1. Introduction
Developing green and low-carbon renewable resources is an important strategy to achieve sustainable development. Increasing attention has been paid to the exploitation and utilization of clean renewable energy, such as solar energy, water energy, and wind energy. However, the output of these renewable resources is intermittent and particularly vulnerable to the effects of time, space, and seasonal climate changes, which can severely limit the stable operation of the electrical grids. To date, constructing various large-scale energy storage systems is an effective tactic to ameliorate this issue. Electrochemical energy storage, which mainly includes secondary battery technology, has attracted extensive attention due to its superiorities of flexibility and convenience, easy maintenance, high energy density, and reliable conversion efficiency [
1]. Therefore, lithium-ion batteries (LIBs) have been widely applied to various portable electronic devices since their commercialization [
2]. Especially in recent years, with the rapid development of the electric vehicle industry, the demand for LIBs has increased sharply. Nevertheless, the limited abundance in the earth’s crust and uneven geographical distribution of lithium resources result in the increasing cost of LIBs year by year, hindering their further application in the field of energy storage [
3]. In contrast, sodium-ion batteries (SIBs) have inexhaustible sodium resources and low cost, and their electrochemical reaction mechanisms are similar to those of LIBs [
4,
5]. Based on this, developing SIBs as an imperative alternative to LIBs has a positive significance for large-scale energy storage systems [
6,
7,
8,
9,
10].
The high-performance anode materials are essential for the large-scale commercialization of SIBs. Although the graphite anode has been successfully commercialized in LIBs, its sodium storage performance in SIBs is poor, mainly due to the larger radius of Na
+ and the instability of the sodium-graphite intercalation compounds [
11]. Therefore, most studies on anode materials for SIBs has turned to non-graphite carbon. Hard carbon (HC) has a higher Na storage capacity (>300 mAh g
−1) and lower Na storage potential (<0.1 V), and it is considered to be one of the most promising anode materials for SIBs [
12,
13,
14]. HC can be obtained by processing resource-rich biomass materials (sucrose [
11], coconut shell [
15], shaddock peel [
16], etc.) and natural polymers (polyvinylpyrrolidone [
17], polyvinyl chloride [
18], polyaniline [
19], etc.). According to an associated report, the HC anode can provide a sodium storage capacity comparable to the lithium storage capacity provided by the graphite anode [
12]. However, there are still some problems in such anode materials [
13]. The most prominent one is that HC materials show low initial Coulombic efficiency (ICE), meaning that large amounts of sodium ions are irreversibly consumed in the first cycle, which seriously diminish the energy density and cycling stability of the batteries [
13]. The limited ICE is mainly caused by two reasons. One is that the hard carbon material itself has a mass of defects and functional groups that can serve as active sites to irreversibly capture sodium ions. The other is that hard carbon materials have a high specific surface area, which can induce the continuous reaction of the electrolyte and the formation of disordered solid electrolyte interface (SEI) film, as well as some undesired side reactions [
13,
20]. To mitigate these issues, some well-thought-out strategies have been proposed, such as surface engineering, structural design and composition regulation, and so on [
13].
In surface engineering, surface coating technology is generally regarded as a serviceable method to ameliorate the ICE of hard carbon materials [
21,
22,
23]. The new versatile interface is committed to suppressing the decomposition of electrolytes by avoiding direct contact between the hard carbon surface and electrolytes, thus reducing adverse side reactions and promoting the formation of well-functioning SEI films. Carbon is often used as a remarkable coating material for the hard carbon anodes of SIBs by virtue of its excellent electrochemical stability and general applicability to common electrolyte systems [
13]. For example, Hu’s group [
24] successfully synthesized hard carbon with a soft carbon coating by pyrolyzing toluene, and the as-prepared material exhibits a relatively high ICE of 83%, while for the uncoated material, only 53%. Ponrouch et al. [
25] used a simple physical method to coat a carbon layer on the HC surface, which significantly improved the ICE from 55% to 70%. Recently, He et al. [
26] also increased the ICE to 94.1% by adding a soft carbon coating to the hard carbon surface. In addition, oxide coating has also been widely studied and applied in the field of new energy storage materials. Therefore, Al
2O
3 coating has been tipped to be available in both SIBs and LIBs to optimize electrochemical performance. Using atomic layer deposition (ALD), Lu et al. [
27] elaborately devised an Al
2O
3 artificial SEI-coated hard carbon anode of an SIB. The deposited Al
2O
3 film not only makes the electrode exhibit high capacity and superior cycling stability, but also improves the ICE from 67% to 75%. Lin [
28] also proved that ultrafine Al
2O
3 nanoclusters can cover the defects on the surface of carbon materials and effectively lessen the decomposition of electrolytes, thus promoting the generation of a thin and homogenous SEI. Recently, our group constructed an amorphous Al
2O
3 layer on a HC surface using an easy-operation coating method [
23], which remarkably improved the ICE of HC from 64.7% to 81.1%. The Al
2O
3 coating can reduce irreversible capacity loss by regulating the microscopic disorder of the HC surface. Furthermore, the homotype heterojunctions formed by HC and coating can induce the formation of an SEI with a regular distribution of organic and inorganic components. In the field of LIBs, Al
2O
3 coating is also considered to be capable of effectively reducing the irreversible consumption of electrode materials and the regeneration of SEI films [
29]. Besides, ZrO
2 coating also makes a considerable contribution to the almost unassailable position of LIBs. The electrochemical properties of a myriad of electrode materials, such as LiNi
0.8Co
0.1Mn
0.1O
2 [
30], Li
xCoO
2 [
31], LiNi
0.6Co
0.2Mn
0.2O
2 [
32], Li[Ni,Mn,Co]O
2 [
33], LiNi
1/3Co
1/3Mn
1/3O
2 [
34], Li[Ni
0.5Mn
0.3Co
0.2]O
2 [
35], and so on, have been improved in varying degrees with the optimization of a ZrO
2 coating. However, the research on ZrO
2 coating for SIBs is still in the blank stage, and there is no elaborate report about it at present. Therefore, it is with great foresight that we explore an appropriate method to construct a versatile ZrO
2 coating on the hard carbon anode surface of SIBs, which can be expected to reduce irreversible sodium ion adsorption and optimize the interface properties, in turn improving the ICE and cycling stability of electrode materials.
Herein, inspired by the extensive application of ZrO2 coating in LIBs, we coated the HC surface with a ZrO2 coating to prepare the HC@ZrO2 material, by using a facile liquid phase coating method. Unlike chemical or physical vapor deposition (CVD, PVD) and atomic layer deposition (ALD), which is commonly used in previous research requiring sophisticated equipment and unmanageable operation processes, the method we adopted only requires two simplified and feasible processes: aqueous phase coating and calcination. The well-designed ZrO2 coating can act as a physical barrier to prevent more active sites from being exposed to the electrolyte, thus reducing the uncontrolled decomposition of the electrolyte. At the same time, the ZrO2 coating can effectively inhibit the continuous destruction and regeneration of SEI, forming thinner SEI with lower electrochemical impedance, which facilitates the electrochemical reaction kinetics. The electrochemical performances of the as-prepared HC@ZrO2 electrodes are significantly enhanced with ICE as high as 79.2%, with excellent cycling performance. The capacity can maintain 82.6% under 1 A g−1 after 2000 cycles. In striking contrast, the ICE of pristine HC without coating is only 64.4%, and the cycling stability is inferior (a capacity retention of 55.8% under 1 A g−1 after 2000 cycles). This study has a certain enlightening effect and it can open up a new way to accelerate the commercial application of SIBs.
3. Results and Discussion
The ZrO
2 coating was constructed as a physical barrier of HC to reduce the occurrence of irreversible side reactions and excessive decomposition of the electrolyte, thus improving the ICE. The raw HC was obtained by a facile hydrothermal process followed by the carbonization of sucrose. Then, the obtained HC material was modified as HC@ZrO
2 according to the experimental steps described in
Figure S1 in the supplementary materials. To obtain the best-performing material, various HC@ZrO
2 materials with ZrO
2 and HC mass ratios of 0.5%, 1%, 1.5%, 3%, and 5% were synthesized, and each sample was named HC@ZrO
2-0.5, HC@ZrO
2-1, HC@ZrO
2-1.5, HC@ZrO
2-3, and HC@ZrO
2-5, respectively.
Figure 1 and
Supplementary Figure S2 exhibit the morphological characterizations of HC and HC@ZrO
2. As shown in the scanning electron microscope (SEM) (
Figure 1a and
Figure S2a) images, the uncoated hard carbon materials appear spherical or gourd shaped with a smooth surface and an average diameter of about 800 nm, which is consistent with the previous reports [
24]. It can be clearly observed from
Figure 1b–f that there is no significant change in the shape and size of HC after ZrO
2 coating, and only a light-colored and evenly distributed villiform coating appears on the surface, indicating an ultrathin ZrO
2 coating layer. With the increase of the ZrO
2 ratio, the surface coating was made thicker and thicker. Therefore, HC@ZrO
2-0.5 is covered with less ZrO
2 and even some smooth HC is exposed, while the material surface of HC@ZrO
2-5 is covered with a dense villiform coating layer, suggesting that this ZrO
2 coating is the thickest among all the samples, which can be more intuitively observed from
Figure S2b–f. To further figure out the composition of the HC surface coating, energy dispersive X-ray spectroscopy (EDX) was used in conjunction with SEM. According to scanning results of mapping (
Figure 1g), it is easy to observe that elements C, O, and Zr are evenly distributed on the HC surface, meaning that the ZrO
2 coating was successfully constructed.
The transmission electron microscopy (TEM) images were adopted to further observe the microstructure of HC and HC@ZrO
2-1. As shown in
Figure S3a and
Figure 1h, the surface of the original HC is very smooth, and after further magnification (
Figure S3b), it can clearly be seen that the sucrose-derived HC possesses a highly disordered structure. In contrast, TEM images of the modified HC@ZrO
2-1material show an obvious difference from HC (
Figure S3c and
Figure 1i,j). A distinctive coating appears on the surface of the HC@ZrO
2-1 material, which is evenly distributed on the HC surface, making its surface become rougher. The functionalized coating plays a crucial part in protecting defects and reducing irreversible capacity. Based on the results of selected area electron diffraction (SAED) in
Figure 1k, it can be concluded that the ZrO
2 coating’s own partial crystal structure, unlike the highly disordered structure of HC, can fill and shield the defects and active sites on the HC surface. In addition, a TEM-DES line scan of HC@ZrO
2-1 (
Figure 1l) shows that Zr content is highest at the edge of the carbon sphere and the subsequent distribution is uniform, indicating the uniform distribution of Zr on the HC surface, which echoes the EDS results. In brief, depending on the SEM and TEM, it is presumed that the ZrO
2 coating exists on the surface of the HC@ZrO
2 material and the thickness of the coating can be changed by controlling the value of the ZrO
2 content.
To further confirm the presence of ZrO
2, the HC and HC@ZrO
2 materials were characterized by X-ray diffraction (XRD). As depicted in
Figure 2a, pristine HC has two wide diffraction peaks of 22.3° and 43.6° at around 2
θ, and the peaks are assigned to (002) and (101) planes, respectively, demonstrating that HC has an amorphous structure [
22]. Moreover, the values of
d(002) and
d(101) can be calculated as 3.98 Å and 2.07 Å, respectively, by the Bragg equation. As for the XRD patterns of HC@ZrO
2, the wide peaks at 2
θ = 22.3° and 43.6° still exist, indicating that the construction of the ZrO
2 coating has no effect on the original HC crystal structure. However, with the increase of the ZrO
2 proportion, some distinct diffraction peaks appear at around 2
θ = 30.1°, 34.9°, 50.2°, 59.7°, 62.7°, and 73.9°, which can all be indexed from the standard pattern of ZrO
2 (JCPDS 49-1642). The layer spacing and corresponding crystal information are shown in
Supplementary Table S1. Combined with XRD and TEM analysis, it is confirmed that the liquid phase coating method can successfully coat the crystal-structured ZrO
2 on an HC surface without changing the intrinsic structure of HC. X-ray photoelectron spectroscopy (XPS) was used to further investigate the effect of the ZrO
2 coating on the HC surface, and
Figure 2b shows the full spectra of HC, HC@ZrO
2-1, and HC@ZrO
2-5. It is observed that unmodified HC has three obvious peaks, which belong to C 1s, O 1s and O KLL, respectively. With the ZrO
2 coating, C 1s, O 1s, and O KLL peaks still exist, and with the increase of the ZrO
2 ratio, the peak intensity of C 1s decreases, while the O 1s and O KLL peak intensities increase. In addition, the XPS spectra of HC@ZrO
2-1 and HC@ZrO
2-5 show Zr-related peaks corresponding to Zr 3s, Zr 3d, and Zr 3p, respectively [
36]. The peak intensity of HC@ZrO
2-5 is higher than that of HC@ZrO
2-1, suggesting that HC@ZrO
2-5 contains the most ZrO
2, which is consistent with SEM and TEM analyses. To explore the effect of the ZrO
2 coating on the HC specific surface area, the Brunauer–Emmett–Teller (BET) specific surface area test was performed on the HC and HC@ZrO
2-1 materials, and the results are summarized in
Table S2. According to the density functional theory (DFT) pore size distribution in
Figure 2c, it can be known that HC has abundant micropores with an average pore volume of 0.014 cm
3 g
−1 and an average pore size of 1.48 nm. Although the HC@ZrO
2-1 material is also dominated by micropores, the pore volume and pore size are larger, with an average pore volume of 0.022 cm
3 g
−1 and an average pore size of 3.87 nm. In addition, the results of the N
2 adsorption-desorption test (
Figure 2d) reveal that the specific surface area of HC is 17.84 m
2 g
−1, while the specific surface area of the modified HC@ZrO
2-1 material increases to 22.35 m
2 g
−1. The increase in specific surface area, pore volume, and pore size may be due to the large specific surface area of the ZrO
2 coating itself, although the irregularly shaped ZrO
2 can fill and shield the inherent defects and active sites of HC.
To provide insight into the effect of the ZrO
2 coating on the electrochemical properties, HC and HC@ZrO
2 were used as working electrodes to assemble half cells for galvanostatic charge and discharge. As can be seen from the initial charge-discharge curves at a current density of 50 mA g
−1 shown in
Figure 3a, the curves of HC@ZrO
2 and HC are basically the same in shape, with a sloped area and a platform area, which correspond to the typical electrochemical characteristics of HC in SIBs [
11,
37]. Simultaneously, this also proves that the ZrO
2 coating does not change the HC structure and sodium storage mechanism. Slightly different from the charge-discharge curve of HC, the ZrO
2 coating significantly reduced the irreversible voltage transition of HC, which is about 1.0 V, corresponding to the process of SEI formation and electrolyte decomposition [
38], representing that the electrolytic decomposition and SEI formation of HC and HC@ZrO
2 materials are different. The ZrO
2 coating can significantly inhibit the electrolyte decomposition reaction at ~1.0 V, thus cutting down the irreversible capacity in the initial charge-discharge process. The corresponding initial reversible capacities and ICE of the HC and HC@ZrO
2 materials are shown in
Table S3. It was noticed that the ICE of HC@ZrO
2 is higher than that of unmodified HC (ICE is 64.4%). Specifically, the ICE values of HC@ZrO
2-0.5, HC@ZrO
2-1, HC@ZrO
2-1.5, HC@ZrO
2-3, and HC@ZrO
2-1 are 77.3%, 79.2%, 75.2%, 72.8%, and 71.8%, respectively.
Figure S4 shows the cyclic voltammetry (CV) tests of HC and HC@ZrO
2-1. As can be seen from the profiles, all curves show a pair of reversible redox peaks at around 0.1 V, suggesting that the ZrO
2 coating does not change the internal structure of HC. In addition, HC shows an irreversible broad cathodic peak between 0.3 and 1.0 V, which is relative to the decomposition of the electrolyte and the formation of SEI. Surprisingly, the intensity of the corresponding peak in the HC@ZrO
2-1 curve is greatly reduced, suggesting that the ZrO
2 coating can effectively reduce the irreversible capacity by suppressing the electrolyte decomposition. To have an in-depth understanding of the influence of the ZrO
2 coating on electrolyte decomposition, differential capacity analysis was carried out on HC and HC@ZrO
2-1, and the results are shown in
Figure 3b. The plots of both pristine HC and HC@ZrO
2 show a pair of reversible redox peaks at around 0.1 V, which correspond to the intercalation behavior of Na
+ in HC [
27,
39,
40]. Furthermore, as can be seen from the insert of
Figure 3b, the peak intensities at ~0.53 V, ~0.71 V, and ~1.12 V decrease significantly after ZrO
2 coating, which further confirms that the ZrO
2 coating can effectively suppress the decomposition of the electrolyte and contribute to the in situ generation of a thin SEI at the HC–electrolyte interface, which is the reason why the HC@ZrO
2 materials can enhance ICE.
Figure 3c details the correlation between the ZrO
2 coating proportion and some specific electrochemical properties of the electrodes. For comparison, HC@ZrO
2-1 exhibits the highest ICE (79.2%), which is 14.8% higher than unmodified HC (64.4%). From the holistic perspective, with the increase of the ZrO
2 coating proportion, ICE increases first and then decreases, while the slope capacity decreases, and the platform capacity stays constant first and then decreases. With lower ZrO
2 content (<1%), ICE increases gradually, slope capacity decreases, and platform capacity remains unchanged, which can be attributed to the fact that the ZrO
2 coating effectively prevents direct contact between the electrolyte and HC surface active sites, significantly hindering the irreversible decomposition of the electrolyte [
13,
41,
42]. However, when the content of ZrO
2 continues to increase, all three indicators show a downward trend, which may be because too much ZrO
2 leads to a too-thick coating that sodium ions cannot enter smoothly. The ZrO
2 coating can effectively reduce sodium storage sites on the surface of HC that derived from defects and functional groups, and has no effect on sodium ion insertion behavior. Therefore, the continuous decrease in slope capacity can verify that sodium ions correspond to the “adsorption” mechanism in the HC slope region, while the lack of an obvious decrease in platform capacity indicates that sodium ions are subject to the “insertion” mechanism in the platform region [
43,
44].
To fully ascertain the effect of the ZrO
2 coating on electrochemical performance, we further compared the cyclic stability and rate performance of HC and HC@ZrO
2.
Figure 3d and
Figure S5a show the cyclic performance test at a current density of 50 mA g
−1. After 50 cycles, HC@ZrO
2-1 exhibits the best reversible capacity of 300.8 mAh g
−1 with an extremely high capacity retention rate. However, the capacities of HC@ZrO
2-3 (200.9 mAh g
−1) and HC@ZrO
2-5 (195.6 mAh g
−1) are both lower than that of HC (
Figure S5a), which may be attributed to the fact that too much ZrO
2 hinders the sodium ions intercalation, thus reducing the platform capacities. Accordingly,
Figure S5b shows the charge-discharge profiles for the selected cycles of HC and HC@ZrO
2-1. HC@ZrO
2-1 has lesser slope capacity, which indicates that the ZrO
2 coating can effectively reduce HC surface defects, thus reducing the irreversible sodium storage capacity. Simultaneously, the Coulombic efficiency of HC@ZrO
2-1 increases rapidly to 95.3% after the first cycle (79.2%), then remain stable at about 98% during the subsequent cycles, indicating that HC@ZrO
2-1 is capable of keeping a relatively complete structure during the long-term cycle.
Figure 3e,f and
Figure S5c show the rate properties of the HC and HC@ZrO
2 materials. Among them, HC@ZrO
2-1 shows the most outstanding rate performance, with a reversible capacity of 307.2 mAh g
−1 at 0.05 A g
−1. Even at the relatively high current density of 1.0 A g
−1, it is still able to deliver a reversible capacity of 88.6 mAh g
−1, while unmodified HC only has a capacity of 58.4 mAh g
−1, with a larger capacity fade (capacity retention rate is 18.4%). Subsequently, the galvanostatic charge and discharge of HC and HC@ZrO
2-1 at a high current density of 1 A g
−1 was performed to further figure out the optimization effect of ZrO
2 coating. It can be observed from
Figure 3g that after 2000 cycles, the HC@ZrO
2-1 material exhibits no obvious capacity fade with an outstanding capacity retention rate of 82.6%, which is far superior to pristine HC (the capacity retention rate is only 55.8%). The superior rate performance and cycle stability of HC@ZrO
2 can be attributed to the reasonable modification of the HC surface by the ZrO
2 coating. Based on the above various electrochemical data, it can be concluded that constructing an appropriate amount of ZrO
2 coating (the mass ratio of HC is 1%) on a hard carbon surface can prevent surface defects from irreversibly capturing sodium ions, and can inhibit the occurrence of some unprofitable side reactions. Additionally, as shown in
Table S4, compared to the published reports, the improvement of the ICE of the ZrO
2 coating on HC is more outstanding, and the preparation method is relatively facile.
To investigate the specific improvement of the ZrO
2 coating on the SEI, SEM examinations of the cycled HC and HC@ZrO
2-1 materials were utilized. As can be seen from
Figure 4a–c, the originally smooth HC surface becomes very rough in the full discharge state (0.01 V), indicating that a large number of SEI layers are generated. In particular, it can be seen more clearly that many thick and uneven SEI layers appear at the intersection of the two carbon spheres (
Figure 4c). The inferior SEI probably derives from the uncontrollable decomposition of the electrolyte and the occurrence of some uncertain side reactions. In sharp contrast, the surface of HC with a uniform ZrO
2 coating can remain in a relatively smooth state after cycling (
Figure 4d,e). Even where two carbon spheres meet, there is no noticeable SEI layer accumulation (
Figure 4f), meaning that the ZrO
2 coating can promote the formation of a thinner SEI. Electrochemical impedance spectroscopy (EIS) was performed to investigate the charge transfer kinetics and SEI evolution of HC and HC@ZrO
2 in more detail.
Figure 4g shows the EIS results of HC||Na and HC@ZrO
2||Na half cells in an initial open circuit voltage state. With the increase of ZrO
2 content, the electrode impedance increases gradually, which may be caused by the poor conductivity of ZrO
2 [
30]. A too-thick ZrO
2 layer can hinder the diffusion of sodium ions, which corresponds to the above conclusion that the platform capacity and specific capacity decrease due to too much ZrO
2. To avoid interference of counter electrodes, the interface properties of HC and HC@ZrO
2-1 were further studied by using a three-electrode setup, as shown in
Figure S6a. As can be observed from the EIS results of HC and HC@ZrO
2-1 discharged to 0.01 V, shown in
Figure 4h, both curves have similar shapes, including two semicircles at a high frequency, which are related to the interfacial impedance (
RSEI) and charge transfer resistance (
RCT), as well as an upward-sloping line representing the Warburg impedance at a low frequency, which is related to Na
+ diffusion in the electrode [
45]. Compared to the initial EIS, the plots of cycled electrodes show an extra feature semicircle, which also confirms the generation of the SEI. The EIS curves are fitted according to the equivalent circuit shown in
Figure S6b, and the results are summarized in
Table S5. The
RSEI and
RCT of pristine HC are 113.3 Ω and 61.7 Ω, while those of HC@ZrO
2-1 are reduced to 79.2 Ω and 58.2 Ω, respectively. In addition, combined with
Figure 4g,h, one can see that the impedance of cycled HC@ZrO
2-1 decreases significantly compared to that of the non-cycled anode. This is mainly because the ZrO
2-derived SEI is thin and uniform, with lower interfacial resistance and charge transfer resistance, which provides favorable conditions for the rapid migration of Na
+. The EIS results of HC and HC@ZrO
2-1 samples after different cycles are shown in
Figure S7. The
RSEI and
RCT of HC@ZrO
2-1 are always lower and change little after long cycles, while those of untreated HC are larger and increase with cycling, further indicating that the ZrO
2 coating can reduce the generation of the SEI, which is consistent with the results of SEM. Furthermore, the XPS was used to determine the effect of the ZrO
2 coating on the SEI components.
Figure 4i shows the XPS full spectra of the HC and HC@ZrO
2-1 electrodes discharged to 0.01 V. The spectrum of HC@ZrO
2-1 not only contains characteristic peaks of Na 1s, O KLL, F KLL, F 1s, O 1s, Na KLL, C 1s, and O 2s that can be observed in HC spectrum, but also shows the Zr 3d and 3p peaks, which also proves that ZrO
2 has been successfully coated on the HC surface [
33]. Compared to the XPS spectra of non-cycled HC and HC@ZrO
2-1 shown in
Figure 2b, the XPS spectra of the cycled anode in
Figure 4i show distinct F 1s, Na 1s, and O 1s peaks, meaning that the electrolyte has decomposed and the SEI that has organic and inorganic components has formed. Yet, it is worth noting that the peak intensities of the Na 1s, F 1s, and O 1s characteristic peaks of HC@ZrO
2-1 which mainly derived from the decomposition of EC/DEC solvents and NaPF
6 salts, are lower than that of HC, further verifying the SEM conclusion that the ZrO
2 coating can effectively inhibit the decomposition of the electrolyte. The high-resolution Zr 3d, F 1s, and O 1s spectra were fitted to obtain a more definite conclusion about the difference between the HC and HC@ZrO
2-1 SEI, as shown in
Figure 4j–l. According to the Zr 3d spectrum of HC@ZrO
2-1 in
Figure 4j, the characteristic peaks for Zr 3d
3/2 and Zr 3d
5/2 are observed at 183.4 eV and 181.2 eV, respectively, representing the Zr
4+ ions in ZrO
2 [
32]. In addition, the peak at 184.0 eV is related to the Zr-F bond, suggesting that the ZrO
2 on the HC surface can react with electrolyte decomposition products and thus improve the stability of the SEI [
28]. Both curves of F 1s show two peaks near 687 eV and 684.5 eV, which can be assigned to F-P and NaF, respectively, which are the main inorganic components of SEI [
27]. Additionally, the F 1s spectrum of HC@ZrO
2-1 also shows a characteristic peak at 685.9 eV, which can be assigned to Zr-F, indicating the existence of the ZrO
2 coating [
33]. Compared to HC, HC@ZrO
2-1 exhibits the weaker peak signal, suggesting that there are fewer inorganic components in the HC@ZrO
2-1 SEI. As we know, the NaF has poor ionic conductivity and excessive accumulation of NaF can severely hinder the diffusion of Na
+, so the reduction of NaF is very beneficial, which is in accordance with the EIS results [
46]. According to the O 1s spectra (
Figure 4l), both plots can be divided into three characteristic peaks, namely ROCO
2Na (535.4 eV), C=O (532.5 eV), and C-O (531 eV), which mainly arose from the reduction of organic solvent in the electrolyte [
46]. Except for these common peaks, the appearance of a Zr-O (530 eV) bond in the HC@ZrO
2-1 also proves the existence of the ZrO
2 coating. Similarly, the peaks in the HC@ZrO
2-1 show a lower intensity than HC. Therefore, combined with all of the above analyses, it can be concluded that ZrO
2 coating can successfully inhibit the reaction of electrolytes and promote the generation of a thinner SEI, in turn accelerating the electrochemical reaction kinetics and contributing to a better ICE, rate performance, and cycling performance of HC.