and no short-circuiting. Finally, 2 mL of conventional organic electrolyte (1 M LiPF6 in EC/DMC, 3
:
7 by volume) was uniformly added for complete wetting.
Constraints of the cells and research objectives governed the choice of electrolyte. Indeed, a deuterated electrolyte was used for the coin-type cell, to minimize incoherent scattering and ensure sufficient data quality despite low active material mass loading. Conversely, the cylindrical cell was filled with conventional electrolyte to demonstrate the feasibility of practical, cost-effective cycling conditions. Both electrolytes were reported to exhibit comparable electrochemical signatures and stability,21 supporting the comparability between the two designs.
For comparison, a CR2032 coin cell was assembled using a single-side coated FeNb11O29 electrode (∼20 mg cm−2), a lithium counter electrode, and a Whatman glass fibre separator impregnated with 0.1 mL of the same conventional organic electrolyte. The cell was cycled at a current rate of C/12 between 1.0 and 3.0 V vs. Li+/Li. The nominal specific capacity C is defined as one electron transfer per transition metal (Fe3+/2+ and Nb5+/4+ redox couples), corresponding to 12 Li+ per formula unit or ∼209 mA h g−1, although the subsequent reduction of Nb4+ to Nb3+ could result in extra capacity.31–43 Throughout the manuscript, all the potentials will be expressed vs. the Li metal counter electrode so vs. Li+/Li.
The cylindrical cell was tested using both D2B and D20 diffractometers (Fig. S4). NPD measurements were first performed on individual components of the cylindrical cell to assess their contributions: pristine FeNb11O29 powder, the electrode coated on Cu foil, and the assembled cell before and after electrolyte filling. These reference data were collected on both D2B and D20 instruments, with acquisition times of 2 h and 5 min, respectively.
On the D2B diffractometer, the first discharge of the cylindrical cell followed a sequence of 2 h at C/12 (1 Li+ per h, 17.38 mA g−1) and 6 h of rest for NPD acquisition. This sequence was repeated five times to reach specific LixFeNb11O29 compositions (x = 0, 2, 4, 6, 8, 10). The subsequent delithiation (charge) was performed outside the D2B diffractometer to restore the cell to its initial state before further measurements on the D20 diffractometer.
On the D20, NPD patterns were collected every 5 minutes throughout three discharge–charge cycles at C/12, C/6 and C/2 rates; during each 5-minute acquisition, these current values correspond to Li+ insertion/extraction rates of 1/12, 1/6 and 1/2 Li+ per FeNb11O29 formula unit, respectively. The first discharge process was conducted stepwise through 11 sequences, each comprising 1 h of discharge at a C/12 rate followed by 1 h of rest for long NPD acquisition of LixFeNb11O29 compositions (x = 0–11). At the end of the first discharge, the cell was charged at C/12 to the initial state. Then, two further cycles were conducted, each consisting of a galvanostatic cycling step at higher rates (C/6 and C/2), followed by a 30-minute constant-voltage hold at the end of discharge and charge to ensure complete reaction.
For Cu and Li, zero shift and cell parameters were refined for the first pattern in each series and subsequently fixed for all subsequent refinements. For lithiated FeNb11O29, the refined parameters included the lattice constants (a, b, c, and β), scale factor, and overall B factor; atomic positions and individual isotropic displacement parameters were not refined. Due to the structural complexity, with 12 crystallographic Li sites (Fig. S5 and Table S1) and the low Li content relative to other atoms, which is typical of Wadsley–Roth phases, localizing Li is challenging. This difficulty was reflected in the literature: while chemically lithiated phases have been analysed using NPD on high crystallinity powders,45 no NPD studies have been reported for electrochemically lithiated samples. Attempted refinement strategies, such as constraining Li to specific sites (only horizontal/vertical windows or pocket sites) or excluding it entirely, yielded negligible changes in cell parameters (<0.1%) and little improvement in fit quality. Therefore, a different approach was used: the Li amount of each lithiated composition is equally distributed over all 12 sites (equal Li site occupancies).
On the other hand, the cylindrical cell29 provides maximum data quality while providing long-term cycling capability (Fig. 1 and S3). The same “null-matrix” alloy was used for the cell body and central rod was used as a current collector. The cell body is a hollow cylinder that houses a “jelly-roll” electrode assembly. The central rod consists of two parts: (i) a longer rod in direct contact with the positive electrode foil and (ii) a shorter rod, connected to the negative electrode by a current tab; these two rods are separated by an insulating part made of polyetheretherketone (PEEK). Owing to its chemical stability and mechanical strength, PEEK is also used for the sealing caps, ensuring that the cell remains airtight.
Regarding cylindrical cell components, Celgard 2500 was selected as a separator due to its high tensile strength, resistance to tear and puncture, decent flexibility, and good ion transport properties. Despite its hydrogen content, which causes incoherent scattering, it remains the best compromise among tested materials (Celgard, PVDF, polyethylene, and PET/alumina composites).29 The current collector is copper mesh and foil, preferred over aluminium to avoid Li–Al alloying and minimize peak overlap with FeNb11O29. Pieces of lithium foil were flattened to low thickness (∼200 µm) to reduce neutron absorption and improve interfacial contact, lowering the cell resistance and easing the rolling process. A double-coated electrode with high mass loading was used to increase the diffraction statistics. A conventional organic electrolyte was employed instead of deuterated ones to reduce cost and evaluate whether high active-material loading could still yield acceptable data quality despite hydrogen background contributions.
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| Fig. 2 Voltage profiles (a) and differential capacity curves (b) of FeNb11O29/Li half-cells in three different setups. | ||
First, at the same current rate and comparable mass loading, the cylindrical and coin cells exhibit similar charge–discharge profiles with characteristic sloping features, consistent with dQ/dV peaks at ∼2.4 V, 1.65 V, and 1.3 V, corresponding to Fe3+/2+, Nb5+/4+ and Nb4+/3+ redox couples, respectively.31–43 The cylindrical cell enables reversible cycling and delivers a capacity corresponding to ∼12 Li+ per formula unit (f.u.), lower than that of the coin cell (∼15 Li+ per f.u.). Its voltage profiles show higher polarisation and weaker dQ/dV peaks than the coin-cell reference, which could arise from local inhomogeneities at the rolled edges, slight variations in lithium thickness, and an imperfect compaction of the outermost layers of the jelly roll—effects that are difficult to eliminate completely by manual rolling. Despite these limitations, the cylindrical cell still exhibits modest polarisation (∼200 mV) and low internal resistance (∼1 Ω, Fig. S6). Increasing the rate to C/6 only led to a slight rise in polarisation and a minor capacity decrease, with approximately ∼10 Li+ exchanged (Fig. S7). Even at C/2, despite more pronounced polarization, the cell still accommodated ∼8 Li+, highlighting its impressive ability to endure high current while obtaining decent specific capacity. This electrochemical stability was still retained during prolonged cycling (Fig. S7). By contrast, the coin-type cell exhibits markedly poorer behaviour even at a much slower C/36 rate: a lower capacity of ∼10 Li+, large internal resistance (≈30–50 Ω), and subsequent voltage instability. These features could be due to unstable contact, electrolyte decomposition and parasitic reactions in the thick self-standing electrode.
For FeNb11O29 electrodes on copper foil (Fig. 3), the Cu reflections dominate the diffractograms regardless of the mass loading. However, with a loading of 20 mg cm−2, the Bragg reflections of FeNb11O29 are significantly strong, comparable in intensity to that of the reference powder at both D2B and D20 beamlines, retaining well-defined peaks up to high Q. This demonstrates the critical role of mass loading in enhancing the signal-to-noise ratio of the active phase. At the D20 beamline, this high loading even allows fast data acquisitions in only five minutes (Fig. S8).
When the full stack (positive, negative, current collectors and separators) is placed inside the cylindrical cell without electrolyte, peak intensity and resolution of FeNb11O29 Bragg reflections decreased significantly, which could be due to incoherent scattering from the Celgard separator and strong absorption by the lithium foil. The influence of Celgard is clear in the diffractogram measured using D20, where it produces significant background signals. After electrolyte filling, the signal-to-noise ratio is slightly further worsened, since the peaks become less defined. Nevertheless, after careful background subtraction, the data quality remains sufficiently good for Rietveld refinement (Fig. S9 and Table S2), by including three phases, FeNb11O29, Cu and Li.
These findings indicate that the conventional non-deuterated electrolyte is not the primary factor that decreases data quality; rather, the dominant contributions come from other cell components, notably the Celgard separator and the lithium foil. Importantly, a sufficiently high material mass—achieved by high areal loading on thin films—can compensate for these penalties and provide diffractograms of sufficient quality for structural analysis.
Operando NPD of the cylindrical cell on the D20 reveals the structural changes of FeNb11O29 at three current rates, together with the electrochemical profiles (Fig. 5). During the initial C/12 discharge, continuous and progressive peak shifts are observed for many reflections, such as (011), (206), (020) and (420), indicating gradual lattice evolution as lithiation proceeds from x = 0 to x = 11. During the subsequent charge, the Bragg reflections shift back reversibly, with nearly all lithium extracted, and the structure returns close to its initial state. At higher rates (C/6 and C/2), this smooth peak shift behaviour is also seen, even though each five-minute acquisition corresponds to larger composition changes, making the patterns slightly less well-defined. Across three cycles, the absence of peak splitting or additional reflections is consistent with a single-phase, solid-solution mechanism. Besides, this demonstrates the robust structural reversibility of FeNb11O29 at fast cycling, which was also previously reported.37,42 Overall, these results highlight the excellent capability of the cylindrical cell to support time-resolved measurements at high currents with good capacity retention.
Comparative analyses of operando NPD data obtained using cylindrical and coin-type cells help clarify the effect of cell designs on electrochemistry and diffraction data. Overall, the NPD patterns of each LixFeNb11O29 composition collected in two cells exhibit comparable peak positions for most reflections, indicating similar structural transitions and the reliability of the cells (Fig. 6). However, differences could still be observed. For the cylindrical cell cycled at C/12, the contour plots exhibit clear, progressive peak shifts on discharge and a reversible evolution on charge, which are especially evident for the (0 1 1), (0 2 0), (4 2 0), (4 2 10), and (7 4 0) Bragg reflections (Fig. 5a), similar to the gradual and reversible peak evolutions in Fig. 6a. The slightly enhanced signal-to-noise ratio at C/6 may come from improved structural homogeneity after the initial C/12 cycle or reduced background scattering due to gravity-induced electrolyte movement in the vertically positioned cell. At C/2, rapid peak shifts during 5-minute acquisition broaden and weaken diffraction signals, lowering the resolution.
By contrast, analogous features are less evident for the coin-type cell cycled at C/36, both in the stacked patterns and in the contour plot (Fig. 6 and S10). First, while the peaks still evolve progressively during discharge, this behaviour becomes weaker or discontinuous at the end of charge, e.g. (0 2 0) reflection showing almost no shift and only a gradual, incomplete recovery of intensity. Additionally, the peak shape and intensity of (
0 10) and (7 0 0) reflections remain nearly unchanged at the end of charge, indicating that the lithiated phase cannot be fully delithiated. After cycling, all reflections exhibit a clear decrease in intensity accompanied by a broadening of their full width at half maximum (FWHM, 2θ in degrees), which suggests the presence of several local lithiation states in the electrode. This could likely arise from the thick self-standing electrode, resulting in inhomogeneous electrochemical reactions and a lithium gradient within the electrode volume. This gradient in the lithiation degree, simplified as Li-rich and Li-poor contribution (Fig. 7), could reasonably explain the above observations: subtle peak evolution, incomplete intensity recovery and broadened FWHM at the end of charge. This interpretation is further supported by the contour plots (Fig. S10), where the shifts of some high-angle Bragg reflections, e.g. (
1 5) and (7 4 0), while unambiguously observed for the cylindrical cell, are absent for the coin-type cell. These results highlight the impact of electrode configuration on data quality, with the cylindrical cell providing more homogeneous electrochemical reactions and, consequently, clearer structural evolution.
Besides the qualitative evaluation, further quantitative analyses allow the comparison of FeNb11O29 cell parameter evolution during operando NPD experiments in different setups (Fig. 7). For the cylindrical configuration, the cell parameters follow similar trends at the three applied current rates, with comparable standard uncertainties. This indicates that the structural changes of FeNb11O29 during lithiation and delithiation are largely independent of kinetics and demonstrated the excellent ability of the cell to sustain electrochemical reversibility at high currents. Compared with the reference data obtained from NPD in coin-type cells, the evolution trends were preserved, even though there were some discrepancies between the two setups. Such differences may come from experimental conditions, including electrode formulation, cycling rate, and, most critically, mass loading and electrode thickness (∼0.2 mm for the cylindrical cell versus ∼1 mm for the coin-type cell). Thicker electrodes are more likely to cause inhomogeneous lithium insertion/extraction across the electrode depth, which may take more time to homogenize and lead to the lattice parameter differences in the two cells. Despite these discrepancies, the general agreement across the three datasets highlights the reliability of cylindrical cells for operando neutron diffraction studies.
Finally, post-cycling analyses were conducted to probe the spatial homogeneity of the cylindrical cell. Vertical NPD scans on the D20 diffractometer using a 1 cm slit at several positions along the electrode height show the characteristic FeNb11O29 reflections at the same 2θ positions across all sections (Fig. S11). The signal-to-noise ratio is lower due to the reduced probed volume, but no shift or broadening indicative of a vertical gradient is observed. Complementary XRD measurements were performed on punched electrodes from different radial and axial positions of the rolled electrode, revealing nearly identical peak positions and only minor fluctuations in refined lattice parameters (Fig. S12). Overall, these results confirm that the jelly roll built from thin, double-coated layers provides uniform contact and pressure, enabling homogeneous reactions throughout the cell.
Coin-type cells are suitable for preliminary investigations, particularly when material availability is limited and fast-charging conditions are not required. Their hydrogen-free components ensure excellent signal-to-noise ratios. They allow the use of self-standing electrodes and small volumes of deuterated electrolytes, which minimizes background scattering and avoids peak overlap, further enhancing diffraction pattern quality. However, thick electrodes can introduce inhomogeneities, high resistance, polarization, and a limited cycling rate. Regarding practicability, their simple assembly facilitates troubleshooting during beamtime, making them a pragmatic choice for foundational studies before more extensive studies using cylindrical cells, if necessary.
Cylindrical cells, on the other hand, are better suited for high-rate cycling studies (e.g., fast-charging materials or kinetic effects on structural evolutions) and cost-effective experiments, as they allow the use of conventional organic electrolytes. This configuration closely mimics that of commercial large-format cells (e.g., 18650), providing realistic operating conditions for upscaling and commercialization studies. While cylindrical cells introduce additional background contributions, careful background subtraction ensures data quality sufficient for structural refinements. Their ability to accommodate double-coated thin films enables (i) sufficient counting statistics, (ii) homogeneous electrochemistry, and (iii) rapid NPD acquisitions (as fast as 5 minutes) and cycling rates up to C/2. These advantages were reflected in this work, where the operando results confirmed the solid-solution mechanism of FeNb11O29 as previously reported, while also demonstrating structural reversibility even at high-rate cycling, rate-induced peak broadening, and challenges associated with Li localization and occupancies in the Wadsley–Roth family.
Looking forward, these findings open perspectives for performing operando neutron powder diffraction, a more accessible and routine tool in battery research. The cylindrical cell represents a promising tool for balancing realistic electrochemistry with sufficiently good data quality, especially for investigating high-rate electrode materials by NPD. The cell design could be further optimized by reducing parasitic scattering and absorption—for example, using thinner lithium foil, alternative separators with reduced background, alternative neutron-transparent current collectors (V or a Ti2.08Zr alloy), partially deuterated electrolyte, or highly crystalline active materials. While each of these strategies can improve data quality, their combined effects on the overall signal-to-noise ratio require further investigation to reach a compromise between applicability and data quality, as these effects depend on the interplay of all cell components. For example, even slight reductions in lithium foil thickness can significantly mitigate neutron absorption, but the overall improvement is affected by the separator, current collector, and electrolyte. Besides, using enriched 7Li foil could theoretically be a strategy to reduce neutron absorption, but its implementation is challenging due to negligible improvement in coherent scattering compared with the 6Li isotope, its high cost, no commercial availability, and the need for extensive validation with 7Li-enriched electrolyte. On the instrumentation side, the combined use of the D2B and D20 diffractometers can offer both high-resolution structural details and time-resolved insights, providing comprehensive information on electrochemical reactions.
Supplementary information is available. See DOI: https://doi.org/10.1039/d5ta10422j.
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