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SECTION | page 1 | Docling页内原序 17 | 新页内顺序 18 | layout_order 17 | body_zone / column_1_of_2 | p1:body_region:0
1. Introduction
#001 | page 1 | Docling页内原序 18 | 新页内顺序 19 | layout_order 18 | body_zone / column_1_of_2 | p1:body_region:0
Lithium ion batteries (LIBs) have been used in electric vehicles because of their high energy density, safety, and low price; however, these qualities need to be further enhanced to extend the maximum distance that electric vehicles can travel before needing to be recharged [1 -3]. Many novel and advanced types of cathode materials have been explored and had their potentials gauged to meet the requirements of a high cell energy density [4]. Lithium-rich layered oxide (LRM), xLi2MnO3 ⋅ (1-x)LiMO2 (M = Ni, Co, Mn) has attracted considerable attention as the most promising alternative for LIBs, due to its high reversible discharge capacity (over 250 mAh g 1 ) and high range of operating voltage (3.0 -4.8 V) [5 -8]. However, its application is limited by the poor cycling and rate performance of LRM, which leads to the destruction of the cathode material structure and an unstable
#002 | page 1 | Docling页内原序 22 | 新页内顺序 25 | layout_order 24 | body_zone / column_2_of_2 | p1:body_region:1
electrode/electrolyte interface [9].
#003 | page 1 | Docling页内原序 23 | 新页内顺序 26 | layout_order 25 | body_zone / column_2_of_2 | p1:body_region:1
To overcome these problems, several approaches have been explored in the past decade, including doping and coating [10 -13]. Recently, a simple and economical strategy has been developed: the formation of a protective interphase on the cathode through the preferential oxidation of additives ( < 5 wt%) added to the electrolyte. These additives have a higher highest occupied molecular orbital than solvents. This ensures that the electrolyte decomposition products do not react with the protective cathode interphase, resulting in the maintenance of interface stability. A variety of electrolyte additives with different molecular structures have been proposed. Tris(trimethylsilyl)phosphate [14,15] has been used as a film-forming additive on lithium-rich cathode materials to improve the electrochemical performance. Tris(trimethylsilyl) borate forms a modified solid electrolyte interphase (CEI) on the cathode, which reduces the capacity fading of a Li[Li0.2Mn0.54Ni0.13Co0.13]
#004 | page 2 | Docling页内原序 3 | 新页内顺序 3 | layout_order 28 | top_margin / column_1_of_2 | p2:body_region:0
O2/Li cell from 81% to 26% after 200 cycles [16]. Lan et al. reported [17] that the electrode capacity retention in an electrolyte without any additive was 40%, which is much lower than the 72% observed in an electrolyte with bis(trimethylsilyl)carbodiimide. The capacity retention of Li1.2Mn0.54Ni0.13Co0.13O2 cathodes was found to increase in an electrolyte with 1 wt% diphenyl disulfide [18]. After 150 cycles, the capacity fading of Li1.2Mn0.54Ni0.13Co0.13O2 was found to decrease from 27.4% in an electrolyte without any additive to 8.8% an electrolyte with 1% 1,3,6-hexanetricarbonitrile [19]. The cycling stability of Li1.2Mn0.525Ni0.175Co0.1O2 cathodes was improved by using 5 wt% di-(2, 2,2 trifluoroethyl) carbonate in the electrolyte, and as a result, the capacity fading decreased from 30% to 11% after 50 cycles [20]. Cha et al. [21] investigated Li-rich/graphite full cells with 1 wt% lithium difluoro (oxalate)borate (LiDFOB) in 1.3 M LiPF6 containing an EC:EMC:DMC electrolyte at a volume ratio of 3:4:3. LiDFOB optimizes the surface composition of both the graphite anode and Li-rich cathode. A stable CEI film was produced on the Li[Li0.2Mn0.56Ni0.16Co0.08]O2 electrode with the presence of the decomposition products of tri(hexafluoro-iso-propyl) phosphate (HFiP). The capacity loss for a Li[Li0.2Mn0.56Ni0.16Co0.08]O2 electrode in an electrolyte with 1% HFiP after 130 cycles was shown to be reduced from 35.5% to 26.7% [22]. Triphenyl phosphite (TPPi) was found to preferentially oxidize over the solvent at an oxidation potential of 4.2 V (vs. Li/Li + ), and the TPPi-derived layer can effectively inhibit electrolyte decomposition [23]. Tu et al. reported that TEP reacted with active oxygen and formed a protective layer that suppressed electrolyte decomposition and the structural destruction of the LRM [24]. Triethyl borate and tripropyl borate have been reported as electrolyte additives that improve the self-discharge property of LRM cathodes [25].
#005 | page 2 | Docling页内原序 4 | 新页内顺序 4 | layout_order 29 | body_zone / column_1_of_2 | p2:body_region:0
Some studies have reported that the improvement of the electrochemical behavior of NCM622-based cells and LNMO-based cells are a result of silicon-based electrolyte additives [26 -28]. In this paper, 1, 3-divinyltetramethyldisiloxane (DTMS) was used as an additive to enhance the electrochemical properties of a Li-rich layered oxide cathode (LRM). Results showed that 2 vol% DTMS effectivity decreased capacity loss of LRM/Li cell from 57.2% to 25%. The possible mechanism for this was investigated further though electrochemical and physical analyses.
SECTION | page 2 | Docling页内原序 5 | 新页内顺序 5 | layout_order 30 | body_zone / column_1_of_2 | p2:body_region:0
2. Experiment
SECTION | page 2 | Docling页内原序 6 | 新页内顺序 6 | layout_order 31 | body_zone / column_1_of_2 | p2:body_region:0
2.1. Preparation of electrolytes and electrodes
#006 | page 2 | Docling页内原序 7 | 新页内顺序 7 | layout_order 32 | body_zone / column_1_of_2 | p2:body_region:0
The LRM cathode was composed of 80 wt% LRM (LRM300, Ningbo Li-rich Battery Material Technology Co., Ltd., China), 10 wt% polyvinylidene fluoride (PVDF) binder, and 10 wt% acetylene black in N -methyl-2-pyrrolidone. The slurry was coated on Al foil, and then vacuum dried at 100 ◦ C for 12 h. The CR2025-cell was fabricated in an Arfilled glove box with a Li sheet as the anode and Celgard 2325 as the separator. The base (BE) electrolyte contained 1 M LiPF6 and included EC/EMC/DMC (1:1:1, in weight). DTMS (Aladdin Co., Ltd., China) was then added into the BE electrolyte. Electrolytes with 2 vol% DTMS were used (Supplementary Material. 1).
#007 | page 2 | Docling页内原序 8 | 新页内顺序 8 | layout_order 33 | body_zone / column_1_of_2 | p2:body_region:0
A total of 1000 ppm of hydrofluoric acid (HF) was then added into the BE and BE + 2 vol%DTMS electrolytes to prepare HF-containing electrolytes using a 40 wt% HF aqueous solution [25]. All electrolytes were prepared in an Ar-filled glove box.
SECTION | page 2 | Docling页内原序 9 | 新页内顺序 9 | layout_order 34 | body_zone / column_1_of_2 | p2:body_region:0
2.2. Electrochemical testing
#008 | page 2 | Docling页内原序 10 | 新页内顺序 10 | layout_order 35 | bottom_margin / column_1_of_2 | p2:body_region:0
The charge -discharge performance of the cells was evaluated using a computer-controlled test system (CT2001A, China). The LRM/Li cells were pre-cycled in the following schedule: 0.1C (1C = 300 mA g 1 ) for three cycles and 0.2C for three cycles at 25 ◦ C between 2.8 and 4.8 V. The LRM/Li cells were then operated for 100 cycles at 0.5C to analyze the cycling performance. The rate capability of the cells was evaluated at a 0.5-1-2-3-5C charge/discharge current. The electrochemical
#009 | page 2 | Docling页内原序 12 | 新页内顺序 12 | layout_order 37 | front_matter / column_2_of_2 | p2:body_region:1
/Li) of EC, DMC, EMC, and DTMS.
#010 | page 2 | Docling页内原序 13 | 新页内顺序 13 | layout_order 38 | front_matter / column_2_of_2 | p2:body_region:1
impedance spectroscopy (EIS) was employed in the frequency range of 10 5 to 0.1 Hz with an amplitude of 5 mV, using a frequency response analyzer (VSP, Bio-logic).
SECTION | page 2 | Docling页内原序 14 | 新页内顺序 14 | layout_order 39 | body_zone / column_2_of_2 | p2:body_region:1
2.3. Physical characterization
#011 | page 2 | Docling页内原序 15 | 新页内顺序 15 | layout_order 40 | body_zone / column_2_of_2 | p2:body_region:1
To understand the influence of DTMS on the cycling performance of LRM/Li cells, scanning electron microscopy (SEM; S-4800, Hitachi), transmission electron microscopy (TEM; JEM-2010, JELO), XRD analysis (XRD; Bruker D8 ADVANCE) using Cu Ka radiation, X-ray photoelectron spectroscopy (XPS; ESCALAB 250Xi), and 19 F nuclear magnetic resonance ( 19 F NMR; AVANCE III 400 MHz) analyses were carried out. The cycled electrodes (LRM and Li) were disassembled, rinsed with dimethyl carbonate solvent, and dried under vacuum.
SECTION | page 2 | Docling页内原序 16 | 新页内顺序 16 | layout_order 41 | body_zone / column_2_of_2 | p2:body_region:1
2.4. Calculations
#012 | page 2 | Docling页内原序 17 | 新页内顺序 17 | layout_order 42 | body_zone / column_2_of_2 | p2:body_region:1
The Gaussian 09 software package was used for theoretical calculations. The equilibrium structures were determined using the B3LYP/6311G(d,p) level [28]. The oxidation potential (Eox) was obtained as follows[28]:
#013 | page 2 | Docling页内原序 18 | 新页内顺序 18 | layout_order 43 | body_zone / column_2_of_2 | p2:body_region:1
Eox (Li + /Li) = [G(M + ) - G(M)]/F - 1.4 V
SECTION | page 2 | Docling页内原序 19 | 新页内顺序 19 | layout_order 44 | body_zone / column_2_of_2 | p2:body_region:1
3. Results and discussion
SECTION | page 2 | Docling页内原序 20 | 新页内顺序 20 | layout_order 45 | body_zone / column_2_of_2 | p2:body_region:1
3.1. Oxidative stability of DTMS
#014 | page 2 | Docling页内原序 21 | 新页内顺序 21 | layout_order 46 | body_zone / column_2_of_2 | p2:body_region:1
The as-calculated oxidation potential and Li + binding affinity (Eb) are often used to forecast the oxidation tendency of an additive on the cathode surface [29,30]. The film-forming electrolyte additives have a lower oxidation potential than the electrolyte solvents. Therefore, the additives dominate the composition of the CEI film on the cathode. Furthermore, a low value of Li + Eb is suitable for the enrichment of the additive on the cathode surface [29]. The calculated Eox values of the solvents and DTMS are listed in Table 1. As per the theoretical calculation results, DTMS (5.58 V) has a lower Eox than EC (7.11 V), DMC (7.00 V), and EMC (6.99 V), indicating that DTMS has a lower oxidation stability than the electrolyte solvents. The optimized structures and solvent-Li + and DTMS-Li + Eb values are seen in Fig. 1. The Eb value of DTMS is lower than those of solvents. This indicates that the interaction between DTMS and Li + is weaker, so DTMS can easily accumulate at the cathode surface. DTMS may thus form a protective film at the positive electrode, as per the theoretical calculation results.
SECTION | page 2 | Docling页内原序 22 | 新页内顺序 22 | layout_order 47 | body_zone / column_2_of_2 | p2:body_region:1
3.2. Impact of DTMS at electrochemical perform
SECTION | page 5 | Docling页内原序 5 | 新页内顺序 5 | layout_order 72 | body_zone / column_1_of_2 | p5:body_region:0
3.3. Interaction of DTMS with HF/F
#015 | page 5 | Docling页内原序 6 | 新页内顺序 6 | layout_order 73 | bottom_margin / column_1_of_2 | p5:body_region:0
To study the interaction of DTMS with HF/F , the cycling performance of the coin cell in the BE + 1000 ppm HF electrolyte and the 2 vol % DTMS-containing + 1000 ppm HF electrolyte was analyzed (Fig. 6a). A significant capacity loss was observed after 40 cycles in the case of the
#016 | page 5 | Docling页内原序 7 | 新页内顺序 7 | layout_order 74 | front_matter / column_2_of_2 | p5:body_region:1
BE + 1000 ppm HF electrolyte: from 246.4 to 60.3 mAh g 1 . However, the discharge capacity in the 2 vol% DTMS-containing + 1000 ppm HF electrolyte changed from 240.3 to 190.6 mAh g 1 . DTMS can effectively suppress the damage to the cathode by HF and improve battery cycle stability. Fig. 6b and c shows the F 1s XPS spectra of the LRM electrodes in the BE + 1000 ppm HF and 2 vol% DTMS + 1000 ppm HF electrolyte. The LiF and Me -F peak intensities are much higher in the BE + 1000 ppm HF electrolyte than in the 2 vol% DTMS-containing + 1000 ppm HF electrolyte. The addition of DMTS could inhibit the fluoride formation.
#017 | page 5 | Docling页内原序 8 | 新页内顺序 8 | layout_order 75 | bottom_margin / column_2_of_2 | p5:body_region:1
NMR spectra are used for analyzing the composition changes after storage for 24 h in the electrolyte upon the addition of HF [32] (Fig. 7). A pair of peaks at 75 ppm can be found for all electrolytes, which are assigned to PF6 [25]. Unlike the BE (Fig. 7a) and DTMS-containing electrolytes (Fig. 7b), the BE + 1000 ppm HF electrolyte shows three additional peaks (Fig. 7c). The pair of weak peaks at 85 ppm is
#018 | page 6 | Docling页内原序 4 | 新页内顺序 4 | layout_order 80 | page_body / column_1_of_2 |
Fig. 7. 19 F NMR spectra of BE and DTMS-containing electrolytes before (a and b) and after (c and d) 1000 ppm HF was added.
#019 | page 6 | Docling页内原序 5 | 新页内顺序 5 | layout_order 81 | bottom_margin / column_1_of_2 |
assigned to PO2F2 formed from the partial hydrolysis of LiPF6 [25], and the peak at 190 ppm corresponds to HF. However, the HF peak intensity for the 2 vol% DTMS-containing + 1000 ppm HF electrolyte is lower than that for the BE + 1000 ppm HF electrolyte (Fig. 7c and d). In addition, a
#020 | page 6 | Docling页内原序 6 | 新页内顺序 6 | layout_order 82 | bottom_margin / column_2_of_2 |
new small peak at 162 ppm corresponding to the BE + 2 vol%DTMS containing 1000 ppm of the HF electrolyte is shown in Fig. 7d, which can be attributed to the reaction between DTMS and HF/F .Supplementary Material 3 presents the 19 F NMR spectra of the DTMS-containing
#021 | page 7 | Docling页内原序 4 | 新页内顺序 3 | layout_order 86 | front_matter / column_1_of_2 | p7:body_region:0
electrolytes collected from the LRM/Li cells after evaluating their cycling performance. In them, the peak at 162 ppm corresponding to the products of the reaction of DTMS with HF/F disappears. Combined with the Si 2p XPS results, this demonstrates that DTMS is involved in film formation on the cathode.
#022 | page 7 | Docling页内原序 6 | 新页内顺序 4 | layout_order 87 | front_matter / column_1_of_2 | p7:body_region:0
The possible DTMS reaction on the interface of the cathode is shown in Fig. 8. We hypothesize that the Si -O bond can react with HF, Lewis acids, and EC [28,33].
SECTION | page 7 | Docling页内原序 7 | 新页内顺序 5 | layout_order 88 | body_zone / column_1_of_2 | p7:body_region:0
4. Conclusions
#023 | page 7 | Docling页内原序 8 | 新页内顺序 6 | layout_order 89 | body_zone / column_1_of_2 | p7:body_region:0
In conclusion, the cycling performance of the LRM cathode can be greatly improved by adding DTMS. The capacity loss decreased from 57.2% to 25% at 0.5C after 100 cycles. Experimental results show that DTMS is preferentially oxidized on the LRM cathode surface to form a more stable CEI layer with Si -O and Si -F bonds, and that it also reacts with the HF/F from the electrolyte, meaning that it is effective for suppressing metal dissolution and enhancing the stability between the electrolyte and cathode.

正文 block 表

#pageDocling 页内原序新页内顺序global layout orderzonecolumnregionbboxtext
11181918body_zonecolumn_1_of_2p1:body_region:0[37.59, 509.71, 253.44, 132.83]Lithium ion batteries (LIBs) have been used in electric vehicles because of their high energy density, safety, and low price; however, these qualities need to be further enhanced to extend the maximum distance that electric vehicles can travel before needing to be recharged [1 -3]. Many novel and advanced types of cathode materials have been explored and had their potentials gauged to meet the requirements of a high cell energy density [4]. Lithium-rich layered oxide (LRM), xLi2MnO3 ⋅ (1-x)LiMO2 (M = Ni, Co, Mn) has attracted considerable attention as the most promising alternative for LIBs, due to its high reversible discharge capacity (over 250 mAh g 1 ) and high range of operating voltage (3.0 -4.8 V) [5 -8]. However, its application is limited by the poor cycling and rate performance of LRM, which leads to the destruction of the cathode material structure and an unstable
21222524body_zonecolumn_2_of_2p1:body_region:1[306.59, 488.79, 125.16, 7.31]electrode/electrolyte interface [9].
31232625body_zonecolumn_2_of_2p1:body_region:1[306.59, 499.22, 253.42, 143.32]To overcome these problems, several approaches have been explored in the past decade, including doping and coating [10 -13]. Recently, a simple and economical strategy has been developed: the formation of a protective interphase on the cathode through the preferential oxidation of additives ( < 5 wt%) added to the electrolyte. These additives have a higher highest occupied molecular orbital than solvents. This ensures that the electrolyte decomposition products do not react with the protective cathode interphase, resulting in the maintenance of interface stability. A variety of electrolyte additives with different molecular structures have been proposed. Tris(trimethylsilyl)phosphate [14,15] has been used as a film-forming additive on lithium-rich cathode materials to improve the electrochemical performance. Tris(trimethylsilyl) borate forms a modified solid electrolyte interphase (CEI) on the cathode, which reduces the capacity fading of a Li[Li0.2Mn0.54Ni0.13Co0.13]
423328top_margincolumn_1_of_2p2:body_region:0[37.59, 55.48, 253.45, 289.75]O2/Li cell from 81% to 26% after 200 cycles [16]. Lan et al. reported [17] that the electrode capacity retention in an electrolyte without any additive was 40%, which is much lower than the 72% observed in an electrolyte with bis(trimethylsilyl)carbodiimide. The capacity retention of Li1.2Mn0.54Ni0.13Co0.13O2 cathodes was found to increase in an electrolyte with 1 wt% diphenyl disulfide [18]. After 150 cycles, the capacity fading of Li1.2Mn0.54Ni0.13Co0.13O2 was found to decrease from 27.4% in an electrolyte without any additive to 8.8% an electrolyte with 1% 1,3,6-hexanetricarbonitrile [19]. The cycling stability of Li1.2Mn0.525Ni0.175Co0.1O2 cathodes was improved by using 5 wt% di-(2, 2,2 trifluoroethyl) carbonate in the electrolyte, and as a result, the capacity fading decreased from 30% to 11% after 50 cycles [20]. Cha et al. [21] investigated Li-rich/graphite full cells with 1 wt% lithium difluoro (oxalate)borate (LiDFOB) in 1.3 M LiPF6 containing an EC:EMC:DMC electrolyte at a volume ratio of 3:4:3. LiDFOB optimizes the surface composition of both the graphite anode and Li-rich cathode. A stable CEI film was produced on the Li[Li0.2Mn0.56Ni0.16Co0.08]O2 electrode with the presence of the decomposition products of tri(hexafluoro-iso-propyl) phosphate (HFiP). The capacity loss for a Li[Li0.2Mn0.56Ni0.16Co0.08]O2 electrode in an electrolyte with 1% HFiP after 130 cycles was shown to be reduced from 35.5% to 26.7% [22]. Triphenyl phosphite (TPPi) was found to preferentially oxidize over the solvent at an oxidation potential of 4.2 V (vs. Li/Li + ), and the TPPi-derived layer can effectively inhibit electrolyte decomposition [23]. Tu et al. reported that TEP reacted with active oxygen and formed a protective layer that suppressed electrolyte decomposition and the structural destruction of the LRM [24]. Triethyl borate and tripropyl borate have been reported as electrolyte additives that improve the self-discharge property of LRM cathodes [25].
524429body_zonecolumn_1_of_2p2:body_region:0[37.59, 348.41, 253.44, 90.99]Some studies have reported that the improvement of the electrochemical behavior of NCM622-based cells and LNMO-based cells are a result of silicon-based electrolyte additives [26 -28]. In this paper, 1, 3-divinyltetramethyldisiloxane (DTMS) was used as an additive to enhance the electrochemical properties of a Li-rich layered oxide cathode (LRM). Results showed that 2 vol% DTMS effectivity decreased capacity loss of LRM/Li cell from 57.2% to 25%. The possible mechanism for this was investigated further though electrochemical and physical analyses.
627732body_zonecolumn_1_of_2p2:body_region:0[37.59, 494.97, 253.43, 101.48]The LRM cathode was composed of 80 wt% LRM (LRM300, Ningbo Li-rich Battery Material Technology Co., Ltd., China), 10 wt% polyvinylidene fluoride (PVDF) binder, and 10 wt% acetylene black in N -methyl-2-pyrrolidone. The slurry was coated on Al foil, and then vacuum dried at 100 ◦ C for 12 h. The CR2025-cell was fabricated in an Arfilled glove box with a Li sheet as the anode and Celgard 2325 as the separator. The base (BE) electrolyte contained 1 M LiPF6 and included EC/EMC/DMC (1:1:1, in weight). DTMS (Aladdin Co., Ltd., China) was then added into the BE electrolyte. Electrolytes with 2 vol% DTMS were used (Supplementary Material. 1).
728833body_zonecolumn_1_of_2p2:body_region:0[37.59, 599.57, 253.44, 38.72]A total of 1000 ppm of hydrofluoric acid (HF) was then added into the BE and BE + 2 vol%DTMS electrolytes to prepare HF-containing electrolytes using a 40 wt% HF aqueous solution [25]. All electrolytes were prepared in an Ar-filled glove box.
82101035bottom_margincolumn_1_of_2p2:body_region:0[37.59, 673.32, 253.45, 70.07]The charge -discharge performance of the cells was evaluated using a computer-controlled test system (CT2001A, China). The LRM/Li cells were pre-cycled in the following schedule: 0.1C (1C = 300 mA g 1 ) for three cycles and 0.2C for three cycles at 25 ◦ C between 2.8 and 4.8 V. The LRM/Li cells were then operated for 100 cycles at 0.5C to analyze the cycling performance. The rate capability of the cells was evaluated at a 0.5-1-2-3-5C charge/discharge current. The electrochemical
92121237front_mattercolumn_2_of_2p2:body_region:1[366.12, 65.88, 134.12, 16.16]/Li) of EC, DMC, EMC, and DTMS.
102131338front_mattercolumn_2_of_2p2:body_region:1[306.59, 153.91, 253.39, 28.23]impedance spectroscopy (EIS) was employed in the frequency range of 10 5 to 0.1 Hz with an amplitude of 5 mV, using a frequency response analyzer (VSP, Bio-logic).
112151540body_zonecolumn_2_of_2p2:body_region:1[306.6, 218.02, 253.4, 80.56]To understand the influence of DTMS on the cycling performance of LRM/Li cells, scanning electron microscopy (SEM; S-4800, Hitachi), transmission electron microscopy (TEM; JEM-2010, JELO), XRD analysis (XRD; Bruker D8 ADVANCE) using Cu Ka radiation, X-ray photoelectron spectroscopy (XPS; ESCALAB 250Xi), and 19 F nuclear magnetic resonance ( 19 F NMR; AVANCE III 400 MHz) analyses were carried out. The cycled electrodes (LRM and Li) were disassembled, rinsed with dimethyl carbonate solvent, and dried under vacuum.
122171742body_zonecolumn_2_of_2p2:body_region:1[306.6, 334.41, 253.4, 38.72]The Gaussian 09 software package was used for theoretical calculations. The equilibrium structures were determined using the B3LYP/6311G(d,p) level [28]. The oxidation potential (Eox) was obtained as follows[28]:
132181843body_zonecolumn_2_of_2p2:body_region:1[306.6, 380.54, 236.56, 9.34]Eox (Li + /Li) = [G(M + ) - G(M)]/F - 1.4 V
142212146body_zonecolumn_2_of_2p2:body_region:1[306.6, 460.54, 253.42, 166.47]The as-calculated oxidation potential and Li + binding affinity (Eb) are often used to forecast the oxidation tendency of an additive on the cathode surface [29,30]. The film-forming electrolyte additives have a lower oxidation potential than the electrolyte solvents. Therefore, the additives dominate the composition of the CEI film on the cathode. Furthermore, a low value of Li + Eb is suitable for the enrichment of the additive on the cathode surface [29]. The calculated Eox values of the solvents and DTMS are listed in Table 1. As per the theoretical calculation results, DTMS (5.58 V) has a lower Eox than EC (7.11 V), DMC (7.00 V), and EMC (6.99 V), indicating that DTMS has a lower oxidation stability than the electrolyte solvents. The optimized structures and solvent-Li + and DTMS-Li + Eb values are seen in Fig. 1. The Eb value of DTMS is lower than those of solvents. This indicates that the interaction between DTMS and Li + is weaker, so DTMS can easily accumulate at the cathode surface. DTMS may thus form a protective film at the positive electrode, as per the theoretical calculation results.
1556673bottom_margincolumn_1_of_2p5:body_region:0[37.59, 704.67, 253.41, 38.72]To study the interaction of DTMS with HF/F , the cycling performance of the coin cell in the BE + 1000 ppm HF electrolyte and the 2 vol % DTMS-containing + 1000 ppm HF electrolyte was analyzed (Fig. 6a). A significant capacity loss was observed after 40 cycles in the case of the
1657774front_mattercolumn_2_of_2p5:body_region:1[306.59, 586.33, 253.42, 93.22]BE + 1000 ppm HF electrolyte: from 246.4 to 60.3 mAh g 1 . However, the discharge capacity in the 2 vol% DTMS-containing + 1000 ppm HF electrolyte changed from 240.3 to 190.6 mAh g 1 . DTMS can effectively suppress the damage to the cathode by HF and improve battery cycle stability. Fig. 6b and c shows the F 1s XPS spectra of the LRM electrodes in the BE + 1000 ppm HF and 2 vol% DTMS + 1000 ppm HF electrolyte. The LiF and Me -F peak intensities are much higher in the BE + 1000 ppm HF electrolyte than in the 2 vol% DTMS-containing + 1000 ppm HF electrolyte. The addition of DMTS could inhibit the fluoride formation.
1758875bottom_margincolumn_2_of_2p5:body_region:1[306.6, 682.73, 253.42, 59.58]NMR spectra are used for analyzing the composition changes after storage for 24 h in the electrolyte upon the addition of HF [32] (Fig. 7). A pair of peaks at 75 ppm can be found for all electrolytes, which are assigned to PF6 [25]. Unlike the BE (Fig. 7a) and DTMS-containing electrolytes (Fig. 7b), the BE + 1000 ppm HF electrolyte shows three additional peaks (Fig. 7c). The pair of weak peaks at 85 ppm is
1864480page_bodycolumn_1_of_2[92.13, 673.38, 415.22, 8.36]Fig. 7. 19 F NMR spectra of BE and DTMS-containing electrolytes before (a and b) and after (c and d) 1000 ppm HF was added.
1965581bottom_margincolumn_1_of_2[37.59, 697.02, 253.41, 38.72]assigned to PO2F2 formed from the partial hydrolysis of LiPF6 [25], and the peak at 190 ppm corresponds to HF. However, the HF peak intensity for the 2 vol% DTMS-containing + 1000 ppm HF electrolyte is lower than that for the BE + 1000 ppm HF electrolyte (Fig. 7c and d). In addition, a
2066682bottom_margincolumn_2_of_2[306.59, 697.02, 253.42, 38.72]new small peak at 162 ppm corresponding to the BE + 2 vol%DTMS containing 1000 ppm of the HF electrolyte is shown in Fig. 7d, which can be attributed to the reaction between DTMS and HF/F .Supplementary Material 3 presents the 19 F NMR spectra of the DTMS-containing
2174386front_mattercolumn_1_of_2p7:body_region:0[37.59, 189.96, 253.44, 49.15]electrolytes collected from the LRM/Li cells after evaluating their cycling performance. In them, the peak at 162 ppm corresponding to the products of the reaction of DTMS with HF/F disappears. Combined with the Si 2p XPS results, this demonstrates that DTMS is involved in film formation on the cathode.
2276487front_mattercolumn_1_of_2p7:body_region:0[37.59, 242.23, 253.43, 28.23]The possible DTMS reaction on the interface of the cathode is shown in Fig. 8. We hypothesize that the Si -O bond can react with HF, Lewis acids, and EC [28,33].
2378689body_zonecolumn_1_of_2p7:body_region:0[37.59, 305.72, 253.42, 80.56]In conclusion, the cycling performance of the LRM cathode can be greatly improved by adding DTMS. The capacity loss decreased from 57.2% to 25% at 0.5C after 100 cycles. Experimental results show that DTMS is preferentially oxidized on the LRM cathode surface to form a more stable CEI layer with Si -O and Si -F bonds, and that it also reacts with the HF/F from the electrolyte, meaning that it is effective for suppressing metal dissolution and enhancing the stability between the electrolyte and cathode.