energy storage materials34293...h.q. pham, m. mirolo and m. tarik et al. energy storage materials 33...

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Energy Storage Materials 33 (2020) 216–229 Contents lists available at ScienceDirect Energy Storage Materials journal homepage: www.elsevier.com/locate/ensm Multifunctional electrolyte additive for improved interfacial stability in Ni-rich layered oxide full-cells Hieu Quang Pham a , Marta Mirolo a,b , Mohamed Tarik c , Mario El Kazzi a , Sigita Trabesinger a,a Electrochemistry Laboratory, Paul Scherrer Institute, Forschungsstrasse 111, 5232 Villigen PSI, Switzerland b Swiss Light Source, Paul Scherrer Institute, Forschungsstrasse 111, 5232 Villigen PSI, Switzerland c Bioenergy and Catalysis Laboratory, Paul Scherrer Institute, Forschungsstrasse 111, 5232 Villigen PSI, Switzerland a r t i c l e i n f o Keywords: Electrolyte additive Ni-rich NCM Voltage fade Electrode–electrolyte interface SEI Li-ion battery a b s t r a c t Improving the interfacial stability between the electrode and the electrolyte at high voltage is a key to success- fully obtain high energy-density Li-ion batteries. Therefore, this study is dedicated to a novel multifunctional electrolyte additive, methoxytriethyleneoxypropyltrimethoxysilane (MTE-TMS), able to stabilize the interface of both Ni-rich layered LiNi 0.85 Co 0.1 Mn 0.05 O 2 (NCM851005) cathode and graphite anode in a full-cell. Electrochem- ical tests reveal that the addition of 1 wt% MTE-TMS significantly improves the long-term cycling stability of the graphite‖NCM851005 full-cell, with an achieved maximum capacity of 198 mAh g 1 and its excellent capacity retention of 84% after 100 cycles at C/5 using upper voltage cut-off of 4.3 V vs Li + /Li. In contrast, the standard electrolyte in absence of MTE-TMS leads to a rapid performance fade. The significantly improved electrochemical performance is attributed to the formation of a stable surface protective film at both the cathode and the anode surfaces upon long-term cycling in elevated voltage window, and thus suppressing the electrolyte decomposition at and structural degradation of both cathode and anode, resulting as well in reduced transition metal transfer between the two electrodes. 1. Introduction Lithium-ion batteries (LIBs) are widely used for portable devices, electrical vehicles, large-scale energy storage systems, and are subject to ongoing modifications to meet the growing demands for higher energy and power densities [1,2]. In recent years, nickel-rich layered oxides (LiNi x Mn y Co z O 2 , x 0.6, x + y + z = 1, Ni-rich NCMs) [3], which are cheaper and contain significantly less of toxic cobalt, offer a higher specific capacity (180 mAh g 1 ) with an average voltage of 3.8 V vs Li + /Li [4], as compared to traditional LiCoO 2 (145 mAh g 1 ) and spinel- LiMn 2 O 4 (120 mAh g 1 ) [5]. However, large-scale application of Ni-rich NCM cathodes is hindered by severe capacity fading during long-term cycling, which is mainly caused by the instability of the Ni-rich NCM cathode–electrolyte interface at high-voltage (above 4.2 V vs Li + /Li), utilization of which would lead to higher energy densities [6–10]. The highly oxidized state of Ni 4+ , formed upon Li + -deintercalation, is spon- taneously reduced to Ni 3+ and Ni 2+ by accepting electrons from the electrolyte, causing severe oxidative decomposition of the electrolyte at the cathodeelectrolyte interface [6–8,10]. This leads to the formation of nucleophilic fluoride (F ) species, which in turn can corrode the tran- sition metals from Ni-rich NCM, causing the structure deterioration of Corresponding author. E-mail addresses: [email protected] (H.Q. Pham), [email protected] (S. Trabesinger). cathode materials [11], when the standard LiPF 6 salt is used. In addition, the similar radius of Li + (0.76 Å) to Ni 2+ (0.69 Å) leads to the intermix- ing of Ni and Li layers, which results in the well-known phase transition from layered hexagonal structure (R 3m) to spinel (Fd 3m) and to cu- bic rock-salt (Fm 3m), causing oxygen release and safety issues [8,12]. This electrochemically inactive rock-salt phase hinders the Li + diffu- sion at the cathode–electrolyte interface, thus resulting in capacity fad- ing. Additionally, crack formation, induced by internal stress in the sec- ondary particles upon repeated Li + -(de)intercalation, provides new sites for the cathode–electrolyte interface reactions, accelerating layered-to- rock-salt phase transition, causing voltage fade [13]. Thus, the protec- tion of the Ni-rich NCMs surface is a key to inhibit their structural deteri- oration, voltage fade, and achieve stable long-term performance. Effec- tive methods to overcome the instability of the interface for the Ni-rich NCM cathodes are surface coating, bulk doping, and electrolyte addi- tives. The surface coating layers, such as metal oxides [14–16] and metal fluorides [17,18], could prevent side reactions by avoiding the exposure of the Ni-rich NCM to the electrolyte, however, they hinder the Li + diffu- sion due to their poor Li + conductivity. Bulk doping [19–21] can reduce Li + /Ni 2+ cation intermixing, stabilizing the layered structure, and block- ing the generation of grain boundary cracks in secondary particles, but https://doi.org/10.1016/j.ensm.2020.08.026 Received 27 July 2020; Received in revised form 17 August 2020; Accepted 25 August 2020 Available online 30 August 2020 2405-8297/© 2020 The Authors. Published by Elsevier B.V. This is an open access article under the CC BY license. (http://creativecommons.org/licenses/by/4.0/)

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Page 1: Energy Storage Materials34293...H.Q. Pham, M. Mirolo and M. Tarik et al. Energy Storage Materials 33 (2020) 216–229 the decomposition of the electrolyte at higher voltage cannot

Energy Storage Materials 33 (2020) 216–229

Contents lists available at ScienceDirect

Energy Storage Materials

journal homepage: www.elsevier.com/locate/ensm

Multifunctional electrolyte additive for improved interfacial stability in

Ni-rich layered oxide full-cells

Hieu Quang Pham

a , Marta Mirolo

a , b , Mohamed Tarik

c , Mario El Kazzi a , Sigita Trabesinger a , ∗

a Electrochemistry Laboratory, Paul Scherrer Institute, Forschungsstrasse 111, 5232 Villigen PSI, Switzerland b Swiss Light Source, Paul Scherrer Institute, Forschungsstrasse 111, 5232 Villigen PSI, Switzerland c Bioenergy and Catalysis Laboratory, Paul Scherrer Institute, Forschungsstrasse 111, 5232 Villigen PSI, Switzerland

a r t i c l e i n f o

Keywords:

Electrolyte additive Ni-rich NCM

Voltage fade Electrode–electrolyte interface SEI Li-ion battery

a b s t r a c t

Improving the interfacial stability between the electrode and the electrolyte at high voltage is a key to success- fully obtain high energy-density Li-ion batteries. Therefore, this study is dedicated to a novel multifunctional electrolyte additive, methoxytriethyleneoxypropyltrimethoxysilane (MTE-TMS), able to stabilize the interface of both Ni-rich layered LiNi 0.85 Co 0.1 Mn 0.05 O 2 (NCM851005) cathode and graphite anode in a full-cell. Electrochem- ical tests reveal that the addition of 1 wt% MTE-TMS significantly improves the long-term cycling stability of the graphite ‖NCM851005 full-cell, with an achieved maximum capacity of 198 mAh g − 1 and its excellent capacity retention of 84% after 100 cycles at C/5 using upper voltage cut-off of 4.3 V vs Li + /Li. In contrast, the standard electrolyte in absence of MTE-TMS leads to a rapid performance fade. The significantly improved electrochemical performance is attributed to the formation of a stable surface protective film at both the cathode and the anode surfaces upon long-term cycling in elevated voltage window, and thus suppressing the electrolyte decomposition at and structural degradation of both cathode and anode, resulting as well in reduced transition metal transfer between the two electrodes.

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. Introduction

Lithium-ion batteries (LIBs) are widely used for portable devices,lectrical vehicles, large-scale energy storage systems, and are subject tongoing modifications to meet the growing demands for higher energynd power densities [ 1 , 2 ]. In recent years, nickel-rich layered oxidesLiNi x Mn y Co z O 2 , x ≥ 0.6, x + y + z = 1, Ni-rich NCMs) [3] , whichre cheaper and contain significantly less of toxic cobalt, offer a higherpecific capacity ( ≥ 180 mAh g − 1 ) with an average voltage of ≈3.8 V vsi + /Li [4] , as compared to traditional LiCoO 2 (145 mAh g − 1 ) and spinel-iMn 2 O 4 (120 mAh g − 1 ) [5] . However, large-scale application of Ni-richCM cathodes is hindered by severe capacity fading during long-termycling, which is mainly caused by the instability of the Ni-rich NCMathode–electrolyte interface at high-voltage (above 4.2 V vs Li + /Li),tilization of which would lead to higher energy densities [6–10] . Theighly oxidized state of Ni 4 + , formed upon Li + -deintercalation, is spon-aneously reduced to Ni 3 + and Ni 2 + by accepting electrons from thelectrolyte, causing severe oxidative decomposition of the electrolyte athe cathode − electrolyte interface [ 6–8 , 10 ]. This leads to the formationf nucleophilic fluoride (F − ) species, which in turn can corrode the tran-ition metals from Ni-rich NCM, causing the structure deterioration of

∗ Corresponding author. E-mail addresses: [email protected] (H.Q. Pham), [email protected] (S.

ttps://doi.org/10.1016/j.ensm.2020.08.026 eceived 27 July 2020; Received in revised form 17 August 2020; Accepted 25 Auguvailable online 30 August 2020 405-8297/© 2020 The Authors. Published by Elsevier B.V. This is an open access ar

athode materials [11] , when the standard LiPF 6 salt is used. In addition,he similar radius of Li + (0.76 Å) to Ni 2 + (0.69 Å) leads to the intermix-ng of Ni and Li layers, which results in the well-known phase transitionrom layered hexagonal structure (R ̄3 m) to spinel (Fd ̄3 m) and to cu-ic rock-salt (Fm ̄3 m), causing oxygen release and safety issues [ 8 , 12 ].his electrochemically inactive rock-salt phase hinders the Li + diffu-ion at the cathode–electrolyte interface, thus resulting in capacity fad-ng. Additionally, crack formation, induced by internal stress in the sec-ndary particles upon repeated Li + -(de)intercalation, provides new sitesor the cathode–electrolyte interface reactions, accelerating layered-to-ock-salt phase transition, causing voltage fade [13] . Thus, the protec-ion of the Ni-rich NCMs surface is a key to inhibit their structural deteri-ration, voltage fade, and achieve stable long-term performance. Effec-ive methods to overcome the instability of the interface for the Ni-richCM cathodes are surface coating, bulk doping, and electrolyte addi-

ives. The surface coating layers, such as metal oxides [14–16] and metaluorides [ 17 , 18 ], could prevent side reactions by avoiding the exposuref the Ni-rich NCM to the electrolyte, however, they hinder the Li + diffu-ion due to their poor Li + conductivity. Bulk doping [19–21] can reducei + /Ni 2 + cation intermixing, stabilizing the layered structure, and block-ng the generation of grain boundary cracks in secondary particles, but

Trabesinger).

st 2020

ticle under the CC BY license. ( http://creativecommons.org/licenses/by/4.0/ )

Page 2: Energy Storage Materials34293...H.Q. Pham, M. Mirolo and M. Tarik et al. Energy Storage Materials 33 (2020) 216–229 the decomposition of the electrolyte at higher voltage cannot

H.Q. Pham, M. Mirolo and M. Tarik et al. Energy Storage Materials 33 (2020) 216–229

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he decomposition of the electrolyte at higher voltage cannot be avoidedsing this strategy. In contrast, using electrolyte additives is a versatile,asy, and economical approach to mitigate these issues [ 6–8 , 11 , 22 ].

Recently, several kinds of electrolyte additives, such as borates [23] ,hosphates [24] , sulfonates [25] , nitriles [26] , and fluorides [27] , haveeen reported in the literature for improving stability and performancef Ni-rich NCM cathodes. The Si-based electrolyte additives have re-ently received substantial attention as effective functional additivesor Ni-rich NCM cathodes [ 11 , 22 , 28 ]. Deng et al. [28] demonstratedhat the addition of 1 wt% diphenyldimethoxysilane (DPDMS) could im-rove cycling performance of Li ‖LiNi 0.6 Co 0.2 Mn 0.2 O 2 (NCM622) half-ells, as the siloxane structure provides active sites (Si − O) to re-ove HF from the electrolyte by affinity, and can, therefore, preventetal-dissolution from NCM622 cathode. Wang et al. [22] proposed 3-

socyanatopropyltriethoxysilane (IPTS) as a high-voltage electrolyte ad-itive to improve Li ‖NCM622 half-cell, finding that the − NCO group,nd its derivatives, could form a stable and uniform surface film athe cathode–electrolyte interface. Jang et al. [11] reported that theilyl functional group, embedded in the organic additive of dimethoxy-imethylsilane (DODSi), improves the surface stability of NCM811 via chemical HF scavenging, owing to the matched chemical reactivity ofi with F – and O with H

+ . Although these Si-based oxidative additivesnhibit surface degradation of Ni-rich NCM cathodes, they are mostlyested in the half-cell configurations without investigating their abilityo reduce crack-formation and voltage fade of Ni-rich NCMs. Moreover,nterface reaction mechanisms, causing performance degradation or im-rovements in full-cells, were not studied, including their effect on theerformance of graphite anode.

In this work we present a novel multifunctional additive, methoxytri-thyleneoxypropyltrimethoxysilane (MTE-TMS), possessing a uniqueunctionality to simultaneously protect both Ni-rich NCM and graphitelectrode surfaces. MTE-TMS improves the long-term cycling stabilityot only of individual half-cells of graphite and Ni-rich NCM but also ofhe full graphite ‖Ni-rich NCM cell. In this study we clarify MTE-TMS ac-ion mechanism on the interfacial stabilization and its correlation withhe enhanced long-term cycling performance.

. Materials and methods

.1. Additive characterization

DFT calculations of the highest unoccupied molecular orbitalHOMO) and lowest unoccupied molecular orbital (LUMO) were per-ormed with the Gaussian 09 software package with a basis set of3LYP/6–311 + (3df, 2p) [22] . Linear sweep voltammetry (LSV) wasonducted to evaluate the anodic stability of electrolytes at a scan ratef 1 mV s − 1 from open-circuit voltage (OCV) of ≈3.0 to 6.0 V vs Li + /Li,ith glassy carbon (Ø = 14 mm) as a working electrode, and lithiumetal as the counter/reference electrode.

.2. Electrode preparation

The cathode was made of 93 wt% LiNi 0.85 Co 0.1 Mn 0.05 O 2 NCM851005, BASF Gemany), 1.5 wt% carbon black SC65 (Imerysraphite and Carbon, Switzerland), 2.5 wt% graphite SFG6L (Imerysraphite and Carbon, Switzerland) and 3 wt% polyvinylidene fluorideinder (PVDF5130, Solvay) suspended in an N-methyl-2-pyrrolidoneNMP, Sigma Aldrich) solvent and cast onto aluminum foil. For full-cellssembly, commercial graphite anode on a copper foil was composedf 95.7 wt% graphite active material (Hitachi), 0.5 wt% carbon blackC65 (Imerys Graphite & Carbon, Switzerland) and 3.8 wt% bindersodium carboxymethyl cellulose (CMC) mixed with styrene butadieneubber (SBR)). The NMP was evaporated under vacuum at 80 °C for 8 h,nd circular electrodes were punched out (Ø = 13 mm for NCM851005

217

nd Ø = 14 mm for graphite) and dried overnight at 120 °C in vacuumn order to remove remaining NMP and absorbed water, before intro-ucing electrodes into an argon-filled glove box. Average active massoading of NCM851005 was ≈8.9 mg cm

− 2 in Li ‖NCM851005 half-cellsnd ≈12.3 mg cm

− 2 in graphite ‖NCM851005 full-cells, respectively.he loading mass of graphite was ≈9.0 mg cm

− 2 . The capacity ratio ofraphite anode to NCM851005 cathode was adjusted to ≈1.1.

.3. Electrochemical performance

Coin-type electrochemical half-cells (PSI standard cells) [29] con-isting of NCM851005 cathode as a working electrode, Li metal foil0.75 mm thick, Alfa Aesar, United States) as a counter electrode, sep-rator (Celgard 2400), and 500 μl standard electrolyte of 1 M LiPF 6 inthylene carbonate (EC):diethyl carbonate (DEC), 3:7 by weight (LP47,ASF SE) without and with an optimal amount of 1 wt% methoxytri-thyleneoxypropyltrimethoxysilane (MTE-TMS, Fluorochem, Ltd., UK)ere assembled in an argon-filled glove box, with water and oxygen

ontent less than 1 ppm. The cyclic voltammetry (CV) measurementsere carried out using an electrochemical workstation (VMP3, BioLogiccience Instruments) at a scanning rate of 0.05 mV s − 1 , and the volt-ge ranges for the Li ‖NCM851005 and the Li ‖graphite half-cells were.0–4.3 V and 0.05–3.0 V vs Li + /Li, respectively. Cells were as wellalvanostatically cycled between 3.0 and 4.3 V at C/5 (42 mA g –1 )ate after two formation cycles at slower C/10 (21 mA g –1 ) using anrbin battery cycler. The AC impedance spectra were recorded duringycling in the frequency range of 10 mHz–100 kHz with an amplitudef 10 mV, using an impedance spectroscopic analyzer (VMP3, BioLogiccience Instruments), after a potentiostatic step of 5 h for equilibration.he impedance spectra were fitted with the use of the Z-View equivalentircuit modeling software. The GITT was used with a constant-currentf C/10 for 10 min, followed by 3 h open-circuit relaxation between 3.0nd 4.3 V. The Li ‖graphite half-cells were cycled between 0.05 and 1.5 Vith initial cycle at C/20 and subsequent cycles at 0.2 C (1 C = 372 mA

− 1 ). Coin-type electrochemical full-cells (PSI standard cells) [29] , consist-

ng of NCM851005 cathode, graphite anode, separator (Celgard 2400)nd standard electrolyte without and with an optimal amount of 1t% MTE-TMS additive, were assembled in an argon-filled glove box.heir charge-discharge cycling performance was tested between 3.0 and.25 V (corresponding to 4.3 V vs Li + /Li) at C/5 (42 mA g − 1 ) afterwo formation cycles at C/10 (21 mA g − 1 ), using an Arbin battery cy-ler. All the electrochemical tests were carried out at room temperature.or additional experiment, determining our additive’s effectiveness inull-cells, the graphite anodes were pre-lithiated. For pre-lithiation theraphite anodes were assembled to the half-cells with metallic Li andharged to 0.05 V vs Li + /Li. Then these graphite anodes were washedn electrolyte and assembled into the full-cells with pristine NMC851005athodes.

.4. Chemical and physical characterization

For differential scanning calorimetry (DSC) tests, the Li ‖NCM851005alf-cells were fully charged to 4.3 V at C/10. Then, the cells were dis-ssembled, and the cathode materials were scraped from the electrodes,etting about 2–5 mg of powders. The powders were sealed in a high-ressure DSC sample pan. The DSC tests were performed on the Perkin-lmer DSC 8000 in the range from 30 to 300 °C with a heating rate of °C min − 1 .

Electrolyte-dependent crack formation for NCM851005 cathodesuring cycling was examined using cross-sectional SEM. Cross-sectionamples of pristine and cycled cathodes were prepared using a Hitachion Mill IM4000 at an acceleration voltage of 4 kV and an ion currentf 120 𝜇A. The milling time was 7 h. The cathodes were transferred to acanning electron microscope (SEM, Zeiss Gemini) and imaged with an

Page 3: Energy Storage Materials34293...H.Q. Pham, M. Mirolo and M. Tarik et al. Energy Storage Materials 33 (2020) 216–229 the decomposition of the electrolyte at higher voltage cannot

H.Q. Pham, M. Mirolo and M. Tarik et al. Energy Storage Materials 33 (2020) 216–229

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cceleration voltage of 10 kV (in-lens and secondary electron detectors).orphology changes on the cathodes and anodes surface were imaged

sing SEM (Zeiss Gemini) at 10 kV. The thickness and uniformity of sur-ace film formed on the cathodes with cycling in different electrolytesere studied using transmission electron microscopy (TEM, FEI Tecnai2) at 120 kV. Cycled cathode active materials were scraped off thelectrodes (cycled in the full-cells) and dispersed in DMC before beingransferred onto a lacey-carbon-supported Cu grid. Structural data forCM851005 cathode after cycling were obtained ex situ by XRD analy-

is, by comparing the patterns of pristine and cycled NCM851005 cath-des. Pristine and cycled NCM851005 active materials were removedrom the pristine and cycled electrodes, and filled into a capillaries withn outside diameter of 0.5 mm with 0.01 mm wall thickness. The capil-aries were then sealed with wax inside an argon-filled glove box. X-rayowder diffraction measurements were performed in the 2 𝜃 range of 10–0° at a scan rate of 1° min − 1 at 45 kV and 40 mA, using a PANalyticalmpyrean diffractometer, equipped with a linear detector (X’Celerator)nd using Cu − K 𝛼 radiation ( 𝜆= 1.5418 Å). Local structural changes inraphite anode material after cycling were investigated, using a Ramanicroscope (Labram HR800, Horiba-Jobin Yvon, Japan), equipped with He–Ne laser (632.8 nm) at 2 mW. A typical spectrum was recorded inhe range of 1000–1800 cm

–1 using a 50 × objective (ULWDMS Plan 50,A = 0.55, Olympus, Japan), accumulating 3 scans with an acquisition

ime of 20 s per scan. The chemical analysis of leached Ni, Co and Mn amounts on anode

as performed on inductively coupled plasma optical emission spec-rometry (ICP-OES, Spectro Arcos). The ICP-OES samples were preparedith the following procedures: cycled graphite anodes were first washedith DMC for three times, then graphite active material was carefully

craped out from the cycled graphite anodes and dissolved into 0.6 mLCl (30%). The resulting transparent solution was subsequently dilutedith milliQ water before being subjected to ICP-OES analyses.

The surface of NCM851005 and graphite were analyzed by ex situPS, using ESCALAB 220iXL spectrometer (Thermo Fisher Scientific)ith focused monochromatized Al K 𝛼 radiation (h 𝜈 = 1486.6 eV). High

esolution spectra were obtained at a power of 150 W under a baseressure of 2 × 10 − 9 mbar. The electrodes, cycled in the full-cells, wereashed with DMC for the removal of residual electrolyte salt, followedy drying in the glove box at room temperature. They were transferredrom the glove box to the XPS chamber without exposure to the air by us-ng a vacuum-sealed transfer holder. The beam size was about 500 μm

2

nd the pass energy was 30 eV. Binding energy was corrected based onhe C-C bond in the C 1s level at 285 eV. Curve-fitting were conductedn the peaks with Gaussian (20%) and Lorentzian (80%) functions usingPSPEAK 4.1 program, till the goodness of fit is minimized, after hav-

ng Shirley-type background correction. The full width half maximumFWHM) of each component in one spectrum was set to be ± 0.2 eV ashe same.

. Result and discussion

.1. Oxidation and reduction behaviors of MTE-TMS

The oxidation and reduction behavior of MTE-TMS can be predictedy calculating the energy levels of the highest occupied molecular or-ital (HOMO) and of the lowest unoccupied molecular orbital (LUMO).he calculation results show that the HOMO energy level of MTE-TMS

s higher than those of EC and DEC solvents ( Fig. 1 a), indicating MTE-MS can be oxidized on the cathode before the solvents of the standardlectrolyte. These calculations are in good agreement with the resultsbtained from linear sweep voltammograms (LSV) shown in Fig. 1 b,erformed using glassy carbon as a working electrode. The electrolyteith MTE-TMS is preferentially oxidized as the oxidative current in LSV

s larger than that for the cell without MTE-TMS, indicating that oxi-ation of electrolyte with the additive starts before the standard elec-rolyte ( Fig. 1 b), with specific MTE-TMS reduction at about 3.75 V (inset

218

n Fig. 1 b). The same tendency is also observed in the cyclic voltammo-rams (CVs) of the NCM851005 ( Figs. 1 c and S1). The onset oxidationotential (inset in Fig. 1 c) is lower for the MTE-TMS-containing elec-rolyte as compared with standard electrolyte, confirming higher oxida-ion activity of MTE-TMS on the cathode surface. The difference betweenhe redox peak potentials ( ΔV) of NCM851005 becomes smaller withhe presence of MTE-TMS additive by ≈24 mV ( Fig. 1 c). This suggestshat MTE-TMS additive decreases the polarization and improves the re-ersibility of NCM851005 cathode during Li + -(de)intercalation [30] .

The reduction of MTE-TMS-containing electrolyte was investigatedsing the CV curves, recorded for the graphite electrodes. A clear re-uction peak is observed at ≈1.5 V for the electrolyte with MTE-TMS Fig. 1 d), in agreement with lower LUMO of MTE-TMS in comparisono standard solvents, and this peak is likely to be a signature of thereferential reduction of MTE-TMS, suggesting that MTE-TMS partici-ates in the formation of a solid electrolyte interface (SEI) layer on theraphite. Overall, theoretical calculations and experimental results re-eal that MTE-TMS could be both oxidized at the cathode and reducedt the anode prior to the carbonate solvents, participating in formation protective surface film on the cathode and the anode, preventing elec-rolyte decomposition in further cycles.

.2. Electrochemical cycling of Li ‖NCM851005 half-cells

Firstly, the half-cells of Li ‖NCM851005 were tested with the stan-ard electrolyte (1 M LiPF 6 /EC:DEC) without and with an optimalmount of 1 wt% MTE-TMS additive (Fig. S2), and their cycling per-ormance and impedance spectra changes during cycling are comparedn Fig. 2 . Without MTE-TMS, the cell exhibits the initial charge andischarge capacities of 243 and 202 mAh g –1 , respectively, with thenitial Coulombic efficiency (ICE) of 83% ( Fig. 2 a). Discharge capac-ty decreases to 92 mAh g –1 after 100 cycles, yielding a very low ca-acity retention of 46 % ( Fig. 2 g), which is accompanied by fadingf redox peak intensities and their shifting positions, identifying theoor reversibility of the phase transition between hexagonal structuresH2 ↔H3) at ≈4.2 V ( Fig. 2 b), and significantly increased interfacial re-istances ( Fig. 2 c, 2 f, 2 i) with cycling. On the other hand, with MTE-MS, a significantly improved cycling performance is observed: initialharge and discharge capacities are 230 and 206 mAh g –1 , respectively,orresponding to ICE of 90 % ( Fig. 2 d), and improved capacity reten-ion of 89 % after 100 cycles ( Fig. 2 g) even under upper voltage cut-offf 4.3 V with a high mass NCM851005 loading of ≈8.9 mg cm

–2 . Theignificantly improved long-term cycling stability is clearly due to theathode–electrolyte interface stabilization by MTE-TMS additive, main-aining the redox peak positions upon multiple Li + -(de)intercalations,esulting in reduction of H2 ↔H3 phase transitions ( Fig. 2 e), with lim-ted increase in the resistance ( Fig. 2 c, 2 f, 2 i) and overpotentials, asupported by galvanostatic intermittent titration technique (GITT) ex-eriments (Fig. S3b).

The layered to rock-salt phase transition as a result of cation mixings known to cause not only capacity decay and overpotential increase butlso voltage fade [13] . In order to evaluate the effect of MTE-TMS onhe voltage fade, the variation of average charge–discharge voltages dur-ng cycling without and with MTE-TMS are compared in Fig. 2 h, whichere calculated by dividing the cell’s energy by the cell’s capacity [31] .oth electrolytes exhibit an increase of the average charge voltage dueo overpotential growth with cycling, however, more in case of the stan-ard electrolyte. The average discharge voltage decays only by 0.054 Vfter 100 cycles from the first average discharge voltage of 3.815 V withTE-TMS, whereas voltage deteriorates by approximately 0.749 V from

he first average discharge voltage of 3.822 V (more than 10 times) forhe cathode with standard electrolyte. This result confirms that the rolef MTE-TMS in stabilizing the cathode–electrolyte interface and cathodetructure leads to reduced voltage fade and improved long-term cyclingerformance.

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Fig. 1. (a) The calculated HOMO and LUMO energy levels for MTE-TMS, EC and DEC; (b) LSV curves on glassy carbon electrode; CV curves of (c) Li ‖NCM851005 and (d) Li ‖graphite cells without and with MTE-TMS additive.

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In addition to enhanced electrochemical performance, the MTE-TMSdditive makes electrolyte safer as can be seen from DSC analysis ofharged cathodes to 4.3 V (Fig. S4). The results show significantly en-anced thermal stability of NCM851005 cathode with MTE-TMS ad-itive: charged cathode in the standard electrolyte exhibits a sharpxothermic peak at ≈209 °C, with a heat generation of 415 J g − 1 , whileTE-TMS shifts an exothermic peak to higher temperature ( ≈213 °C),

nd a reduced heat generation by ≈25% (295 J g − 1 ).

.3. Electrochemical cycling of graphite ‖NCM851005 full-cells

Considering the effects of MTE-TMS additive on the electrochemicalerformance of both Li ‖NCM851005 ( Fig. 2 ) and Li ‖graphite (Fig. S5)alf-cells, the full-cells of graphite ‖NCM851005 were assembled andested with standard electrolyte without and with 1 wt% MTE-TMS ad-itive in a voltage window between 3.0 and 4.25 V (corresponding to.3 V vs Li + /Li). Comparison of their electrochemistry is presented inig. 3 . MTE-TMS additive in the full-cells, similarly to half-cells, causes significant improvement in long-term cycling performance, as shownn Fig. 3 e. The maximum capacity of 198 mAh g − 1 ( Fig. 3 c) with signif-cantly higher capacity retention of 84 % at the 100th cycle and highoulombic efficiency of 99.8% ( Fig. 3 e, f) were obtained. By contrast,

ower capacities and Coulombic efficiencies, a rapid capacity fade (re-ention of 61 % at the 100th cycle) and larger voltage polarization werebserved for the full-cell, cycled without MTE-TMS ( Fig. 3 a, b, e, f).

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In the dQ/dV plots one can see that while redox peaks, due to chargend discharge processes, are well preserved in the presence of MTE-TMSdditive ( Fig. 3 d), in the standard electrolyte ( Fig. 3 b), a substantialoss of redox peak stability and capacity with cycling occurs, which isssociated with structural degradation of active materials. This empha-izes the critical role of MTE-TMS additive in stabilizing the electrolyte–lectrodes interface for improved full-cell cycling stability. Although cy-ling stability is improved by the presence of MTE-TMS, capacity reten-ion (84%) is still lower than that of half-cell ( Fig. 2 g). The reasonsehind can be: (i) effectivity of MTE-TMS is reduced in full-cells, orii) lithium inventory loss during SEI formation on graphite anode dur-ng the first cycle [32] . To confirm that MTE-TMS is equally effectiven full-cells, experiments with pre-lithiated graphite anode were per-ormed. These results support our reasoning that less favorable capacityetention in full- as compared to half-cells is caused indeed by the lossf active Li in irreversible side reactions during the first cycle [32] . Theull-cell with MTE-TMS and pre-lithiated graphite (Fig. S6) showed theame capacity retention (89%) as in case of the half-cell ( Fig. 2 ), affirm-ng effectivity of MTE-TMS.

.4. Cycling-induced morphological changes

Fig. 4 shows the cross-sectional and top-view SEM images of theristine NCM851005, cycled without and with MTE-TMS additive inhe full-cells for 100 cycles. The cross-sectional view ( Fig. 4 a) clearly

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Fig. 2. Voltage profiles and their differential plots for Li ‖NCM851005 half-cells, cycled between 3.0 and 4.3 V in the standard electrolyte (a, b) without and (d, e) with MTE-TMS additive. Comparison of (g) cycling performance, (h) average charge–discharge voltages, (c, f) impedance evolution, and (i) changes in the interfacial resistances determined by fitting with the equivalent circuit in (c).

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hows that pristine NCM851005 particles are crack-free, have smoothurface, and are compact. Cycling in the standard electrolyte withoutTE-TMS results in the formation of internal cracks within secondary

articles ( Fig. 4 c), generated along the grain boundaries from the corend propagating to the surface [ 8 , 33–35 ]. The crack formation is as-ribed to strain due to the stress arising from the anisotropic latticexpansion and contraction of different grains inside secondary particlespon repeated Li + -(de)intercalation [ 8 , 12 , 35 , 36 ]. The cracks facilitatehe penetration of the electrolyte into the cathode particles along therimary particle boundaries through the crack network, leading to ex-ansion of cracks and formation of new cathode − electrolyte interface37] . A thick surface film covers the whole surface of the primary par-icles ( Fig. 4 d), as a results of the electrolyte decomposition [8] .

The crack formation and the degradation of the surface of primaryarticles lead to a loss of electrical contact between the primary particles38–44] , thus deteriorating the full-cell cycling performance ( Fig. 3 and e). However, such crack formation is significantly reduced withhe use of MTE-TMS additive, despite few hairline cracks still visiblen Fig. 4 e. Besides, the morphology of primary particles is sustainedn the cycled cathode ( Fig. 4 f), and a very thin surface film, probablyormed by additive decomposition products, is visible on the surface ofhe particles. This implies that MTE-TMS participates in the formationf a stable surface-protective film, avoiding the direct contact between

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CM851005 particles and electrolyte, thus inhibiting the reactions athe cathode − electrolyte interface, and in such a way reducing the de-elopment and propagation of cracks.

The SEM images of graphite anodes, before and after cycling in thetandard electrolyte without and with MTE-TMS additive, are shown inig. 5 . The pristine graphite anode ( Fig. 5 a, b) has a uniform smooth sur-ace. After cycling in the standard electrolyte without MTE-TMS ( Fig. 5 c,), the graphite’s surface is completely covered by a thick polymer-likeayer and surface is rougher than that of pristine. However, with MTE-MS additive ( Fig. 5 e, f), the surface of graphite remains smooth withew nano- to sub-micrometer plate-like crystals, confirming the effec-ively passivating SEI. This indicates the role of MTE-TMS in protectinghe graphite anode as well as reducing the electrolyte decomposition,hus improving the full-cell cycling performance ( Fig. 3 ).

.5. Cycling-induced bulk structural changes

In order to compare the structural stability of NCM851005, cycledithout and with additive, the full-cells after the 100th cycle were dis-ssembled, and the NCM851005 cathodes were taken out for the ex situRD analysis. In case of pristine NCM851005 cathode ( Fig. 6 a-i), all

he major peaks in the XRD patterns are identified to layered hexago-al structure (R ̄3 m). The a and c lattice parameters of pristine material

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Fig. 3. Voltage profiles and their differential capac- ity plots of graphite ‖NCM851005 full-cells, cycled be- tween 3.0 and 4.25 V at C/5 in the standard elec- trolyte (a-b) without and (c-d) with MTE-TMS addi- tive, comparison of (e) cycling performance and (f) Coulombic efficiency.

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re 2.8713 and 14.1883 Å, respectively, with a c / a ratio of 4.9415 andnit cell volume of 101.2955 Å3 . While after 100 cycles without MTE-MS, the broadened (003) reflection is weakened and greatly shifted to

ower 2 𝜃 region ( Fig. 6 b-ii) due to the loss of structural order and crys-allinity, as compared to pristine ( Fig. 6 b-i). At the same time the (104)eflection ( Fig. 6 c-ii) is shifted to higher 2 𝜃 region, which suggests theecrease of ab -plane [23] . This correlates to the substantial loss of redoxeak ordering and intensity in the dQ/dV plots after cycling ( Fig. 3 b).n comparison, the use of MTE-TMS additive lead to the significantlymproved structural stability, as indicated by reduced magnitude in thehift of the (003) ( Fig. 6 b-iii) and the (104) ( Fig. 6 c-iii) reflections, asell as their reduced broadening and weakening after cycling, in agree-ent to well-maintained redox-peaks in the dQ/dV plots ( Fig. 3 d).

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Fig. 6 d shows the changes in the lattice parameters and cell vol-me of NCM851005 cathode with cycling. Both cycled cathodes exhibitattice expansion along the c -axis and contraction along the ab -plane,owever, to much higher degree in absence of MTE-TMS. Note thatRD patterns of cycled cathodes were collected from fully discharged

ull-cells, thus the changes in the lattice parameters are reflecting thei inventory loss during cycling [ 8 , 23 , 45–47 ]. In case of the loss of ac-ive Li, the a parameter typically decreases due to the smaller ionic ra-ius of the transition-metal ions as a result of oxidation [48] . In con-rast, the c parameter increases due to the creation of Li-deficient stateith a stronger electrostatic repulsion between the oxygen–oxygen lay-

rs across the Van der Waals gap [ 45 , 49 ]. As a result, a decrease of unitell volume is observed for both cycled cathodes, consistent with ear-

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Fig. 4. Cross-sectional SEM images of sec- ondary particles and top-view images for of primary particles of (a-b) pristine NCM851005 cathode and cathodes cycled (c-d) without and (e-f) with MTE-TMS additive, taken from

graphite ‖NCM851005 full-cells after 100 cy- cles.

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ier reports [ 8 , 45 , 46 , 48 ]. However, in the standard electrolyte, the cellolumes significantly decreases (by 0.95 % from pristine) due to theattice contraction/expansion, crack formation ( Fig. 4 c), and probablyue to degradation of layered structure, while the use of MTE-TMS ad-itive results in significantly smaller cell-volume change (by 0.49 %), ingreement with significantly improved cell performance.

The structural degradation, induced by interface reactions, is accom-anied by metal leaching from NCM-materials, therefore, an ICP-OESnalysis to detect Ni, Co and Mn on the graphite counter electrode wasarried out. Fig. 6 e compares the amounts of the metals (Ni, Co andn) leached from NCM851005 during cycling and accumulated on the

raphite electrodes during 100 cycles in full-cells. The amounts of met-ls deposited on the graphite cycled in the standard electrolyte with-ut MTE-TMS were high, confirming the occurrence of metal-dissolutionrom NCM851005 cathode and that these metal species are deposited onhe anode surface. These metallic deposits can readily react with the SEInd electrolyte, possibly catalyzing the electrolyte decomposition andeading to the thicker SEI layer, as observed by SEM ( Fig. 5 c,d), and in-rease the loss of active lithium. However, presence of these elements isignificantly reduced while cycling with MTE-TMS additive, suggestingnhanced structural stability of NCM851005 cathode in the electrolyteith MTE-TMS. Overall, the combination of XRD and ICP-OES data in-icate that MTE-TMS helps to preserve the structure of NCM851005,educes metal-dissolution from cathode and metal-deposition on theraphite during long-term cycling.

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The structural degradation of anode was investigated by Raman spec-roscopy, it being very sensitive to graphite’s structural changes. Fig. 7hows the Raman spectra of graphite anode: pristine and after 100 cyclesn standard and in MTE-TMS-containing electrolyte. Raman spectrum ofristine anode consists of prominent G-band at 1582 cm

–1 , and relativelyeak D-band at 1335 cm

–1 [50] . Cycling of anodes in both electrolytesesults in the growth of D-band at the expense of G-band, indicating decrease in graphite structural ordering, along with the formation ofp 3 -hybrid carbon-containing SEI species [51] . In general, the degreef disorder of carbon is evaluated using the relative intensity ratio of-band to G-band (R = I D /I G ). The higher the R value, the higher the

tructural disorder. The R increases from 0.344 for the pristine anode, to.439 after cycling with MTE-TMS additive, and to a significantly largeralue of 0.706 for graphite cycled in the standard electrolyte. The lower value with MTE-TMS additive indicates the greater structural preser-ation of graphite and relatively thin SEI layer, as observed in SEM im-ges ( Fig. 5 e, 5 f). In addition, a new shoulder at 1614 cm

− 1 observedor both cycled anodes, the so-called D ′ -band, attributed to oxidized sp 2

arbon that represents surface defects [52] , supporting the occurrencef structural disordering during cycling. The D ′ -band is relatively weakor the anode cycled with MTE-TMS additive, as compared to that cy-led with standard electrolyte, again indicating structural preservationmprovement when cycling in presence of MTE-TMS. This suggests thathe use of our multifunctional electrolyte additive preserves better notnly the structural stability of NCM851005 cathode but also structure of

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Fig. 5. SEM images and photographs (inset) of the (a-b) pristine and graphite electrodes cycled (c-d) without and (e-f) with MTE-TMS additive, taken from

graphite ‖NCM851005 full-cells after 100 cycles.

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raphite anode, affecting positively the cycling performance of full-cell Fig. 3 ).

.6. Interface characterization

To better understand the surface chemistry changes due to the pres-nce of additive, ex situ XPS was used to investigate the compositions ofhe surface on cycled NCM851005 and graphite electrodes, recoveredrom the full-cells.

Fig. 8 A shows comparison of the XPS spectra of pristine and cy-led cathodes, depending on the electrolyte composition. In the Ni 3ppectra, cycling without and with additive results in a significant dif-erence: without MTE-TMS, the peaks of pristine material ( Fig. 8 A-a)re no longer visible after cycling ( Fig. 8 A-b) mainly because of a thickayer formed by electrolyte-degradation ( Fig. 8 B-b), as compared tohe uncycled cathode ( Fig. 8 B-a). Spectral features are, however, wellaintained for NCM851005 electrode, cycled with MTE-TMS additive

Fig. 8 A-c), where Ni signal is clearly resolved. Peak of NCM851005 lat-ice (dark blue) M − O (M = Ni, Co, Mn) at 529.8 eV [ 27 , 53–57 ] in the

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1s spectrum is also still clearly visible for the cycled cathode withTE-TMS additive, whereas it is completely shielded by other com-

ounds on the electrode surface after cycling in the standard electrolyteue to the formation of thick surface film with high coverage, causedy severe electrolyte oxidation [58] . These results indicate that MTE-MS induces formation of thinner surface film and prevent further elec-rolyte decomposition, consistent with our TEM results, where cathodeycled is covered with a thin and mostly uniform surface film ( ≈8 nmn thickness) ( Fig. 8 B-c). A new broad peak at 533.8 eV in the O 1spectra (green), ascribed to various C–O-bond-containing compounds,nd an enhanced peak at 532.4 eV, characteristic for C = O (dark yel-ow), can both be attributed to O-containing electrolyte decompositionroducts [ 53 , 54 ]. Higher concentration of C–O with MTE-TMS additivemplies the accumulation of C–O containing decomposition products ofhe additive. In the C 1s spectra, new peaks of C − O (286.1 eV), C = O288 eV) and CO 3

2- (290 eV) functionalities from carbonate solventsecomposition are observed on both cycled cathodes, besides the peaksf C − H/C − C and C − F (PVDF) visible for pristine [ 53 , 54 ]. Higher con-entration of C = O and CO 3 without MTE-TMS can be explained by the

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Fig. 6. (a) Powder XRD patterns of pristine (i) and cycled without (ii) and with MTE-TMS additive (iii) cathodes, their reflections of (b) (003) and (c) (104) planes, as well as (d) changes of lattice parameters and cell volume. (e) The metal disssollution from NCM851005 as determined by ICP-OES from the cycled graphite anodes, taken from graphite ‖NCM851005 full-cells.

Fig. 7. Raman spectra for graphite anodes taken from graphite ‖NCM851005 full-cells, cycled between 3.0 and 4.25 V in the standard electrolyte without and with MTE-TMS additive for 100 cycles.

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ore intense oxidative decomposition of carbonate solvents. In the Fs spectra, both cycled cathodes show new peaks close to 687.8 and85.5 eV, attributable to Li x PF y O z and LiF, respectively, from LiPF 6 ecomposition in addition to the peak of PVDF at 688.8 eV, visibleor pristine electrode [ 5 , 28 , 53 , 54 , 59 ]. Lower concentration of electri-ally resistive LiF on the cycled cathode with MTE-TMS additive mightontribute to the decrease in the interfacial resistance and enhancedull-cell performance ( Fig. 3 c, e). In addition, features of PVDF binder,n cathode cycled with MTE-TMS additive, still remain clearly visi-le, contrary to their vague features for electrode cycled without MTE-MS, confirming a thinner surface film formed with MTE-TMS addi-ive, consistent with C 1s spectra results. In the P 2p spectra, higheroncentration of Li x PF y (137.1 eV) and Li x PF y O z (134.1 eV) species,hich are the decomposition products of LiPF 6 (LiPF 6 → LiF + PF 5 ,F 5 + H 2 O → POF 3 + 2HF and POF 3 + ne − + nLi → Li x PO y F z + LiF) 22 , 28 ], are observed at the cycled cathode without MTE-TMS as com-ared to the one with MTE-TMS. These results indicate that MTE-MS effectively scavenges the acidic species (e.g. HF, PF 5 and PF 3 O)rom the electrolyte, which is characteristic for Si − O functional group 11 , 60 ], leading to improved surface stability of the NCM851005athode. The most significant difference between the two electrolytess revealed in the Si 2p spectra: the use of MTE-TMS additive re-ults in the presence of Si–C [ 5 , 61 ], Si–O [ 22 , 28 ] and Si–F [ 22 , 62 ]eatures at 103.9, 103.3 and 102 eV, respectively, confirming that

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Fig. 8. (A) XPS spectra for chemical surface com- position determination and (B) TEM images of (a) pristine NCM851005 cathode and cycled cath- odes taken from graphite ‖NCM851005 full-cells cycled between 3.0 and 4.25 V in the standard electrolyte (b) without and (c) with MTE-TMS ad- ditive for 100 cycles.

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he surface film is built from the oxidative decomposition productsf MTE-TMS.

Surface chemistry studies of cycled cathodes have shown that, afterycling in the standard electrolyte, the surface film is mainly composedf LiPF 6 -derived inorganic species including LiF, Li x PF y , Li x PF y O z andi 2 CO 3 at a relatively high concentration, originating from carbonateolvents. In contrast, the surface of the cathode, cycled with MTE-TMSdditive, is covered with organic compounds, along the MTE-TMS de-omposition products, forming a relatively thin and mostly uniform sur-ace film, as the Ni and metal–oxygen bonds can be still detected.

Fig. 9 shows XPS spectra illustrating the chemical changes ofraphite anode surface after prolonged cycling. The C 1s spectrum of

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ristine anode ( Fig. 9 a) contains a strong peak at 285 eV, correspond-ng to C − C/C − H bonds in carbon, tiny peaks at 286.7 and 288 eV fromO– and CO 2 of CMC binder, and at 285.7 eV characteristic to SBR 51 , 53 , 54 , 63 , 64 ].

The O 1s spectrum shows two peaks at 533.8 and 531.8 eV, arisingrom the CMC binder due to the presence of C − O and C = O functionalroups, respectively [ 51 , 59 , 64 ]. After cycling, changes on de-lithiatedraphite electrodes are observed on both cycled anodes ( Fig. 9 b,c) andre mainly due to the formation of the SEI. New peaks, characteristic to − O (286.1 eV), C = O (288 eV) and CO 3

2- (290 eV) functionalities, areresent in the C 1s spectra, while the corresponding O 1s peaks are ob-erved at 532.4 and 533.7 eV [ 58 , 65 ]. These contributions are attributed

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Fig. 9. XPS spectra for chemical surface composition determination of (a) pristine graphite anode and cycled anodes taken from graphite ‖NCM851005 full-cells, cycled between 3.0 and 4.25 V in the standard electrolyte (b) without and (c) with MTE-TMS additive for 100 cycles.

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o Li 2 CO 3 , alkyl carbonate and carboxylate salts from electrolyte de-omposition products [ 51 , 58 , 65 ], and are more intense for electrodesycled without MTE-TMS. A new shoulder at ≈282.6 eV in the C 1spectrum from the electrode, cycled in standard electrolyte ( Fig. 9 c), isf particular importance, as it is due to the presence of lithiated graphitepecies (LiC x ) [59] , implying that not all Li + ions could de-intercalaterom graphite and return to the cathode. This lithium loss to the anodes most likely due to a high overpotential [46] , as observed with full-cellycling results shown in Fig. 3 a. Differences are also observed in the F 1snd P 2p spectra. Peaks characteristic of Li x PF y O z and LiF, are observedn the F 1s spectra at 687.4 and 685.5 eV, while peaks are present in the

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2p spectra at 137.1 and 134.1 eV for Li x PF y and Li x PF y O z [5] , for cellsycled both with and without additive. These originate from the decom-osition of LiPF 6 salt, supported by the Li 1s spectra. However, the usef MTE-TMS additive leads to a notable decrease in the concentration ofoth P − F − O and Li − F compounds, confirming the role of MTE-TMS incavenging the acidic species. The evidence of the Si-containing speciesenerated via reductive decomposition MTE-TMS are observed in thei 2p spectrum of anode cycled with MTE-TMS additive ( Fig. 9 c), simi-arly to the case of NCM85105 cathode. The XPS results of the graphitenodes indicate that while the SEI layer, formed in the standard elec-rolyte, includes relatively high concentrations of LiF, Li x PF y /Li x PF y O z ,

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Scheme 1. Schematic representation of interfacial phenomena occurring in the graphite ‖NCM851005 full-cells, cycled between 3.0 and 4.25 V in the standard electrolyte (a) without and (b) with MTE-TMS additive.

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nd Li 2 CO 3 , MTE-TMS reductive decomposition products are presents the SEI species at the surface of anode cycled with MTE-TMS addi-ive. Note that MTE-TMS oxidizes and reduces before the standard elec-rolyte, as shown in LSV and CV ( Fig. 1 ), MTE-TMS additive might un-ergo earlier decomposition during early cycles, forming the relativelyhin surface film/SEI layer, composed of Si-containing species and pro-iding surface structural robustness to NCM851005 as well as graphite.he summary of MTE-TMS additive working principle is illustrated incheme 1 b.

. Conclusions

The MTE-TMS dual action electrolyte additive, able to protect bothathode and anode, has been studied and its working mechanism clari-ed. LSV and CV electrochemical experiments confirmed the hypothesis,aised from results of density functional theory calculations, that MTE-MS is oxidized and reduced prior to the standard carbonate solvents. Exitu analysis showed that MTE-TMS forms a stable and thin surface pro-ective film on the NCM851005, containing Si species, which effectivelyeduced crack formation, metal-dissolution, and structural degradationf the cathode. MTE-TMS also forms a stable SEI layer on the graphitenode, stabilizing graphite structure and preventing thickening of theEI.

MTE-TMS’ effectivity, on both anode and cathode, results in supe-ior cycling performance of the full-cells, with 1 wt% MTE-TMS in elec-rolyte, delivering high capacity of 198 mAh g − 1 , along with an excellentapacity retention of 84% after 100 cycles at C/5, while cycled to up-er cut-off voltage of 4.25 V (4.3 vs Li + /Li). Our results demonstratehat MTE-TMS has a potential to help the realization of high energy-ensity Li-ion batteries through enabling wider working voltage rangeor Ni-rich oxide cathodes.

ata availability

The raw/processed data can be provided by authors upon reasonableequest.

uthor contributions

H.Q.P. and S.T. designed the study and wrote the manuscript. M. M.nd M. E. K. performed the XPS measurements. M. T. conducted the ICP-ES characterizations. S.T. supervised the project. All authors discussed

he results, and commented on this manuscript.

eclaration of competing interest

None

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cknowledgements

This work was financially supported by the BASF Scientific Networkn Electrochemistry and Batteries, and the SCCER Heat and Electricitytorage.

upplementary materials

Supplementary material associated with this article can be found, inhe online version, at doi:10.1016/j.ensm.2020.08.026 .

eferences

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