CN107507964A - A kind of preparation method of soft carbon, hard carbon core shell structure negative material - Google Patents

A kind of preparation method of soft carbon, hard carbon core shell structure negative material Download PDF

Info

Publication number
CN107507964A
CN107507964A CN201610414923.0A CN201610414923A CN107507964A CN 107507964 A CN107507964 A CN 107507964A CN 201610414923 A CN201610414923 A CN 201610414923A CN 107507964 A CN107507964 A CN 107507964A
Authority
CN
China
Prior art keywords
hard carbon
starch
temperature
shell structure
core shell
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
CN201610414923.0A
Other languages
Chinese (zh)
Inventor
仲林
谢秋生
张鹏昌
杜辉玉
陈然
陈志明
薄维通
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.)
Shanghai Shanshan Technology Co Ltd
Original Assignee
Shanghai Shanshan Technology Co Ltd
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 Shanghai Shanshan Technology Co Ltd filed Critical Shanghai Shanshan Technology Co Ltd
Priority to CN201610414923.0A priority Critical patent/CN107507964A/en
Publication of CN107507964A publication Critical patent/CN107507964A/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
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/362Composites
    • H01M4/366Composites as layered products
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • 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
    • H01M4/58Selection 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
    • H01M4/583Carbonaceous material, e.g. graphite-intercalation compounds or CFx
    • H01M4/587Carbonaceous material, e.g. graphite-intercalation compounds or CFx for inserting or intercalating light metals
    • 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
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Composite Materials (AREA)
  • Engineering & Computer Science (AREA)
  • Inorganic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

The present invention relates to battery material technical field, specifically a kind of soft carbon, the preparation method of hard carbon core shell structure negative material, it is characterised in that use following preparation method:(1), ammonium chloride is added to the water, stir to obtain aqueous ammonium chloride solution, then adds starch, continues to be uniformly mixing to obtain mixture;(2), pre- carbonization;(3) starch base hard carbon, is prepared;(4) emulsion, is prepared;(5), it is spray-dried;(6), heating carbonization, is cooled to room temperature and gets product.Compared with the existing technology, preparation method is simple, and cost is low, environmentally safe by the present invention;After the soft carbon prepared, hard carbon core shell structure negative material are applied to lithium ion battery, make the permanent hair styling that there is the characteristics of cyclical stability is strong, electric conductivity is strong, rate charge-discharge is good.

Description

A kind of preparation method of soft carbon, hard carbon core shell structure negative material
Technical field
The present invention relates to battery material technical field, specifically a kind of soft carbon, hard carbon core shell structure negative pole The preparation method of material.
Background technology
With the development of science and technology, people propose higher requirement to the performance of electrochmical power source (battery). Such as, the development of integrated circuit technique makes electronic instrument small, portability, correspondingly requires that battery has There is the characteristics of small volume, in light weight, higher than energy;Space exploration technology and national defence, military equipment technology Continuous development requires that battery has high-energy-density and long storage life;The reinforcement of environmental protection consciousness makes people couple The development growing interest of electric automobile, and this battery should then have big ratio energy and specific power.Numerous Battery system in, lithium battery so that its operating voltage is high, energy density is big and shows one's talent the advantages that light weight, Paid attention to by countries in the world.
The development of portable electric appts was advanced by leaps and bounds in the last few years.In addition, lithium rechargeable battery also by Gradually it is pushed to field of traffic.Thus requirement to lithium rechargeable battery is constantly improving, due to it is this more High requirement, limitation of the graphite cathode material in terms of capacity and power characteristic are just obvious all the more.This Under background, hard carbon has promising negative material as one kind and gradually closed by more research workers very much Note.
The content of the invention
The purpose of the present invention is overcome the deficiencies in the prior art, there is provided a kind of cyclical stability is strong, electric conductivity is strong, The good soft carbon for lithium ion battery of rate charge-discharge, hard carbon core shell structure negative material.
To achieve the above object, a kind of soft carbon, the preparation method of hard carbon core shell structure negative material are designed, its It is characterised by using following preparation method:
(1), ammonium chloride is added to the water, stir to obtain aqueous ammonium chloride solution, then adds starch, after It is continuous to be uniformly mixing to obtain mixture;The mass concentration of described aqueous ammonium chloride solution is 0.5~30g/L, The weight of ammonium chloride and starch ratio is 1: 1~200;
(2), mixture is put into vacuum drying chamber, is dried in vacuo 1 hour, be carbonized 1h in advance, obtains pre- carbon Compound, vacuum drying temperature are 60 DEG C~100 DEG C, and pre- carburizing temperature is 100 DEG C~320 DEG C;
(3), pre- carbide is put into atmosphere furnace, and under inert gas shielding, temperature is 700~1000 DEG C, Heating rate is 5 DEG C of min, and constant temperature time is 0.1~10 hour, drops to room temperature, obtains starch base hard carbon;
(4) covering and emulsifying agent, deionized water, are made into emulsion, emulsifying agent: covering: go from The weight ratio of sub- water is 1~5: 50: 100~449;
(5) it is, starch base hard carbon: emulsion=1~1: 100 starch base hard carbon and emulsion by weight ratio Stir, be spray-dried, the temperature of import is 180 DEG C~250 DEG C during spray drying, outlet Temperature is 100 DEG C~120 DEG C;
(6), the product after spray drying is placed in tube furnace, under inert gas shielding, heating carbonization, Carburizing temperature is 1000~2000 DEG C, and heating rate is 5 DEG C of min, and carbonization time is 1h~24h, cold But got product to room temperature;
Described covering uses any in asphalt, coal tar pitch, petroleum residual oil or coal measures residual oil Kind.
The starch is in farina, cornstarch, wheaten starch, sweet potato starch, kudzuvine root starch It is one or more.
Atmosphere in described atmosphere furnace is nitrogen or argon gas.
Compared with the existing technology, preparation method is simple, and cost is low, environmentally safe by the present invention;Prepare Soft carbon, hard carbon core shell structure negative material be applied to lithium ion battery after, make the permanent hair styling that there is stable circulation The characteristics of property is strong, electric conductivity is strong, rate charge-discharge is good.
Brief description of the drawings
Fig. 1 is the electron microscopic picture of embodiment 6.
Embodiment
Below in conjunction with embodiment, technical scheme is further described through.
Embodiment 1
Step 1:Weigh 2g ammonium chlorides to be added in 1000ml water, stir, it is beautiful then to add 100g Rice starch, continue to stir, obtain mixture;
Step 2:Mixture is put into vacuum drying chamber, 100 DEG C are dried in vacuo 1 hour, 150 DEG C of pre- carbon Change 1h, obtain pre- carbide;
Step 3:Pre- carbide is put into atmosphere furnace, is warming up under nitrogen protection with 5 DEG C/min speed 700 DEG C, constant temperature is cooled to room temperature after 5 hours, obtains starch base hard carbon.
Step 4:Pitch and emulsifying agent, deionized water are made into emulsion, described emulsifying agent: pitch: The weight ratio of deionized water is 1: 50: 449;
Step 5:By starch base hard carbon: the weight of emulsion stirs than 1: 1, is spray-dried, spray The temperature of import is 180 DEG C when mist is dried, and outlet temperature is 100 DEG C.
Step 6:Product after spray drying is placed in tube furnace, with 5 DEG C/min speed under nitrogen protection 1150 DEG C of carbonization 3h are heated to, room temperature is cooled to and produces soft carbon/hard carbon core shell structure negative material.
Embodiment 2
Step 1:Weigh 2g ammonium chlorides to be added in 1000ml water, stir, it is beautiful then to add 100g Rice starch, continue to stir, obtain mixture;
Step 2:Mixture is put into vacuum drying chamber, 90 DEG C are dried in vacuo 1 hour, 150 DEG C of pre- carbonizations 1h, obtain pre- carbide;
Step 3:Pre- carbide is put into atmosphere furnace, is warming up under nitrogen protection with 5 DEG C/min speed 700 DEG C, constant temperature is cooled to room temperature after 2 hours, obtains starch base hard carbon.
Step 4:Petroleum residual oil and emulsifying agent, deionized water are made into emulsion, described emulsifying agent: stone Dregs of fat oil: the weight ratio of deionized water is 1: 50: 200;
Step 5:By starch base hard carbon: the weight of emulsion stirs than 2: 3, is spray-dried, spray The temperature of import is 180 DEG C when mist is dried, and outlet temperature is 100 DEG C;
Step 6:Product after spray drying is placed in tube furnace, with 5 DEG C/min speed under nitrogen protection 1250 DEG C of carbonization 3h are heated to, room temperature is cooled to and produces the soft carbon to be invented/hard carbon core shell structure negative pole material Material.
Embodiment 3
Step 1:Weigh 3g ammonium chlorides to be added in 1000ml water, stir, it is beautiful then to add 100g Rice starch, continue to stir, obtain mixture;
Step 2:Mixture is put into vacuum drying chamber, 90 DEG C are dried in vacuo 1 hour, 200 DEG C of pre- carbonizations 1h, obtain pre- carbide;
Step 3:Pre- carbide is put into atmosphere furnace, is warming up under nitrogen protection with 5 DEG C/min speed 1000 DEG C, constant temperature is cooled to room temperature after 2 hours, obtains starch base hard carbon.
Step 4:Petroleum residual oil and emulsifying agent, deionized water are made into emulsion, described emulsifying agent: coal It is residual oil: the weight ratio of deionized water is 1: 50: 300;
Step 5:By starch base hard carbon: the weight of emulsion stirs than 2: 3, is spray-dried, spray The temperature of import is 180 DEG C when mist is dried, and outlet temperature is 100 DEG C.
Step 6:Product after spray drying is placed in tube furnace, with 5 DEG C/min speed under nitrogen protection 1250 DEG C of carbonization 3h are heated to, room temperature is cooled to and produces soft carbon/hard carbon core shell structure negative material.
Embodiment 4
Step 1:Weigh 3g ammonium chlorides to be added in 1000ml water, stir, it is beautiful then to add 100g Rice starch, continue to stir, obtain mixture;
Step 2:Mixture is put into vacuum drying chamber, 90 DEG C are dried in vacuo 1 hour, 200 DEG C of pre- carbonizations 1h, obtain pre- carbide;
Step 3:Pre- carbide is put into atmosphere furnace, is warming up under nitrogen protection with 5 DEG C/min speed 1000 DEG C, constant temperature is cooled to room temperature after 2 hours, obtains starch base hard carbon.
Step 4:Petroleum residual oil and emulsifying agent, deionized water are made into emulsion, described emulsifying agent: coal It is residual oil: the weight ratio of deionized water is 1: 50: 300;
Step 5:By starch base hard carbon: emulsion stirs by weight 2: 3, is spray-dried, spray The temperature of import is 180 DEG C when mist is dried, and outlet temperature is 100 DEG C;
Step 6:Product after spray drying is placed in tube furnace, with 5 DEG C/min speed under nitrogen protection 1750 DEG C of carbonization 3h are heated to, room temperature is cooled to and produces soft carbon, hard carbon core shell structure negative material.
Embodiment 5
Step 1:Weigh 3g ammonium chlorides to be added in 1000ml water, stir, then add 100g horses Bell sweet potato starch, continue to stir, obtain mixture;
Step 2:Mixture is put into vacuum drying chamber, 90 DEG C are dried in vacuo 1 hour, 200 DEG C of pre- carbonizations 1h, obtain pre- carbide;
Step 3:Pre- carbide is put into atmosphere furnace, is warming up under nitrogen protection with 5 DEG C/min speed 1000 DEG C, constant temperature is cooled to room temperature after 2 hours, obtains starch base hard carbon;
Step 4:Petroleum residual oil and emulsifying agent, deionized water are made into emulsion, described emulsifying agent: coal It is residual oil: the weight ratio of deionized water is 1: 50: 300;
Step 5:By starch base hard carbon: the weight of emulsion stirs than 2: 3, is spray-dried, spray The temperature of import is 180 DEG C when mist is dried, and outlet temperature is 100 DEG C;
Step 6:Product after spray drying is placed in tube furnace, with 5 DEG C/min speed under nitrogen protection 1250 DEG C of carbonization 3h are heated to, room temperature is cooled to and produces soft carbon/hard carbon core shell structure negative material.
Embodiment 6
Step 1:Weigh 3g ammonium chlorides to be added in 1000ml water, stir, it is small then to add 100g Wheat starch, continue to stir, obtain mixture;
Step 2:Mixture is put into vacuum drying chamber, 90 DEG C are dried in vacuo 1 hour, 200 DEG C of pre- carbonizations 1h, obtain pre- carbide;
Step 3:Pre- carbide is put into atmosphere furnace, is warming up under nitrogen protection with 5 DEG C/min speed 1000 DEG C, constant temperature is cooled to room temperature after 2 hours, obtains starch base hard carbon.
Step 4:Petroleum residual oil and emulsifying agent, deionized water are made into emulsion, described emulsifying agent: coal It is residual oil: the weight ratio of deionized water is 1: 50: 300;
Step 5:By starch base hard carbon: the weight of emulsion stirs than 2: 3, is spray-dried, spray The temperature of import is 180 DEG C when mist is dried, and outlet temperature is 100 DEG C;
Step 6:Product after spray drying is placed in tube furnace, with 5 DEG C/min speed under nitrogen protection 1750 DEG C of carbonization 3h are heated to, room temperature is cooled to and produces soft carbon/hard carbon core shell structure negative material.
Embodiment 7
Step 1:Weigh 3g ammonium chlorides to be added in 1000ml water, stir, then add 100g kinds Sweet potato starch, continue to stir, obtain mixture;
Step 2:Mixture is put into vacuum drying chamber, 90 DEG C are dried in vacuo 1 hour, 170 DEG C of pre- carbonizations 1h, obtain pre- carbide;
Step 3:Pre- carbide is put into atmosphere furnace, is warming up under nitrogen protection with 5 DEG C/min speed 800 DEG C, constant temperature is cooled to room temperature after 7 hours, obtains starch base hard carbon.
Step 4:Petroleum residual oil and emulsifying agent, deionized water are made into emulsion, described emulsifying agent: coal It is residual oil: the weight ratio of deionized water is 1: 50: 250;
Step 5:By starch base hard carbon: the weight of emulsion stirs than 2: 3, is spray-dried, spray The temperature of import is 180 DEG C when mist is dried, and outlet temperature is 100 DEG C.
Step 6:Product after spray drying is placed in tube furnace, with 5 DEG C/min speed under nitrogen protection 1750 DEG C of carbonization 3h are heated to, room temperature is cooled to and produces soft carbon/hard carbon core shell structure negative material.
Embodiment 8
Step 1:Weigh 3g ammonium chlorides to be added in 1000ml water, stir, then add 100g Pueraria lobotas Powder, continue to stir, obtain mixture, stir;
Step 2:Mixture is put into vacuum drying chamber, 90 DEG C are dried in vacuo 1 hour, 200 DEG C of pre- carbonizations 1h, obtain pre- carbide;
Step 3:Pre- carbide is put into atmosphere furnace, is warming up under nitrogen protection with 5 DEG C/min speed 1000 DEG C, constant temperature is cooled to room temperature after 2 hours, obtains starch base hard carbon.
Step 4:Petroleum residual oil and emulsifying agent, deionized water are made into emulsion, described emulsifying agent: coal It is residual oil: the weight ratio of deionized water is 1: 50: 300;
Step 5:By starch base hard carbon: the weight of emulsion stirs than 2: 3, is spray-dried, spray The temperature of import is 180 DEG C when mist is dried, and outlet temperature is 100 DEG C.
Step 6:Product after spray drying is placed in tube furnace, with 5 DEG C/min speed under nitrogen protection 1950 DEG C of carbonization 3h are heated to, room temperature is cooled to and produces soft carbon/hard carbon core shell structure negative material.
The soft carbon prepared in the embodiment of the present invention, hard carbon core shell structure negative material are subjected to following half-cell Test:
Soft carbon prepared by the present invention, hard carbon core shell structure negative material, the N- containing 6~7% Kynoar Methyl pyrrolidone and 2% conductive black are well mixed, and are applied on copper foil, and the pole piece coated is put into temperature It is standby to be dried in vacuo 4 hours in 110 DEG C of vacuum drying chambers.
Simulated battery is assemblied in the German Braun glove box of applying argon gas and carried out, electrolyte 1M LiPF6+EC: DEC: DMC=1: 1: 1 (volume ratio), metal lithium sheet are to electrode, chemical property Test carried out on U.S. ArbinBT2000 type cell testers, charging/discharging voltage scope be 0.005 to 1.0V, charge-discharge velocity 0.1C, test result see the table below:
The soft carbon prepared in the embodiment of the present invention, hard carbon core shell structure negative material are carried out into following full battery to survey:
Referring to Fig. 1, soft carbon prepared by the embodiment of the present invention 6, hard carbon core shell structure negative material are as lithium battery Negative pole, cobalt acid lithium is molten as positive pole, 1M-LiPF6EC: DMC: EMC=1: 1: 1 (volume ratio) Liquid makees electrolyte assembling and helps battery, tests it in 670 weeks capability retentions of 1C charge and discharges 94.18%.

Claims (3)

1. the preparation method of a kind of soft carbon, hard carbon core shell structure negative material, it is characterised in that prepared using following Method:
(1), ammonium chloride is added to the water, stir to obtain aqueous ammonium chloride solution, then adds starch, after It is continuous to be uniformly mixing to obtain mixture;The mass concentration of described aqueous ammonium chloride solution is 0.5~30g/L, The weight of ammonium chloride and starch ratio is 1: 1~200;
(2), mixture is put into vacuum drying chamber, is dried in vacuo 1 hour, be carbonized 1h in advance, obtains pre- carbon Compound, vacuum drying temperature are 60 DEG C~100 DEG C, and pre- carburizing temperature is 100 DEG C~320 DEG C;
(3), pre- carbide is put into atmosphere furnace, and under inert gas shielding, temperature is 700~1000 DEG C, Heating rate is 5 DEG C of min, and constant temperature drops to room temperature after 0.1~10 hour, obtains starch base hard carbon;
(4) covering and emulsifying agent, deionized water, are made into emulsion, described emulsifying agent: covering: The weight ratio of deionized water is 1~5: 50: 100~449;
(5) it is, starch base hard carbon: emulsion=1~1: 100 starch base hard carbon and emulsion by weight ratio Stir, be spray-dried, the temperature of import is 180 DEG C~250 DEG C during spray drying, outlet Temperature is 100 DEG C~120 DEG C;
(6), the product after spray drying is placed in tube furnace, under inert gas shielding, heating carbonization, Carburizing temperature is 1000~2000 DEG C, and heating rate is 5 DEG C/min, and carbonization time is 1h~24h, Room temperature is cooled to get product;
Described covering uses any in asphalt, coal tar pitch, petroleum residual oil or coal measures residual oil Kind.
2. a kind of soft carbon, the preparation method of hard carbon core shell structure negative material as claimed in claim 1, it is special Sign is:The starch is farina, cornstarch, wheaten starch, sweet potato starch, kudzuvine root starch In one or more.
3. a kind of soft carbon, the preparation method of hard carbon core shell structure negative material as claimed in claim 1, it is special Sign is:Atmosphere in described atmosphere furnace is nitrogen or argon gas.
CN201610414923.0A 2016-06-14 2016-06-14 A kind of preparation method of soft carbon, hard carbon core shell structure negative material Pending CN107507964A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610414923.0A CN107507964A (en) 2016-06-14 2016-06-14 A kind of preparation method of soft carbon, hard carbon core shell structure negative material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610414923.0A CN107507964A (en) 2016-06-14 2016-06-14 A kind of preparation method of soft carbon, hard carbon core shell structure negative material

Publications (1)

Publication Number Publication Date
CN107507964A true CN107507964A (en) 2017-12-22

Family

ID=60678535

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610414923.0A Pending CN107507964A (en) 2016-06-14 2016-06-14 A kind of preparation method of soft carbon, hard carbon core shell structure negative material

Country Status (1)

Country Link
CN (1) CN107507964A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108682804A (en) * 2018-04-25 2018-10-19 福建翔丰华新能源材料有限公司 A kind of hard carbon cladding soft carbon is used as the preparation method of lithium ion battery negative material
CN108878774A (en) * 2018-06-26 2018-11-23 上海汉行科技有限公司 A kind of complex carbon material and its preparation method and application
CN109742399A (en) * 2018-12-18 2019-05-10 宁波容百新能源科技股份有限公司 A kind of anode material of lithium-ion battery and preparation method thereof
CN110877908A (en) * 2018-09-06 2020-03-13 天津大学 Preparation method of corn starch pyrolysis hard carbon electrode material
CN116731527A (en) * 2023-06-15 2023-09-12 浙江华宇钠电新能源科技有限公司 Asphalt mixture and application thereof in preparing sodium ion battery for vehicle
CN117384323A (en) * 2023-12-12 2024-01-12 成都锂能科技有限公司 Starch-based precursor material and preparation method and application thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101969122A (en) * 2010-09-14 2011-02-09 东莞市迈科新能源有限公司 Core-shell structured carbon for cathode material of lithium ion battery and preparation method thereof
CN102610795A (en) * 2011-01-20 2012-07-25 宁波宏远炭素工业有限公司 Preparation method of lithium ion battery carbon cathode material coating layer
CN102683661A (en) * 2012-06-01 2012-09-19 中国东方电气集团有限公司 Method for preparing hard carbon negative electrode materials of lithium ion battery

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101969122A (en) * 2010-09-14 2011-02-09 东莞市迈科新能源有限公司 Core-shell structured carbon for cathode material of lithium ion battery and preparation method thereof
CN102610795A (en) * 2011-01-20 2012-07-25 宁波宏远炭素工业有限公司 Preparation method of lithium ion battery carbon cathode material coating layer
CN102683661A (en) * 2012-06-01 2012-09-19 中国东方电气集团有限公司 Method for preparing hard carbon negative electrode materials of lithium ion battery

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108682804A (en) * 2018-04-25 2018-10-19 福建翔丰华新能源材料有限公司 A kind of hard carbon cladding soft carbon is used as the preparation method of lithium ion battery negative material
CN108682804B (en) * 2018-04-25 2021-05-25 深圳市翔丰华科技股份有限公司 Preparation method of lithium ion battery cathode material with hard carbon-coated soft carbon
CN108878774A (en) * 2018-06-26 2018-11-23 上海汉行科技有限公司 A kind of complex carbon material and its preparation method and application
CN108878774B (en) * 2018-06-26 2020-11-24 上海汉行科技有限公司 Composite carbon material and preparation method and application thereof
CN110877908A (en) * 2018-09-06 2020-03-13 天津大学 Preparation method of corn starch pyrolysis hard carbon electrode material
CN110877908B (en) * 2018-09-06 2022-07-01 天津大学 Preparation method of corn starch pyrolysis hard carbon electrode material
CN109742399A (en) * 2018-12-18 2019-05-10 宁波容百新能源科技股份有限公司 A kind of anode material of lithium-ion battery and preparation method thereof
CN116731527A (en) * 2023-06-15 2023-09-12 浙江华宇钠电新能源科技有限公司 Asphalt mixture and application thereof in preparing sodium ion battery for vehicle
CN116731527B (en) * 2023-06-15 2023-10-31 浙江华宇钠电新能源科技有限公司 Asphalt mixture and application thereof in preparing sodium ion battery for vehicle
CN117384323A (en) * 2023-12-12 2024-01-12 成都锂能科技有限公司 Starch-based precursor material and preparation method and application thereof
CN117384323B (en) * 2023-12-12 2024-03-08 成都锂能科技有限公司 Starch-based precursor material and preparation method and application thereof

Similar Documents

Publication Publication Date Title
CN107507964A (en) A kind of preparation method of soft carbon, hard carbon core shell structure negative material
CN104201339B (en) Anode and preparation method thereof and the application in lithium-sulfur cell
CN103887502B (en) A kind of Delanium lithium ion battery negative material and preparation method thereof
CN102368561B (en) Chargeable and dischargeable lithium sulfur cell
CN106486653A (en) A kind of liquid phase coating modified graphite cathode material and preparation method thereof
CN105098185A (en) Composite cathode material, preparation method thereof, lithium ion secondary battery negative plate and lithium ion secondary battery
CN103208618B (en) Carbon in lithium ion battery sulphur composite positive pole and preparation method thereof
CN104953186B (en) The preparation technology and negative pole of a kind of lithium ion battery mend lithium device
CN104393290A (en) Aluminum-ion battery using MoS2 as positive electrode material and preparation method of battery
Benmayza et al. Electrochemical and thermal studies of LiNi0. 8Co0. 15Al0. 015O2 under fluorinated electrolytes
CN103972508B (en) A kind of inorganic doping/coating modification native graphite, preparation method and application thereof
CN106960954A (en) A kind of preparation method and application of Prussian blue/graphene/sulphur composite
CN106159267A (en) A kind of preparation method of sulfur carbon composite
CN103682320A (en) Preparation method of sodium ion battery anode material
CN106025183A (en) Preparation method of carbon-based flexible film electrode for lithium ion batteries
CN104681782A (en) Lithium ion secondary battery composite positive material and preparation method thereof
CN102130359A (en) Lithium sulfur battery and preparation method thereof
CN106450474A (en) Gelled polymer electrolyte membrane and preparation method thereof
CN108258209A (en) A kind of carbide/carbon nano tube/graphene carries sulphur composite material and preparation method and application
CN103400993B (en) Battery anode and lithium ion battery
CN107658461B (en) Method for preparing ferric fluoride/carbon composite material by taking organic iron compound as raw material
CN106486641A (en) A kind of lithium ion battery modified artificial graphite cathode and preparation method thereof
CN105489882A (en) Positive pole piece, preparation method thereof and lithium ion battery
CN104466182A (en) Nitrogen-doped nanocarbon coated/oxidized modified graphite composite material and preparation method thereof
CN106532046A (en) Lithium-doped graphite 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
RJ01 Rejection of invention patent application after publication

Application publication date: 20171222