Literature DB >> 31592476

An in Situ Template for the Synthesis of Tunable Hollow Carbon Particles for High-Performance Lithium-Sulfur Batteries.

Xiang Ding1, Junling Jin1, Xiaobing Huang1, Shibiao Zhou1, Anguo Xiao1, Yuandao Chen1, Chenggang Zuo1.   

Abstract

Nanostructured materials with hollow interior voids are gaining great attention due to their fantastic geometries and unique physicochemical properties competent for many applications. However, the development of a fast approach to prepare the hollow structured particles remains challenging. Herein, a new and efficient in situ hard-template method was developed to synthesize hollow carbon nano- and microparticles using the as-prepared SiO2 particles as a hard template directly, without any separation, drying, or redispersion. In this way, the hollow carbon particles with tunable diameters and shell thickness can be synthesized readily, which is simpler and more efficient than the traditional ones. In addition, the universality of this strategy allows us to study the different behaviors of hollow carbon particles in lithium-sulfur batteries when the architectures of hollow particles (i.e., diameter, shell thickness, etc.) were changed. We believe that this in situ method is applicable for synthesizing other core-shell or hollow structured materials (e.g., metal oxide), and also, the high performance of hollow carbon particles in lithium-sulfur batteries and beyond can be further explored.
Copyright © 2019 American Chemical Society.

Entities:  

Year:  2019        PMID: 31592476      PMCID: PMC6777082          DOI: 10.1021/acsomega.9b02287

Source DB:  PubMed          Journal:  ACS Omega        ISSN: 2470-1343


Introduction

Hollow carbon nano- and microparticles have widespread applications in the fields of catalysis,[1] electrochemistry,[2,3] energy (e,g., dye-sensitized solar cells),[4] supercapacitors,[5] rechargeable batteries,[6−8] and biotechnology[9,10] due to their hollow structure, physical stability, chemical inertness, high conductivity, and biocompatibility. To date, the most commonly used synthesis approach has been the well-known hard-template method,[11] the steps of which usually consist of the synthesis of core particles as a template followed by coating the presynthesized core particles (e.g., silica gel,[12] polystyrene,[13] or metal (oxide) nanoparticles[14,15]) with a layer of carbon and finally removing the core to form a hollow structure. Despite considerable research on this process having been carried out over the past few decades, a significant problem remains in that the core particles aggregate after centrifugation and drying before they are reused as templates. One effective approach has been a long ultrasonic treatment in order to redisperse the core particles; however, the individual and uniform distribution of core particles from the dried solid powders in solution appears to be irreversible in most cases, such as in the redispersion of silica gel.[16−22] Inevitably, the aggregation of core particles results in a poor distribution of the interior hollow structures of particles. To overcome this problem and simplify the process, we present an in situ hard-template method for the synthesis of hollow carbon particles in which the as-prepared core particles are directly used as templates without any separation. Then the hollow carbon particles with tunable diameters and shell thickness were synthesized readily, which is simpler and more efficient than the traditional ones. In addition, the feasibility of our strategy allows us to study the different electrochemical behaviors of hollow carbon particles in lithiumsulfur batteries when the architectures of hollow particles (i.e., diameter, shell thickness, etc.) were changed. We hope that this in situ method is applicable for synthesizing more core–shell, yolk–shell, and hollow structured materials for wider applications with greater performances besides the lithiumsulfur battery application.

Results and Discussion

Synthetic Features

The great features of our presented strategy are being efficient, convenient, and cost-effective in which there is no need for separation during the hard-template method (Figure a). In detail, silica gel templates with different particle diameters were prepared first by varying the molar ratio of (3-mercaptopropyl)trimethoxysilane (MPTMS, 0.1–10 g) and water (Figure b). Sucrose was then added as a carbon source (0.5–15.4 g), and water was then added into the primary silica gel solution while stirring. Next, the mixture underwent hydrothermal treatment in an autoclave while stirring for several hours. The core–shell structured SiO2@C-rich particles were formed after the hydrothermal reaction (C-rich indicates that the shell materials are rich in carbonaceous materials[23]) (Figure c). After this step, hollow carbon particles were obtained followed by the carbonization of SiO2@C-rich to SiO2@C and then HF etching of the SiO2 core.
Figure 1

Typical SEM images and particle size distributions of (a,b) SiO2 template and (c,d) SiO2@C (the carbon shell is after calcination). The inset picture of panel (c) is the local TEM image of SiO2@C.

Typical SEM images and particle size distributions of (a,b) SiO2 template and (c,d) SiO2@C (the carbon shell is after calcination). The inset picture of panel (c) is the local TEM image of SiO2@C.

Architectural Features

The hollow carbon particles (i.e., HCP) with different diameters were obtained as shown in Figure . Scanning electron microscopy (SEM) and transmission electron microscopy (TEM) images show that well-dispersed hollow carbon particles with an average diameter of 162 nm were prepared using 0.5 g of MPTMS and 2.0 g of sucrose (Figure a,b,a1) (i.e., HCP-162-22). Note that the abbreviation of the HCP-diameter-shell thickness means the hollow carbon particles with a certain diameter and shell thickness. By increasing the amount of carbon precursor in the form of sucrose from 2.0 to 3.3 g, the average shell thickness could be finely controlled from 22 to about 34 nm (Figure b1,c,c1). This result confirms that the shell thickness can be readily tuned by varying the concentration of carbon precursors. Alternatively, by increasing the amounts of MPTMS and sucrose to 10 and 15.4 g simultaneously, large, hollow carbon particles with an average diameter of 415 nm were synthesized. Their shell thickness was about 82 nm, and their spherical interior void was 251 nm in diameter (i.e., HCP-415-82). Increasing the amount of MPTMS increased the size of the silica particles, and increasing the amount of sucrose increased the thickness of the particle shells. Note that the hollow carbon particles prepared using this strategy have high surface areas. For example, high surface areas of 1631 and 1495 cm2 g–1 with a broad pore size distribution were confirmed for the samples HCP-162-22 and HCP-415-82 (Figure ).
Figure 2

Characterizations of the typical HCP. (a) SEM and (b) TEM images of HCP-162-22 (the acronym of HCP-162-22 represents hollow carbon particles with an average diameter of 162 nm and shell thickness of 22 nm, the followed example is the same for comparison). (a1) Particle size and (b1,c1) the shell thickness distributions of HCP-162-22 and HCP-174-34. TEM images of (c) HCP-174-34 and (d) HCP-415-82. (d1) Particle size and the shell thickness histogram of the HCP-415-85.

Figure 3

BET analysis of HCP. Nitrogen adsorption–desorption isotherms and (f) pore size distributions of the (a) HCP-162-22 and (b) HCP-415-82. The unit of dv/dD is cm3 g–1 nm–1.

Characterizations of the typical HCP. (a) SEM and (b) TEM images of HCP-162-22 (the acronym of HCP-162-22 represents hollow carbon particles with an average diameter of 162 nm and shell thickness of 22 nm, the followed example is the same for comparison). (a1) Particle size and (b1,c1) the shell thickness distributions of HCP-162-22 and HCP-174-34. TEM images of (c) HCP-174-34 and (d) HCP-415-82. (d1) Particle size and the shell thickness histogram of the HCP-415-85. BET analysis of HCP. Nitrogen adsorption–desorption isotherms and (f) pore size distributions of the (a) HCP-162-22 and (b) HCP-415-82. The unit of dv/dD is cm3 g–1 nm–1. Moreover, a series of particles of different sizes (130–415 nm) and shell thicknesses (8–82 nm) could be synthesized by changing the amounts of MPTMS and sucrose (Figure ). This experiment demonstrates the feasibility of this method. Using this strategy, the SiO2 core particles were used directly without any separation, washing, drying, or redispersion, which is very different from other methods.[16−22] In addition, the SiO2 core can be removed completely, as confirmed by the energy-dispersive X-ray spectroscopy (EDX) (Figure c). These results confirm that an in situ hard template can be used to prepare hollow carbon particles over a wide range of sizes and shell thicknesses. More importantly, this concept can be easily extended to other kinds of systems with different core particles, such as polystyrene,[24] carbon colloids,[25] and metal (oxide) nanoparticles.[26] This approach facilitates the preparation of core–shell structured and hollow metal (oxide) particles at reduced energy and cost as it is simpler and more effective than traditional hard-template methods.
Figure 4

TEM images of (a) HCP-131-8 and (b) HCP-184-29 prepared from 0.4 g MPTMS/1.0 g sucrose and 0.7 g MPTMS/4.0 g sucrose, respectively.

TEM images of (a) HCP-131-8 and (b) HCP-184-29 prepared from 0.4 g MPTMS/1.0 g sucrose and 0.7 g MPTMS/4.0 g sucrose, respectively.

Sulfur Impregnation

To date, research has focused on the use of varied carbon materials in lithiumsulfur batteries because nanostructured carbon materials such as layered graphene (oxide),[27] carbon nanotubes,[28] and porous carbon[29] play a critical role in embedding sulfur, enhancing the conductivity of electrodes, and suppressing diffusion of the polysulfide intermediates in order to maintain good cyclic performance. Previous results have confirmed the role of carbon as the host for sulfur.[9−11] Recently, some efforts have focused on using hollow carbon particles as substrates due to their intriguing hollow structures.[30−32] However, the electrochemical properties have always been studied under a relative low current density (e.g., 0.1, 0.25 C, wherein 1 C = 1675 mA g–1) due to the intrinsic fast capacity degradation of Li–S battery systems, especially at high current densities. Herein, we investigated the performances of three kinds of hollow carbon particles in lithiumsulfur applications at a high current density (e.g., 1 C) and found that one type showed good performance. We also discuss the effects of particle size and shell thickness on electrochemical properties. First, sulfur was impregnated into hollow carbon particles using the vapor method. After impregnation, the S@HCP composite still maintained its spherical structure and showed relatively individual distribution (Figure a,b). The elemental distribution analysis of a typical S@HCP-415-82 particle confirms the presence of a large amount of sulfur concentrated in the hollow interior (Figure c). However, due to the differences in particle size and shell thickness, the hollow carbon particles showed different abilities to encapsulate sulfur and increase shell thickness. As shown in Figure d, HCP-415-82 particles demonstrated the highest sulfur content (58.5 wt %) compared with HCP-162-22 (48.2 wt %) and HCP-174-34 (55.0 wt %). Particle size and shell thickness clearly determine the sulfur-encapsulation ability, even when particles have similar hollow structures. Moreover, the variation in the evaporation curves of sulfur from the S@HCP composite demonstrates the difference in strength between the carbon host and sulfur (Figure d). The HCP-162-22 particles show the strongest interaction with sulfur. The temperature at which complete evaporation occurred was about 430 °C, which is much higher than those of HCP-174-34 (300 °C) and HCP-415-82 (340 °C). Besides, the comparative XRD patterns of the HCP-415-82 and S@ HCP-415-82 also confirm that sulfur was impregnated into the hollow carbon spheres.
Figure 5

TEM images of (a) S@HCP-162-22 and (b) S@HCP-415-82. (c) Typical elemental distribution analysis of individual composite particle of S@HCP-415-82. The straight line of carbon signal is normal because the beam energy cannot fully penetrate the particles to the reverse side of the shell. (d) Thermogravimetric analysis of hollow composite C–S particles after sulfur impregnation. (e) Comparative XRD patterns of HCP-415-82 and S@HCP-415-82.

TEM images of (a) S@HCP-162-22 and (b) S@HCP-415-82. (c) Typical elemental distribution analysis of individual composite particle of S@HCP-415-82. The straight line of carbon signal is normal because the beam energy cannot fully penetrate the particles to the reverse side of the shell. (d) Thermogravimetric analysis of hollow composite C–S particles after sulfur impregnation. (e) Comparative XRD patterns of HCP-415-82 and S@HCP-415-82.

Lithium–Sulfur Applications

The electrochemical measurements were performed in the half-cell using the electrolytes of 1.0 M bis(trifluoromethane)sulfonimide lithium salt (LiTFSI) and 0.4 M LiNO3 in 1,3-dioxolane/dimethoxyethane (DOL/DME, v/v = 1/1). A typical cyclic voltammetry (CV) curve of S@HCP-415-82 particles within a cutoff voltage window of 1.8–2.8 V is shown in Figure a. According to the mechanisms for oxidation and reduction of S8 during discharge–charge,[33,34] the peak at around 2.37 V could be attributed to the reduction of elemental sulfur to higher-order lithium polysulfides (Li2S, 4 ≤ x < 8).[35] Generally, these polysulfides were in a metastable phase and could dissolve easily into the electrolyte, thereby giving rise to the degradation of the Li–S battery during the charge–discharge process.[36,37] The characteristic peak near 2.04 V was caused by further reduction of the higher-order lithium polysulfides to lower-order lithium polysulfides (Li2S, x < 2) and eventually to Li2S.[38−40] Inversely, the oxidation process in the Li–S cell also occurs in two stages. The oxidation peak at 2.42 V can be attributed to the formation of Li2S (x > 2) from Li2S. This process continues until the lithium polysulfide is completely consumed and elemental sulfur is produced at 2.53 V. As the cycle number increases, the CV peak positions and intensities only undergo very small changes, indicating the relatively good reversibility and stability. This appears to be due to the hollow interior structure and the suitable thickness of the shell, which is beneficial for preventing the loss of sulfur into the electrolyte and maintaining high utilization of the active sulfur in the redox reactions.[32,41−44]
Figure 6

(a) Cyclic voltammetry curves at 0.1 mV s–1 scanning rate, (b) galvanostatic charge–discharge profiles, and (c) cycling performance of S@HCP-415-82 at a rate of 1 C from the 1st to 100th cycles. (d) Typical charge–discharge curves in the rate test. Comparative reaction behaviors of the sulfur in the (e) large (e.g., S@HCP-415-82) and (f) small (e.g., S@HCP-162-22) hollow carbon particles.

(a) Cyclic voltammetry curves at 0.1 mV s–1 scanning rate, (b) galvanostatic charge–discharge profiles, and (c) cycling performance of S@HCP-415-82 at a rate of 1 C from the 1st to 100th cycles. (d) Typical charge–discharge curves in the rate test. Comparative reaction behaviors of the sulfur in the (e) large (e.g., S@HCP-415-82) and (f) small (e.g., S@HCP-162-22) hollow carbon particles. The electrochemical performance of S@HCP-415-82 was further demonstrated by the voltage versus capacity profiles (Figure b), which is well consistent with the CV curves. We find that the cell can cycle well at a high rate of 1 C with an initial capacity of 900 mA h g–1. Besides, the average capacity can achieve 792 mA h g–1 in the initial 100 cycles where the capacity retention is 76.3%. By contrast, average capacities of 570 and 447 mA h g–1 were obtained for the S@HCP-174-34 and S@HCP-162-22, respectively. The capacities of the Li–S cell using the S@HCP-174-34 and S@HCP-162-22 electrodes decrease from 773 to 384 mA h g–1 and from 703 to 250 mA h g–1 with capacity retentions of 49.5 and 35.4%, respectively, after the same cycling period (Figure c). Thus, the S@HCP-415-82 composite exhibits the best performance. In addition, high capacities of 1391, 1160, 985, 845, 658, and 338 mA h g–1 can be delivered for the S@HCP-415-82 at rates of 0.1, 0.25, 0.5, 1, 2.5, and 5 C, respectively (Figure d). Although these results show the effect of particle size and shell thickness on electrochemical performance, rational correlation and reason for the difference need to be further investigated due to the complexities of the reduction and oxidation processes in lithiumsulfur batteries.[45−47] Our preliminary results show that a medium particle size could be probably good for the fast transportation of electrons and lithium ions during the reactions (Figure e), while a small particle size (i.e., small hollow voids) and a thin shell thickness might decrease the transportation rate of electrons and lithium ions. In addition, a too small particle size might bring more contact boundaries within the electrode and then cause an increased electric resistance, thereby leading to a low sulfur utilization and a low capacity (Figure f). Besides, the thin shell is not good for suppressing the lithium polysulfide shuttling effect because the polysulfide is easy to diffuse outside from the hollow particles. As a result, the S@HCP-415-82 demonstrates a good rate capability and long cycle life over 200 cycles even at a high rate of 2.5 C, under which a high average capacity of 578 mA h g–1 can be delivered (Figure ).
Figure 7

(a) Rate capabilities, (b) galvanostatic charge–discharge profiles, and (c) cycling performance of S@HCP-415-82 at a rate of 2.5 C from the 1st to 200th cycles.

(a) Rate capabilities, (b) galvanostatic charge–discharge profiles, and (c) cycling performance of S@HCP-415-82 at a rate of 2.5 C from the 1st to 200th cycles.

Conclusions

In summary, a simple and efficient in situ hard-template method was developed to synthesize hollow carbon nano- and microparticles using SiO2 particles as a template directly, without any separation, drying, or redispersion. This strategy not only bypasses tedious steps such as centrifugation, oven drying of core particles, and particle redispersion but also reduces the cost and energy consumption compared to traditional methods. Undoubtedly, this concept could be further extended to other kinds of systems in which polystyrene, carbon, and metal (oxide) particles are used as templates to synthesize core–shell structured and hollow particles. Additionally, the prepared hollow carbon particles have good performance in the lithiumsulfur battery application, particularly at the high rate conditions. We found that particle size and shell thickness largely determine electrochemical performance, which will be helpful for further investigations of hollow carbon particles in lithiumsulfur batteries and beyond.

Experimental Section

Materials Preparations

The hollow carbon particles were synthetized, and sulfur impregnation was carried out as follows. First, 0.4–10 g of (3-mercaptopropyl)trimethyloxysilane (MPTMS) (Sigma Aldrich) was added dropwise into 100 mL of distilled water with vigorous stirring until the solution became transparent. Next, 0.05 mL of NH4OH was added to the solution (pH = 11), and the reaction was allowed to progress for 12 h at room temperature. After completion of the reaction, a silica colloidal solution with monodispersed SiO2 particles was formed. Subsequently, 1.0–15.4 g of carbon precursor was dissolved into 200 mL of distilled water and mixed with the SiO2 colloidal solution, which was then transferred into a stainless steel autoclave. Hydrothermal treatment was carried out at 180 °C for 5 h. The resulting slurry was filtered and washed with distilled water and ethanol. The obtained powder was vacuum-dried at 100 °C for 24 h and annealed at 1000 °C for 2 h under an argon atmosphere. The resulting black powder was immersed in an aqueous HF solution for 24 h to etch away the SiO2 template followed by filtration and washing. After this step, hollow carbon particles (HCP) were obtained. For the sulfur impregnation, 0.3 g of hollow carbon particles and 1. 0 g of elemental sulfur were placed on the separated ends of a Y-type glass, and then the Y-type tube was sealed under vacuum. The Y-type glass tube was then heated to 600 °C over 4 h (heating rate, 2 °C min–1) and then cooled to room temperature.

Materials Characterizations

The architectural structures of particles were characterized by scanning electron microscopy (SEM), which was performed on a field-emission Hitachi S-4800 instrument operating at an accelerating voltage of 10 kV. The core–shell and hollow characteristics of particles were confirmed by transmission electron microscopy (TEM), which was performed using an FEI Tecnai G2 S-Twin instrument with a field-emission gun operating at 200 kV. Thermogravimetric (TG) analysis was performed from room temperature to 500 °C with a heating rate of 10 °C min–1 under the N2 flow using an STA 449 Jupiter (NETZSCH) thermogravimetry analyzer. The N2 adsorption/desorption measurements were conducted with a Micromeritics ASAP 2010 instrument at −196 °C after the sample was degassed at 200 °C for 6 h under vacuum conditions. The pore sizes were estimated from the pore size distribution curves from the adsorption isotherms using the Barrett–Joyner–Halenda (BJH) method.

Electrochemical Measurement

The sulfur-based electrode was prepared as follows. The active materials S@HCP and polyvinylidene fluoride (PVDF) binder were mixed in N-methyl-2-pyrrolidone (NMP) to form a uniform slurry, which was then cast on the Al foil and then roll-pressed after vacuum drying at 40 °C to remove the residual solvent. The sulfur loading on the electrode was controlled at around 1.23 mg cm–2. The electrode was punched into a circular piece before assembling the battery. The electrochemical tests with the configuration of S@HCP-based electrode|separator|metallic lithium were performed using R2032 coin-type cells, which were assembled in an argon-filled glove box using the electrolytes of 1.0 M LiTFSI and 0.4 M LiNO3 in DOL/DME. The used volume of the electrolyte for each cell was about 150 μL. Cyclic voltammetry (CV) studies were performed using a VMP3 electrochemical workstation at a scan rate of 0.25 mV s–1 (Bio-Logic). The galvanostatic charge–discharge performances were measured under cutoff voltages of 1.8–2.8 V using a Land battery testing system at room temperature.
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Review 7.  Current Status and Future Prospects of Metal-Sulfur Batteries.

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Journal:  Adv Mater       Date:  2019-05-13       Impact factor: 30.849

8.  3D interconnected porous carbon nanosheets/carbon nanotubes as a polysulfide reservoir for high performance lithium-sulfur batteries.

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9.  Scalable Approach To Construct Free-Standing and Flexible Carbon Networks for Lithium-Sulfur Battery.

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10.  General Method for the Synthesis of Hollow Mesoporous Carbon Spheres with Tunable Textural Properties.

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