The XRD spectra of the samples are presented in Fig. 1a, where all spectral peaks of both samples align perfectly with those of standard anatase TiO2. Due to the low carbon ratio in TiO2@C, or its presence in an amorphous form, the characteristic peaks of carbon were not detected in the TiO2@C sample. In comparison to pure TiO2, TiO2@C exhibited lower crystallinity and broader diffraction peaks, which indicate a smaller grain size attributed to the effective suppression of carbon. Furthermore, the structural characteristics of the samples were analyzed using raman spectroscopy, as shown in Fig. 1b. In both samples, five distinct peaks were observed near 145, 203, 395, 521, and 635 cm − 1, corresponding to the typical raman vibration modes of TiO2 [26]. Additionally, two faint Raman peaks at 1599 and 1348 cm − 1 in the TiO2@C composite material were identified as the G and D peaks of carbon [27]. Figure S1 presents the TG-DSC curve of TiO2@C. The TG curve demonstrates a weight loss up to 300°C, which is primarily attributed to the vaporization of surface-adsorbed water. Following this, a rapid decrease in weight is observed between 300°C and 500°C, accompanied by a significant exothermic peak at 375°C, which is attributed to the combustion and elimination of carbon. The carbon content, as determined from the TG-DSC curve, is calculated to be approximately 7.9%.
The morphology of samples prepared through different processes was analyzed using SEM. Figure S2 illustrates the precursor, which displays an irregular shape characterized by several interconnected nanospheres (Figure S2a). Upon closer inspection, the precursor appears as a slightly rough spheroid with an approximate size of 500 nm (Figure S2b). Following heat treatment in various atmospheres, the overall morphology of the TiO2@C and TiO2 samples remains largely unchanged compared to the precursor (Figs. 2a, c). However, a subtle distinction in surface morphology is observed, with TiO2 exhibiting a relatively rougher surface due to the combustion of carbon during the precursor's heat treatment in an air atmosphere (Figs. 2b, d). This combustion effectively promotes the further growth of TiO2 grains, providing visual evidence for the inhibitory role of carbon in TiO2 grain growth. TEM was employed to investigate the internal structure of the TiO2@C composite material. As shown in Fig. 2e, the TiO2@C nanospheres possess a compact solid internal structure, indicating that the TiO2@C composite has a low specific surface area (SSA). Figure 2f presents HRTEM image of the TiO2@C,
revealing clear lattice fringes corresponding to the anatase TiO2 (101) crystal plane. Notably, amorphous carbon (shown as a white curved region) closely envelops the TiO2 without discernible boundaries, suggesting a potential co-existence process during the formation of the TiO2@C precursor. This co-existence process facilitates the persistent polymerization of 3-aminophenol and methanal around TiO2, with the resulting polymer effectively preventing the aggregation of primary TiO2 grains. The electron diffraction pattern depicted in Fig. 2g indicates that TiO2 within the TiO2@C sample exists in a polycrystalline state. Additionally, Fig. 2h displays the elemental distribution mapping for TiO2@C, revealing a uniform distribution of C, Ti and O elements within the composite.
Figure 3 illustrates the SSA and pore size of both samples. As shown in Fig. 3a, there is no discernible hysteresis loop in the nitrogen adsorption/desorption curves for either sample at relative pressures (P/P0) of 0.5 and 1.0, indicating that the SSA of TiO2@C and TiO2 is quite small. The SSA values for TiO2@C and TiO2 were determined to be 10.41 and 9.84 m² g⁻¹, respectively. Furthermore, Fig. 3b indicates that the pore sizes of TiO2@C and TiO2 are predominantly concentrated at 4.8 and 4.3 nm, respectively. The observed difference in pore sizes can be attributed to the inhibition of TiO2 grain growth by carbon during the heat treatment of the TiO2@C composite in an argon atmosphere. Such small SSA not only contribute to an increase in the tap density of the anode electrode material, thereby enhancing its volumetric energy density, but also significantly reduce the contact area between the active material and electrolyte. This reduction leads to a decrease in side reactions and an improvement in the ICE of the TiO2@C electrode.
Figure 4a presents the XPS full spectrum of both samples, indicating the presence of C, Ti and O elements on the surface of TiO2@C. Figure 4b illustrates the high-resolution XPS (HR-XPS) spectra of the Ti 2p for both TiO2@C and TiO2. The Ti 2p HR-XPS spectra of the TiO2 sample reveal a pair of peaks located at 463.9 and 458.2 eV, corresponding to the binding energies of 2p1/2 and 2p3/2 of Ti4+ [28]. In contrast, the Ti 2p HR-XPS spectra of the TiO2@C sample exhibit two pairs of peaks: a prominent pair at 464.8 and 458.9 eV, which correspond to 2p1/2 and 2p3/2 of Ti4+, and another pair at 463.8 and 458.2 eV, attributed to 2p1/2 and 2p3/2 of Ti3+ [29]. Notably, the binding energy of Ti4 + in the TiO2@C sample is higher, which can be ascribed to the presence of Ti3+. Figure 4c displays the O 1s HR-XPS spectrum of the TiO2@C sample, where three peaks can be fitted at 531.9, 530.2 and 529.9 eV, corresponding to the oxygen vacancy (O-Ti3+), O-C, and O-Ti4 + bonds, respectively [30]. The formation of O-Ti3 + in the TiO2@C may result from insufficient oxygen during heat treatment in an argon atmosphere. Previous studies have confirmed that the presence of O-Ti3 + not only enhances the intrinsic conductivity of TiO2 but also increases the active sites for lithium storage in TiO2@C composite materials [31]. Figure 4d illustrates the HR-XPS of C 1s in TiO2@C, where the two fitted peaks at 284.8 and 283.4 eV correspond to the binding energies of C-C/C = C and C-O bonds, respectively [32].
Through the analysis of the aforementioned test results, this paper proposes a surface-confined in-situ inter-growth mechanism for the formation of TiO2@C, as illustrated in Fig. 5. The experimental synthesis process described herein involves only three reactants: TBOT, methanal, and 3-aminophenol. Initially (Step I), due to the high concentration of NH3·H2O, TBOT rapidly hydrolyzes to form primary TiO2 grains, while NH4 + accumulate on its surface. Concurrently, methanal and 3-aminophenol undergo rapid polymerization to generate 3-aminophenol-methanal (3-APM) oligomers in the presence of NH4+, which subsequently accumulate around the primary TiO2 grains, resulting in the formation of high-density TiO2@3-APM microspheres. Subsequently (Step II), following thermal treatment under an argon atmosphere, TiO2@3-APM is transformed into TiO2@C with oxygen vacancies due to the absence of an oxygen source.
In the preparation of nano-TiO2, NH3·H2O solution is typically excluded because of its propensity to induce rapid hydrolysis of the titanium source, leading to significant particle aggregation of TiO2. In contrast, the synthesis method presented in this paper strategically leverages the rapid hydrolysis properties of the titanium source, facilitating the formation of a micro-environment on the TiO2 surface that triggers the polymerization of 3-aminophenol with methanal. The advantages of this approach are as follows: The technical route is straightforward, time-efficient, and does not require precise control, thereby enhancing its feasibility for commercial preparation; The micro-environment created around the primary TiO2 promotes a close association between TiO2 and 3-APM oligomers, which is essential for the subsequent thermal treatment aimed at achieving a highly integrated carbon and TiO2 structure.
The electrochemical behavior of TiO2@C electrode was investigated using CV, with the result presented in in Fig. 6a. During the initial discharge process, the CV curve reveals a broad reduction peak between 1.75 and 1 V, indicative of the initial Li + insertion into TiO2@C and the formation of the solid electrolyte interphase (SEI) [33]. Subsequently, during the charging process, the Li + extraction potential is observed to be approximately 2.2 V. In the subsequent cycles, the CV curves demonstrate a notable overlap, with the Li + insertion potential shifting towards a higher value. This observation suggests that the TiO2@C electrode has undergone a degree of activation, exhibiting excellent electrochemical reversibility and structural stability. The discharge/charge curves for both electrodes during the first three cycles at a current density of 0.2 A/g are presented in Fig. 6b and Figure S3. The initial discharge specific capacities of the TiO2@C and TiO2 electrodes are 584.4 and 368.2 mAh/g, respectively. Correspondingly, the initial charge specific capacities are 438.3 mAh/g for TiO2@C and 272.4 mAh/g for TiO2. The ICE for TiO2@C and TiO2 electrodes are 75% and 74%, respectively, surpassing those reported in previous studies (Fig. 6c) [16, 20, 23, 34–36]. These results demonstrate that the experimental approach employed in this study effectively enhances the ICE of the electrode by minimizing their SSA. The discharge/charge curves of both the TiO2@C and TiO2 electrodes over the subsequent two cycles exhibit a significant degree of overlap, indicating the high reversibility of these electrode materials during the Li + insertion and extraction processes. Furthermore, the reversible specific capacity of the TiO2@C electrode is approximately 1.6 times greater than that of the TiO2 electrode. This enhancement can be attributed to the intimate connection between TiO2 and carbon within the TiO2@C composite, which facilitates the full participation of the TiO2 active material. Additionally, the presence of oxygen vacancies provides extra Li + storage active sites. Figures 6 (d, e) illustrate the cyclic and rate performance of both electrodes. As depicted in Fig. 6d, both electrodes demonstrate remarkable cyclic stability, with only a slight decrease in reversible specific capacity during the initial cycles. The reversible specific capacities recorded during the second cycle for the TiO2@C and TiO2 electrodes are 466.4 and 287.5 mAh/g, respectively. After 200 cycles, the reversible specific capacities are maintained at 426.8 and 275.9 mAh/g, respectively. The capacity retention rates for the TiO2@C and TiO2 electrodes, relative to their second cycle capacities, are 91.5% and 95.6%, respectively. Notably, the TiO2 electrode exhibits a superior capacity retention rate compared to the TiO2@C electrode, which may be attributed to the TiO2 electrode undergoing stronger activation during repeated charge and discharge cycles, thereby enabling more TiO2 active sites to participate in Li+. As the current density increases, the reversible specific capacities of both the TiO2@C and TiO2 electrodes exhibit a gradual decline, as illustrated in Fig. 6e. The average reversible specific capacities of the TiO2@C electrode at current densities of 0.1, 0.2, 0.5, 1.0, 2.0, and 5.0 A/g are 512.9, 468.2, 417.4, 350.9, 299.1, and 210.1 mAh/g, respectively, which surpass those reported in previous studies (Fig. 6f) [20, 37–42]. Upon returning the current density to 0.1 A/g, the average reversible specific capacity is recorded at 511.8 mAh/g, indicating remarkable cycling reversibility. In contrast, the reversible capacity of TiO2 is only 124.3 mAh/g at a current density of 5.0 A/g, which is significantly lower than that of TiO2@C. This disparity suggests that the incorporation of carbon and the presence of oxygen vacancies considerably enhance the electrochemical kinetics of TiO2@C. The long-term cycling stability of the TiO2@C electrode, as demonstrated in Fig. 6g, confirms that it possesses an extended cycling life and stable coulombic efficiency. After 2000 cycles, the reversible specific capacity decreases from an initial value of 216.8 mAh/g to 203.8 mAh/g, resulting in an impressive capacity retention rate of 94%. This translates to a capacity decay rate of only 0.003% per cycle, indicating that the TiO2@C composite maintains exceptional structural integrity.
The electrochemical kinetics of TiO2@C and TiO2 electrodes were investigated using EIS and GITT, with the results presented in Fig. 7. The EIS data indicate that the TiO2@C electrode exhibits reduced charge transfer resistance (Rct), as shown in Fig. 7a. Figure 7b illustrates the GITT curves for both electrodes. The diffusion rates of Li + during the charge and discharge processes were calculated using the following equation: [30]. The diffusion rates of Li+, depicted in Figs. 7c and 7d, indicate that the TiO2@C electrode achieves a diffusion rate ranging from approximately 10 − 9 to 10 − 10 cm² s − 1, which is significantly higher than that of the TiO2 electrode. By integrating the findings from the EIS and GITT tests, it can be concluded that the optimal composite structure of TiO2 with carbon, coupled with the presence of oxygen vacancies, collectively enhances the electrochemical kinetics of the TiO2@C electrode, thereby resulting in superior electrochemical performance.