1. Introduction
The development of modern energy storage systems is undoubtedly a consequential part of the implementation of carbon-neutral strategies in response to the current environmental situation. Lithium-sulfur (Li-S) batteries are one of the most promising expected candidates due to their high energy density (2600 Wh kg
-1) and high theoretical capacity (1675 mAh g
-1)[
1,
2]. Additionally, sulfur is extremely rich in the earth, nonpoisonous, and eco-friendly [
3]. Nevertheless, there are still obstructs in the way of practical commercial application. (i) Sulfur and Li
2S have poor electrical conductivity and the insulating properties render it more difficult to transport ions and electrons; (ii) the cathode will be seriously damaged by the significant volume expansion due to the density difference between sulfur and Li
2S. (iii) The intermediate polysulfides (LiPSs) dissolving in the organic electrolyte will shuttle between the anode and cathode during the reaction process, and this undesirable shuttle effect is not conducive to the full utilization of active material sulfur [
4]. This undesirable irreversible side reaction is not beneficial to the maximum utilization of active material sulfur. Moreover, the sluggish conversion kinetics between interface redox kinetics from LiPSs to Li
2S results in a disappointing decay rate of capacity and electrochemical polarization [
5].
To solve the above problems, most research focused on the design of the functional sulfur host [
6,
7], appropriate separator modification [
8,
9], and electrolyte optimization [
10,
11]. Among them, modifying separator is a facile strategy to seek a good cycle lifespan of Li-S batteries, and the ideal separators can effectively fix the LiPSs on the side of the cathode to prevent them from reacting with the lithium anode [
12,
13]. Simultaneously, the functional layer can also serve as the second current collector to ensure the fast transmission of electrons and act as a storage for LiPSs. Among the various adjustments made to the separator, carbon materials are a major focus due to the high electrical conductivity and the enhanced wettability of electrolytes [
14]. Carbon materials, such as conductive carbon nanotubes (CNTs) [
15], porous carbon, and carbon nanofiber (CNFs) [
16], can effectively reduce the internal interface impedance and charge transfer resistance, improve the Li
+ diffusion kinetics [
17]. However, single non-polar carbon material modified separator cannot fully inhibit the shuttle effect relying solely on weak physical adsorption or electrostatic interaction [
18]. Polar materials, such as transition metal compounds, produce robust polar chemical interaction on LiPSs and can catalyze the conversion of LiPSs to increase the reaction kinetics of Li-S chemistry [
19]. Therefore, the reasonable combination of polar metal oxides, carbides, nitrides, and sulfides with carbon-based materials has shown outstanding properties and become a popular choice in the field of sulfur host design or separator modification of Li-S batteries [
20,
21,
22,
23]. Fe
3C with the advantages of low price, simple preparation, high conductivity, strong polarity, and remarkable electrochemical catalysis ability make it excellent in the field of LiPSs catalysis. Li et al. synthesized a Janus electrode comprising Fe
3C nanoparticles as active catalytic sites, and the electrode displays synergistic dual adsorption–electrocatalysis function, which can assuage shuttle effect by facilitating the kinetics of redox reactions from the soluble LiPSs to the insoluble LiPSs efficiently [
24].
Two-dimensional (2D) materials, such as graphene (GN) and MXene, are seen as a high-quality option for electrochemical energy storage study [
25,
26,
27], due to excellent ductility, high specific surface area, and exceptional electrical conductivity [
28]. Besides, the unique 2D structure can not only provide a great quantity of ion transport channels in the electrochemical kinetics process but also act as a physical barrier for LiPSs. Therefore, it will be highly promising to compound Fe
3C with 2D material GN to achieve the dual physical/chemical adsorption of polysulfide and enhanced redox reaction kinetics.
In this work, we prepared a novel Fe
3C decorated folic acid-derived GN-like N-doped carbon sheet (Fe
3C@N-CS) as the LiPSs catalyst to modify the separator of Li-S batteries. After the hydrothermal method, freeze-drying, and calcination process, the folic acid produces a GN-like structure with interconnected porous lamellar structures with high specific surface area to ensure generous ion migration channels (
Figure 1). More importantly, the barrier produced by self-inter-stacking can also serve as a physical barrier to enhance the efficiency of LiPSs capture. The well-dispersed polar Fe
3C nanoparticles on the nanosheet assure abundant chemical adsorption and active catalytic sites to enhance the reaction kinetics of the LiPSs by catalyzing the redox conversion. Profiting from the synergy efficiency of chemisorption and catalytic properties of Fe
3C and the physisorption of highly conductive 2D carbon nanosheets, the Li-S batteries with Fe
3C@N-CS modified separators demonstrated brilliant specific capacity with an excellent capacity of 1260 mAh g
-1 at 0.2 C and outstanding cycling stability with 0.06% capacity decay per cycle at 1 C over 500 cycles. Even at a high sulfur loading of 4.0 mg cm
-2, the batteries still accomplish exceptional cycle stability and rate performance.
3. Results and discussion
The microstructure of samples is observed by scanning electron microscope (SEM). Untreated folic acid shows the agglomeration morphology at the micron level (
Figure S1a,b). After the calcination, the folic acid-derived carbon exhibits two-dimensional carbon nanosheet characteristics as well as GN-like layering and wrinkle structure (
Figure 2a and
Figure S2). The SEM images of Fe
3C@N-CS (
Figure 2b,c) demonstrate that the crinkled and lamellar microstructure is perfectly inherited, and the surface of the lamellar sheet becomes rougher. At the same observation scale, the Fe
3C@N-CS lamellar structure with a unique interconnected porous structure provides more active site exposure as well as an increased contact interface with LiPSs (
Figure S3).
The transmission electron microscope (TEM) images (
Figure 2d,e) also reveal the typically GN-like unilateral and wrinkle-layered structure of Fe
3C@N-CS, which offers rich channels for ion migration. (
Figure S4). The lattice spacing of 0.47 nm can be measured under high-resolution TEM (HRTEM), which corresponds to the (001) crystal plane of Fe
3C (
Figure 2f). The circled part shows the graphitized lattice streaks of carbon catalyzed by Fe at high temperature [
29,
30]. The high-angle annular dark field SEM (STEM-HAADF) image (
Figure 2g) and EDS mapping of Fe
3C@N-CS (
Figure 2h) show that the folding characteristics of the signal-layer two-dimensional structure and the uniform distribution of the characteristic elements (Fe, O, N, C) constituting the Fe
3C@N-CS. X-Ray diffractometer (XRD) characterization results reveal the material composition of Fe
3C@N-CS and N-CS (
Figure 3a).
The diffraction peaks of as-prepared Fe
3C are almost in agreement with Fe
3C (PDF#85-0871), demonstrating the successful synthesis of Fe
3C [
24].
Figure 3b shows that the Fe
3C@N-CS modified separator can restore the original shape without the slag phenomenon after folding, which shows good flexibility for practical application. In the cross-sectional SEM image (
Figure 3c), the Fe
3C@N-CS modified separator shows that the thickness of the Fe
3C@N-CS functional layer is about 7.63 μm, and the average mass loading on each separator is only 0.16 mg cm
-2, which is beneficial to improve the mass-energy density of the battery. The contact angle test is used to evaluate the wetting condition of the different separators to the electrolyte. After dropping the electrolyte for 5 s, the electrolyte permeates fast into the Fe
3C@N-CS modified separator, and the contact angle is about θ=2.48°. In comparison, the traditional PP separator shows a contact angle of θ=48.48°. The excellent hydrophilic property allows fast ion diffusion across the Fe
3C@N-CS modified separator.
X-Ray Photoelectron Spectrometer (XPS) is carried out to measure the chemical state and composition of samples.
Figure S4 shows that the Fe
3C@N-CS consisted of Fe, O, N, and C. In the HRXPS spectra of Fe 2p, there are four peaks (
Figure 4a) which can be distinguished at 709.3 eV, 714.04 eV, 722.2 eV, and 725.92 eV. The four peaks can be assigned to Fe
2+ and Fe
3+ [
24]. In the C 1s HRXPS spectrum of Fe
3C@N-CS (
Figure 4b), the peaks corresponding to C=C/C–C, C, C–N, and -C=O bonds are observed at 283.08 eV, 284.23 eV, 286.78 eV, and 290.08 eV, respectively [
31]. The presence of C-N bond indicates the successful doping of nitrogen in carbon. The N 1s HRXPS spectrum can be fitted to four components corresponding to pyrrole-N (397.33 eV), pyridine-N (396.58 eV), graphite-N (399.28 eV), and C-N (403.73 eV) (
Figure 4c) [
32]. In the O 1s HRXPS spectrum (
Figure 4d), oxygen vacancy, lattice oxygen, and hydroxyls species are detected at 531.53 eV, 530.63 eV, and 529.43 eV, respectively [
32]. The abundant oxygen vacancies can provide active sites during redox reactions, which is beneficial for anchoring and conversion of LiPSs.
To evaluate the effect of Fe
3C@N-CS modified separator on the electrochemical performance of Li-S batteries, simple S/CB composites were used as sulfur cathode materials to estimate the electrochemical performance. The cycle performance at 0.2 C (
Figure 5a) shows that the cell with Fe
3C@N-CS modified separator delivers a high initial discharge capacity of 1260 mAh g
-1, coinciding with 75.2 % of the theoretical capacity of sulfur, which shows much more stable performance than the cells with N-CS modified separator and PP separator. The galvanostatic charge/discharge curves in
Figure 5b shows that the cell with Fe
3C@N-CS modified separator possesses longer plateaus and lower overpotential (ΔE) than others, proving the reduced electrochemical polarization and the rapid reaction kinetics of LiPSs. At 1 C (
Figure 5c), the cycle performance of the cell with Fe
3C@N-CS modified separator is still prominent, compared with the cells with N-CS modified separator and normal PP separator. For the long-term cycle of 1 C (
Figure S5), the initial capacity of the cell with Fe
3C@N-CS modified separator exhibits excellent cycling performance with a high capacity of 890 mA h g
-1 and low average capacity decay rate per cycle of only 0.06% after 500 cycles. The cycle stability of the batteries is revealed by the slight changes in the charging and discharging platform of the galvanostatic charge-discharge curve at 1 C for 150 cycles (
Figure S6). The rate performance (
Figure 5d) of the cells with various separators shows that the cell with Fe
3C@N-CS modified separator delivers higher reversible specific capacities of 1158.93, 878.1, 757.7, 641.7, and 464.86 mAh g
-1 at 0.2, 0.5, 1, 2, and 4 C, respectively than that using N-CS and PP separator, which can be attributed to the excellent catalytic effect of Fe
3C and rich defect sites caused by N doping. The galvanostatic charge/discharge curves of the initial cycle from 0.2 C to 4 C are displayed (
Figure 5e), and the polarization potential increases gradually with the increase of current density, even up to a high current density of 4 C, two typical discharge platforms can also maintain, indicating the effective transformation of sulfur species.
Figure 5f shows the electrochemical impedance spectroscopy of cells with different separators, and the profiles consist of a semicircle and a slope line, which correspond to the charge transfer resistance (R
ct) and the Warburg impedance, respectively. As expected, the R
ct of the cell with Fe
3C@N-CS modified separator is lower than that of PP and N-CS separators owing to the abundant electron migration channels provided by highly graphitized 2 D conductive plane produced by the catalytic action of iron [
33].
To evaluate the potential of practicality, the rate performance of the cells with Fe
3C@N-CS modified separator under high sulfur loading of 4 mg cm
-2 was evaluated and shown in
Figure 5g,h. Under the condition of high sulfur load and high current density, a relatively regular charging and discharging platform is still maintained. The cell with the Fe
3C@N-CS modified separator still exhibits the reversible capacity of 1095.8, 809.31, 713.22, 582.33, and 864.79 mAh g
-1 at 0.2 C, 0.5 C,1 C, 2 C and back to 0.2 C, respectively, which indicates good performance on the redox reaction of LiPSs of Fe
3C particles and the enhancement of electrochemical reaction kinetics. This demonstrates the cooperative effect of physical and chemical adsorption can effectively alleviate the shuttle effect under a high sulfur loading state, and thus heighten the utilization rate of sulfur active materials.
In the cyclic voltammetry (CV) curves (
Figure 6a), for the cathodic scan, the first peak at 2.67 V, corresponds to the transformation of ring-opening reduction S
8 to soluble long-chain Li
2S
x (4≤x≤8). And the second peak at 2.01 V corresponds to the reduction of Li
2S
x (4≤x≤8) to the short chain Li
2S
2/Li
2S
. Subsequently, in the anodic scan, the implication of the oxidation peak at 2.36 V represents that the short-chain Li
2S/Li
2S
2 is oxidized to the long-chain LiPSs further Li
8S/S [
34]. The cell with Fe
3C@N-CS modified separator shows a higher current response density than the cells with N-CS modified separator or PP. The same phenomenon was obtained at other different scanning rates (
Figure S7), proving the positive effect of Fe
3C@N-CS on accelerating the redox kinetics. To verify the ability of Fe
3C@N-CS to catalyze the LiPSs redox reaction, the symmetric cells were tested, as shown in
Figure 4b. The cells with Fe
3C@N-CS modified separator show higher reversibility redox current response, and a smaller potential difference between oxidation peak and reduction peak, which indicate that Fe
3C@N-CS has strong catalytic activity than N-CS, thus accelerating the conversion kinetics of sulfur species.