[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

CN109167040A - Method for applying carbon fluoride additive to lithium-sulfur battery and application of carbon fluoride additive - Google Patents

Method for applying carbon fluoride additive to lithium-sulfur battery and application of carbon fluoride additive Download PDF

Info

Publication number
CN109167040A
CN109167040A CN201810986904.4A CN201810986904A CN109167040A CN 109167040 A CN109167040 A CN 109167040A CN 201810986904 A CN201810986904 A CN 201810986904A CN 109167040 A CN109167040 A CN 109167040A
Authority
CN
China
Prior art keywords
lithium
sulfur cell
fluorination
carbon
fluorocarbons
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201810986904.4A
Other languages
Chinese (zh)
Inventor
霍峰蔚
高聪
李盛
邵梦
吴健生
郑冰
张伟娜
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nanjing Tech University
Original Assignee
Nanjing Tech University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nanjing Tech University filed Critical Nanjing Tech University
Priority to CN201810986904.4A priority Critical patent/CN109167040A/en
Publication of CN109167040A publication Critical patent/CN109167040A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/52Reclaiming serviceable parts of waste cells or batteries, e.g. recycling
    • 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
    • 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
    • H01M4/364Composites as mixtures
    • 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
    • H01M4/58Selection 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
    • 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
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624Electric conductive fillers
    • H01M4/625Carbon or graphite
    • 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
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/628Inhibitors, e.g. gassing inhibitors, corrosion inhibitors
    • 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
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/84Recycling of batteries or fuel cells

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Composite Materials (AREA)
  • Materials Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Inorganic Chemistry (AREA)
  • Secondary Cells (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

The invention relates to an additive which can be used as a lithium-sulfur battery anode material and performance comparison thereof under different proportions, belonging to the field of energy storage. The carbon fluoride, active substance sulfur, conductive carbon and binder PVDF are mechanically ground to be compounded to manufacture the lithium-sulfur battery, and the cycle life and the rate capability of the lithium-sulfur battery are improved by using fluorine-doped carbon generated by carbon fluoride discharge. The carbon fluoride as an additive of the lithium-sulfur battery can not only provide additional conductive carbon at the positive electrode, but also absorb lithium polysulfide by the fluorine-doped carbon. The lithium-sulfur battery prepared by using the additive has the advantages of higher capacity, longer cycle life, stable charge and discharge efficiency, easy obtainment and low cost of raw materials, simple production process and harmless reaction process, and the advantages are favorable for the application of the method to industrial actual production.

Description

A kind of fluorination carbonaceous additive is used for the method and its application of lithium-sulfur cell
Technical field
The present invention relates to the performances under additive and its different ratio that one kind can be used as lithium sulfur battery anode material to compare, Belong to energy storage field.
Background technique
In the past few decades, the safety of lithium ion battery Yin Qigao, and be widely used in 3C Product (computer, Communication and consumption electronic product).But the energy density of commercial li-ion battery is lower at present, onlyNothing Method meets the demand of growing emerging large-scale energy storage technology, such as electric car and power grid energy storage etc..In numerous elder generations Into rechargeable battery system in, lithium sulphur (Li-S) battery is by extensive concern and is studied, because it is with high theoretical specific volume AmountHigh theoretical specific energy (2500W h-1) and sulphur is very rich on earth, cheap, nontoxic, ring Border is friendly.
Although lithium-sulfur cell has the advantages that so many, there is also many problems to restrict its commercialization.These are asked Topic is as described below: 1) active material sulphur and electric discharge final product lithium sulfide are nonconducting, it is low which results in the utilization rate of sulphur and Special capacity fade is very fast;2) reaction of Salmon-Saxl, which generates lithium sulfide, leads to serious volume expansion, and general 80%;3) reaction intermediate is long The more lithium sulfides of chain are soluble in electrolyte, lead to " shuttle effect ";4) problems of cathode of lithium itself are badly in need of solving, such as lithium branch Brilliant growth.These problems lead to low coulombic efficiency, capacity quickly and reduce low with active material utilization efficiency.Therefore it improves and leads It is electrically protected with cathode of lithium, raw material sources are extensive, and the simple lithium-sulfur cell of production technology is particularly important.
Summary of the invention
The purpose of the present invention is using fluorocarbons as additive, the method for the commercially viable lithium-sulfur cell of exploitation high-performance, and And a kind of method of electrode material waste waste utilization is provided, i.e., after Li/ fluorocarbons one-shot battery is finished, generate anode waste Play the role of promoting chemical property in lithium-sulfur cell again.
To solve technical problem of the invention, the technical scheme is that fluorination carbonaceous additive is for lithium-sulfur cell Fluorocarbons is added to active material sulphur, conductive carbon and binder PVDF and matched in the mixture for 7:2:1 by method, carries out machine Tool ground and mixed makes lithium-sulfur cell as positive electrode after mixing, is promoted using the Fluorin doped carbon that fluorocarbons electric discharge generates The cycle life and high rate performance of lithium-sulfur cell.
Preferably, the fluorocarbons includes fluorographite, fluorination coke, fluorinated carbon fiber, fluorination carbosphere, fluorination charcoal Black, fluorination micro crystal graphite or fluorographite microplate.
Preferably, 5-20% fluorination carbonaceous additive is added in lithium-sulfur cell.
Preferably, 10% fluorination carbonaceous additive is added in lithium-sulfur cell.
Preferably, the fluorocarbons reaction generates carbon, increases the electric conductivity of galvanic electricity pole.
Preferably, the Fluorin doped carbon of the generation can adsorb more lithium sulfides, thus inhibit the shuttle effect of more lithium sulfides, Improve the chemical property of lithium-sulfur cell.
Preferably, the charging/discharging voltage of the lithium-sulfur cell is 1.8-3.0V.
Preferably, it can be used as energy storage to apply in computer, communication and consumer electronics sector.
A kind of preparation method of high-performance lithium-sulfur cell, preparation process are as follows: fluorocarbons (expedition group) is used as lithium sulphur The anode additive of battery, elemental sulfur are used as the positive active material of lithium-sulfur cell.
The method for preparing lithium-sulfur cell, first, in accordance with active material: conductive agent: binder mass ratio is that 7:2:1 will be positive After material sulphur, conductive agent Super P and polyvinylidene fluoride mechanical lapping, then into the mixture after grinding it is added 0/5/10/ 20% fluorocarbons is uniformly mixed in solvent N-methyl pyrilidone, is uniformly mixed to obtain and is dispersed uniform slurry, then will Uniformly it is coated on utter misery aluminium foil.Then the electrode slice made is dried into 12h in 60 DEG C of normal drying casees, be then transferred to 12h is dried in 60 DEG C of vacuum drying oven.Using metal lithium sheet as cathode, 1.0M LiTFSI, 5%LiNO3DME:DOL=1: 1Vol% is electrolyte, and diaphragm uses commercialized 2400 diaphragm of Celgar, and battery case model 2025, in glove box, (oxygen contains Amount is less than 0.5ppm, and water content is less than assembling button cell in 0.5ppm).
Battery assembly carries out rate charge-discharge on cell tester (the blue electric battery test system in Wuhan) after completing and follows Ring test, operating voltage 1.8-3V, data acquisition are drawn by origin data processing software after completing, are analyzed.
The utility model has the advantages that
Fluorocarbons can not only provide additional conductive carbon, but also Fluorin doped carbon as lithium-sulfur cell additive in anode More lithium sulfides can also be adsorbed.The lithium-sulfur cell capacity with higher prepared using the additive, cycle life is longer, stablizes Efficiency for charge-discharge, furthermore raw material be easy to get and low cost, the simplicity of production technology, reaction process is innoxious, these advantages Be conducive to this method and be applied to industrialization actual production.
Fluorocarbons has been used as being commercialized disposable lithium-battery, can generate LiF and C (Fluorin doped carbon) when discharging, so not It only causes to waste and pollute, and also increase its cost in this way.Based on this, we want to be promoted using the discharging product of fluorocarbons The chemical property of lithium-sulfur cell, cardinal principle are that fluorocarbons is made into slurry with sulphur mixing as additive, by it, are then done At electrode slice, in first discharge process of lithium-sulfur cell, fluorocarbons generates LiF and C, and this is an irreversible process, This is also equivalent to increase conductive carbon in anode, and Fluorin doped carbon can adsorb more lithium sulfides, inhibit the shuttle of more lithium sulfides Effect.The chemical property of lithium-sulfur cell not only can be greatly improved, and the cost of lithium-sulfur cell can be reduced.
Detailed description of the invention
Fig. 1 is fluorocarbons X-ray diffractogram.
Fig. 2 is fluorocarbons as additive and additive-free lithium-sulfur cell long circulating performance map.
Fig. 3 is fluorocarbons as additive and additive-free lithium-sulfur cell high rate performance figure.
Fig. 4 is fluorocarbons as the impedance after additive and additive-free lithium-sulfur cell circulation.
Specific embodiment
Below in conjunction with specific implementation example, it is intended to further illustrate that the present invention is not intended to limit the present invention.
Embodiment 1
5mg fluorocarbons is weighed, 70mg sulphur, 20mg conductive agent Super P, 10mg polyvinylidene fluoride is in Solvents N-methyl pyrrole It is uniformly mixed, will uniformly be coated on utter misery aluminium foil, then by the electrode slice made in 60 DEG C of normal dryings in pyrrolidone 12h is dried in case, is then transferred in 60 DEG C of vacuum drying oven and is dried 12h.Using metal lithium sheet as cathode, 1.0M LiTFSI, 5% LiNO3DME:DOL=1:1Vol% is electrolyte, and diaphragm uses commercialized 2400 diaphragm of Celgar, battery case model 2025, button cell is assembled in glove box (oxygen content is less than 0.5ppm, and water content is less than 0.5ppm).
Battery assembly carries out rate charge-discharge on cell tester (the blue electric battery test system in Wuhan) after completing and follows Ring test, operating voltage 1.8-3V, data acquisition are drawn by origin data processing software after completing, are analyzed.
When battery uses 0.1C charge and discharge in blue electric system, first circle specific discharge capacity reaches 719.8mAh g-1, then use When 0.5C charge and discharge, third circle specific discharge capacity 508.4mAh g-1, after 150 circles, specific discharge capacity also reaches 464.2mAh g-1;When with 1C charge and discharge, first circle specific capacity is 439.3mAh g-1, after 400 enclose, the also surplus 248.5mAh g of specific capacity-1;Multiplying power Impedance afterwards is 6 Ω.
Embodiment 2
10mg fluorocarbons is weighed, 70mg sulphur, 20mg conductive agent Super P, 10mg polyvinylidene fluoride is in Solvents N-methyl It is uniformly mixed, will uniformly be coated on utter misery aluminium foil in pyrrolidones, it is then that the electrode slice made is common dry at 60 DEG C 12h is dried in dry case, is then transferred in 60 DEG C of vacuum drying oven and dries 12h.Using metal lithium sheet as cathode, 1.0M LiTFSI, 5%LiNO3DME:DOL=1:1Vol% is electrolyte, and diaphragm uses commercialized 2400 diaphragm of Celgar, battery case model It is 2025, assembles button cell in glove box (oxygen content is less than 0.5ppm, and water content is less than 0.5ppm).
Battery assembly carries out rate charge-discharge on cell tester (the blue electric battery test system in Wuhan) after completing and follows Ring test, operating voltage 1.8-3V, data acquisition are drawn by origin data processing software after completing, are analyzed.
For battery when using 0.1C charge and discharge in blue electric system, first circle specific discharge capacity reaches 901.3mAh g-1, then use 0.5C When charge and discharge, third circle specific discharge capacity 577.3mAh g-1, after 150 circles, specific discharge capacity also reaches 508.3mAh g-1; When with 1C charge and discharge, first circle specific capacity is 486.9mAh g-1, after 400 enclose, the also surplus 338.4mAh g of specific capacity-1
Embodiment 3
20mg fluorocarbons is weighed, 70mg sulphur, 20mg conductive agent Super P, 10mg polyvinylidene fluoride is in Solvents N-methyl It is uniformly mixed, will uniformly be coated on utter misery aluminium foil in pyrrolidones, it is then that the electrode slice made is common dry at 60 DEG C 12h is dried in dry case, is then transferred in 60 DEG C of vacuum drying oven and dries 12h.Using metal lithium sheet as cathode, 1.0M LiTFSI, 5%LiNO3DME:DOL=1:1Vol% is electrolyte, and diaphragm uses commercialized 2400 diaphragm of Celgar, battery case model It is 2025, assembles button cell in glove box (oxygen content is less than 0.5ppm, and water content is less than 0.5ppm).
Battery assembly carries out rate charge-discharge on cell tester (the blue electric battery test system in Wuhan) after completing and follows Ring test, operating voltage 1.8-3V, data acquisition are drawn by origin data processing software after completing, are analyzed.
For battery when using 0.1C charge and discharge in blue electric system, first circle specific discharge capacity reaches 862.5mAh g-1, then use 0.5C When charge and discharge, third circle specific discharge capacity 616.2mAh g-1, after 150 circles, specific discharge capacity also reaches 488.1mAh g-1; When with 1C charge and discharge, first circle specific capacity is 555.4mAh g-1, after 400 enclose, the also surplus 346.9mAh g of specific capacity-1;After multiplying power Impedance is 2 Ω.
Of the invention is not limited to the above embodiment the specific technical solution, all technologies formed using equivalent replacement Scheme be the present invention claims protection scope.

Claims (8)

1. it is a kind of fluorination carbonaceous additive be used for lithium-sulfur cell method, it is characterised in that: by fluorocarbons be added to active material sulphur, Conductive carbon and binder PVDF proportion are to carry out mechanical lapping mixing in the mixture of 7:2:1, and positive electrode system is used as after mixing Make lithium-sulfur cell, the cycle life and high rate performance of lithium-sulfur cell are promoted using the Fluorin doped carbon that fluorocarbons electric discharge generates.
2. fluorination carbonaceous additive according to claim 1 is used for lithium-sulfur cell method, it is characterised in that: the fluorocarbons packet It is micro- to include fluorographite, fluorination coke, fluorinated carbon fiber, fluorination carbosphere, fluorination carbon black, fluorination micro crystal graphite or fluorographite Piece.
3. fluorination carbonaceous additive according to claim 1 is used for lithium-sulfur cell method, it is characterised in that: 5-20% to be fluorinated Carbonaceous additive is added in lithium-sulfur cell.
4. fluorination carbonaceous additive according to claim 3 is used for lithium-sulfur cell method, it is characterised in that: by 10% fluorocarbons Additive is added in lithium-sulfur cell.
5. fluorination carbonaceous additive according to claim 1 is used for lithium-sulfur cell method, it is characterised in that: the fluorocarbons is anti- Carbon should be generated, the electric conductivity of galvanic electricity pole is increased.
6. fluorination carbonaceous additive according to claim 1 is used for lithium-sulfur cell method, it is characterised in that: the fluorine of the generation Doped carbon can adsorb more lithium sulfides, to inhibit the shuttle effect of more lithium sulfides, improve the chemical property of lithium-sulfur cell.
7. fluorination carbonaceous additive according to claim 1 is used for lithium-sulfur cell method, it is characterised in that: the lithium-sulfur cell Charging/discharging voltage be 1.8-3.0V.
8. prepared fluorination carbonaceous additive is used for the application of lithium-sulfur cell according to claim 1, it is characterised in that: can be used as energy Source storage is applied in computer, communication and consumer electronics sector.
CN201810986904.4A 2018-08-28 2018-08-28 Method for applying carbon fluoride additive to lithium-sulfur battery and application of carbon fluoride additive Pending CN109167040A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810986904.4A CN109167040A (en) 2018-08-28 2018-08-28 Method for applying carbon fluoride additive to lithium-sulfur battery and application of carbon fluoride additive

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810986904.4A CN109167040A (en) 2018-08-28 2018-08-28 Method for applying carbon fluoride additive to lithium-sulfur battery and application of carbon fluoride additive

Publications (1)

Publication Number Publication Date
CN109167040A true CN109167040A (en) 2019-01-08

Family

ID=64897001

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810986904.4A Pending CN109167040A (en) 2018-08-28 2018-08-28 Method for applying carbon fluoride additive to lithium-sulfur battery and application of carbon fluoride additive

Country Status (1)

Country Link
CN (1) CN109167040A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109921004A (en) * 2019-03-19 2019-06-21 北京化工大学 A kind of lithium sulfur battery anode material and its application
CN111628166A (en) * 2020-06-04 2020-09-04 合肥工业大学 Three-dimensional lithium sulfide electrode for lithium-sulfur battery and preparation method thereof
CN111628150A (en) * 2020-06-04 2020-09-04 合肥工业大学 Carbon-coated lithium sulfide composite electrode for lithium-sulfur battery and preparation method thereof
CN114784452A (en) * 2022-05-24 2022-07-22 南京工业大学 Method for preparing lithium-sulfur battery diaphragm material by using fluorine-containing covalent organic framework material
CN114824587A (en) * 2022-05-30 2022-07-29 中国科学院长春应用化学研究所 Lithium air/carbon fluoride composite battery

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104716296A (en) * 2013-12-11 2015-06-17 上海空间电源研究所 Sulfur-containing composite anode, preparation method thereof and lithium-sulfur battery using sulfur-containing composite anode as anode
CN106169561A (en) * 2016-09-30 2016-11-30 上海空间电源研究所 A kind of sulfur system anode composite pole piece, the battery comprising it and preparation method thereof
CN107316967A (en) * 2017-06-26 2017-11-03 上海空间电源研究所 A kind of barrier film, preparation method and the usage for including active interlayer
CN107895794A (en) * 2017-11-23 2018-04-10 中国航发北京航空材料研究院 A kind of high specific energy lithium fluorocarbon battery
CN107910502A (en) * 2017-11-15 2018-04-13 上海空间电源研究所 A kind of lithium battery anode composite manufacture method and the battery

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104716296A (en) * 2013-12-11 2015-06-17 上海空间电源研究所 Sulfur-containing composite anode, preparation method thereof and lithium-sulfur battery using sulfur-containing composite anode as anode
CN106169561A (en) * 2016-09-30 2016-11-30 上海空间电源研究所 A kind of sulfur system anode composite pole piece, the battery comprising it and preparation method thereof
CN107316967A (en) * 2017-06-26 2017-11-03 上海空间电源研究所 A kind of barrier film, preparation method and the usage for including active interlayer
CN107910502A (en) * 2017-11-15 2018-04-13 上海空间电源研究所 A kind of lithium battery anode composite manufacture method and the battery
CN107895794A (en) * 2017-11-23 2018-04-10 中国航发北京航空材料研究院 A kind of high specific energy lithium fluorocarbon battery

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
吴锋 等: "化学结合力载体在锂硫电池中的应用", 《化学进展》 *
李国欣 主编: "《新型化学电源技术概论》", 31 May 2007, 上海科学技术出版社 *
裴海娟 等: "导电碳修饰隔膜在高硫载量锂硫电池中的作用", 《储能科学与技术》 *
陈子冲 等: "锂硫电池硫正极材料研究进展", 《材料导报A:综述篇》 *

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109921004A (en) * 2019-03-19 2019-06-21 北京化工大学 A kind of lithium sulfur battery anode material and its application
CN109921004B (en) * 2019-03-19 2021-01-12 北京化工大学 Lithium-sulfur battery positive electrode material and application thereof
CN111628166A (en) * 2020-06-04 2020-09-04 合肥工业大学 Three-dimensional lithium sulfide electrode for lithium-sulfur battery and preparation method thereof
CN111628150A (en) * 2020-06-04 2020-09-04 合肥工业大学 Carbon-coated lithium sulfide composite electrode for lithium-sulfur battery and preparation method thereof
CN111628150B (en) * 2020-06-04 2021-10-08 合肥工业大学 Carbon-coated lithium sulfide composite electrode for lithium-sulfur battery and preparation method thereof
CN114784452A (en) * 2022-05-24 2022-07-22 南京工业大学 Method for preparing lithium-sulfur battery diaphragm material by using fluorine-containing covalent organic framework material
CN114784452B (en) * 2022-05-24 2023-09-26 南京工业大学 Method for preparing lithium-sulfur battery diaphragm material by using fluorine-containing covalent organic framework material
CN114824587A (en) * 2022-05-30 2022-07-29 中国科学院长春应用化学研究所 Lithium air/carbon fluoride composite battery

Similar Documents

Publication Publication Date Title
CN103700820B (en) A kind of lithium ion selenium battery with long service life
CN110416531B (en) Bismuth oxyhalide aqueous zinc ion secondary battery positive electrode and preparation method and application thereof
CN103435105B (en) A kind of ferriferous oxide/carbon composition lithium ion battery cathode material and its preparation method and application
CN105489901B (en) A kind of preparation method and applications of lithium-sulfur cell three-dimensional carbon collector
CN109004199B (en) Preparation method of biomass hard carbon material for negative electrode of sodium-ion battery
CN109167040A (en) Method for applying carbon fluoride additive to lithium-sulfur battery and application of carbon fluoride additive
CN110148787B (en) Electrolyte for improving capacity of lithium-sulfur battery and lithium-sulfur battery
CN102082259A (en) Lithium secondary battery electrodes and production method thereof
CN102244288B (en) Lithium-phosphorus secondary battery
CN110611084B (en) Lithium-sulfur secondary battery with long cycle life and 100% coulombic efficiency
CN107946538A (en) Lithiumation sulfur electrode and preparation method and application
CN108922788A (en) A kind of PEDOT@Na3(VOPO4)2F composite material, preparation method and its application
CN104617283A (en) Lithium-sulfur battery carbon fiber reinforced three-dimensional graphene-sulfur positive electrode material, preparation method of material and preparation method of positive electrode
CN109704302A (en) A kind of phosphorus doping porous carbon materials and its preparation and the application in lithium-sulfur cell coated separator
CN103427068B (en) A kind of positive electrode and preparation method thereof for lithium-sulfur cell
CN107946564B (en) Rich in Na4Mn2O5/Na0.7MnO2Composite material and preparation method and application thereof
CN109286002B (en) Multi-bark biomass carbon-loaded red phosphorus sodium ion battery negative electrode material and preparation method thereof
CN102024989A (en) Preparation method of high-voltage lithium-ion battery
CN104183836B (en) A kind of lithium-sulfur cell anode composite material
CN109962231A (en) Metal foil is used as lanthanum ion secondary battery negative pole and lanthanum ion secondary cell and preparation method thereof
CN105680016B (en) One kind contains addition of C o3O4Lithium sulfur battery anode material and preparation method
CN108987755A (en) Method for applying lignosulfonate as binder to lithium-sulfur battery and application of lignosulfonate
CN114284476A (en) Preparation method of carbon composite sodium-ion battery positive electrode material
CN103367728A (en) Activated natural graphite modified Li2FeSiO4 cathode material and its preparation method
CN108258244B (en) Novel lithium ion/potassium ion battery negative electrode material and preparation method thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20190108

RJ01 Rejection of invention patent application after publication