• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
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    • 专利摘要:
    PROCESS TO FORM MINERALS IN EXPANDED AND DERIVED HEXAGONAL LAYERS USING ELECTROCHEMICAL LOADING. The present invention discloses processes for forming minerals in expanded hexagonal layers (HLMs) and their derivatives using electrochemical loading. The process includes using HLM rocks (20) as electrodes (100) immersed in an electrolytic slurry (50) that includes an organic solvent, metal ions and expanded HLM (24). Electrolysis introduces organic solvent and ions from the metallic salt of the slurry into the spacing between layers that separate the intermediate layers of the HLM rock, thus forming the charged HLM of the first stage that exfoliates from the HLM rock. The process includes expanding the loaded HLM from the first stage by applying expansion force.
    公开号:BR112013028162B1
    申请号:R112013028162-6
    申请日:2012-11-22
    公开日:2020-10-27
    发明作者:Gordon Chiu；Junzhong Wang；Kian Ping Loh
    申请人:National University Of Singapore；
    IPC主号:
    专利说明:

    Priority Claim
    [0001] This application claims the priority benefit of North American Provisional Application Serial No. 61 / 570.330, filed on December 14, 2011, and whose application is incorporated by reference in this document in the jurisdictions where such incorporation is recognized. Domain
    [0002] The present disclosure relates to the processing of minerals in hexagonal layers and, particularly, relates to a process for forming expanded hexagonal layer minerals and their derivatives using electrochemical charge. Prior Art
    [0003] There is a class of minerals that are formed from sheets or layers that have a hexagonal crystal structure and that are referred to in this document as minerals in hexagonal layers. Such minerals include graphite, molybdenum disulfide, tungsten disulfide (diselenide), hexagonal boron nitride, vanadium pentoxide, vanadium X oxides (e.g., vanadium selenium oxide) and similar minerals.
    [0004] Graphite is perhaps the best known of hexagonal layered minerals because it exhibits basal cleavage, good electrical and thermal conductivity, refractoriness and resistance to acids. It is an important component in several technologies, such as cutting-edge alternative energy solutions, including batteries and hydrogen fuel cells. It is also used in the production of electrodes and brushes for electric motors. Graphite is also a key component in refractory and metallurgical materials and is used as a release agent in molds, dies and form liners when making metal and casting parts.
    [0005] Graphite is obtained by mining ore rich in graphite (ie graphite stone) and crushing it to sand consistency to allow the graphite to be removed. The ground material is then subjected to a series of flotation processes to extract the graphite.
    [0006] A variant of graphite is expanded graphite, which is graphite that has been treated so that the distance of the intermediate layer between the individual crystal planes is expanded beyond the usual van der Waals distances. Expanded graphite has a much greater energy and gas storage capacity than ordinary graphite.
    [0007] Conventionally, the graphite stone has to be ground before it can be processed as expanded graphite. To produce expanded graphite using prior art, ground graphite flakes are immersed in concentrated acids. All of these processes use a lot of energy, and the acid intercalation process creates many defects in the graphite, which negatively affect the electrical conductivity of the graphite. Acid work is also generally not preferred, as they are caustic and difficult to handle.
    [0008] Graphene is a derivative of graphite and comprises a two-dimensional sheet of atomic carbon hexagonally disposed with very attractive physical, optical and mechanical properties, including high load carrier mobility, thermal conductivity record and rigidity.
    [0009] Low-layered graphenes (FLG), which can be derived from the exfoliation of graphite or graphite oxide, have better dispersion properties and, therefore, can form more homogeneous mixtures or compounds with other materials than graphite. It is expected that the best performance can be achieved where FLG substitutes for graphite flakes are used as a major component in coatings, metallurgy or refractories.
    [0010] Efficient processes are necessary for the formation of minerals in expanded hexagonal layers and their derivatives, without the need to perform complex and potentially dangerous processing steps. summary
    [0011] The present disclosure refers to a process that can transform minerals in hexagonal layers into an expanded form with almost 90% yield in a single pass, without the need for any form of pre-treatment, such as grinding, and without the need to use acids.
    [0012] One aspect of the disclosure includes a process of forming an expanded hexagonal layered mineral (HLM). The process includes immersing at least a portion of an HLM rock in the slurry consisting of a mixture of expanded HLM rock, a metal salt and an organic solvent, in which the HLM rock has atomic intermediate layers, each with a hexagonal lattice structure with intermediate atomic layers separated by spacing between layers. The process also includes electrochemically loading the HLM rock by incorporating the HLM rock into at least one electrode and performing electrolysis through the slurry using at least one electrode, thus introducing the organic solvent and ions of the metallic salt in the slurry in the spacing between layers of the HLM rock to form the charged HLM from the first stage that exfoliates from the HLM rock. The process also includes expanding the HLM loaded from the first stage by applying an expansion force to increase the spacing between layers between the atomic layers.
    [0013] Another aspect of the disclosure is a composition of matter useful for carrying out electrochemical loading of a hexagonal layered mineral (HLM), comprising: HLM rock: from 25 to 65% by weight or from 15 to 20% by weight ; HLM flake: 0.1 to 10% by weight or 0.1 to 5% by weight; and an electrolyte of 100 to 200 g / L or 80 to 160 g / L of LiCICM (5 to 10% by weight) in propylene carbonate: 40 to 80% by weight or 70 to 80% by weight.
    [0014] Another aspect of the development is a process of forming expanded graphite from the graphite stone with atomic intermediate layers separated by spacings between layers. The process includes immersing at least a portion of the graphite stone in the slurry consisting of a mixture of expanded graphite, a metal salt and an organic solvent. The method also includes electrochemically charging the graphite stone by incorporating the graphite stone into at least one electrode and performing electrolysis through the slip using at least one electrode, thus introducing the organic solvent and ions from the metallic salt of the slip in the spacing between layers of the graphite stone to form the charged graphite from the first stage that exfoliates from the graphite stone. The method also includes expansion of the electrochemically charged graphite from the first stage by applying an increasing force to increase the spacing between layers between the atomic layers. The method optionally includes forming the slurry to have the following composition: graphite stone: 25 to 65% by weight or 15 to 20% by weight; graphite flake: from 0.1 to 10 or 0.1 to 5% by weight; and an electrolyte of 100 to 200 g / L or 80 to 160 g / L of LiCICU (5 to 10% by weight) in propylene carbonate: 40 to 80% by weight or 70 to 80% by weight.
    [0015] The general description above and the detailed description below provide modalities for the disclosure, and are intended to provide an overview or framework for understanding the nature and character of the disclosure, as claimed. Associated drawings are included to provide a greater understanding of the disclosure and are incorporated into, and form a part of this specification. The drawings illustrate various modalities of the disclosure and, together with the description, serve to explain the principles and operations of the disclosure. For example, subject to restrictions on fluid dynamics, electrical energy and container volume, the description below is scalable to any physical dimensions.
    [0016] The claims are incorporated into, and form part of this specification. Brief Description of Drawings
    [0017] Figure 1 is a schematic diagram of an electrochemical loading system configured to perform the electrochemical loading of one or more HLM stones in the formation of expanded HLM and its derivatives;
    [0018] Figure 2 is a schematic diagram illustrating an exemplary configuration of an HLM rock electrode in the form of a metal cage that defines an interior configured to contain one or more HLM rocks;
    [0019] Figure 3 is a top-down view of an exemplary electrode matrix that defines a plurality of electrodes, where the polarity of the electrode varies with a chessboard pattern;
    [0020] Figure 4 is a schematic diagram of an electrochemical loading system that is similar to that of Figure 1 and that illustrates a modality that uses a conveyor to transport the expanded HLM to a container;
    [0021] Figure 5 is a schematic diagram illustrating how expanded graphite forms FLG nanoplates; and
    [0022] Figures 6A to 6D are various graphs of experimental data, taken on samples of expanded graphite and FLG.
    [0023] The various elements represented in the drawings are merely representative and are not necessarily drawn to scale. Certain sections of them can be exaggerated, while others can be minimized. The drawings are intended to illustrate a modality exemplifying the revelation that can be properly understood and carried out by people skilled in the art. Detailed Description
    [0024] The present disclosure relates to a process for forming minerals in expanded hexagonal layers (HLMs) and their derivatives using electrochemical loading. The description below is based, in part, on graphite as an exemplary HLM, the derivatives of which include FLG and graphene flakes that have desirable physical properties for a variety of applications. The processes described below in this document generally apply to HLMs, and portions of the description based on graphite as an exemplary HLM are for illustration only, not limiting.
    [0025] The following definitions apply to the description established here.
    [0026] Hexagonal layered mineral (HLM): a mineral that has a crystal structure defined by layers ("atomic layers") or leaves that have a six-sided (hexagonal) reticular structure. Exemplary HLMs include graphite, molybdenum disulfide, tungsten disulfide (diselenide), hexagonal boron nitride, vanadium pentoxide, vanadium X oxides (for example, vanadium selenium oxide) and similar minerals.
    [0027] Rock HLM: Mineral rock in hexagonal layers.
    [0028] Graphite: an example HLM which is a crystalline form of carbon in which carbon atoms are linked in layers (atomic layers), with a six-sided (hexagonal) reticular structure.
    [0029] Graphite stone: a natural graphite mineral that is extracted directly, without any form of purification, and that is an example of an HLM rock.
    [0030] Slurry: HLM flakes, generated from crushed or crushed HLM, as well as HLM derivatives, mixed with organic solvent and salt to form a viscous liquid with good electrical conductivity.
    [0031] HLM loaded from the first stage: HLM flakes that were electrochemically loaded in the process described below, before expansion. The HLM flakes here are considered to have undergone the expansion of the first stage.
    [0032] Expanded HLM: HLM has been treated so that the spacing between the layers between the atomic layers in the crystal lattice that are loosely bonded has been expanded beyond the van der Waals distances common in the crystal.
    [0033] Graphene: A single sheet (atomic layer) of bound sp2 atomic carbon.
    [0034] Graphene with few layers (FLG): several layers of graphene stacked proportionally (according to the stacking sequence of Bernal AB) or not.
    [0035] FL-HLM: hexagonal layered mineral with few layers, of which FLG is an example.
    [0036] Electrochemical charging: a process by which a voltage is applied to a material that acts as an electrode or electrolyte, and through which the electric current passes through the material, and ionic conduction occurs in the electrolyte. In the case where the material is an HLM, such as graphite, and the electrolyte includes organic compounds, the charging process conducts ions and organic compounds originating from the electrolyte to the spacing between layers between the atomic intermediate layers of the HLM. Electrochemical charging system
    [0037] Figure 1 is a schematic diagram of an electrochemical loading system ("system") 10 configured to perform the electrochemical loading processes of one or more HLM 20 rocks, according to the disclosure. System 10 includes a container 40 containing an electrolytic HLM-based slurry (“slurry”) 50. In one example, the slurry 50 is initially contained in a reservoir 60 and is introduced into container 40 through a tube inlet 62 and removed from container 40 via an outlet tube 64 by operating a circulation pump 66. In one example, the slurry 50 removed from container 40 via outlet tube 64 is directed to a storage tank 68 with a valve 69.
    [0038] An exemplary slurry 50 contains small pieces of HLM (for example, ground HLM), derivatives of HLM, expanded HLM or their combinations, mixed with an organic solvent and a salt. For example, when HLM 20 rocks are in the form of graphite, the slurry 50 contains small pieces of graphite (ground), graphite derivatives, expanded graphite or their combinations mixed with an organic solvent and a salt. An exemplary solvent includes a combination of propylene carbonate and lithium perchlorate, ethylene carbonate, ionic liquids, and phosphonium-based perchlorate ionic salts / liquids. Salts can be based on a variety of ions, such as potassium, lithium, sodium, iron and the like. The slurry 50 is constituted as an electrolytic medium to ensure continuous charging during the electrochemical exfoliation process, by providing a low resistance path between the electrodes, thereby sustaining a high charge current during electrolysis.
    [0039] In one example, the viscosity of the slurry 50 is controlled during the electrochemical loading process by adding expanded HLM 24 to the slurry. In one example, the viscosity of the slurry 50 ranges from 0.05 Pa »S to 50 Pa» S.
    An exemplary slip 50 has the following composition: HLM rock: 25 to 65% by weight or 15 to 20% by weight; graphite flake: from 0.1 to 10 or from 0.1 to 5% by weight; and an electrolyte of 100 to 200 g / L or 80 to 160 g / L of LiCICU (5 to 10% by weight) in propylene carbonate: 40 to 80% by weight or 70 to 80% by weight.
    [0041] System 10 includes an inert gas source 70 and a tube 72, with an end that is immersed in the slurry 50. An exemplary gas for the inert gas source 70 is N2 or Ar. The inert gas source 70 it serves to form gas bubbles 74 in the slurry 50 to provide a mechanism for agitating the slurry.
    [0042] System 10 may also include a mechanical stirrer 80 which is immersed in the slurry 50 and which serves to stir (e.g., stir, mix, skim, etc.) the slurry. Other agitation mechanisms can be used to agitate the slurry 50, such as bars for acoustic magnetic stirring, etc., and the mechanical and gaseous agitation mechanisms are demonstrated by way of example.
    [0043] In one example, one or more porous dividers 98 are used to define different regions or cells in the container 40.
    [0044] System 10 also has a first outlet tube 90 that serves to remove residues 54 that accumulate at the bottom of the container 40 and a second outlet tube 94 that serves to remove graphite stone flakes from the slurry 50 , as described in more detail below.
    [0045] System 10 also includes two or more electrodes 100, one of which is shown by way of example as being placed at the bottom of container 40 and is referred to as a lower electrode 100B. At least one other electrode 100 includes HLM 20 rock and such electrodes are referred to herein as "rock electrodes". Electrodes 100 are also connected to a power supply 110 by a wire, 101. Power supply 110 provides an electrical potential between electrodes 100. In one example, power supply 110 is configured to provide an alternating electrical potential of so that electrodes 100 alternate between anodes and cathodes. Power supply 110 can also provide direct current. The rock electrodes 100 can be either anodes or cathodes, or they can alternate between being anodes and cathodes, varying the electrical potential and thus their polarity.
    [0046] Rock electrodes 100 can have a variety of different configurations, each of which includes at least one HLM 20 rock. Figure 1 shows a simple configuration, where two HLM 20 rocks are both directly electrically connected to the power supply 110 by means of wires 101 and thus directly serve as two rock electrodes 100. Figure 2 is a schematic diagram illustrating an exemplary configuration, where the rock electrode 100 comprises a metal cage 102 which defines a configured interior 108 to contain one or more HLM rocks 20. The metal cage 102 is electrically connected to the power supply 110 by means of wire 101. Figure 3 is a top-down view of an exemplary electrode matrix 106 that defines a plurality of electrodes 100 where the polarity of the electrodes varies with a chessboard pattern. Each electrode 100 in the electrode matrix 106 defines a corresponding interior matrix 108, each configured to contain one or more HLM rocks 20.
    [0047] Figure 4 is a schematic diagram of system 10 that is similar to that shown in Figure 1 and that includes a conveyor 150. The conveyor 150 is configured so that a part of it moves through the slurry 50. The conveyor 150 can be formed from a belt or chain and is configured to pick up and transport flakes of HLM 22 to a storage container 96 that have been exfoliated from the HLM 20 rock, as described below. Electrochemical loading to form first stage HLM
    [0048] A first major step in the process of forming expanded HLM includes electrochemically loading the HLM to form charged HLM from the first stage. With reference to Figure 1, an aspect of the process includes electrochemically loading the slurry 50. In one example, the slurry 50 enters container 40 through inlet tube 62 and flows out of the container through outlet tube 64 due to action of the circulation pump 66. To electrochemically charge the slurry 50, the rock electrodes 100 are inserted into the slurry, as shown in Figure 1. In one example, the electrodes 100 (including the lower electrode 100B) are both voltage positive (interspersed negative ions, for example, CIO <) and negative voltage (interspersed positive ions, for example, Li +), so that a good electric field permeates the fluid 50.
    [0049] The electrochemical charging process is described from now on using graphite as an exemplary HLM.
    [0050] To electrochemically charge the graphite stone 20, the rock electrodes 100 are used to create an electric field with the graphite stone. In one example, the charge voltage supplied by the power supply 110 to the electrodes 100 is in the range of about 10 V to 20 V DC with a current between about 0.2 A and 2 A. As discussed above, a voltage CA can also be provided. In one example, the agitation of the slurry 50, as provided by the mechanical stirrer 80 and the gaseous agitation of the gas bubbles 74 of the gas tube 72 helps to exfoliate the graphite flakes 22 during the electrochemical loading process. In one example, the charging voltage and current of the power supply 110 are monitored so that the process can be operated in galvanostatic or potentiometric mode.
    [0051] When the graphite stone 20 is electrochemically charged, it produces flakes of graphite 22 that enter and become part of the slurry 50. In one example, the expanded graphite 24 is added to the slurry 50 at appropriate times to maintain or change (e.g., improve) the viscosity and conductivity of the slurry. This also allows the charging current of the power supply 110 to be maintained or changed, so that the charging current will decrease if the resistance of the slurry 50 increases.
    [0052] The electrochemical loading process described above causes the slurry 50 to contain graphite flakes loaded from the first stage 22. A portion of the slurry 50 is removed from container 40 by tube 94 to storage container 96 or transported to it by conveyor 150. Referring to Figure 4, this process is carried out by conveyor 150. The slurry 50 supplied to the storage container 96 is decanted to recover graphite flakes loaded from the first stage 22, as well as a certain amount of material that does not reacted (for example, unloaded graphite, expanded graphite, etc.). Thermal expansion of the HLM loaded from the first stage
    [0053] A second main step in the process includes thermal expansion of the HLM loaded from the first stage to form expanded HLM 24 by applying an expansion force. The expansion force can include at least one of heating, ultrasound and pressure.
    [0054] This second step includes removing the solvent from the decanted slurry 50 to substantially remove the solvent. A solvent removal process includes directing jets of inert gas, such as nitrogen, into the decanted 50 slurry. The resulting material is washed in a container with deionized water (eg 3 times) to remove any remaining solvent while allowing , that the solids decant at the bottom of the container, leaving the HLM loaded from the first stage.
    [0055] Then, the water is removed (for example, by suction or gravity drying), and the container that holds the HLM loaded from the first stage is subjected to the aforementioned expansion force. In one example, the expansion force is heating, in which the loaded HLM from the first stage is heat treated, for example, on a heating plate heated to a temperature in the range of about 200 ° C to 300 ° C, open air. This causes the charged HLM of the first stage to expand (that is, the atomic intermediate layers begin to separate) to form expanded HLM 24. This expansion process usually takes less than 5 minutes.
    [0056] Then, water is added to the expanded HLM 24 to allow hydraulic classification, in which the expanded HLM floats to the top surface of the water and is removed, for example, by skimming through a paddle or scraping process. The impurities sink and are separated.
    [0057] The electrochemical loading step and the expansion step can be repeated several times in the processed material to improve the exfoliation yield, dispersion and porosity of the expanded HLM 24. As mentioned above, a single pass through the process can provide a 90% yield. Repeating the process on the processed material can improve this low-layer graphene yield by up to more than 90%. Formation of low-layer graphene nanoplates (FLG)
    [0058] A third main step in the process includes processing the expanded HLM 24 to form HLM nanoplates or flakes 22, as schematically illustrated in Figure 5. The expanded graphite is subjected to ultrasound and / or ground in a liquid medium to obtain FLG 22 dispersible. The liquid medium can be a hydrophobic or hydrophilic solvent, or a mixture of both with a surfactant, such as N, N-dimethylformamide, propylene carbonate, N-methyl-2-pyrrolidone (NMP), dimethyl sulfoxide (DMSO), dimethylformamide ( DMF) and the like. Water or water with sodium dodecyl sulfate (SDS) can also be used as the liquid medium. Ultrasound can be applied using energy ultrasound, bath ultrasound or fluidized ultrasound. The planetary ball mill with colloidal grinding can be applied to obtain the dispersible FLG. In one example, the grinding process is applied first, followed by ultrasound. Experimental measurements
    [0059] An important verification of the quality of exfoliated graphene is the comparison of its lithium capacity in the lithium-ion battery with that of commercial expanded graphite. Figure 6A shows the voltage graph (y-axis) versus the reversible lithium capacity (x-axis) where the exfoliated graphene is used as the anode. The anode was manufactured with exfoliated graphene and binder (Kynar 2801) in a weight ratio of 80:20 using N-methylpyrrolidone (NMP) as the solvent for the binder. Etched copper foil (15 pm thick, from China) was used as the current collector. A solution of LiPFθ 1M in ethylene carbonate (EC) + dimethyl carbonate (DMC) (1: 1 v / v) (Merck) was used as the electrolyte, with a Watman paper membrane serving as a separator. The lithium foil (Kyokuto metal Co., Japan) was used as the reference electrode and counter. CR2016 size coin-shaped batteries (20 mm in diameter and 1.6 mm thick) were manufactured in a glove box filled with Ar gas. Cyclic voltammetry and charge-discharge cycles were performed at room temperature (RT = 24 ° C) using a Bitrode multiple battery tester (SCN model, Bitrode, USA) and a Mac-pile II system (Bio-logic, France), respectively. To ensure the electrolyte percolated, the cells were aged for 12 hours before being measured.
    [0060] The results show that the exfoliated graphene produced from the process described here (Figure 6A shows a much greater reversible capacity of 340 mAh / g than the commercial expanded graphite sample shown in the similar graph in Figure 6B, which has a reversible capacity of only 120 mAh / g). The different curves are for different cycle numbers (1-12 in Figure 6A and 1,2, 5, 10, 20 and 30 in Figure 6B).
    [0061] Figure 6C and Figure 6D show the graphs of capacity versus number of cycles for it, comparing the capacity of the exfoliated graphene produced as revealed in this document (Figure 6C) with that of commercial expanded graphite (prior art) (Figure 6D). The results show that the exfoliated graphene formed using the processes disclosed in this document has a very stable cyclic behavior and has a greater capacity than commercial samples of the prior art.
    [0062] It will be evident to those skilled in the art that various modifications and variations can be made to the present revelation without departing from the spirit and scope of the revelation. Therefore, it is intended that the present disclosure encompasses the modifications and variations of this disclosure provided, provided that they are within the scope of the appended claims and their equivalents. For example, the processes described in this document can be performed over a wide range of scales, subject only to reasonable physical limitations based on the limits of fluid dynamics, electrical energy and container volume.
    权利要求:
    Claims (13)
    [0001]
    1. Process of formation of an expanded hexagonal layered mineral (HLM), characterized by the fact that it comprises: immersion of at least a portion of an HLM rock in a slurry consisting of a mixture of expanded HLM rock, a metallic salt and a organic solvent, in which the HLM rock has atomic intermediate layers, each with a hexagonal reticular structure, with the atomic intermediate layers separated by spacings between layers; electrochemical loading of the HLM rock, incorporating the HLM rock in at least one electrode and performing electrolysis by the slip using at least one electrode, thus introducing the organic solvent and ions of the metallic salt of the slip into the spacings between layers of the HLM rock to form the loaded HLM from the first stage that exfoliates from the HLM rock; and expanding the HLM loaded from the first stage by applying an expansion force to increase the spacing between layers between the atomic layers; wherein the slurry has the following composition: - HLM rock: 15 to 20% by weight; - HLM flake: 0.1 to 5% by weight; and - an electrolyte of 80 to 160 g / L of LiCICU (5 to 10% by weight) in propylene carbonate: 70 to 80% by weight.
    [0002]
    2. Process according to claim 1, characterized by the fact that HLM is selected from the group of HLMs comprising: graphite, molybdenum disulfide, tungsten disulfide (diselenide), hexagonal boron nitride, vanadium pentoxide and vanadium X oxides.
    [0003]
    3. Process according to claim 1, characterized by the fact that the expansion force includes at least one among heating, ultrasound and pressure.
    [0004]
    4. Process according to claim 3, characterized by the fact that the slurry has a viscosity in the range of 0.05 Pa «S to 50 Pa-S.
    [0005]
    5. Process, according to claim 4, characterized by the fact that it also comprises the conservation of viscosity in the interval during the electrochemical loading step by the addition of expanded HLM to the slurry.
    [0006]
    6. Process according to claim 1, characterized by the fact that it also comprises the formation of at least one electrode from a metal cage configured to contain the HLM rock.
    [0007]
    7. Process according to claim 1, characterized by the fact that it also comprises the use of several multiple electrodes, each including at least one HLM rock.
    [0008]
    8. Process according to claim 1, characterized by the fact that it also comprises the transport of the HLM loaded from the first stage of the slurry to a storage container.
    [0009]
    9. Process according to claim 1, characterized by the fact that it also comprises the agitation of the slurry during the electrochemical loading step.
    [0010]
    10. Process according to claim 1, characterized by the fact that the metal ions include lithium ions, and in which the organic solvent comprises propylene carbonate.
    [0011]
    11. Composition of useful material to perform the electrochemical loading of a hexagonal layered mineral (HLM), characterized by the fact that it comprises: - HLM rock: 15 to 20% by weight; - HLM flake: 0.1 to 5% by weight; and - an electrolyte of 80 to 160 g / L of LiCICU (5 to 10% by weight) in propylene carbonate: 70 to 80% by weight.
    [0012]
    12. Composition of matter according to claim 11, characterized by the fact that the composition is in the form of a slurry with a viscosity in the range of 0.05 Pa * S to 50 Pa * S.
    [0013]
    13. Material composition according to claim 11, characterized by the fact that the HLM is selected from the group of HLMs comprising: graphite, molybdenum disulfide, tungsten disulfide (diselenide), hexagonal boron nitride, pentoxide vanadium and vanadium X oxides.
    类似技术:
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    同族专利:
    公开号 | 公开日
    CA2832682C|2018-06-12|
    JP6030148B2|2016-11-24|
    BR112013028162A2|2017-01-10|
    ES2655830T3|2018-02-21|
    IL228779A|2017-11-30|
    AU2012353015B2|2016-08-11|
    IL228779D0|2013-12-31|
    SG194136A1|2013-11-29|
    WO2013089642A1|2013-06-20|
    KR20140103032A|2014-08-25|
    EP2791057A4|2015-08-26|
    CA2832682A1|2013-06-20|
    PL2791057T3|2018-03-30|
    US20140027299A1|2014-01-30|
    KR102090341B1|2020-03-18|
    US9221687B2|2015-12-29|
    JP2015507320A|2015-03-05|
    EP2791057A1|2014-10-22|
    EP2791057B1|2017-11-01|
    AU2012353015A1|2013-10-31|
    WO2013089642A8|2013-09-19|
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    法律状态:
    2018-03-27| B15K| Others concerning applications: alteration of classification|Ipc: B82Y 40/00 (2011.01) |
    2018-04-03| B06F| Objections, documents and/or translations needed after an examination request according art. 34 industrial property law|
    2019-07-23| B06U| Preliminary requirement: requests with searches performed by other patent offices: suspension of the patent application procedure|
    2020-06-30| B09A| Decision: intention to grant|
    2020-10-27| B16A| Patent or certificate of addition of invention granted|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 22/11/2012, OBSERVADAS AS CONDICOES LEGAIS. |
    优先权:
    申请号 | 申请日 | 专利标题
    US201161570330P| true| 2011-12-14|2011-12-14|
    US61/570,330|2011-12-14|
    PCT/SG2012/000440|WO2013089642A1|2011-12-14|2012-11-22|Process for forming expanded hexagonal layered minerals and derivatives using electrochemical charging|
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