CN107665990B - Chloride battery positive plate and preparation method thereof - Google Patents

Chloride battery positive plate and preparation method thereof Download PDF

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CN107665990B
CN107665990B CN201610611499.9A CN201610611499A CN107665990B CN 107665990 B CN107665990 B CN 107665990B CN 201610611499 A CN201610611499 A CN 201610611499A CN 107665990 B CN107665990 B CN 107665990B
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chloride
carbon
chlorine
binder
controlling
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CN107665990A (en
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唐怀远
王媛珍
王康彦
金源
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Hengdian Group DMEGC Magnetics Co Ltd
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Hengdian Group DMEGC Magnetics Co Ltd
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    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/58—Selection 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
    • H01M4/582—Halogenides
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/04—Processes of manufacture in general
    • H01M4/043—Processes of manufacture in general involving compressing or compaction
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/58—Selection 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
    • H01M4/583—Carbonaceous material, e.g. graphite-intercalation compounds or CFx
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/621—Binders
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624—Electric conductive fillers
    • H01M4/625—Carbon or graphite
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10—Energy storage using batteries

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

The invention relates to a chloride battery positive plate and a preparation method thereof, wherein the battery positive plate comprises a chloride, a carbon material, a binder and a current collector; the mass ratio of the chloride to the carbon material to the binder is (40-98): (1-40): 1-20), wherein the chloride is obtained by reacting chlorine with organic salt. In the battery positive plate, the chloride generated by the reaction of chlorine and organic salt is used as the positive active substance, so that the prepared secondary battery has higher specific energy, can realize quick charge and discharge, has long cycle life and low raw material cost.

Description

Chloride battery positive plate and preparation method thereof
Technical Field
The invention relates to the field of secondary batteries, in particular to a battery positive plate and a preparation method thereof, and particularly relates to a chloride battery positive plate and a preparation method thereof.
Background
With the rapid development of society, environmental pollution and the shortage of traditional energy sources, people need more efficient and more environment-friendly energy sources to replace or supplement the traditional energy sources, which leads to more and more demands on hybrid electric vehicles and pure electric vehicles. The battery is the heart of the electric vehicle and is the hot spot of the current investment, and the lithium ion power battery is considered as the power battery with the most development potential for the electric vehicle; however, with the development of noble metals such as nickel, cobalt, lithium and the like, the raw materials of the lithium ion power battery greatly increase, and the popularization and the application of new energy vehicles are restricted; the poor safety and the poor recovery economic benefit of the lithium ion power battery are also important factors restricting the development of the lithium ion power battery.
Therefore, the solution of seeking a power battery with low cost, environmental protection and safe use is still the first problem to be solved by new energy automobiles.
Halogen is an element which is stored in the earth crust abundantly, and has the advantages of large storage capacity, mature extraction process, environmental protection in production, no pollution in recovery and low price, and the halogen is taken as the anode material and is an ideal electrode material. Chlorine is a covalent compound formed by sharing electron pairs among different halogen atoms, and the chlorine has active chemical properties, and if the chlorine can be used in the field of batteries, a new idea is provided for realizing a power battery with low cost, environmental protection and safe use.
Disclosure of Invention
In order to solve the above technical problems, the present inventors have found through research that a power battery having low cost, environmental protection, safe use and high specific energy can be obtained when a chloride generated by reacting chlorine gas with an organic salt is used as a positive electrode active material in a positive electrode sheet of the battery, thereby achieving the present invention.
In a first aspect, the present invention provides a battery positive electrode sheet comprising a chloride, a carbon material, a binder, and a current collector; the mass ratio of the chloride to the carbon material to the binder is (40-98): (1-40): 1-20).
The term "comprising" as used herein means that it may include, in addition to the components, other components which impart different characteristics to the positive electrode sheet of the battery. In addition, the term "comprising" as used herein may be replaced by "being" or "consisting of … …" as closed.
In the invention, the mass ratio of the chloride to the carbon material to the binder is (40-98): (1-40): 1-20). The applicant states that the mass ratio ranges of the components cover the specific points of the ranges, for example, the mass ratio of the chloride, the carbon material and the binder can be: 40:1:1, 40:4:1, 40:10:1, 40:20:1, 40:30:1, 40:40:1, 40:1:5, 40:1:10, 40:1:20, 50:1:1, 50:4:7, 50:15:18, 60:5:1, 60:7:7, 65:10:6, 70:1:5, 80:6:13, 85:4:12, 90:40:1, 92:12:5, or 98:40:17, and specific point values therebetween, are limited in space and for brevity, the invention is not exhaustive of the specific point values included in the ranges.
According to the invention, the chloride is obtained by reacting chlorine (chlorine gas) with an organic salt.
The chloride provided by the invention is used as a novel chemical system, and is added into the positive active material, so that the prepared secondary battery has higher specific energy, rapid charge and discharge are realized, the cycle life is prolonged, and the raw material cost is low.
According to the invention, the organic salt has the general formula [ X ]]+Z-(ii) a Wherein, [ X ]]+Represents an organic cation, Z-Represents an anion.
The organic salt is composed of organic cations with larger volume and anions with smaller volume, and the substance has a plurality of unique properties, such as stable physicochemical properties, extremely low vapor pressure and difficult volatilization, good solubility to both organic and inorganic substances, controllable polarity and the like.
In the present invention, the organic cation may be any one of imidazolium ion, pyridinium ion, pyrrolium ion, piperidinium ion, morpholinium ion, quaternary ammonium ion or quaternary phosphonium ion or a combination of at least two thereof, for example, may be any one of imidazolium ion, pyridinium ion, pyrrolium ion, piperidinium ion, morpholinium ion, quaternary ammonium ion or quaternary phosphonium ion, and a typical but non-limiting combination is: imidazolium ions and pyridinium ions; pyridinium ions and pyrrolium ions; morpholinium ions, quaternary ammonium ions, quaternary phosphonium ions and the like.
According to the invention, the organic cation is preferably a quaternary ammonium ion, which has the following advantages over other organic cations: the quaternary ammonium salt (organic salt containing quaternary ammonium salt ions) is a common chemical, and the production process is mature, the price is low, and the quaternary ammonium salt can be purchased and used in a large scale.
In the present invention, the anion may adopt F-、Cl-、Br-、I-、PF6 -、PB4 -、CN-、SCN-、CF3SO3 -、CF3COO-、SbF6 -、N(CF3SO2)2 -、N(CN)2 -、ClO4 -、HSO4 -、HCO3 -、OH-Or NO3 -Any one or a combination of at least two of them, for example, may be F-、Cl-、Br-、I-、PF6 -、PB4 -、CN-、SCN-、CF3SO3 -、CF3COO-、SbF6 -、N(CF3S02)2 -、N(CN)2 -、ClO4 -、HSO4 -、HCO3 -、OH-Or NO3 -A typical but non-limiting combination of any of: f-And Cl-；Br-And I-；I-And PF6 -；Cl-、Br-And SCN-And the like.
Illustratively, the organic salt in the present invention may be: 1-butyl-3-methylimidazolium hexafluorophosphate ([ C)4-min]PF4) 1, 3-bis (2, 6-diisopropylphenyl) imidazolium chloride, 2-chloro-1, 3-dimethylimidazolium hexafluorophosphate, 1-N-butyl-3-methylimidazolium hexafluorophosphate, 1-methyl-3-propylimidazolium iodide, cetylpyridinium chloride, pyridinium trichloride, N-allyl-2-alkylpyridinium chloride, 1-butyl-1-methylpiperidinium chloride, chlorodipiperidinium hexafluorophosphate, cetyltrimethylammonium chloride, tetramethylammonium chloride, ethyltriphenylphosphine chloride or hexadecyltributylphosphine chloride.
The chloride in the invention is obtained by reacting chlorine gas with organic salt. The chloride is added into the positive active material, so that the prepared secondary battery has higher specific energy, and the high performance, low cost, environmental protection and safe use of the power battery are realized.
According to the invention, the chloride is formed by reacting chlorine with the above-mentioned organic salt [ X ]]+Z-The chemical reaction of the compound prepared by the reaction of mixing can be expressed by the following equation:
4Cl2+[X]+Z-→[X]+[Cl8Z]-or Cl2+[X]+Z-→[X]+[CL2Z]-
In this chemical reaction, 1 [ X ]]+Z-Molecule, up to 4 Cl can be complexed2The molecular, and therefore, molar ratio of chlorine to organic salt can be set in the range of (1-4): 1.
In the invention, the chloride is added into the positive active material, so that the secondary aluminum battery can have higher specific energy, and the theoretical specific energy of the chloride is as high as 755 mAh/g; the American Stanford university published An ultra fast rechargeable aluminum-ion battery in the journal Nature 2015, 4 months, and the specific capacity of the battery anode material is lower and is only 60-70 mAh/g; by WS2、MoS2Although the specific capacity of the aluminum battery serving as the anode is higher, the aluminum battery is expensive and is not suitable for large-scale application; VO (vacuum vapor volume)2、TiO2、Cr2O3、MnO2、FeOx、MoO2The aluminum battery with the layered metal oxide as the anode has working voltage less than 1.5V and specific capacity less than 180 mAh/g.
Illustratively, in the present invention the chloride may be: tetraethylammonium trichloride, tetrabutylammonium trichloride, 1-ethyl-3-methyl-trichloroimidazole, phenyltrimethylammonium trichloride, benzyltriethylammonium trichloride, benzyltrimethylammonium trichloride, dodecyltrimethylammonium trichloride.
The chloride in the present invention can be prepared by the following method, but is not limited thereto:
(a) respectively taking chlorine and organic salt, controlling the mol ratio of the chlorine to the organic salt to be (1-4):1, firstly putting the organic salt into a closed container, and introducing inert gas into the closed container, wherein the inert gas is preferably nitrogen and/or argon;
(b) adding chlorine gas into the closed container, controlling the whole process to be 1-60min, stirring and cooling in the adding process, and controlling the temperature to be within 50 ℃;
(c) and cooling to room temperature after the chlorine is added to obtain the chloride.
According to the invention, the chloride is preferably prepared by the above method, which has the advantages that: the method can be completed in a closed reaction container at one time by one-time feeding without processes of purification, evaporation, filtration and the like, and the production period can be shortened to within 1 hour.
In the process for the preparation of chlorides according to the invention, the molar ratio of chlorine to organic salt in step (a) is (1-4):1, and may be, for example, 1:1, 2:1, 3:1 or 4:1, and the specific values between the above values, which are limited by space and for the sake of brevity, are not exhaustive, and the invention is not intended to include the specific values in the ranges specified.
In the preparation process of the chloride in the present invention, the closed container in step (a) may be a closed container known in the art, for example, a high pressure reactor, and is not particularly limited herein. In the closed container, an inert gas must be introduced, and the inert gas can be an inert gas commonly used in the art, such as nitrogen, argon, helium, etc., preferably nitrogen, argon or a mixture thereof.
In the preparation process of the chloride in the invention, the time for controlling the whole reaction process in the step (b) is 1-60min, for example, 1min, 5min, 10min, 12min, 15min, 20min, 25min, 30min, 35min, 40min, 45min, 50min, 55min or 60min, and the specific values between the above values are limited by space and for the sake of brevity, the invention is not exhaustive to the specific values included in the range; the reaction temperature is controlled within 50 ℃ in order to prevent the volatilization of chlorine and ensure the full reaction of chlorine and organic salt.
The carbon material in the present invention functions as a conductive agent. As the conductive agent, any electron conductive material can be used as long as it does not adversely affect the battery performance. For example, carbon black such as acetylene black or ketjen black may be used, and conductive materials such as natural graphite (scale graphite, flake graphite, and earthy graphite), artificial graphite, carbon whiskers, carbon fibers, metal (copper, nickel, aluminum, silver, and gold) powders, metal fibers, and conductive ceramic materials may be used. In particular, any one of them may be used, or two or more of them may be contained as a mixture. The amount of the additive is usually 1 to 30% by mass of the active material.
According to the present invention, the conductive agent is preferably a carbon material, which is commercially available, and the source of the conductive agent is not particularly limited.
The invention adopts cheap and easily available carbon material as conductive material, compared with conductive material such as three-dimensional graphite, the carbon material can greatly reduce the cost of the battery, and can be widely applied to industrial production.
According to the present invention, the carbon material may be selected from any one or a combination of at least two of graphite, carbon quantum dots, activated carbon, carbon fibers, carbon nanotubes, carbon aerogel, mesoporous carbon, graphene, carbon black, nanocarbon powder, mesocarbon microbeads or hard carbon, for example, any one of graphite, carbon quantum dots, activated carbon, carbon fibers, carbon nanotubes, carbon aerogel, mesoporous carbon, graphene, carbon black, nanocarbon powder, mesocarbon microbeads or hard carbon, typically but not limited to a combination of: graphite and carbon quantum dots; activated carbon and carbon fibers; carbon aerogels and mesoporous carbon; graphene, carbon black and nano carbon powder; mesocarbon microbeads and hard carbon; graphene, carbon black, nano carbon powder, mesocarbon microbeads and the like.
The carbon material in the present invention is preferably any one or a combination of at least two of carbon nanotube, carbon quantum dot, graphite, carbon black or nano carbon powder, such as any one of carbon nanotube, carbon quantum dot, graphite, carbon black or nano carbon powder, and typical but not limiting combinations are: carbon nanotubes and carbon quantum dots; carbon quantum dots and graphite; graphite and carbon black; carbon quantum dots, graphite, and carbon black; graphite, carbon black, nano carbon powder and the like.
According to the invention, the binder may be selected from carboxymethylcellulose (CMC) and styrene-butadiene rubber (SBR) in which the ratio of CMC to SBR is (0.5-5):1, for example 0.5:1, 1:1, 1.5:1, 2:1, 2.5:1, 3:1, 3.5:1, 4:1, 4.5:1 or 5:1, and may be any one of polyvinylidene fluoride (PVDF), LA133 and LA 132.
LA132 and LA133 are both a battery binder produced by fontindol and are an aqueous dispersion of an acrylonitrile multipolymer.
The binder of the present invention is preferably polyvinylidene fluoride (PVDF) because of its good stability and corrosion resistance. The amount of the positive electrode active material added is usually 1 to 30% by mass based on the mass of the positive electrode active material.
According to the invention, the current collector can adopt any one of aluminum foil, carbon-coated aluminum foil, foamed aluminum, carbon paper, carbon-plastic composite film or carbon fiber felt.
In a second aspect, the invention also provides a preparation method of the battery positive plate, which comprises the following steps:
(1) putting chloride, a carbon material and a binder into a ball mill, wherein the mass ratio of the chloride to the carbon material to the binder is (40-98) to (1-40) to (1-20), and carrying out ball milling for 5-120 min;
(2) adding a solvent into a ball milling tank, enabling the mass ratio of the total mass of the chloride, the carbon material and the binder to the solvent to be (40-60) to (60-40), and carrying out ball milling for 60-120min to obtain anode slurry;
(3) coating the positive electrode slurry on a current collector, and controlling the coating thickness of one side to be 100-300 mu m;
(4) drying the coated pole piece;
(5) and extruding the dried pole piece to obtain the battery positive pole piece.
According to the preparation method of the battery positive plate, the concrete selection and the mass ratio of the chloride, the carbon material and the binder in the step (1) are the same as the limitations of the chloride, the carbon material and the binder in the first aspect of the invention, and the details are not repeated herein.
The preparation method of the chloride in the step (1) is the same as the preparation method of the chloride in the first aspect of the invention, and is not described herein again.
In the method for preparing the positive electrode sheet for a battery according to the present invention, the mixing container for the chloride, the carbon material and the binder may be selected from apparatuses known in the art, for example, a planetary mixer, or a ball mill, for example, a ball mill pot. When a ball milling pot device is used, the sufficient mixing of the chloride, the carbon material and the binder can be completed, the ball milling time can be controlled to be 5-120min, for example, 5min, 10min, 20min, 30min, 45min, 50min, 62min, 70min, 85min, 90min, 102min, 110min or 120min, and the specific values between the above values are limited by space and for the sake of brevity, the invention is not exhaustive of the specific values included in the ranges.
According to the invention, in the preparation method of the battery positive plate, the mass ratio of the total mass of the chloride, the carbon material and the binder to the solvent in the step (2) is (40-60): (60-40), for example, 40:60, 42:60, 45:60, 48:60, 50:60, 55:60, 60:40, 60:42, 60:45, 60:50 or 60:58, and the specific values between the above values are limited by space and for the sake of brevity, and the invention is not exhaustive.
The solvent used in the present invention is used as a dispersant for preparing a solid component. The solvent may be any one of water, N-methylpyrrolidone (NMP), dimethylformamide, dimethylacetamide, or dimethylsulfoxide, or a combination of at least two thereof.
The solvent used in the present invention depends on the type of binder, and when PVDF is used, the solvent is NMP; when SBR, LA133 or L132 is used, the solvent is water. Usually, when SBR is used as the binder, CMC is used in combination.
The time for solvent dispersion of the chloride, the carbon material and the binder is generally controlled to be 60-120min, for example, 60min, 70min, 80min, 90min, 100min, 105min, 110min, 112min, 115min or 120min, and specific values between the above values are limited by space and for the sake of brevity, and the invention is not exhaustive.
According to the invention, the positive electrode slurry obtained in the step (2) is coated on the current collector by adopting a coating machine, and the single-side coating thickness is controlled to be 100-300 μm, such as 100 μm, 120 μm, 150 μm, 200 μm, 250 μm or 300 μm; and then drying the coated pole piece, and extruding the dried pole piece to obtain the battery positive plate.
According to the invention, in the preparation method of the battery positive plate, the drying in the step (4) adopts vacuum baking, the vacuum degree adopted by the vacuum baking is-0.08 to-0.10 MPa, for example, -0.08MPa, -0.085MPa, -0.09MPa, -0.095MPa or-0.10 MPa, the temperature is controlled at 100-125 ℃, for example, 100 ℃, 102 ℃, 105 ℃, 108 ℃, 110 ℃, 115 ℃, 120 ℃ or 125 ℃, the time is controlled at 180-360min, for example, 180min, 200min, 210min, 220min, 250min, 300min or 360min, and the like.
According to the preparation method of the battery positive plate, the extrusion in the step (5) is carried out by adopting a double-roller machine, and the pressure of the double rollers is controlled to be 50-300 tons during the extrusion.
According to the invention, the preparation method of the battery positive plate can be specifically carried out by adopting the following steps:
(1) putting chloride, a carbon material and a binder into a ball mill, wherein the mass ratio of the chloride to the carbon material to the binder is (40-98): 1-40): 1-20, and carrying out ball milling for 5-120 min;
the preparation method of the chloride in the step (1) comprises the following steps:
(a) respectively taking chlorine and organic salt, controlling the mol ratio of the chlorine to the organic salt to be (1-4):1, firstly putting the organic salt into a closed container, and introducing inert gas into the closed container, wherein the inert gas is preferably nitrogen and/or argon;
(b) adding chlorine gas into the closed container, controlling the whole process to be 1-60min, stirring and cooling in the adding process, and controlling the temperature to be within 50 ℃;
(c) after the chlorine is added, cooling to room temperature to obtain the chloride;
(2) adding a solvent into a ball mill, enabling the mass ratio of the total mass of the chloride, the carbon material and the binder to the solvent to be (40-60) to (60-40), and carrying out ball milling for 60-120min to obtain anode slurry;
(3) coating the positive electrode slurry on a current collector, and controlling the coating thickness of one side to be 100-300 mu m;
(4) putting the coated pole piece into a vacuum drying oven, and performing vacuum baking, wherein the vacuum degree is controlled to be-0.08 to-0.10 MPa, the temperature is controlled to be 100-;
(5) and extruding the dried pole piece by using a double-roller machine, and controlling the pressure of the double rollers to be 50-300 tons to obtain the battery positive pole piece.
Illustratively, the preparation method of the battery positive plate provided by the invention is carried out by adopting the following steps:
(1) putting chloride, a carbon material and a binder into a ball milling tank, wherein the mass ratio of the chloride to the carbon material to the binder is 70:20:10, and carrying out ball milling for 5 min;
the preparation method of the chloride in the step (1) comprises the following steps:
(a) respectively taking chlorine and organic salt, controlling the mol ratio of the chlorine to the organic salt to be 4:1, firstly putting the organic salt into a closed container, and introducing nitrogen into the closed container;
(b) adding chlorine into the closed container, controlling the whole process to be 2min, and cooling while stirring in the adding process, wherein the temperature is controlled to be within 50 ℃;
(c) after the chlorine is added, cooling to room temperature to obtain the chloride;
(2) adding a solvent into a ball milling tank, enabling the mass ratio of the total mass of the chloride, the carbon material and the binder to the solvent to be 60:40, and carrying out ball milling for 120min to obtain anode slurry;
(3) coating the positive electrode slurry on a current collector, and controlling the coating thickness of a single surface to be 100 mu m;
(4) putting the coated pole piece into a vacuum drying oven, and baking in vacuum at a vacuum degree of-0.08 MPa, a temperature of 105 ℃ and a time of 210 min;
(5) and extruding the dried pole piece by using a double-roll machine, and controlling the pressure of the double rolls to be 100 tons to obtain the battery positive pole piece.
Or, the preparation method of the battery positive plate of the invention adopts the following steps:
(1) putting chloride, a carbon material and a binder into a ball milling tank, wherein the mass ratio of the chloride to the carbon material to the binder is 80:10:10, and carrying out ball milling for 60 min;
the preparation method of the chloride in the step (1) comprises the following steps:
(a) respectively taking chlorine and organic salt, controlling the mol ratio of the chlorine to the organic salt to be 1:1, firstly putting the organic salt into a closed container, and introducing nitrogen and argon into the closed container;
(b) adding chlorine into the closed container, controlling the whole process to be 60min, and cooling while stirring in the adding process, wherein the temperature is controlled to be within 50 ℃;
(c) after the chlorine is added, cooling to room temperature to obtain the chloride;
(2) adding a solvent into a ball milling tank to ensure that the mass ratio of the total mass of the chloride, the carbon material and the binder to the solvent is 40:60, and carrying out ball milling for 60min to obtain anode slurry;
(3) coating the positive electrode slurry on a current collector, and controlling the coating thickness of one side to be 300 mu m;
(4) putting the coated pole piece into a vacuum drying oven, and baking in vacuum, wherein the vacuum degree is controlled at-0.10 MPa, the temperature is controlled at 125 ℃, and the time is controlled for 360 min;
(5) and extruding the dried pole piece by using a double-roller machine, and controlling the pressure of the double rollers to be 300 tons to obtain the battery positive pole piece.
In the present invention, the battery positive electrode sheet obtained as described above can be used in a secondary battery, and the secondary battery can be produced by a technique known in the art, for example, by the following method:
and assembling the positive plate, the negative plate and the partition plate of the battery, injecting ionic liquid serving as electrolyte, sealing, cleaning and forming to obtain a battery product.
For the negative electrode and the separator in the battery product, materials known in the art are used, and are not particularly limited.
The chloride battery positive plate can be widely applied to aluminum secondary batteries, magnesium secondary batteries and the like, can improve the specific energy of the secondary batteries, and can obtain the power batteries with low cost, environmental protection and safe use.
Compared with the prior art, the invention has at least the following beneficial effects:
(1) the chloride provided by the invention is used as a novel chemical system and exists in the positive active material of the battery in a liquid form. By adding the chloride into the positive active material, the theoretical specific energy of the positive active material can be as high as 755mAh/g, so that the prepared secondary battery has higher specific energy, quick charge and discharge are realized, the cycle life is long, and the cost of raw materials is low;
(2) the preparation method of the chloride provided by the invention can be completed in a closed container at one time by one-time feeding without processes of purification, evaporation, filtration and the like, and has the advantages of high production efficiency, high yield, short production period and small investment;
(3) the invention adopts cheap and easily available carbon material as conductive material, compared with conductive material such as three-dimensional graphite, the carbon material can greatly reduce the cost of the battery, and can be widely applied to industrial production.
Drawings
FIG. 1 is a graph comparing the discharge curves of example 4 and comparative example 3.
The present invention is described in further detail below. The following examples are merely illustrative of the present invention and do not represent or limit the scope of the claims, which are defined by the claims.
Detailed Description
The positive electrode active material and the positive electrode sheet for a battery used in the present invention were prepared on a laboratory scale by the following general methods:
general preparation method of chloride:
(a) respectively taking chlorine and organic salt, controlling the mol ratio of the chlorine to the organic salt to be (1-4):1, firstly putting the organic salt into a closed container, and introducing inert gas into the closed container, wherein the inert gas is preferably nitrogen and/or argon;
(b) adding chlorine gas into the closed container, controlling the whole process to be 1-60min, stirring and cooling in the adding process, and controlling the temperature to be within 50 ℃;
(c) and cooling to room temperature after the chlorine is added to obtain the chloride.
The battery positive plate comprises the following components:
a battery positive electrode sheet comprising a chloride, a carbon material, a binder, and a current collector; the mass ratio of the chloride to the carbon material to the binder is (40-98): (1-40): 1-20).
Electrochemical results are as follows:
the target material was tested in a metal anode test electrochemical cell to determine the specific capacity of the positive active material and to confirm whether it has the ability to undergo charge and discharge cycling. The metal anode test electrochemical cell containing the positive active material was constructed as follows:
general procedure for making metal test electrochemical cells:
(1) putting chloride, a carbon material and a binder into a ball mill, wherein the mass ratio of the chloride to the carbon material to the binder is (40-98): 1-40): 1-20, and carrying out ball milling for 5-120 min;
(2) adding a solvent into a ball mill, enabling the mass ratio of the total mass of the chloride, the carbon material and the binder to the solvent to be (40-60) to (60-40), and carrying out ball milling for 60-120min to obtain anode slurry;
(3) coating the positive electrode slurry on a current collector, and controlling the coating thickness of one side to be 100-300 mu m;
(4) putting the coated pole piece into a vacuum drying oven, and performing vacuum baking, wherein the vacuum degree is controlled to be-0.08 to-0.10 MPa, the temperature is controlled to be 100-;
(5) extruding the dried pole piece to obtain the battery positive pole piece;
(6) and assembling the positive plate, the negative plate and the partition plate of the battery, injecting ionic liquid serving as electrolyte, sealing, cleaning and forming to obtain a battery product.
For the purpose of facilitating an understanding of the present invention, the present invention will now be described by way of examples. It should be understood by those skilled in the art that the examples are only for the understanding of the present invention and should not be construed as the specific limitations of the present invention.
Example 1
And (3) manufacturing a positive electrode:
(1) placing tetraethyl ammonium trichloride, carbon nanotubes and polyvinylidene fluoride (PVDF) into a ball milling tank, wherein the mass ratio of the tetraethyl ammonium trichloride to the carbon nanotubes to the PVDF is 85:10:5, and carrying out ball milling for 15 min;
the preparation method of tetraethyl ammonium trichloride comprises the following steps:
(a) respectively taking chlorine and tetraethylammonium chloride, controlling the mol ratio of the chlorine to the organic salt to be 1:1, firstly putting the tetraethylammonium chloride into a high-pressure reaction kettle, and introducing nitrogen into the high-pressure reaction kettle;
(b) adding chlorine gas into the high-pressure reaction kettle, controlling the whole process to be 60min, stirring and cooling in the dropping process, and controlling the temperature to be within 50 ℃;
(c) after the chlorine is dripped, cooling to room temperature to obtain the tetraethyl ammonium trichloride;
(2) adding N-methyl pyrrolidone into a ball milling tank, enabling the mass ratio of the total mass of tetraethylammonium trichloride, the carbon nano tubes and polyvinylidene fluoride (PVDF) to the mass of the N-methyl pyrrolidone to be 40:60, and carrying out ball milling for 60min to obtain anode slurry;
(3) coating the positive electrode slurry on an aluminum foil, and controlling the coating thickness of one side to be 300 mu m;
(4) putting the coated pole piece into a vacuum drying oven, and baking in vacuum, wherein the vacuum degree is controlled at-0.10 MPa, the temperature is controlled at 125 ℃, and the time is controlled for 360 min;
(5) and extruding the dried pole piece by using a double-roller machine, and controlling the pressure of the double rollers to be 300 tons to obtain the battery positive pole piece.
Manufacturing an aluminum secondary battery:
and assembling the prepared positive plate and the aluminum foil as negative plates and a diaphragm lamination, packaging by using an aluminum-plastic film, then filling electrolyte into a glove box, sealing, cleaning and forming to obtain the aluminum secondary battery.
Example 2
In the chloride preparation process, the molar ratio of chlorine to tetraethylammonium chloride was controlled at 2:1 as compared to example 1, otherwise the same as in example 1.
Example 3
In the chloride preparation process, the molar ratio of chlorine to tetraethylammonium chloride was controlled at 3:1 as compared to example 1, otherwise the process was the same as example 1.
Example 4
In the chloride preparation process, the molar ratio of chlorine to tetraethylammonium chloride was controlled to be 4:1 as compared to example 1, otherwise the process was the same as example 1.
Comparative example 1
In the chloride preparation process, the molar ratio of chlorine to tetraethylammonium chloride was controlled at 1:2 as compared to example 1, otherwise the process was the same as example 1.
Example 5
In comparison with example 1, in the preparation method of chloride, the cation of the raw material organic salt is morpholinium ion, the organic salt is specifically N-ethyl-N-butyl morpholine, and the chloride is specifically N-ethyl-N-butyl morpholine trichloro salt, and the rest is the same as example 1.
Example 6
In comparison with example 1, in the method for preparing a chloride, imidazolium ions are used as cations of the raw material organic salt, 1-ethyl-3-methyl-imidazolium chloride is specifically selected as the organic salt, and 1-ethyl-3-methyl-imidazolium trichloride is specifically selected as the chloride, and the rest is the same as example 1.
Example 7
In comparison with example 1, in the preparation method of chloride, pyridinium ions are used as cations of raw material organic salts, N-ethylpyridinium chloride is specifically selected as organic salts, and N-ethylpyridinium trichloride is specifically selected as chloride, and the rest is the same as example 1.
Example 8
Compared with the example 1, in the preparation method of the chloride, the cation of the raw material organic salt adopts quaternary phosphonium salt ion, the organic salt is specifically tributyl ethyl phosphonium chloride, and the chloride is specifically tributyl ethyl phosphonium trichloride, and the rest is the same as the example 1.
Comparative example 2
In comparison with example 1, the same procedure as in example 1 was repeated except that instead of chloride, polyaniline was used as a positive electrode active material.
Comparative example 3
In comparison with example 1, molybdenum disulfide was used as a positive electrode active material instead of chloride, and the rest was the same as example 1.
Comparative example 4
In comparison with example 1, graphite was used as a positive electrode active material instead of chloride, and the rest was the same as example 1.
Example 9
The carbon material used was carbon quantum dots as compared with example 1, and the rest was the same as example 1.
Example 10
Compared with the example 1, the mass ratio of the mesophase microspheres and the carbon nanotubes used as the carbon material is 5:1, and the rest is the same as the example 1.
Example 11
Compared with the example 1, the mass ratio of sodium carboxymethyl cellulose (CMC) to styrene-butadiene rubber (SBR) is controlled to be 2:1, water is used as a solvent, and the mass ratio of the total mass of tetraethylammonium trichloride, carbon nano tubes, sodium carboxymethyl cellulose and styrene-butadiene rubber to water is 50:50, and the rest is the same as the example 1.
Example 12
Compared with the example 1, the LA133 is used as a binder, water is used as a solvent, the mass ratio of the total mass of the tetraethylammonium trichloride, the carbon nanotubes and the LA133 to the water is 45:55, and the rest is the same as the example 1.
Example 13
Compared with the embodiment 1, the foamed aluminum is adopted as the current collector, and the rest is the same as the embodiment 1.
Example 14
Compared with the embodiment 1, the carbon-plastic composite film is adopted as the current collector, and the rest is the same as the embodiment 1.
Example 15
And (3) manufacturing a positive electrode:
(1) putting tetrabutylammonium trichloride, a carbon quantum dot and polyvinylidene fluoride (PVDF) into a ball milling tank, wherein the mass ratio of the tetrabutylammonium trichloride to the carbon quantum dot to the PVDF is 93:2:5, and carrying out ball milling for 15 min;
the preparation method of tetrabutylammonium trichloride comprises the following steps:
(a) respectively taking chlorine and tetrabutylammonium chloride, controlling the mol ratio of the chlorine to the tetrabutylammonium chloride to be 3:1, firstly putting the tetrabutylammonium chloride into a high-pressure reaction kettle, and introducing nitrogen and argon into the high-pressure reaction kettle;
(b) adding chlorine into the high-pressure reaction kettle, controlling the whole process to be 100min, stirring and cooling in the adding process, and controlling the temperature to be within 50 ℃;
(c) after the chlorine is added, cooling to room temperature to obtain tetrabutylammonium trichloride;
(2) adding N-methyl pyrrolidone into a ball milling tank, enabling the mass ratio of the total mass of tetrabutyl ammonium trichloride, carbon quantum dots and polyvinylidene fluoride (PVDF) to the mass of the N-methyl pyrrolidone to be 42:58, and carrying out ball milling for 100min to obtain anode slurry;
(3) coating the positive electrode slurry on an aluminum foil, and controlling the coating thickness of one side to be 210 mu m;
(4) putting the coated pole piece into a vacuum drying oven, and baking in vacuum, wherein the vacuum degree is controlled at-0.09 MPa, the temperature is controlled at 115 ℃, and the time is controlled for 300 min;
(5) and extruding the dried pole piece by using a double-roller machine, and controlling the pressure of the double rollers to be 20 tons to obtain the battery positive pole piece.
Manufacturing of the magnesium secondary battery:
and assembling the prepared positive plate, the magnesium negative plate and the diaphragm lamination, packaging by using an aluminum plastic film, then filling electrolyte into a glove box, sealing, cleaning and forming to obtain the magnesium secondary battery.
And (3) testing the battery performance:
the secondary batteries obtained in examples 1 to 15 and comparative examples 1 to 4 were subjected to charge and discharge performance tests, and the specific results are shown in table 1.
The specific energy of the discharge curves of the batteries of comparative example 4 and comparative example 3 are shown in fig. 1.
And (4) testing standard: the battery was subjected to charge and discharge experiments, charged to a rated voltage at 0.5C, discharged at 0.5C, and discharged to a voltage of 1V, and the charge and discharge data are shown in table 1.
TABLE 1
Figure BDA0001064042770000181
Figure BDA0001064042770000191
As can be seen from fig. 1, in example 4, compared with comparative example 3, the voltage can reach 2.8V by using chloride as the positive active material, so that the specific energy of the positive electrode of the battery can reach more than 482mAh/g at most; the voltage of comparative example 3 was only 1.5V, and the specific energy of the positive electrode was only 200 mAh/g. Therefore, example 4 uses chloride to produce a secondary battery having a higher specific energy than the secondary battery using molybdenum disulfide as a positive electrode active material, compared to comparative example 3.
As can be seen from Table 1, examples 1 to 4, compared with comparative example 1, can increase the specific energy of the positive electrode of the battery to 400mAh/g and have excellent cycle life by controlling the mole ratio of chlorine gas to organic salt to be (1 to 4): 1; compared with comparative examples 2-4, examples 1-8 adopt chloride as the positive active material, the voltage can reach more than 2.8V at most, the specific energy of the battery positive electrode is more than 400mAh/g, and the cycle life is excellent; examples 9-15 also provide the desired specific energy of the battery after adjustment of the carbon material, binder, current collector, and parameters. Thus, the advantages of the present invention are clearly apparent.
The result is integrated to obtain that the chloride is added into the positive active material, so that the voltage platform is high, the prepared secondary battery has higher specific energy, rapid charge and discharge are realized, the cycle life is prolonged, the raw material cost is low, and the chloride has important application value.
The applicant declares that the present invention illustrates the detailed structural features of the present invention through the above embodiments, but the present invention is not limited to the above detailed structural features, that is, it does not mean that the present invention must be implemented depending on the above detailed structural features. It should be understood by those skilled in the art that any modifications of the present invention, equivalent substitutions of selected components of the present invention, additions of auxiliary components, selection of specific modes, etc., are within the scope and disclosure of the present invention.
The preferred embodiments of the present invention have been described in detail, however, the present invention is not limited to the specific details of the above embodiments, and various simple modifications may be made to the technical solution of the present invention within the technical idea of the present invention, and these simple modifications are within the protective scope of the present invention.
It should be noted that the various technical features described in the above embodiments can be combined in any suitable manner without contradiction, and the invention is not described in any way for the possible combinations in order to avoid unnecessary repetition.
In addition, any combination of the various embodiments of the present invention is also possible, and the same should be considered as the disclosure of the present invention as long as it does not depart from the spirit of the present invention.

Claims (13)

1. A positive electrode sheet for a battery, comprising a chloride, a carbon material, a binder and a current collector; the mass ratio of the chloride to the carbon material to the binder is (40-98): (1-40): 1-20);
the chloride is obtained by reacting chlorine gas with organic salt;
the organic salt has a general formula of [ X]+Z-(ii) a Wherein, [ X ]]+Represents an organic cation, Z-Represents an anion;
the organic cation is any one or the combination of at least two of pyrrolium ion, piperidinium ion, morpholinium ion, quaternary ammonium salt ion or quaternary phosphonium salt ion; the anion is F-、Cl-、Br-、I-、PF6 -、PB4 -、CN-、SCN-、CF3SO3 -、CF3COO-、SbF6 -、N(CF3SO2)2 -、N(CN)2 -、ClO4 -、HSO4 -、HCO3 -、OH-Or NO3 -Any one or a combination of at least two of;
the chloride is prepared by the following method, and the method comprises the following steps:
(a) respectively taking chlorine and organic salt, controlling the mol ratio of the chlorine to the organic salt to be (2-4):1, firstly putting the organic salt into a closed container, and introducing nitrogen and/or argon into the closed container;
(b) adding chlorine gas into the closed container, controlling the whole process to be 1-60min, stirring and cooling in the adding process, and controlling the temperature to be within 50 ℃;
(c) and cooling to room temperature after the chlorine is added to obtain the chloride.
2. The positive electrode sheet according to claim 1, wherein the organic cation is a quaternary ammonium salt ion.
3. The positive electrode sheet according to claim 1, wherein the carbon material is any one or a combination of at least two of graphite, carbon quantum dots, activated carbon, carbon fibers, carbon nanotubes, carbon aerogels, mesoporous carbon, graphene, carbon black, nanocarbon powder, mesocarbon microbeads, or hard carbon.
4. The positive electrode sheet according to claim 3, wherein the carbon material is any one or a combination of at least two of carbon nanotubes, carbon quantum dots, graphite, carbon black, or carbon nanopowders.
5. The positive electrode sheet according to claim 1, wherein the binder is one selected from the group consisting of CMC and SBR, and PVDF, LA133 and LA 132.
6. The positive electrode sheet according to claim 5, wherein PVDF is used as a binder.
7. The positive electrode sheet according to claim 1, wherein the current collector is any one or a combination of at least two of aluminum foil, foamed aluminum, carbon paper, carbon-plastic composite film or carbon fiber felt.
8. The method for producing a positive electrode sheet for a battery according to any one of claims 1 to 7, comprising the steps of:
(1) putting chloride, a carbon material and a binder into a ball mill, wherein the mass ratio of the chloride to the carbon material to the binder is (40-98): 1-40): 1-20, and carrying out ball milling for 5-120 min;
(2) adding a solvent into a ball mill, enabling the mass ratio of the total mass of the chloride, the carbon material and the binder to the solvent to be (40-60) to (60-40), and carrying out ball milling for 60-120min to obtain anode slurry;
(3) coating the positive electrode slurry on a current collector, and controlling the coating thickness of one side to be 100-300 mu m;
(4) drying the coated pole piece;
(5) and extruding the dried pole piece to obtain the battery positive pole piece.
9. The method of claim 8, wherein the chloride of step (1) is prepared by a method comprising the steps of:
(a) respectively taking chlorine and organic salt, controlling the mol ratio of the chlorine to the organic salt to be (2-4):1, firstly putting the organic salt into a closed container, and introducing nitrogen and/or argon into the closed container;
(b) adding chlorine gas into the closed container, controlling the whole process to be 1-60min, stirring and cooling in the adding process, and controlling the temperature to be within 50 ℃;
(c) and cooling to room temperature after the chlorine is added to obtain the chloride.
10. The method according to claim 8, wherein the solvent in the step (2) is any one or a combination of at least two of water, NMP, dimethylformamide, dimethylacetamide, dimethylsulfoxide and acetone.
11. The method as claimed in claim 8, wherein the drying in step (4) is performed by vacuum baking at a vacuum degree of-0.08 to-0.10 MPa and a temperature of 100 ℃ and 125 ℃ for 180min and 360 min.
12. The method according to claim 8, wherein the extrusion in the step (5) is performed by a twin roll press, and the pressure between the rolls is controlled to be 50 to 300 tons.
13. Preparation process according to one of claims 8 to 12, characterized in that it comprises the following steps:
(1) putting chloride, a carbon material and a binder into a ball mill, wherein the mass ratio of the chloride to the carbon material to the binder is (40-98): 1-40): 1-20, and carrying out ball milling for 5-120 min;
the preparation method of the chloride comprises the following steps:
(a) respectively taking chlorine and organic salt, controlling the mol ratio of the chlorine to the organic salt to be (2-4):1, firstly putting the organic salt into a closed container, and introducing nitrogen and/or argon into the closed container;
(b) adding chlorine gas into the closed container, controlling the whole process to be 1-60min, stirring and cooling in the adding process, and controlling the temperature to be within 50 ℃;
(c) after the chlorine is added, cooling to room temperature to obtain the chloride;
(2) adding a solvent into a ball mill, enabling the mass ratio of the total mass of the chloride, the carbon material and the binder to the solvent to be (40-60) to (60-40), and carrying out ball milling for 60-120min to obtain anode slurry;
(3) coating the positive electrode slurry on a current collector, and controlling the coating thickness of one side to be 100-300 mu m;
(4) putting the coated pole piece into a vacuum drying oven, and performing vacuum baking, wherein the vacuum degree is controlled to be-0.08 to-0.10 MPa, the temperature is controlled to be 100-;
(5) and extruding the dried pole piece by using a double-roller machine, and controlling the pressure of the double rollers to be 50-300 tons to obtain the battery positive pole piece.
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