CN110998933A - Core-shell complexes - Google Patents

Core-shell complexes Download PDF

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CN110998933A
CN110998933A CN201880050730.9A CN201880050730A CN110998933A CN 110998933 A CN110998933 A CN 110998933A CN 201880050730 A CN201880050730 A CN 201880050730A CN 110998933 A CN110998933 A CN 110998933A
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core
transition metal
shell
mos
metal chalcogenide
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郑光远
唐伟
罗健平
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Agency for Science Technology and Research Singapore
National University of Singapore
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National University of Singapore
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J13/00Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
    • B01J13/02Making microcapsules or microballoons
    • B01J13/20After-treatment of capsule walls, e.g. hardening
    • B01J13/22Coating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J13/00Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
    • B01J13/02Making microcapsules or microballoons
    • B01J13/04Making microcapsules or microballoons by physical processes, e.g. drying, spraying
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/362Composites
    • H01M4/366Composites as layered products
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • H01M4/386Silicon or alloys based on silicon
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/58Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
    • H01M4/581Chalcogenides or intercalation compounds thereof
    • H01M4/5815Sulfides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00Nanotechnology for materials or surface science, e.g. nanocomposites
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y40/00Manufacture or treatment of nanostructures
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Abstract

The present invention relates to a core-shell composite and a method for preparing the same, wherein the core-shell composite comprises a core of non-metallic particles having a hollow internal structure, the core being encapsulated in a shell of a transition metal chalcogenide. In a preferred embodiment, the core-shell composite is molybdenum disulfide (MoS)2) Layer encapsulated hollow sulfur particles. In another embodiment, the core-shell composite may be used as a cathode material.

Description

Core-shell complexes
Cross Reference to Related Applications
The present application claims the benefit of singapore application No. 10201704587U filed on 5.6.2017, which is incorporated herein by reference.
Technical Field
The present invention generally relates to core-shell composites useful as cathode materials. The invention also relates to a method for preparing the core-shell composite and an electrode comprising the core-shell composite.
Background
With the electrification of transportation systems, the use of intermittent renewable energy sources such as solar and wind energy, there is a need to develop rechargeable batteries with higher energy density and lower cost. Lithium-sulfur (Li-S) batteries are considered to be one of the most promising approaches to overcome the above challenges, as
(1) The theoretical capacity of the sulfur cathode is high (1675 mAhg)-1Based on the original sulfur); and is
(2) The natural abundance of sulfur is high.
However, practical application of Li-S batteries faces several obstacles, such as limited cycle life. This problem is mainly attributed to the intermediate product lithium polysulfide (Li)2Sx,x>3) Dissolution into the electrolyte, large volume changes (-80%) of sulfur particles, destroying electrode structural integrity and sulfur and Li2The insulating property of S. Efforts have been made to date to address these problems by trapping soluble lithium polysulphides.
To overcome the above problems, recent studies have involved the encapsulation of sulfur in ordered porous CMK-3 carbon, and the most common strategies have been implemented to encapsulate active sulfur within conductive matrices, such as meso/microporous/hollow carbon, carbon nanotubes/fibers, and conductive polymers, among others. Although improving performance, this physical structure can only partially mitigate polysulfide leakage due to incomplete encapsulation of sulfur. Functional groups have also been introduced as encapsulation building blocks to adsorb lithium polysulphides. In particular, well-designed polymers, functionalized graphene, and nitrogen-doped carbon matrices, among others, are used to achieve strong interactions between lithium polysulfides and polar surfaces. Similar strategies can be achieved by using hydrophilic metal oxides, sulfides, metal organic frameworks, and their derivatives as lithium polysulfide sorbents. However, to date, the above attempts do not appear to solve the above problems, such as complete encapsulation of sulfur in the cathode.
Accordingly, there is a need to provide suitable cathode materials that overcome or at least ameliorate one or more of the disadvantages described above.
Disclosure of Invention
In one aspect, a core-shell composite is provided, the core-shell composite comprising a core of non-metallic particles having a hollow interior structure, the core being encapsulated in a shell of a transition metal chalcogenide.
The transition metal chalcogenide may have a layered conformal cage structure. Advantageously, each layer of the conformal cage structure may be tightly bonded together by van der Waal's interaction, making the shell mechanically strong and stable while maintaining the morphology of the composite under extreme conditions, such as when subjected to vacuum. More advantageously, the strong van der waals interactions between transition metal chalcogenide layers enable the formation of sealed nanocages for trapping non-metallic particles.
More advantageously, the hollow structure of the core, together with the layered shell (with the aforementioned van der waals interactions), can be balanced against each other to accommodate any inward volume change when the core-shell composite is stressed. When the core-shell composite is used as an electrode material, the core-shell composite undergoes lithiation, which may cause the above-described stress. Thus, the hollow structure of the core can advantageously accommodate inward volume changes during lithiation.
In another aspect, a method is provided for preparing a core-shell composite comprising a core of non-metallic particles having a hollow interior structure, the core being encapsulated in a shell of a transition metal chalcogenide, the method comprising the steps of:
a) mixing a suspension of surfactant-encapsulated non-metallic particles with a transition metal chalcogenide to combine the transition metal chalcogenide with the surfactant; and
b) removing the surfactant to obtain the core-shell complex.
In another aspect, an electrode is provided comprising a plurality of core-shell composites, wherein each composite comprises a core of non-metallic particles having a hollow interior structure, the core being encapsulated in a shell of a transition metal chalcogenide.
Advantageously, the transition metal chalcogenide of the shell may be multilayered and capable of conforming to the shape of the core, and thus, the transition metal chalcogenide may be considered to have a "layered conformal cage". The transition metal chalcogenide may exhibit good bonding with lithium polysulfide in the core, thereby preventing the intermediate product lithium polysulfide (Li)2Sx,x>3) Dissolving into the electrolyte. Further advantageously, the core particle may not have any significant volume expansion upon lithiation. As noted above, the transition metal chalcogenide or transition metal dichalcogenide may comprise a multilayered sheet, wherein the sheet may be nano-sized (hence referred to as a nanosheet). The sheet (or nanoplatelets) may have atomic defects. Advantageously, the presence of the above-mentioned atomic defects may promote the interaction between the lithium polysulphides and the core of the complex, when the lithium-sulphide battery undergoes charge-discharge cycles, thus reducing the degradation of the non-metal constituting the core.
Definition of
The following words and terms used herein shall have the indicated meanings:
as used herein, the term "composite" or "composite material" refers to a material system consisting of a mixture or combination of two or more micro-or macro-components that differ in form and chemical composition and are substantially insoluble in each other.
As used herein, the term "encapsulate" refers to the formation of one or more layers of shell material on the surface of a core particle. The encapsulation method is used to avoid dissolution of the core particles in a solvent such as an electrolyte. In addition, such encapsulation also serves to protect the core particle from degradation, for example, when the core particle is exposed to extreme conditions such as high vacuum.
As used herein, the term "exfoliation" refers to the detachment and exfoliation of one or more layers of the transition metal chalcogenide from the bulk of the transition metal chalcogenide.
The word "substantially" does not exclude "completely", e.g., a composition that is "substantially free" of Y may be completely free of Y. The word "substantially" may be omitted from the definition of the invention, if necessary.
Unless otherwise specified, the term "comprising" and grammatical variations thereof is intended to mean "open" or "inclusive" language such that they include the recited elements but also allow for inclusion of additional, unrecited elements.
As used herein, the term "about" in the context of concentrations of ingredients of a formulation generally refers to +/-5% of the stated value, more generally +/-4% of the stated value, more generally +/-3% of the stated value, more generally +/-2% of the stated value, and even more generally +/-1% of the stated value. Even more typically +/-0.5% of the value.
Throughout this disclosure, certain embodiments may be disclosed in a range format. It is to be understood that the description of the range format is merely for convenience and brevity and should not be construed as an inflexible limitation on the scope of the disclosed ranges. Thus, the description of a range should be considered to have specifically disclosed all the possible sub-ranges as well as individual numerical values within that range. For example, description of a range such as 1 to 6 should be considered to specifically disclose sub-ranges such as 1 to 3, 1 to 4, 1 to 5, 2 to 4, 2 to 6, 3 to 6, etc., as well as individual numbers within that range such as 1, 2, 3, 4, 5, 6. The interpretation applies regardless of the breadth of the range.
Certain embodiments may also be broadly and generically described herein. Each of the narrower species and subgeneric groupings falling within the generic disclosure also form part of the disclosure. This includes the generic description of embodiments with a proviso or negative limitation removing any subject matter from the genus, regardless of whether or not the excised material is specifically recited herein.
Detailed Description
Exemplary, non-limiting embodiments of core-shell composites comprising a core of non-metallic particles having a hollow interior structure encapsulated in a shell of a transition metal chalcogenide will now be disclosed.
A transition metal chalcogenide as defined herein may have a layered conformal cage structure. Each layer of the conformal cage structure may be bonded together by van der waals interactions. The layers are advantageously tightly bonded to each other due to van der waals interactions between the layers, such that the shell is mechanically strong and stable while maintaining the morphology of the composite under extreme conditions (e.g., when subjected to vacuum). Strong van der waals interactions between transition metal chalcogenide layers may allow formation of a sealed nanocage for trapping non-metallic particles.
As noted above, the hollow structure of the core, together with the layered shell (with the aforementioned van der waals interactions), can balance each other to accommodate any inward volume change when the core-shell composite is stressed. When the core-shell composite is used as an electrode material, the core-shell composite undergoes lithiation, which may cause the above-described stress. Thus, the hollow structure of the core can advantageously accommodate inward volume changes during lithiation.
The non-metallic particles of the core-shell composite as described above may be sulfur particles, silicon particles, phosphorus particles, or oxides thereof.
The transition metal in the transition metal chalcogenide as defined herein may be selected from the elements of groups 3 to 11 of the periodic table of elements. Non-limiting examples of such transition metals include zinc (Zn), titanium (Ti), vanadium (V), zirconium (Zr), chromium (Cr), molybdenum (Mo), manganese (Mn), iron (Fe), cobalt (Co), nickel (Ni), and tungsten (W). Other suitable transition metal elements not shown here may also be used.
The transition metal chalcogenide may be a transition metal monothio compound, a transition metal dichalcogenide, or a transition metal trichalcogenide. Non-limiting examples of transition metal monothio compounds include ZnX and CdX, where X is sulfur (S), selenium (Se), or tellurium (Te). Thus, such transition metal monochalcogenides may be referred to as zinc sulfide, zinc selenide, zinc telluride, cadmium sulfide, cadmium selenide, and cadmium telluride, respectively.
The transition metal dichalcogenide may be of the formula MX2Wherein X is similar to the above definition. Non-limiting examples of transition metal dichalcogenides include MoSe2、WSe2、NiSe2、CoSe2、TiSe2、MoS2、WS2、NiS2、CoS2、TiS2、MoTe2、WTe2、NiTe2、CoTe2And TiTe2. It should be understood that other suitable transition metal dichalcogenides may also be used as the shell material.
As mentioned above, transition metal trithionic compounds may also be used as shell materials.
It should be understood that each transition metal chalcogenide may have a particular stoichiometry due to the electronic structure in the transition metal chalcogenide. Thus, for a given transition metal chalcogenide, it may not exist in all of the forms described above, i.e., in the form of transition metal monothiogens, transition metal dichalcogenides, and transition metal trithiogens. For the sake of clarity, for example zinc sulphide, only as ZnS, not as ZnS2Or ZnS3Are present. Furthermore, only MoS can be present2And MoS3In form, but not as MoS.
The transition metal chalcogenide, which may be a transition metal monothio compound, a transition metal dichalcogenide compound, or a transition metal trichalcogenide compound, may be present in its crystalline form, amorphous form, or mixtures thereof. In preferred embodiments, the transition metal dichalcogenide may be in its crystalline form, amorphous form, or mixtures thereof.
The transition metal chalcogenide may have at least one layer of sheet. When the transition metal chalcogenide has at least two layers of sheets, such transition metal chalcogenide may take a layered structure and thus may be referred to as a layered transition metal chalcogenide. Thus, the transition metal monothio compounds, transition metal dichalcogenides, and transition metal trichalcogenides may be in the form of layered transition metal monothio compounds, layered transition metal dichalcogenides, and layered transition metal trichalcogenides, respectively.
In one embodiment, transition metal chalcogenides such as transition metal dichalcogenides may comprise multilayered sheets, wherein the sheets may be nano-sized (hence referred to as nanosheets). The sheet (or nanoplatelets) may have atomic defects. Defects may be generated during the exfoliation of the sheet or nanoplatelets. The presence of atomic defects in the sheet (or nanoplatelets) can make the core-shell composite, as defined herein, strong and stable. Delamination of the bulk transition metal dichalcogenide may occur due to increased spacing between the multilayered sheets. As will be further noted below, the increased spacing may be caused by the method used to form the core-shell composite.
As noted above, the layered transition metal chalcogenide, such as a layered transition metal dichalcogenide, may be a single layer, a bilayer, or a multilayer transition metal dichalcogenide. For the avoidance of doubt, the layered transition metal dichalcogenide may have 2, 3, 4, 5, 6, 7, 8, 9 or 10 layers. Preferably, the layered transition metal dichalcogenide has 4 to 10 layers, more preferably 5 to 7 layers.
The interlayer spacing of the layered transition metal chalcogenide, such as layered transition metal dichalcogenide, may be in the range of about 0.3nm to about 2nm, such as about 0.3nm to about 0.5nm, about 0.3nm to about 0.8nm, about 0.3nm to about 1nm, about 0.3nm to about 1.5nm, about 0.5nm to about 0.8nm, about 0.5nm to about 1nm, about 0.5nm to about 1.5nm, about 0.5nm to about 2nm, about 0.8nm to about 1nm, about 0.8nm to about 1.5nm, about 0.8nm to about 2nm, about 1nm to about 1.5nm, about 1nm to about 2nm, or about 1.5nm to about 2 nm. The interlayer spacing between the layers of the layered transition metal chalcogenide is preferably from about 0.5nm to about 0.8nm, more preferably from about 0.6nm to about 0.7 nm.
The core-shell composite as defined above may be structurally stable when placed under high vacuum for extended periods of time. As used herein, the term "high vacuum" refers to a pressure of about 10-4Pascal (Pa) to about 10-9A range between Pa, e.g. about 10-4Pa, about 10-5Pa, about 10-6Pa, about 10-7Pa, about 10-8Pa, about 5X 10-9Pa, about 2X 10-9Pa or about 10-9Vacuum condition of Pa. As used above, "longer period of time" refers to a period of time from about 1 minute to about 5 hours, such as about 1 minute, about 5 minutes, about 10 minutes, about 30 minutes, about 1 hour, about 2 hours, about 3 hours, about 4 hours, or about 5 hours.
The sealing structure of the shell may be capable of protecting the inner core from degradation or phase change, such as sublimation. Thus, advantageously, the core-shell composite can increase the sublimation temperature of the core particle.
The mass loading of the non-metallic particles in the core-shell composite can range from about 40 wt% to about 90 wt%, such as about 40 wt%, about 45 wt%, about 50 wt%, about 55 wt%, about 60 wt%, about 65 wt%, about 70 wt%, about 75 wt%, about 80 wt%, about 85 wt%, or about 90 wt%. The mass loading of the non-metallic particles in the core-shell composite is preferably in the range of about 60 wt% to about 90 wt%.
Furthermore, the core-shell composite as defined above may be a regularly shaped particle, such as a spherical particle, or an irregularly shaped particle.
The particle size of the core-shell composites as defined herein may be in the range of about 50nm to about 5000nm (or about 5 μm), such as about 50nm to about 100nm, about 50nm to about 200nm, about 50nm to about 500nm, about 50nm to about 800nm, about 50nm to about 1000nm, about 50nm to about 2000nm, about 50nm to about 3000nm, about 50nm to about 4000nm, about 100nm to about 200nm, about 100nm to about 500nm, about 100nm to about 800nm, about 100nm to about 1000nm, about 100nm to about 2000nm, about 100nm to about 3000nm, about 100nm to about 4000nm, about 100nm to about 5000nm, about 500nm to about 800nm, about 500nm to about 1000nm, about 500nm to about 2000nm, about 500nm to about 3000nm, about 500nm to about 4000nm, about 500nm to about 5000nm, about 1000nm to about 2000nm, about 3000nm to about 3000nm, about 2000nm, about 3000nm, about 1000 to about 2000nm, about 3000nm, From about 2000nm to about 5000nm, from about 3000nm to about 4000nm, from about 3000nm to about 5000nm, or from about 4000nm to about 5000 nm. Particle size may refer to the diameter or equivalent diameter of an irregularly shaped composite.
The particle size of the core-shell composites as defined herein is preferably in the range of about 100nm to about 1000nm (or about 1 μm), more preferably in the range of about 300nm to about 800 nm.
Thus, with respect to the above aspects, there is also provided a core-shell composite comprising a core of non-metallic particles having a hollow interior structure, the core being encapsulated in a shell of a transition metal chalcogenide, wherein the core is partially or fully (or completely) encapsulated by the shell.
Exemplary, non-limiting embodiments of methods for making a core-shell composite comprising a core of non-metallic particles having a hollow interior structure, the core being encapsulated in a shell of a transition metal chalcogenide will now be disclosed.
There is provided a process for preparing a core-shell composite comprising a core of non-metallic particles having a hollow interior structure, the core being encapsulated in a shell of a transition metal chalcogenide, the process comprising the steps of:
a) mixing a suspension of surfactant-encapsulated non-metallic particles with a transition metal chalcogenide to combine the transition metal chalcogenide with the surfactant; and
b) the surfactant is removed to obtain the core-shell complex.
The above method can be considered as a self-assembly process in which spontaneous recombination occurs without an external stimulus or initiator due to the binding between the surfactant and the transition metal chalcogenide. When the surfactant is removed, such as in step (b), the transition metal chalcogenide may be considered as a shell that at least partially encapsulates the core of the non-metallic particle having a hollow interior structure. Thus, the shell of the transition metal chalcogenide may substantially entirely or completely encapsulate the core of the non-metallic particle having a hollow interior structure.
The transition metal chalcogenide used in the above method may be a exfoliated transition metal chalcogenide. Accordingly, there is also provided a process for preparing a core-shell composite comprising a core of non-metallic particles having a hollow interior structure, the core of the non-metallic particles being encapsulated in a shell of a transition metal chalcogenide, the process comprising the steps of:
a) mixing a suspension of surfactant-encapsulated non-metallic particles with a exfoliated transition metal chalcogenide to combine the exfoliated transition metal chalcogenide with the surfactant; and
b) the surfactant is removed to obtain the core-shell complex.
Similar to the above, this method can be considered as a self-assembly process in which spontaneous recombination occurs without an external stimulus or initiator due to the bonding between the surfactant and the exfoliated transition metal chalcogenide. When the surfactant is removed, such as in step (b), the exfoliated transition metal chalcogenide may be considered as a shell that at least partially encapsulates the core of the non-metallic particle having a hollow interior structure. Thus, the shell of the exfoliated transition metal chalcogenide may substantially entirely or completely encapsulate the core of the non-metallic particle having a hollow interior structure.
The non-metallic suspension may be highly dispersed, such as monodisperse. As mentioned above, the non-metallic particles may be sulphur particles, silicon particles, phosphorus particles or oxides thereof.
The methods described herein may further comprise: before the mixing step (a), steps a-i) mix the nonmetallic precursor with a surfactant under conditions of a suitable temperature and a suitable medium.
Specifically, the surfactant-encapsulated non-metallic suspension may be prepared by mixing the non-metallic precursor with the surfactant in a suitable medium at room temperature, such as about 20 ℃ to about 30 ℃, and then adding the acid to form a mixture. The room temperature can be about 20 ℃, about 21 ℃, about 22 ℃, about 23 ℃, about 24 ℃, about 25 ℃, about 26 ℃, about 27 ℃, about 28 ℃, about 29 ℃ or about 30 ℃. The mixture is then stirred at room temperature for about 1 to 3 hours (e.g., about 1 hour, about 2 hours, or about 3 hours) to provide a solid product.
Thus, steps a-i) of the methods described herein may further comprise: step a-ii) adding an acid to the mixture obtained from step a-i).
The step of preparing the surfactant encapsulated non-metallic suspension may be performed in a single step at room temperature. Thus, it will be appreciated that this step can be scaled up industrially. The solid product containing the surfactant-encapsulated non-metallic particles can be separated from the reaction medium using suitable separation techniques known in the art. Non-limiting examples of separation techniques used herein are filtration and centrifugation.
The surfactant-encapsulated non-metallic particles obtained from this step may be redispersed in a suitable medium and collected again by a suitable separation technique. Finally, the surfactant encapsulated non-metallic particles obtained from this step may be re-dispersed in distilled water to provide a surfactant encapsulated non-metallic suspension for further use. The concentration of the surfactant encapsulated non-metallic suspension may be about 1mg mL-1To about 6mg mL-1E.g. about 1mg mL-1About 2mg mL-1About 3mg mL-1About 4mg mL-1About 5mg mL-1Or about 6mg mL-1Preferably about 4mg mL-1
The nonmetallic precursor used to prepare the above-described surfactant-encapsulated nonmetallic suspension may be selected from salts, solvates, or hydrates of the nonmetallic precursor. If surfactant encapsulated sulfur particles are desired, a sulfur-containing salt, such as sodium thiosulfate, can be used. It is to be understood that the sulfur-containing salts provided herein are not limiting and thus can be extended to other suitable sulfur-containing salts.
In the above method, the acid may be selected from weak acids, strong acids, organic acids or inorganic acids. Preferred acids are strong acids, more preferred acids are strong mineral acids such as hydrochloric acid.
Suitable media may be selected from organic solventsAn agent, an aqueous solution or a mixture of an organic medium and an aqueous medium forming a single phase, preferably an aqueous medium of polyvinylpyrrolidone (PVP) solution. When PVP is used, its concentration in solution may be about 0.1M (1M ═ 1mol L)-1) To about 1M, such as about 0.1M, about 0.2M, about 0.3M, about 0.4M, about 0.5M, about 0.6M, about 0.7M, about 0.8M, about 0.9M, about 1M, preferably about 0.4M.
Furthermore, when a PVP solution is used, the molecular weight of the PVP may be in the range of about 30000Da to about 100000Da, such as about 30000Da, about 40000Da, about 50000Da, about 60000Da, about 70000Da, about 80000Da, about 90000Da or about 100000 Da.
The transition metal chalcogenide or exfoliated transition metal chalcogenide may be prepared by contacting a transition metal chalcogenide with a lithium precursor to form a transition metal chalcogenide or exfoliated transition metal chalcogenide. For the avoidance of doubt, steps a-iii) may be carried out to contact the transition metal chalcogenide with a lithium precursor to form a exfoliated transition metal chalcogenide prior to step (a) of the process described herein. The lithium precursor used may be an organolithium solution as defined below.
The transition metal chalcogenide or exfoliated transition metal chalcogenide may be prepared by lithium intercalation or other suitable methods. When lithium intercalation is used, the transition metal chalcogenide crystals may be dissolved in an organolithium solution in an anhydrous organic solvent under an inert atmosphere to produce Lix-a transition metal chalcogenide. This product can be recovered with an anhydrous organic solvent through a separation-washing cycle to remove excess lithium and organic residues. The product may then be dried, redissolved in an aqueous medium, and sonicated for about 30 minutes to about 2 hours, such as about 30 minutes, about 60 minutes, about 90 minutes, or about 2 hours, to allow the exfoliation process to occur. The peeling may occur partially or completely. However, it should be understood that complete stripping is desirable.
Li can be achieved by inserting solvent molecules such as water molecules into van der Waal's layersx-exfoliation of transition metal chalcogenides. Insert water moleculeTo mean forced hydration of lithium intercalation into the transition metal chalcogenide. The exfoliated transition metal chalcogenide suspension may be collected for further use at a concentration of about 0.5mg mL-1To about 4mg mL-1In a range of (1), such as about 0.5mg mL-1About 1mg mL-1. About 1.5mg mL-1About 2mg mL-1About 2.5mgmL-1About 3mg mL-1About 3.5mg mL-1Or about 4mg mL-1
The core-shell composite as defined herein may be prepared by mixing the surfactant-encapsulated non-metallic suspension and the exfoliated transition metal chalcogenide suspension with agitation for about 30 minutes to about 2 hours, such as about 30 minutes, about 60 minutes, about 90 minutes, or about 2 hours. The core-shell complex may be collected by at least 3 separation-washing cycles. Thus, the separation-washing cycle may suitably be repeated at least 3, 4, 5, 6, 7, 8, 9, 10 or more times. The separation-washing step can remove surfactants and impurities. The exfoliated transition metal chalcogenide (which may be in the form of a flake) may compact and encapsulate the core after removal of surfactants and impurities. Thus, when the core-shell complex is formed, the complex may be free of solvents or impurities, such as water molecules.
Non-limiting examples of the organolithium solution include a butyllithium solution, a pentyllithium solution, or a hexyllithium solution, and preferably a butyllithium solution. In one embodiment, the organic solvent used may be selected from N-methyl-2-pyrrolidone, pentane, hexane, heptane or octane. In another embodiment, inert atmosphere may refer to an atmosphere substantially free of oxygen or oxidizing agents, and thus may refer to an atmosphere under nitrogen or argon. In one embodiment, the drying process may be performed using a suitable drying technique. Non-limiting examples of drying techniques include vacuum and heat.
The exfoliated transition metal chalcogenide may be as described above. The exfoliated transition metal chalcogenide may be in the form of a sheet or sheet. The lateral dimension of the lamellae as described above may be in the range of about 200nm to about 2 μm (or 2000nm), such as about 200nm to about 400nm, about 200nm to about 600nm, about 200nm to about 800nm, about 200nm to about 1000nm, about 200nm to about 1500nm, about 400nm to about 600nm, about 400nm to about 800nm, about 400nm to about 1000nm, about 400nm to about 1500nm, about 400nm to about 2000nm, about 600nm to about 800nm, about 600nm to about 1000nm, about 600nm to about 1500nm, about 600nm to about 2000nm, about 800nm to about 1000nm, about 800nm to about 1500nm, about 800nm to about 2000nm, about 1000nm to about 1500nm, about 1000nm to about 2000nm, or about 1500nm to about 2000 nm. Such transverse dimension refers to the dimension of one or more faces of the sheet.
When the nonmetal suspension is mixed with the exfoliated transition metal chalcogenide compound and then subjected to a separation-washing cycle as described above, flakes of the exfoliated transition metal chalcogenide compound may adhere or bond to the surfactant on the surface of the hollow structure of the nonmetal particles and may be stacked together due to van der Waal's attraction. The exfoliated transition metal chalcogenide flakes may encapsulate (or at least partially encapsulate) the hollow structure of the non-metallic particles after removal of the surfactant. Due to electrostatic interaction, the flakes can encapsulate the hollow structure of the non-metallic particles. The surfactant is then removed during the separation-wash cycle, as the surfactant is soluble in the solution.
Suitable surfactants used may be polymers containing hydrophilic groups selected from polyvinylpyrrolidone, polyvinylpyridine, polyvinylimidazole, preferably polyvinylpyrrolidone, or non-polymeric surfactants such as sodium stearate or dodecylbenzene sulfonate.
Exemplary, non-limiting embodiments of electrodes comprising a plurality of core-shell composites will now be disclosed, wherein each composite comprises a core of non-metallic particles having a hollow interior structure, the core being encapsulated in a shell of a transition metal chalcogenide.
The transition metal chalcogenide may have a layered conformal cage structure. As described above, each layer of the conformal cage structure may be bonded together by van der Waals interactions.
Electrodes comprising various core-shell composites as defined above may be used for lithium-sulfide electricityAnd (4) a pool. Advantageously, the layered conformal cage of transition metal chalcogenides exhibits good bonding with lithium polysulfide, thereby preventing intermediate lithium polysulfide (Li)2Sx,x>3, such as 4, 5, 6, 7, 8, 9 or 10) is dissolved into the electrolyte. Further advantageously, upon lithiation, the core particle does not have any significant volume expansion.
As noted above, the transition metal chalcogenide or transition metal dichalcogenide may comprise a multilayered sheet, wherein the sheet may be nano-sized (hence referred to as a nanosheet). The sheet (or nanoplatelets) may have atomic defects. Advantageously, the presence of the above-mentioned atomic defects promotes the interaction between the lithium polysulphides and the core of the complex when the lithium-sulphide battery undergoes charge-discharge cycles, thereby reducing the degradation of the non-metal constituting the core.
In one embodiment, the loading mass of the core-shell composite loaded into the electrode may be about 0.5mg cm-2To about 10mg cm-2E.g. about 0.5mg cm-2To about 1mg cm-2About 0.5mg cm-2To about 2mg cm-2About 0.5mg cm-2To about 5mg cm-2About 1mg cm-2To about 2mg cm-2About 1mg cm-2To about 5mg cm-2About 1mg cm-2To about 10mg cm-2About 2mg cm-2To about 5mg cm-2About 2mg cm-2To about 10mg cm-2Or about 5mg cm-2To about 10mg cm-2
The electrodes may be prepared according to methods known in the art, except that the material of the electrode is replaced with the core-shell composite disclosed herein. For example, the electrode may be prepared by mixing Vapor Grown Carbon Fiber (VGCF) and polyvinylidene fluoride (PVDF) binder with a core-shell composite in N-methyl-2-pyrrolidone (NMP) to form a slurry. The slurry can be coated onto a copper foil and dried under vacuum overnight.
In one embodiment, the electrode may be used in a battery. The battery may be used in electric vehicles and stationary storage systems. In one embodiment, the electrode can achieve up to about 1660mAhg-1High specific capacity of (2).The specific capacity may be a discharge capacity. Advantageously, the electrodes can achieve about 500mAhg when charged/discharged at higher rates such as 3C and 5C, respectively-1To 600mAhg-1And about 300mAhg-1To 450mAhg-1The discharge capacity of (2).
An electrode as defined herein may have long term stability, 1000 cycles at 1C, with a decay of about 0.049% per cycle. Improved electrochemical performance can be observed by discharging the capacity with a current in the range of about 0.1C to about 5C.
As will be appreciated by those skilled in the art, significant problems associated with the practical application of Li-S batteries include the intermediate product lithium polysulfide (Li)2Sx,x>3) Dissolution into the electrolyte, large volume change of sulfur particles and destruction of electrode structural integrity and sulfur and Li2The insulating properties of S can be addressed by the disclosure including the invention shown in the examples provided.
Drawings
The drawings illustrate the disclosed embodiments and serve to explain the principles of the disclosed embodiments. It is to be understood, however, that the drawings are designed solely for the purposes of illustration and not as a definition of the limits of the invention.
FIG. 1 shows a schematic view of a
[ FIG. 1 ] A]Is a MoS as described in example 12A plurality of images and graphs obtained from characterization of the sheeting. FIG. 1A: MoS2Scanning Transmission Electron Microscope (STEM) images of the flakes, field of view (FOV)2048 nm; FIG. 1B: MoS2High resolution STEM images of the lamella, FOV 16 nm; FIG. 1C: MoS2Atomic STEM image of the flake, FOV 2.5 nm; FIGS. 1D-1F: images from simulation, indicating MoS2Sulfur vacancy based defects on the flakes. The FOV of FIG. 1D is 1.5 nm; FIG. 1G: vapor Grown Carbon Fiber (VGCF), reduced graphene oxide (rGO), and MoS2Flakes with 0.005mol L-1Li of (2)2S9A digital image of the solution mixture; FIG. 1H: with Li2S9Solution treated MoS2Raman spectra of the flakes (labeled regions are magnified in fig. 1I).
FIG. 2
[ FIG. 2 ]]Is MoS before and after treatment with 1-undecanethiol as described in example 12Fourier transform infrared spectroscopy (FTIR) spectroscopy. The figure also depicts CH2Asymmetric telescopic, CH2Symmetrically telescopic, CH2Characteristic bands of shear and C-S stretch.
FIG. 3
[ FIG. 3 ]]Is a MoS as described in example 12And MoS treated with 1-undecanethiol2(blocked MoS)2) With 0.005M Li2S9A mixed digital image.
FIG. 4
[ FIG. 4 ]]Is a description of the step (a) synthesis procedure and step (b) MoS set forth in example 22Schematic representation of lithiation/delithiation process of cage-encapsulated hollow sulfur spheres. FIG. 4A depicts a MoS2The whole process of the cage-encapsulated hollow sulfur spheres (synthesis process and lithiation/delithiation process). The arrows depict the MoS substantially encapsulating hollow sulfur spheres (or cores)2A cage; FIG. 4B shows that soluble lithium polysulfides can be effectively trapped in MoS2Inside the cage. The figure shows the MoS as shown in FIG. 4A2An enlarged version of the cage-encapsulated hollow sulfur spheres (arrows depict MoS's that substantially encapsulate the hollow sulfur spheres (or sulfur cores)2A cage).
FIG. 5
[ FIG. 5 ]]Is a MoS as described in example 22Characterization of cage-encapsulated hollow sulfur spheres a plurality of Scanning Electron Microscope (SEM) images were obtained. FIGS. 5A-5D: MoS with magnification of 100x, 10000x, 75000x and 65000x respectively2SEM image of @ S complex; FIG. 5E: SEM image of sulfur ball, magnification is 20000 x; and FIG. 5F: mixing MoS2Hollow MoS after sulfur removal in cage-encapsulated hollow sulfur spheres2SEM image of the skeleton at magnification 20000 x.
FIG. 6
[ FIG. 6 ]]Is a MoS as described in example 22Cage-encapsulated hollow sulfur spheres (MoS)2@ S complex) of the sample. FIG. 6A: MoS2Cage-encapsulated hollow sulfur spheres (MoS)2@ S Complex) Transmission Electron microscope (STEM)) Image, magnification 87000 ×; FIG. 6B: MoS2Cage-encapsulated hollow sulfur spheres (MoS)2@ S complex) at a magnification of 87000 x; FIG. 6C: MoS2Cage-encapsulated hollow sulfur spheres (MoS)2@ S composite) energy dispersive X-ray (EDX) line scans; FIGS. 6D-6F: MoS at magnifications of 435000x (D), 435000x (E) and 620000x (F), respectively2Cage-encapsulated hollow sulfur spheres (MoS)2@ S complex); FIGS. 6G-6I: MoS with magnification of 87000x (G), 40000x (H) and 435000x (F), respectively2Cage-encapsulated hollow sulfur spheres (MoS)2@ S complex) showing MoS2The layered stack of cages remains continuous throughout the bending zone.
FIG. 7
[ FIG. 7 ]]Is the MoS described in example 22@ S Complex and MoS2A plurality of charts and tables of EDX analysis of empty cages.
FIG. 8
[ FIG. 8 ]]Is MoS2Multiple X-ray powder diffraction (XRD) patterns of the @ S complex. Fig. 8B is an enlarged XRD pattern of the marked area of fig. 8A.
FIG. 9
[ FIG. 9 ]]Is a MoS as described in example 22@ S composite, pristine sulfur spheres and pristine MoS2A thermogravimetric analysis (TGA) of (a).
FIG. 10 shows a schematic view of a
[ FIG. 10 ]]Is a MoS as described in example 32Cage-encapsulated hollow sulfur spheres (MoS)2@ S complex) are obtained. FIG. 10A: MoS2The charge/discharge curves of the @ S complex at different rates; FIG. 10B: MoS2The circulating capacity of the @ S compound under different multiplying powers; FIG. 10C: MoS2The long-term cycling ability at 0.5C of @ S composite, rGO (rGO @ S) mixed with sulfur spheres, and original sulfur spheres; FIG. 10D: MoS2Long-term cycling ability of the @ S complex at 1C; FIG. 10E: based on MoS2The @ S digital image demonstrating the soft-package battery; FIG. 10F: using MoS-based2The @ S digital image demonstrating that the soft package battery supplies power to the LED lamp; FIG. 10G: using MoS-based2Demonstration of @ SAnd the digital image shows that the soft package battery supplies power for the small electric fan.
FIG. 11
[ FIG. 11 ]]Is prepared from MoS before and after lithiation as described in example 42Cage-encapsulated hollow sulfur spheres (MoS)2@ S complex) of the sample. FIG. 11A: with loading of MoS2A digital image of a pouch cell of a glassy carbon substrate of @ S; fig. 11B and 11C: MoS before lithiation2SEM images of @ S complex at 50000x and 10000x magnification, respectively; fig. 11D and 11E: MoS after lithiation2SEM images of @ S complex at 50000x and 10000x magnification, respectively; FIG. 11F: MoS before and after lithiation2@ S particle size statistics.
Examples
Non-limiting examples of the present invention and comparative examples will be further described in more detail by referring to specific examples, which should not be construed as limiting the scope of the present invention in any way.
Example 1: defect modified MoS2Solution stripping and characterization of flakes
In order to obtain highly dispersed single/multilayer MoS2Aqueous suspension of flakes, first of all, commercially available MoS2The powder is intercalated with lithium to form LixMoS2Which is then easily exfoliated by forced hydration with the aid of sonication. As can be seen in the Scanning Transmission Electron Microscope (STEM) image shown in FIG. 1A, a typical MoS2The thickness of the sheet ranges from a single layer to multiple layers, with transverse dimensions of up to several microns. Typical void defects generated during the lift-off process may be in the MoS2Clearly observed on the sheets (see fig. 1B). Based on the expanded and simulated STEM images, these defects were shown to have a high concentration of sulfur vacancies (see fig. 1C and 1D).
To detect Li2SxTo MoS2Chemisorption of the flakes to produce 0.005mol L-1Li2S9DOL/DME (1:1v/v) solution and with MoS2The powders were mixed in an argon-filled glove box (DOL: 1, 3-dioxolane, available from St.Louis, Mo., USAgamma-Aldrich (Sigma-Aldrich); DME: dimethyl ether, available from Sigma-Aldrich of st louis, missouri, usa. As shown in FIG. 1G, yellow Li2S9The solution is mixed with a small amount of MoS2Complete decolorization upon flake powder mixing, indicating MoS2Flake pair Li2SxThe chemical adsorption of (A) is strong. With Li2S9After solution treatment, MoS2Raman spectrum of the flake powder showed 198cm-1、225cm-1And 490cm-1Centered on a new broad peak, they are very close to the characteristic absorbance of the S — S bond in lithium polysulfides (see fig. 1H).
Typical MoS2Red shift in absorbance to Li2Sx-MoS2Evidence is provided for complex formation (see figure 1I). In contrast, no Li was observed after mixing with Vapor Grown Carbon Fiber (VGCF) called conductive additive2S9A distinct color change of the solution. When mixed with similar amounts of rGO powder (which has been used as a lithium polysulfide blocker), only slight color decay was observed, indicating that lithium polysulfide vs MoS compared to reduced graphene oxide (rGO) powder2The capturing of flake powder is more efficient. Lithium polysulfide to MoS2The strong chemisorption of the flakes was attributed to MoS2The sulfur vacancy concentration on the flakes is high. To further demonstrate this, 1-undecanethiol (which has been shown to compensate for sulfur vacancies via sulfhydryl groups) was used to block MoS2Sulfur vacancies in the flakes (see fig. 2). Furthermore, blocking sulfur vacancies significantly reduces lithium polysulfide to MoS as shown in fig. 32Binding on the flakes, indicating lithium polysulfide to MoS2The chemisorption of sulfur vacancies on the flakes was strong.
Example 2: MoS2Synthesis and characterization of cage-encapsulated hollow sulfur spheres
In addition to the strong chemisorption of lithium polysulfides to sulfur vacancies, the effective physical confinement of sulfur can also enable strong trapping of lithium polysulfides and effective accommodation of outward volume expansion during lithiation. MoS2The cage encapsulation must be highly conformal to provide consistent protection for each sulfur sphere. Thus, the present embodiment illustratesA unique and easily implemented synthesis method using MoS2A highly dispersed suspension of flakes and polyvinylpyrrolidone (PVP) encapsulated hollow sulfur spheres was developed as shown in fig. 4A.
a) Preparation of a monodisperse solution of PVP-sulphur particles
A monodisperse solution of PVP-sulfur particles (hereinafter abbreviated to PVP-S) was prepared by a solution synthesis method. In a typical synthesis, 50mL of 80mM aqueous sodium thiosulfate (Sigma-Aldrich, St. Louis, Mo.) is mixed with 50mL of 0.4M PVP (molecular weight-55000, Sigma-Aldrich, St. Louis, Mo.) at room temperature. Then, 0.4mL of concentrated HCl was added to Na with magnetic stirring2S2O3In PVP solution. After stirring at room temperature for 2 hours, the product was collected by centrifugation at 7000rpm for 10 minutes. The product was then redispersed in a 0.4M PVP solution and collected again by centrifugation at 6000rpm for 10 minutes. The product was redispersed in distilled water for use. The resulting solution was designated solution A and had a concentration of about 4mg mL-1
b) Peel-off MoS2Preparation of the suspension of
By intercalating lithium into MoS under sonication2Forced hydration to prepare MoS2A dispersion. By mixing 2g of natural MoS in a glove box filled with argon2Crystals (Sigma-Aldrich from st louis, missouri) were stirred in 20mL of a solution of 1.6M butyllithium (Sigma-Aldrich from st louis, missouri) in anhydrous hexane to effect lithium intercalation. Then, Li was recovered by filtrationxMoS2And washed with anhydrous hexane to remove excess lithium and organic residues. After vacuum drying, Li is addedxMoS2Mixed with water and placed in an ultrasonic bath for 1 hour. By insertion of water molecules into the van der Waals layer, Li is achievedxMoS2Peeling off. Then, MoS is collected2A suspension of flakes was kept in reserve at a concentration of about 1mg mL-1(referred to as solution B).
c)MoS2@ S compositePreparation of the substance
In a typical synthesis, 20mL of solution a is added to 40mL of solution B with stirring. After stirring for 1 hour, the MoS was collected by filtration2Encapsulated sulfur particle product (MoS)2@ S complex) washed with water/methanol (3 times) to remove polymer and impurities.
MoS when mixed with PVP-S suspension2The flakes adhered to the PVP on the surface of the hollow sulfur spheres, stacked together due to van der waals attraction, and wrapped around the sulfur spheres after the polymer was removed (see fig. 4A and 4B). FIGS. 5A-5D illustrate MoS2Typical Scanning Electron Microscope (SEM) images of the @ S composite, which exhibited a morphology and spherical diameter similar to its sulfur sphere precursor shown in figure 5E, but with a rough surface with typical wrinkles. These wrinkles result from the 2D flakes being re-stacked on the surface of the sulfur spheres. During SEM characterization, sublimation of sulfur in a high vacuum system can produce significant pores and cracks on the bare sulfur spheres, as shown in fig. 5E. In contrast, conformal MoS2The cladding may prevent sublimation of the internal sulfur in a high vacuum, indicating effective physical encapsulation of the sulfur. The MoS is depicted in FIG. 5F2Hollow MoS after sulfur removal in cage-encapsulated hollow sulfur spheres2SEM image of the skeleton.
The Transmission Electron Microscope (TEM) image shown in FIG. 6A and the STEM image of FIG. 6B clearly show MoS2The spherical form of the @ S complex. The energy dispersive X-ray (EDX) line scan clearly indicates the distribution of sulfur signal and High Angle Annular Dark Field (HAADF) intensity as shown in fig. 6C. It should be noted that since the Mo La peak and the S Ka peak substantially overlap, the MoS may be adjusted based on additional considerations of the contribution of the Mo Ka line in the EDX pattern shown in FIG. 72Composition of sulfur in the @ S complex.
High resolution TEM images show MoS with crystalline sulfur spheres stacked in multiple layers (5-7 layers)2The sheet is conformally wrapped, as shown in FIGS. 6D and 6E, to form MoS2A nanocage. FIG. 6F shows a typical MoS2The nano-cage has a van der Waals gap of about 0.61 nm; the presence of (026) facets in high resolution TEM (HR-TEM) demonstrates the crystalline nature of the sulfur globules. Up to now, the steam pressure of sulfur has been highTherefore, elemental sulfur was not characterized for lattice resolution using high vacuum TEM.
By MoS2The sulfur spheres can survive for long periods of time in high vacuum TEM under 200KV electron irradiation and can be characterized multiple times without structural degradation. In MoS2Defects and/or distortions can be observed in HR-TEM images of nanocages (see fig. 6D and 6F, highlighted with blue circles). Multi-layer stack structure allowing MoS2Defects exist on the nanocages while preventing sublimation of sulfur. In addition to acting as an effective chemisorbent for soluble lithium polysulfides, these defects provide unique channels for transporting lithium ions during lithiation/delithiation.
The X-ray powder diffraction (XRD) pattern as shown in FIG. 8 further confirmed the crystallinity of the hollow sulfur spheres and MoS outside the sulfur particles2And (4) uniformly wrapping. MoS based on thermogravimetric analysis (TGA) shown in FIG. 92The sulfur mass loading in the @ S composite is about 65%, which is a relatively high mass loading. After removal of sulfur spheres by vacuum heating (as evidenced by EDX analysis shown in fig. 7), the free standing MoS2The structure of the cage remains intact as shown in fig. 6G and 6H. The HR-TEM image in FIG. 6I clearly shows MoS2The layered stack structure of the cage remains continuous throughout the bending region, which may partially accommodate the outward volume expansion of the sulfur spheres during lithiation.
Example 3: MoS2Cage-encapsulated hollow sulfur spheres (MoS)2@ S composite) electrochemical performance
Evaluation of MoS Using Li half-cell (2032 type)2Electrochemical performance of @ S composite. Vapor Grown Carbon Fiber (VGCF) and polyvinylidene fluoride (PVDF) binder with MoS2The @ S complex was mixed in N-methyl-2-pyrrolidone (NMP) to form a slurry, thereby preparing a load mass of-1.5 mg cm-2The working electrode of (1). The slurry was then coated onto copper foil and dried under vacuum overnight. Testing the cell at room temperature at a potential range of 1.6V or 1.8V to 2.6V; and the specific capacity was calculated based on the mass of sulfur only.
When the compound is mixed at different magnifications (0.1C, 0.2C, 0.5C, 1C and 2C, wherein,1C=1672mAhg-1) At the time of evaluation, MoS2@ S exhibits a characteristic Li-S voltage curve, as shown in FIG. 10A. At 0.1C, MoS2@ S shows 1660mAhg-1Based on the mass of sulfur, whereas at higher rates of 0.2C, 0.5C, 1C and 2C, 1430mAhg can be obtained, respectively-1、1137mAhg-1、930mAhg-1And 720mAhg-1The discharge capacity of (2).
Two plateau discharge curves for a typical sulfur cathode can be obtained at various feature rates (fig. 10B). MoS when charged/discharged at higher rates of 3C and 5C2@ S may be implemented as 508mAhg, respectively-1And 305mAhg-1The discharge capacity of (2) is as shown in fig. 10B. MoS considering the insulating properties of sulfur and its lithiated products2This rate capability of @ S is considered significant.
It is important to note that 2H-MoS2(semiconductor) will partially convert to a metallic 1-T phase upon lithiation, having 10-100S cm-1High electrical conductivity. This high conductivity can improve the utilization of insulating sulfur and its lithiated intermediates.
FIG. 10C illustrates MoS2The cyclability of the @ S complex and control samples (sulfur spheres, sulfur spheres mixed with rGO, abbreviated rGO/S) at 300 cycles at 0.5C. MoS2The discharge capacity of @ S shows a gradual increase in the initial cycle, which can be explained as sulfur goes through MoS2Increased accessibility of defect/distortion diffused lithium ions on the sheet, and 2-H MoS2Gradual conversion to 1-T metal MoS2The effectiveness of the sulfur is increased. After the initial activation process, by MoS2@ S the battery exhibited 956mAhg of capacity even after 300 cycles-1Shows a higher capacity retention of 83.2% (of the initial discharge capacity) with a capacity fade of 0.056% per cycle. In the absence of MoS2In the case of the cage, the battery made of sulfur spheres showed rapid capacity fade at the initial cycle, and after 300 cycles, the capacity retention rate was only 49.1%, demonstrating MoS2The cage plays an important role in preventing leakage of the active material during long-term cycling.
As shown in fig. 10C, the mixture of rGO was able to partially mitigate the severe initial capacity fade of the sulfur spheres. However, the capacity retention of the battery made from rGO/S after 300 cycles was about 50.2%, with a capacity fade of 0.166% per cycle (vs MoS)2Much higher compared to @ S), which is similar to sulfur sphere electrodes, suggesting that rGO with functional groups on the surface can only partially retain polysulfides for a limited number of cycles. When cycling at 1C, by MoS2The battery made of @ S also exhibited good cycling ability. At 1C, the cell exhibited up to 585mAhg-1A slight capacity fade of 0.0449% per cycle was achieved (see fig. 10D).
Finally, the mass ratio of the product can be easily increased, since the synthesis step is easy to implement. At load masses up to 30-40mg (based on sulfur mass), pouch cells can be assembled as shown in fig. 10E, which can power LED lamps and can even power small fans, as shown in fig. 10F and 10G.
Example 4: MoS after lithiation2Characterization of the @ S Complex
To evaluate MoS after lithiation2Volume expansion of the @ S Complex2The @ S composite was dispersed and drop cast on a 20 x 1mm glass carbon plate without the addition of carbon conductive and polymeric binders. Using a carrier loaded with MoS2The pouch cell was assembled in a glove box filled with argon gas using a glassy carbon plate of @ S composite as a working electrode and Li foil as a counter electrode (fig. 11A).
After lithiation to 1.5V at 0.5C, the glassy carbon plates were recovered from the pouch cells and rinsed with a mixed solution of 1,3-DOL and DME (1: 1V/V). MoS on a glassy carbon substrate before and after the first lithiation is depicted in FIGS. 11B-11E2Typical SEM images of the @ S complex. MoS2The size distribution of @ S is shown in FIG. 11F. Based on the above results, MoS can be inferred2The spherical morphology of @ S remains intact after lithiation. In addition, MoS before and after lithiation2No significant size differences were observed in @ S. The results show that MoS2The cage can effectively avoid the volume expansion of the sulfur ball, and the hollow space in the sulfur ball can be suitableInward volume expansion upon lithiation. A well-preserved morphology may help maintain a stable electrode-electrolyte interface, limiting leakage of lithium polysulfide into the electrolyte.
Industrial applicability
As described above, since the theoretical capacity of the sulfur cathode is high and the natural abundance of sulfur is high, the Li-S battery is considered to be good. Thus, such rechargeable Li-S batteries with high specific energy may find wide application, such as in electric vehicles (including high altitude long endurance drones or HALE UAVs) as well as in fixed storage systems.
Obviously, various other modifications and adaptations of the present invention will be apparent to those skilled in the art after reading the foregoing disclosure without departing from the spirit and scope of the invention, and all such modifications and adaptations are intended to fall within the scope of the appended claims.

Claims (22)

1. A core-shell complex comprising: a core of a non-metallic particle having a hollow interior structure, the core being encapsulated in a shell of a transition metal chalcogenide.
2. The core-shell composite of claim 1 wherein the non-metallic particles are sulfur, silicon, phosphorus particles, or oxides thereof.
3. The core-shell complex of claim 1 or claim 2 wherein the transition metal in the transition metal chalcogenide is selected from the group consisting of group 3 to group 11 elements of the periodic table.
4. The core-shell complex of any one of the preceding claims wherein the transition metal chalcogenide is a transition metal dichalcogenide.
5. The core-shell complex of claim 4 wherein the transition metal dichalcogenide is selected from the group consisting of: MoSe2、WSe2、NiSe2、CoSe2、TiSe2、MoS2、WS2、NiS2、CoS2、TiS2、MoTe2、WTe2、NiTe2、CoTe2And TiTe2
6. The core-shell complex of claim 4 or claim 5 wherein the transition metal dichalcogenide is in a crystalline form, an amorphous form, or a mixture thereof.
7. The core-shell composite of any of claims 4 to 6 wherein the transition metal dichalcogenide comprises at least one layer of sheet.
8. The core-shell composite of any of claims 4 to 6 wherein the transition metal dichalcogenide comprises at least two layers of sheet material.
9. The core-shell composite of claim 7 or claim 8 wherein the at least one sheet or the at least two sheets of the transition metal dichalcogenide have atomic defects.
10. The core-shell composite of claim 8 wherein the transition metal dichalcogenide comprising at least two layers of sheet material has an interlayer spacing in the range of 0.3nm to 2 nm.
11. The core-shell composite of any of claims 1 to 10 wherein the non-metallic particles are present in a range of 40 wt% to 90 wt% based on the total weight of the core-shell composite.
12. The core-shell complex of any one of claims 1 to 11 wherein the particle size is in the range of 50nm to 5 mm.
13. A process for preparing a core-shell composite comprising a core of non-metallic particles having a hollow interior structure, said core being encapsulated in a shell of a transition metal chalcogenide, said process comprising the steps of:
a) mixing a suspension of surfactant-encapsulated non-metallic particles with a transition metal chalcogenide to combine the transition metal chalcogenide with the surfactant; and
b) removing the surfactant to obtain the core-shell complex.
14. The method of claim 13, further comprising: before the mixing step (a), steps a-i) mix the nonmetallic precursor with a surfactant under conditions of a suitable temperature and a suitable medium.
15. The method of claim 14, further comprising: step a-ii) adding an acid to the mixture obtained from step a-i).
16. A method according to claim 14 or claim 15, wherein the nonmetallic precursor is in the form of a salt, a solvate, or a hydrate.
17. The method of claim 15, wherein the acid is a weak acid, a strong acid, an organic acid, or an inorganic acid.
18. The method of any of claims 13-17, wherein the transition metal chalcogenide is a exfoliated transition metal chalcogenide.
19. The method as recited in claim 18, further comprising: prior to step (a), steps a-iii) contacting the transition metal chalcogenide with a lithium precursor to form the exfoliated transition metal chalcogenide.
20. The method of claim 18 or claim 19, wherein the exfoliated transition metal chalcogenide is in the form of a flake or sheet.
21. The method of claim 20, wherein the exfoliated transition metal chalcogenide in platelet form has a lateral dimension in the range of 200nm to 2 μ ι η.
22. An electrode comprising a plurality of core-shell composites, wherein each composite comprises a core of non-metallic particles having a hollow interior structure, the core being encapsulated in a shell of a transition metal chalcogenide.
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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111540888A (en) * 2020-04-29 2020-08-14 齐鲁工业大学 CoSe2Hollow carbon nanosphere/S composite lithium-sulfur battery positive electrode material and preparation method thereof
CN112289988A (en) * 2020-09-30 2021-01-29 合肥国轩高科动力能源有限公司 Silver-doped silicon and tungsten ditelluride composite anode material and preparation method and application thereof
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CN114788040A (en) * 2021-07-21 2022-07-22 宁德新能源科技有限公司 Positive pole piece, electrochemical device comprising positive pole piece and electronic device
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1245540A (en) * 1996-11-29 2000-02-23 耶达研究及发展有限公司 Method for preparation of metal intercalated fullerene-like metal chalcogenides
US20130065128A1 (en) * 2011-09-12 2013-03-14 The Board Of Trustees Of The Leland Stanford Junior University Encapsulated sulfur cathodes for rechargeable lithium batteries
CN104492460A (en) * 2014-12-11 2015-04-08 浙江大学 Metallic oxide/metal sulfide hollow nanospheres as well as preparation method and application thereof
CN104934602A (en) * 2015-06-19 2015-09-23 上海交通大学 Molybdenum disulfide/carbon composite material and preparation method thereof
CN106129384A (en) * 2016-09-07 2016-11-16 中南大学 The complex of carbon/sulfur of a kind of manganese dioxide nano-plates cladding, preparation method and applications

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE69710787T2 (en) * 1996-05-22 2002-11-21 Moltech Corp COMPOSITE CATHODES, ELECTROCHEMICAL CELLS WITH COMPOSITE CATHODES AND METHOD FOR THE PRODUCTION THEREOF

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1245540A (en) * 1996-11-29 2000-02-23 耶达研究及发展有限公司 Method for preparation of metal intercalated fullerene-like metal chalcogenides
US20130065128A1 (en) * 2011-09-12 2013-03-14 The Board Of Trustees Of The Leland Stanford Junior University Encapsulated sulfur cathodes for rechargeable lithium batteries
CN104492460A (en) * 2014-12-11 2015-04-08 浙江大学 Metallic oxide/metal sulfide hollow nanospheres as well as preparation method and application thereof
CN104934602A (en) * 2015-06-19 2015-09-23 上海交通大学 Molybdenum disulfide/carbon composite material and preparation method thereof
CN106129384A (en) * 2016-09-07 2016-11-16 中南大学 The complex of carbon/sulfur of a kind of manganese dioxide nano-plates cladding, preparation method and applications

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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CN111540888B (en) * 2020-04-29 2022-11-08 齐鲁工业大学 CoSe 2 Hollow carbon nanosphere/S composite lithium-sulfur battery positive electrode material and preparation method thereof
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CN112289988B (en) * 2020-09-30 2022-05-06 合肥国轩高科动力能源有限公司 Silver-doped silicon and tungsten ditelluride composite anode material and preparation method and application thereof
CN114788040A (en) * 2021-07-21 2022-07-22 宁德新能源科技有限公司 Positive pole piece, electrochemical device comprising positive pole piece and electronic device
WO2023000211A1 (en) * 2021-07-21 2023-01-26 宁德新能源科技有限公司 Positive electrode plate, electrochemical device comprising same, and electronic device
CN113571708A (en) * 2021-07-28 2021-10-29 苏州创奇新能源科技有限公司 Heterojunction ZnSe/CoSe based on positive and negative electrode protection of lithium-sulfur full cell2Preparation method of universal carrier
CN113571708B (en) * 2021-07-28 2023-11-28 苏州创奇新能源科技有限公司 Heterojunction ZnSe/CoSe based on positive and negative electrode protection of lithium-sulfur full battery 2 Method for preparing universal carrier
WO2024074353A1 (en) * 2022-10-03 2024-04-11 Northvolt Ab A silicon-based particulate material for use in an anode active material for a lithium-ion battery cell
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