The current disclosure relates to cathodes for rechargeable lithium-sulfur (Li—S) batteries containing a nanocomposite of sulfur and graphene. In particular, the cathode may contain amorphous sulfur nanoparticles distributed on a graphene surface. The disclosure further relates to Li—S batteries containing such a cathode and methods of making such a cathode using hydroxylated graphene.
Batteries may be divided into two principal types, primary batteries and secondary batteries. Primary batteries may be used once and are then exhausted.
Secondary batteries are also often called rechargeable batteries because after use they may be connected to an electricity supply, such as a wall socket, and recharged and used again. In secondary batteries, each charge/discharge process is called a cycle. Secondary batteries eventually reach an end of their usable life, but typically only after many charge/discharge cycles.
Secondary batteries are made up of an electrochemical cell and optionally other materials, such as a casing to protect the cell and wires or other connectors to allow the battery to interface with the outside world. An electrochemical cell includes two electrodes, the positive electrode or cathode and the negative electrode or anode, an insulator separating the electrodes so the battery does not short out, and an electrolyte that chemically connects the electrodes.
In operation the secondary battery exchanges chemical energy and electrical energy. During discharge of the battery, electrons, which have a negative charge, leave the anode and travel through outside electrical conductors, such as wires in a cell phone or computer, to the cathode. In the process of traveling through these outside electrical conductors, the electrons generate an electrical current, which provides electrical energy.
At the same time, in order to keep the electrical charge of the anode and cathode neutral, an ion having a positive charge leaves the anode and enters the electrolyte and a positive ion also leaves the electrolyte and enters the cathode. In order for this ion movement to work, typically the same type of ion leaves the anode and joins the cathode. Additionally, the electrolyte typically also contains this same type of ion. In order to recharge the battery, the same process happens in reverse. By supplying energy to the cell, electrons are induced to leave the cathode and join the anode. At the same time a positive ion, such as Li+, leaves the cathode and enters the electrolyte and a Li+ leaves the electrolyte and joins the anode to keep the overall electrode charge neutral.
In addition to containing an active material that exchanges electrons and ions, anodes and cathodes often contain other materials, such as a metal backing to which a slurry is applied and dried. The slurry often contains the active material as well as a binder to help it adhere to the backing and conductive materials, such as a carbon particles. Once the slurry dries it forms a coating on the metal backing
Unless additional materials are specified, batteries as described herein include systems that are merely electrochemical cells as well as more complex systems.
Several important criteria for rechargeable batteries include energy density, power density, rate capability, cycle life, cost, and safety. The current lithium-ion battery technology based on insertion compound cathodes and anodes is limited in energy density. This technology also suffers from safety concerns arising from the chemical instability of oxide cathodes under conditions of overcharge and frequently requires the use of expensive transition metals. Accordingly, there is immense interest to develop alternate cathode materials for lithium-ion batteries. Sulfur has been considered as one such alternative cathode material.
Lithium-sulfur (Li—S) batteries are a particular type of rechargeable battery. Unlike most rechargeable batteries in which the ion actually moves into and out of a crystal lattice, the ion in lithium-sulfur batteries reacts with lithium in the anode and with sulfur in the cathode even in the absence of a precise crystal structure. In most Li—S batteries, the anode is lithium metal (Li or Li0). In operation, lithium leaves the metal as lithium ions (Li+) and enters the electrolyte when the battery is discharging. When the battery is recharged, lithium ions (Li+) leave the electrolyte and plate out on the lithium metal anode as lithium metal (Li). At the cathode, during discharge, particles of elemental sulfur (S) react with the lithium ion (Li+) in the electrolyte to form Li2S. When the battery is recharged, lithium ions (Li+) leave the cathode, allowing the cathode to revert to elemental sulfur (S).
Sulfur is an attractive cathode candidate as compared to traditional lithium-ion battery cathodes because it offers an order of magnitude higher theoretical capacity (1675 mAh g−1) than the currently employed cathodes (<200 mAh g−1) and operates at a safer voltage range (1.5-2.5 V). This high theoretical capacity is due to the ability of sulfur to accept two electrons (e) per atom. In addition, sulfur is inexpensive and environmentally benign.
However, the major problem with a sulfur cathode is its poor cycle life. The discharge of sulfur cathodes involves the formation of intermediate polysulfide ions, which dissolve easily in the electrolyte during the charge-discharge process and result in an irreversible loss of active material during cycling. The high-order polysulfides (Li2Sn, 4≦n≦8) produced during the initial stage of the discharge process are soluble in the electrolyte and move toward the lithium metal anode, where they are reduced to lower-order polysulfides. Moreover, solubility of these high-order polysulfides in the liquid electrolytes and nucleation of the insoluble low-order sulfides (i.e., Li2S2 and Li2S) result in poor capacity retention and low Coulombic efficiency. In addition, shuttling of these high-order polysulfides between the cathode and anode during charging, which involves parasitic reactions with the lithium anode and re-oxidation at the cathode, is another challenge. This process results in irreversible capacity loss and causes the build-up of a thick, irreversible Li2S barrier on the electrodes during prolonged cycling, which is electrochemically inaccessible. Overall, the operation of Li—S cells is so dynamic that novel electrodes with optimized compositions and structure are needed to maintain the high capacity of sulfur and overcome the challenges associated with the solubility and shuttling of polysulfides. Thus, in prior Li—S batteries, polysulfides have been treated as an active intermediate product of useful electrochemical reactions. For example, some prior batteries have sought to trap polysulfide within the cathode and have achieved an actual, reversible utilization of 1.3 e− per sulfur atom.
In addition to problems with polysulfide formation, sulfur is an insulator with a resistivity of 5×10−30 S/cm at 25° C., resulting in a poor electrochemical utilization of the active material and poor rate capacity. Although the addition of conductive carbon to the sulfur material could improve the overall electrode conductivity, the cores of the sulfur particles, which have little or no contact with conductive carbon, will still be highly resistive.
Previous attempts to address the conductivity problem have sought to increase the fraction of sulfur in contact with carbon. Several approaches have been pursued, such as forming sulfur-carbon composites with carbon black or nanostructured carbon. For example, a mesoporous carbon framework filled with amorphous sulfur with the addition of polymer has been found to exhibit a high reversible capacity of approximately 1000 mAh/g after 20 cycles. However, most traditional methods to synthesize sulfur-carbon composites include processing by a sulfur melting route, resulting in high manufacturing costs due to additional energy consumption. Also, several reports have noted that the sulfur content in the sulfur-carbon composites synthesized by the sulfur melting route is limited to a relatively low value in order to obtain acceptable electrochemical performance, leading to a lower overall capacity of the cathode.
Moreover, synthesizing homogeneous sulfur-carbon composites through conventional heat treatment is complicated. In the conventional synthesis of sulfur-carbon composites, sulfur is first heated above its melting temperature, and the liquid sulfur is then diffused to the surface or into the pores of carbon substrates to form the sulfur-carbon composite. A subsequent high-temperature heating step is then required to remove the superfluous sulfur on the surface of the composites, leading to a waste of some sulfur. Thus, the conventional synthesis by the sulfur melting route may not be scaled-up in a practical manner to obtain a uniform industry-level sulfur-carbon composite.
As another alternative, a sulfur deposition method to synthesize a core-shell carbon/sulfur material for lithium-sulfur batteries has been recently reported. However, cyclability and rate capability associated with this deposition process are not satisfactory. Furthermore, the sulfur deposition process is very sensitive and must be carefully controlled during synthesis. Otherwise, a composite with poor electrochemical performance is produced.
Previous attempts to integrate sulfur with graphene have also been made. A graphene-sulfur composite material in which sulfur particles are wrapped by polyethylene glycol (PEG) and graphene sheets showed stable capacities of 600 mAh/g over 100 cycles. Also, a one-pot reaction has been developed to obtain a graphene-enveloped sulfur composite which had high sulfur content of 87 wt % with acceptable cycling stability. In addition, a graphene oxide (GO) network anchoring sulfur has been found to effectively enhance the cycle performance of lithium-sulfur batteries. While graphene-sulfur composite cathodes demonstrate promising electrochemical performance, their synthesis is usually complicated and challenging for large-scale application. Simpler, solution-based synthesis without heat treatment produces large crystalline sulfur particles, resulting in low utilization of active materials and poor rate performance.
Accordingly, a need remains for a highly functional, readily synthesized sulfur-hydroxylated graphene cathode material.
In one embodiment, the present disclosure provides a sulfur-hydroxylated graphene nanocomposite including at least one hydroxylated graphene sheet with a surface and a plurality of amorphous sulfur nanoparticles homogeneously distributed on the surface. The nanocomposite substantially lacks sulfur microparticles.
In other embodiments, the disclosure provides a cathode and a battery containing the nanocomposite.
In still another embodiment, the disclosure provides a method of making a sulfur-hydroxylated graphene nanocomposite by exposing a hydroxylated graphene to a sulfur-containing solution for a time sufficient with ultrasonication to allow formation of homogeneously distributed sulfur nanoparticles on a surface of the hydroxylated graphene.
The following abbreviations are commonly used throughout the specification:
A more complete understanding of the present embodiments and advantages thereof may be acquired by referring to the following description taken in conjunction with the accompanying drawings, which, when discussing sulfur-hydroxylated graphene nanocomposites, relate to embodiments of the present disclosure. The current specification contains color drawings. Copies of these drawings may be obtained from the USPTO.
The current disclosure relates to cathodes for rechargeable lithium-sulfur (Li—S) batteries containing a nanocomposite of sulfur and hydroxylated graphene. In particular, the cathode may contain amorphous sulfur nanoparticles distributed on a graphene surface. The disclosure further relates to Li—S batteries containing such a cathode and methods of making such a cathode using hydroxylated graphene.
“Graphene” as used in the present disclosure, may include any sheet-like material that is substantially one atom-thick and substantially formed from double bonded carbon atoms. Graphene may also be characterized by the honeycomb appearance of the carbon atoms. Graphene may include graphene oxide. Hydroxylated graphene may include graphene oxide with mainly hydroxyl groups and few or no carboxyl groups or epoxy bridges. The study of graphene remains a highly dynamic field. Accordingly, graphene, as used herein, unless otherwise specifically indicated, includes graphene variations presently in existence as well as any developed in the future otherwise compatible with this disclosure.
Sulfur-hydroxylated graphene nanocomposites of the present disclosure may contain amorphous sulfur nanoparticles distributed on a hydroxylated graphene surface. These nanoparticles may be substantially made of elemental sulfur. The nanoparticles may be distributed uniformly on the hydroxylated graphene surface.
In one embodiment, the nanocomposite may contain at least 30 wt % sulfur, at least 50 wt % sulfur, at least 80 wt % sulfur, or at least 90 wt % sulfur. It may also include ranges of sulfur by wt % between any of these endpoints.
In one embodiment, sulfur microparticles may be substantially absent from the sulfur-hydroxylated graphene nanocomposite. In particular, less than 5% less than 2%, or less than 1% of the particles may be microparticles.
The hydroxylated graphene may be in the form of a sheet, although when cathodes are formed, layers of graphene sheets may be used, so long as they remain sufficiently spaced to allow lithium ion (Li+ movement). Cathodes may also contain other materials to improve conductivity or mechanical stability, such as metal foil or other conductive foil on which the sulfur-hydroxylated graphene nanocomposite is deposited.
The close electrochemical contact between sulfur nanoparticles and the hydroxylated graphene, which is highly conductive, allows the formation of cathodes that, when placed in a Li—S battery exhibit reversible discharge capacities of at least 1,022 mAh/g (based on mass of S) after 100 cycles at C/2, at least 955 mAh/g (based on mass of S) after 100 cycles at C1, or at least 647 mAh/g (based on mass of S) after 100 cycles at 2C. Capacity retention over 100 cycles may be at least 80% or at least 90%. These batteries may also exhibit a Coulombic efficiency of at least 95%. Additionally, the amorphous state of sulfur particles in the nanocomposite has close contact with the hydroxylated graphene substrate, preventing the dissolution of polysulfides during use of the cathode. Sulfur nanoparticles provide short pathways for ion and electron transport. The unique sponge-like morphology of the sulfur-hydroxylated graphene nanocomposite allows complete electrolyte penetration and absorbs the strain from cycling-induced volume changes during battery use.
Unless otherwise indicated by the context, the term “battery” as uses herein includes both simple electrochemical cells and more complex multi-cell arrangements.
According to one embodiment, the disclosure provides a battery with a cathode containing a sulfur-hydroxylated graphene nanocomposite as described herein, an anode suitable for use with the cathode and in which lithium ions (Li+) can intercalate or be deposited, such as lithium metal (Li or Li0), lithiated silicon, lithiated tin, Li4Ti5O12,, lithium-containing oxides or sulfides, or lithium-containing organics, such as Li2C6O6, Li2C8H4O4, Li2C6H4O4, or other lithium-containing materials, and an electrolyte suitable for use with the cathode and anode, such as lithium trifluoromethanesulfonate (LiCF3SO3, 1 M) or other lithium salts, such as lithium bis(trifluoromethanesulfonyl)imide (LITFSI, 1 M)) and lithium nitrate (LiNO3 ,0.1 M), dissolved in 1,3-dioxalane (DOL) and 1,2-dimethoxyethane (DME) (1:1, vol, or other solvents, such as tetra(ethylene glycol)dimethyl ether). The battery may also contain a separator to electrically insulate the cathode and anode. In some batteries, the separator may also be the electrolyte.
Batteries of the present disclosure may also contain contacts, a casing, or wiring. In the case of more sophisticated batteries, they may contain more complex components, such as safety devices to prevent hazards if the battery overheats, ruptures, or short circuits. Particularly complex batteries may also contain electronics, storage media, processors, software encoded on computer readable media, and other complex regulatory components.
Batteries may be in traditional forms, such as coin cells or jelly rolls, or in more complex forms such as prismatic cells. Batteries may contain more than one electrochemical cell and may contain components to connect or regulate these multiple electrochemical cells.
Batteries of the present disclosure may be used in a variety of applications. They may be in the form of standard battery size formats usable by a consumer interchangeably in a variety of devices. They may be in power packs, for instance for tools and appliances. They may be usable in consumer electronics including cameras, cell phones, gaming devices, or laptop computers. They may also be usable in much larger devices, such as electric automobiles, motorcycles, buses, delivery trucks, trains, or boats. Furthermore, batteries according to the present disclosure may have industrial uses, such as energy storage in connection with energy production, for instance in a smart grid, or in energy storage for factories or health care facilities, for example in the place of generators.
Sulfur-graphene nanocomposites of the present disclosure may be formed using an in situ sulfur deposition method of hydroxylated graphene at room temperature. In particular, the sulfur-hydroxylated graphene nanocomposites may be formed through hydroxyl group-induced heterogeneous nucleation of bonded sulfur atoms through extraction from a sulfur salt solution
Hydroxylated graphene nanosheets may be prepared by any suitable method, including, but not limited to, ultrasonication-hydrothermal methods, ball-milling methods or Chemical Vapor Deposition methods. Hydroxylated graphene may be in the form of sheets, such as graphene nanosheets.
The sulfur salt solution may be any salt solution from which sulfur may be extracted through hydroxyl group nucleation in an acidic environment.
Sulfur nanoparticle deposition may be substantially complete in less than one hour.
Due to strong interactions between the hydroxyl groups on the graphene and sulfur in the sulfur salt in solution and any intermediate polysulfides, the sulfur nanoparticles formed on the graphene surface are amorphous.
In a particular embodiment, shown in
The following examples are provided to further illustrate specific embodiments of the disclosure. They are not intended to disclose or describe each and every aspect of the disclosure in complete detail and should not be so interpreted.
Pristine graphene nanosheets (SkySpring Nanomaterials Inc., USA) were synthesized through a mechanical exfoliation method. Sodium hydroxide (NaOH, Fisher Scientific, AR), sodium thiosulfate (Na2S2O3, Fisher Scientific, AR), hydrochloride acid (HCl, 37%, Fisher Scientific, AR), lithium nitrate (LiNO3, Fisher Scientific, AR), poly(vinylidene fluoride) (PVDF 1120, Kureha), carbon black (SuperP, Alfa Aesar), N-methyl-2-pyrrolidinone (NMP, anhydrous, 99.5%, Sigma-Aldrich), lithium trifluoromethanesulfonate (LiCF3SO3, 98%, Acros Organics), 1,3-dioxolane (DOL, Acros Organics), and 1,2-dimethoxyethane (DME, Acros Organics) were used as received.
Pristine graphene nanosheets (1.0 g) were dispersed in aqueous NaOH (3.2 g) solution (40 mL, 2 M) with the aid of ultrasonication (Sonics & Materials, Inc) for 30 minutes at room temperature as described in D. Yang, G. Guo, J. Hu, C. Wang, D. Jiang, J. Mater. Chem. 18:350 (2008) portions relating to generating hydroxylated carbon nanotubes, incorporated in material part by reference herein. Next, the mixture was transferred into a stainless steel reaction autoclave (50 mL) with a polytetrafluoroethylene liner, heated to 180° C. for 2 hours, and cooled to room temperature. The reaction mixture was washed with methanol and de-ionized (DI) water until the pH reached 7.0 and dried in a vacuum oven at 50° C.
A general description of the method used in this example is provided in
Sulfur-graphene nanocomposites formed in Example 1 were subjected to structural and chemical analysis.
The morphology of the sulfur-hydroxylated graphene nanocomposite was examined with a FEI Quanta 650 scanning electron microscope (SEM). The sulfur-graphene nanocomposite possesses a sponge-like morphology with fully exfoliated graphene nanosheets as shown in
Elemental mapping and the composition of the nanocomposite was analyzed by energy dispersive X-ray spectroscopy (EDS, FEI). Results are shown in
To examine the surface characteristics of the sulfur-hydroxylated graphene nanocomposite, X-ray photoelectron spectroscopy (XPS, Kratos Analytical Company) analysis of the hydroxylated graphene without sulfur and sulfur-hydroxylated graphene nanocomposite was performed. Results are shown in
To further confirm the surface characteristics of the graphene without sulfur and the sulfur-hydroxylated graphene nanocomposite, Fourier transform-infrared spectroscopy (FTIR, Perkin-Elmer Spectrum RX-1) was also performed, the results of which are presented in
The XPS and FTIR results confirm that the hydroxyl groups were introduced onto the graphene nanosheets, and the hydroxyl groups were involved in the sulfur deposition reaction, resulting in some sulfur attached to the graphene with uniform morphology.
Crystal structural characterization was carried out with a Philips X-ray Diffractometer (XRD) with CuKa radiation between 10 and 80° at a scan rate of 0.04° s−1. XRD was conducted on pure sulfur powder, pristine graphene nanosheets, and the sulfur-hydroxylated graphene nanocomposite, as shown in
Sulfur-graphene nanocomposites formed in Example 1 were subjected to electrochemical analysis in CR2032 coin cells. The cathode contained 80 wt % of sulfur-hydroxylated graphene nanocomposite, a high loading of active material, and was prepared by mixing sulfur-hydroxylated graphene nanocomposite (80 wt %), SuperP (10 wt %), and PVDF binder (10 wt %) in an N-methylpyrrolidone (NMP) solution. The well-mixed slurry was then cast onto an aluminium foil and the resulting film was dried in an oven at 50° C. CR2032 coin cells consisting of a metallic lithium anode, a Celgard separator, and the sulfur-hydroxylated graphene nanocomposite cathode were assembled in an argon-filled glovebox. The electrolyte used was LiCF3SO3(1 M) and LiNO3(0.1 M) dissolved in 1,3-dioxalane (DOL) and 1,2-dimethoxyethane(DME) (1:1, vol). Galvanostatic cycling was conducted with an Arbin battery cycler at 2.8-1.8 V (vs. Li/Li+) at room temperature.
The reduction and oxidation plateaus remained relatively constant over 100 cycles as shown in the selected discharge/charge curves in
To examine the electrochemical cycle performance, cells with the sulfur-hydroxylated graphene nanocomposite cathodes were cycled at rates of C/2, 1C, and 2C (1C=1,675 mA/g based on mass of S), as shown in
Pristine graphene nanosheets without hydroxylation were also coupled with sulfur following the same chemical deposition method as described in Example 1 to form sulfur-graphene microcomposites. Comparative sulfur-hydroxylated graphene nanocomposites were also formed. Sulfur content in both materials was 50 wt %. In contrast to the sulfur-hydroxylated graphene nanocomposite, the materials formed without hydroxyled graphene contained micro-sized sulfur particles, which may be seen in the SEM images (
The large capacity difference between the two composites remained relatively uniform during cycling, indicating little change in the utilization of active materials during cycling.
The sulfur-hydroxylated graphene nanocomposite may contain residual hydroxyl groups, which may attract polysulfides during cycling through hydrophilic-hydrophilic interactions as shown in
UV-visible absorption spectroscopy was used to characterize the polysulfide species and their content in the electrolyte after the cells as described in Example 3 completed a certain number of cycles. Typically, the cells containing the sulfur-hydroxylated graphene nanocomposite cathode were cycled at C/2 rate for 1, 3, 5, or 8 cycles and rested for 3 days; each cycled cathode (discharged state) was then soaked in 8 mL of a mixed solution of DOL/DME (1:1, vol) for 5 minutes. The resulting solution was then characterized by a Cary 5000 Spectrophotometer (Varian). A baseline correction was used to deduct the influence of the mixture of DOL/DME (1:1, vol).
UV-visible absorption spectroscopy results are presented in
The cycle performance of the Li—S batteries with the sulfur-hydroxylated graphene nanocomposites possessing different sulfur contents were also compared in
Although only exemplary embodiments of the disclosure are specifically described above, it will be appreciated that modifications and variations of these examples are possible without departing from the spirit and intended scope of the disclosure. For instance, numeric values expressed herein will be understood to include minor variations and thus embodiments “about” or “approximately” the expressed numeric value unless context, such as reporting as experimental data, makes clear that the number is intended to be a precise amount.
This application claims priority under 35 U.S.C. §119 to U.S. Provisional Patent Application Ser. No. 61/776,119 filed Mar. 11, 2013. The contents of which is incorporated by reference herein in its entirety.
Number | Date | Country | |
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61776119 | Mar 2013 | US |