CN108011090A - Prepare method, the battery cathode prepared by this method and the lithium ion battery of negative electrode of lithium ion battery - Google Patents

Prepare method, the battery cathode prepared by this method and the lithium ion battery of negative electrode of lithium ion battery Download PDF

Info

Publication number
CN108011090A
CN108011090A CN201711256708.3A CN201711256708A CN108011090A CN 108011090 A CN108011090 A CN 108011090A CN 201711256708 A CN201711256708 A CN 201711256708A CN 108011090 A CN108011090 A CN 108011090A
Authority
CN
China
Prior art keywords
copper powder
carried out
powder
reduction treatment
oxidation
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.)
Granted
Application number
CN201711256708.3A
Other languages
Chinese (zh)
Other versions
CN108011090B (en
Inventor
苏彤
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.)
SHANXI CHANGHAN NEW ENERGY TECHNOLOGY Co.,Ltd.
Original Assignee
Shenzhen Wanjia Interactive 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 Shenzhen Wanjia Interactive Technology Co Ltd filed Critical Shenzhen Wanjia Interactive Technology Co Ltd
Priority to CN201711256708.3A priority Critical patent/CN108011090B/en
Publication of CN108011090A publication Critical patent/CN108011090A/en
Application granted granted Critical
Publication of CN108011090B publication Critical patent/CN108011090B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

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
    • 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
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/134Electrodes based on metals, Si or alloys
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • H01M4/386Silicon or alloys based on silicon
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624Electric conductive fillers
    • H01M4/626Metals
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Abstract

The present invention provides the method for preparing Porous Cu silicon lithium ion battery cathode, including:The different copper powder of particle diameter and silica flour are chosen as raw material;First oxidation processes are carried out to copper powder;First reduction treatment is carried out to the copper powder after oxidation, to reduce CuO particle surfaces so as to form the porous steel structure of Lacking oxygen type, between 200nm 500nm, porosity is 20 35% in the aperture of its mesoporous;Second oxidation processes are carried out to copper powder;Second reduction treatment is carried out to the copper powder after oxidation, to reduce CuO particle surfaces so as to form the porous steel structure of Lacking oxygen type, between 300nm 600nm, porosity is 25 45% in the aperture of its mesoporous;Copper powder after reduction is mixed with silica flour, then carries out ball milling, wherein the mass ratio of the copper powder and silica flour after reduction is 4:1‑1:1, Ball-milling Time control is 10h 15h, so as to obtain the powder of alloying;Obtained alloying powder is subjected to sieving processing;Then the 3rd reduction treatment is carried out to the alloying powder after sieving.Battery cathode good cycle, after multi-turn circulation, capacity retention ratio is high.

Description

Prepare method, the battery cathode prepared by this method and the lithium of negative electrode of lithium ion battery Ion battery
Technical field
The present invention relates to a kind of negative electrode of lithium ion battery preparation method and negative electrode of lithium ion battery, prepared by more particularly to one kind The method and Porous Cu silicon lithium ion battery cathode of Porous Cu silicon lithium ion battery cathode.
Background technology
Current energy and environment crisis getting worse, the harm brought is drastically consumed to solve non-renewable energy resources, for The exploitation of new energy becomes more and more important.Lithium ion battery is because have high energy density, memory-less effect, advantages of environment protection As new energy storage device.Lithium ion battery is generally using activated carbon etc. as negative material, because activated carbon and other carbon materials Allotrope is expected because cheap, and performance is stablized, and commercial applications, but carbon material theoretical capacity is only 372mAh/g, it is difficult to meet the demand of the power-equipment of rapid development.For the energy density of further lifting lithium ion battery, bear The selection of pole material and structure design are most important.For cupric oxide because cheap, theoretical capacity is higher to be subject to research field Pay much attention to.But the poorly conductive of cupric oxide becomes major defect.It is more at present using compound and bag to solve conductivity problems The mode covered improves the electric conductivity and stability for aoxidizing copper-based anode.Silicium cathode material is because theoretical capacity is up to 4200mAh/g As the research emphasis of current enterprise and research institutions, but likewise, the poorly conductive of silicon and its coefficient of expansion height so that silicon It is difficult to separately as commercial li-ion cell negative electrode material, while expansion/contractive effect of silicon easily leads to the dusting of material and takes off The shortcomings that falling, ultimately resulting in sharp-decay and the short circuit of performance.
The information for being disclosed in the background section is merely intended to understanding of the increase to the general background of the present invention, without answering It has been the prior art well known to persons skilled in the art when being considered as recognizing or implying the information structure in any form.
The content of the invention
It is more it is an object of the invention to provide preparing the method for Porous Cu silicon lithium ion battery cathode, being prepared by this method Hole copper silion cell anode and lithium ion battery, so that the shortcomings that overcoming the prior art.
To achieve the above object, the present invention provides a kind of method for preparing Porous Cu silicon lithium ion battery cathode, it is special Sign is:Method includes:The different copper powder of particle diameter and silica flour are chosen as raw material;First oxidation processes are carried out to copper powder;It is right Copper powder after oxidation carries out the first reduction treatment, and the porous steel structure of Lacking oxygen type is formed to reduce CuO particle surfaces, wherein The aperture in hole is between 200nm-500nm, porosity 20-35%;Second oxidation processes are carried out to copper powder;To the copper after oxidation Powder carries out the second reduction treatment, and to reduce CuO particle surfaces so as to form the porous steel structure of Lacking oxygen type, the aperture of its mesoporous exists Between 300nm-600nm, porosity 25-45%;Copper powder after reduction is mixed with silica flour, then carries out ball milling, its The mass ratio of copper powder and silica flour after middle reduction is 4:1-1:1, Ball-milling Time control is 10h-15h, so as to obtain alloying Powder;Obtained alloying powder is subjected to sieving processing;Then the 3rd is carried out to the alloying powder after sieving and goes back original place Reason.
Preferably, in above-mentioned technical proposal, copper powder size 5-10um, silica flour particle diameter is 100-150nm.
Preferably, in above-mentioned technical proposal, carrying out the first oxidation processes to copper powder is specially:In 500-600 DEG C of condition Under, to the oxidation processes of copper powder progress 2-3h.
Preferably, in above-mentioned technical proposal, carrying out the first reduction treatment to the copper powder after oxidation is specially:In hydrogen gas Under conditions of atmosphere, temperature are 500-600 DEG C, the reduction treatment of 2-3h is carried out to copper powder.
Preferably, in above-mentioned technical proposal, carrying out the second oxidation processes to copper powder is specially:In 550-650 DEG C of condition Under, to the oxidation processes of copper powder progress 2-3h.
Preferably, in above-mentioned technical proposal, carrying out the second reduction treatment to the copper powder after oxidation is specially:In hydrogen gas Under conditions of atmosphere, temperature are 550-650 DEG C, the reduction treatment of 2-3h is carried out to copper powder.
Preferably, in above-mentioned technical proposal, method further includes:After the 3rd reduction treatment is carried out to alloying powder, The alloying powder after the 3rd reduction is corroded using dust technology.
Present invention also offers a kind of Porous Cu silicon lithium ion battery cathode, it is characterised in that:Porous Cu silicon lithium ion electricity Pond anode is prepared by preceding method.
Present invention also offers a kind of lithium ion battery, it is characterised in that:Lithium ion battery includes Porous Cu silicon lithium ion Battery cathode, Porous Cu silicon lithium ion battery cathode are prepared by preceding method.
Compared with prior art, the present invention has the advantages that:
The defects of to solve above-mentioned Cu oxide and silicon-based anode.The present invention is using simple oxidation-reduction process in copper Particle surface formed loose structure, and by obtained Porous Cu presoma and nanoscale silicon powder progress ball milling prepare it is porous Copper-silicon lithium electricity advanced composite material (ACM), further by after ball milling advanced composite material (ACM) carry out the pore-creating of dust technology anticaustic and Reduction treatment under hydrogen shield atmosphere, the copper corrosion of part is fallen and reduces copper oxide particle to form hierarchical porous structure electricity Pole.It is advantageous that:1st, to original copper powders using redox port-creating method twice, first time redox cause it is smaller, compared with Shallow hole, second of redox cause hole becomes larger to deepen, and are conducive to subsequently compound with Si powder;2nd, the copper of loose structure Grain can form silicon embedded type structure, buffer volumes expansion effect in mechanical milling process;3rd, porous steel structure has excellent conduction Property can effectively improve the electronic conduction ability at silicon-copper interface, further improve chemical property;4th, porous steel structure is conducive to carry The load capacity of high activity silicon, further improves specific capacity;5th, selection raw material is rich in minerals, and preparation method is simple.
Brief description of the drawings
Fig. 1 is the SEM figures of 1 Porous Cu according to an embodiment of the invention.
Embodiment
Explicitly indicated that unless otherwise other, otherwise in entire disclosure and claims, term " comprising " or its change Change such as "comprising" or " including " etc. and will be understood to comprise stated element or part, and do not exclude other members Part or other parts.The raw material of the present invention can be purchased from chemical reagent shop, and heat treatment can be in conventional heat-treatment furnace Middle progress.The porosity of the present invention is defined as " pore area and the ratio of total surface area ".
Embodiment 1
The different copper powder of particle diameter and silica flour are chosen as raw material;First oxidation processes are carried out to copper powder;After oxidation Copper powder carries out the first reduction treatment, and the porous steel structure of Lacking oxygen type, the aperture of its mesoporous are formed to reduce CuO particle surfaces In 200nm, porosity 20%;Second oxidation processes are carried out to copper powder;Second reduction treatment is carried out to the copper powder after oxidation, with Reduction CuO particle surfaces are so as to form the porous steel structure of Lacking oxygen type, and between 300nm, porosity is in the aperture of its mesoporous 25%;Copper powder after reduction is mixed with silica flour, then carries out ball milling, wherein the mass ratio of the copper powder and silica flour after reduction For 4:1, Ball-milling Time control is 10h, so as to obtain the powder of alloying;Obtained alloying powder is carried out at sieving Reason;Then the 3rd reduction treatment is carried out to the alloying powder after sieving.Preferably, in above-mentioned technical proposal, copper powder size is 5um, silica flour particle diameter are 100nm.Carrying out the first oxidation processes to copper powder is specially:Under conditions of 500 DEG C, 2h is carried out to copper powder Oxidation processes.Carrying out the first reduction treatment to the copper powder after oxidation is specially:In hydrogen atmosphere, the condition that temperature is 500 DEG C Under, the reduction treatment of 2h is carried out to copper powder.Carrying out the second oxidation processes to copper powder is specially:Under conditions of 550 DEG C, to copper powder Carry out the oxidation processes of 2h.Carrying out the second reduction treatment to the copper powder after oxidation is specially:It it is 550 DEG C in hydrogen atmosphere, temperature Under conditions of, the reduction treatment of 2h is carried out to copper powder.Method further includes:To alloying powder carry out the 3rd reduction treatment it Afterwards, the alloying powder after the 3rd reduction is corroded using dust technology.
Embodiment 2
The different copper powder of particle diameter and silica flour are chosen as raw material;First oxidation processes are carried out to copper powder;After oxidation Copper powder carries out the first reduction treatment, and the porous steel structure of Lacking oxygen type, the aperture of its mesoporous are formed to reduce CuO particle surfaces In 500nm, porosity 35%;Second oxidation processes are carried out to copper powder;Second reduction treatment is carried out to the copper powder after oxidation, with Reduction CuO particle surfaces are so as to form the porous steel structure of Lacking oxygen type, and between 600nm, porosity is in the aperture of its mesoporous 45%;Copper powder after reduction is mixed with silica flour, then carries out ball milling, wherein the mass ratio of the copper powder and silica flour after reduction For 1:1, Ball-milling Time control is 15h, so as to obtain the powder of alloying;Obtained alloying powder is carried out at sieving Reason;Then the 3rd reduction treatment is carried out to the alloying powder after sieving.Preferably, in above-mentioned technical proposal, copper powder size is 10um, silica flour particle diameter are 150nm.Carrying out the first oxidation processes to copper powder is specially:Under conditions of 600 DEG C, copper powder is carried out The oxidation processes of 3h.Carrying out the first reduction treatment to the copper powder after oxidation is specially:In hydrogen atmosphere, the bar that temperature is 600 DEG C Under part, the reduction treatment of 3h is carried out to copper powder.Carrying out the second oxidation processes to copper powder is specially:Under conditions of 650 DEG C, to copper Powder carries out the oxidation processes of 3h.Carrying out the second reduction treatment to the copper powder after oxidation is specially:In hydrogen atmosphere, temperature 650 Under conditions of DEG C, the reduction treatment of 3h is carried out to copper powder.Method further includes:To alloying powder carry out the 3rd reduction treatment it Afterwards, the alloying powder after the 3rd reduction is corroded using dust technology.
Embodiment 3
The different copper powder of particle diameter and silica flour are chosen as raw material;First oxidation processes are carried out to copper powder;After oxidation Copper powder carries out the first reduction treatment, and the porous steel structure of Lacking oxygen type, the aperture of its mesoporous are formed to reduce CuO particle surfaces In 350nm, porosity 30%;Second oxidation processes are carried out to copper powder;Second reduction treatment is carried out to the copper powder after oxidation, with Reduction CuO particle surfaces are so as to form the porous steel structure of Lacking oxygen type, and the aperture of its mesoporous is in 500nm, porosity 40%;Will Copper powder after reduction is mixed with silica flour, then carries out ball milling, wherein the mass ratio of the copper powder and silica flour after reduction is 2:1, Ball-milling Time control is 12h, so as to obtain the powder of alloying;Obtained alloying powder is subjected to sieving processing;Then 3rd reduction treatment is carried out to the alloying powder after sieving.Preferably, in above-mentioned technical proposal, copper powder size 7um, silica flour Particle diameter is 120nm.Carrying out the first oxidation processes to copper powder is specially:Under conditions of 550 DEG C, the oxidation of 2.5h is carried out to copper powder Processing.Carrying out the first reduction treatment to the copper powder after oxidation is specially:Under conditions of hydrogen atmosphere, temperature are 550 DEG C, to copper Powder carries out the reduction treatment of 2.5h.Carrying out the second oxidation processes to copper powder is specially:Under conditions of 580 DEG C, copper powder is carried out The oxidation processes of 2.5h.Carrying out the second reduction treatment to the copper powder after oxidation is specially:It it is 580 DEG C in hydrogen atmosphere, temperature Under the conditions of, the reduction treatment of 2.5h is carried out to copper powder.Method further includes:To alloying powder carry out the 3rd reduction treatment it Afterwards, the alloying powder after the 3rd reduction is corroded using dust technology.
Embodiment 4
The different copper powder of particle diameter and silica flour are chosen as raw material;First oxidation processes are carried out to copper powder;After oxidation Copper powder carries out the first reduction treatment, and the porous steel structure of Lacking oxygen type, the aperture of its mesoporous are formed to reduce CuO particle surfaces In 300nm, porosity 25%;Without the second redox;Carrying out the first oxidation processes to copper powder is specially:At 750 DEG C Under conditions of, to the oxidation processes of copper powder progress 10h.Carrying out the first reduction treatment to the copper powder after oxidation is specially:In hydrogen Under conditions of atmosphere, temperature are 700 DEG C, the reduction treatment of 10h is carried out to copper powder.Remaining condition, step and 1 phase of parameter embodiment Together.
Embodiment 5
The different copper powder of particle diameter and silica flour are chosen as raw material;First oxidation processes are carried out to copper powder;After oxidation Copper powder carries out the first reduction treatment, and the porous steel structure of Lacking oxygen type, the aperture of its mesoporous are formed to reduce CuO particle surfaces In 100nm, porosity 15%;Second oxidation processes are carried out to copper powder;Second reduction treatment is carried out to the copper powder after oxidation, with Reduction CuO particle surfaces are so as to form the porous steel structure of Lacking oxygen type, and the aperture of its mesoporous is in 200nm, porosity 20%;It is right Copper powder carries out the first oxidation processes:Under conditions of 500 DEG C, the oxidation processes of 1h are carried out to copper powder.After oxidation Copper powder carries out the first reduction treatment:Under conditions of hydrogen atmosphere, temperature are 500 DEG C, the reduction of 1h is carried out to copper powder Processing.Carrying out the second oxidation processes to copper powder is specially:Under conditions of 550 DEG C, the oxidation processes of 1h are carried out to copper powder.To oxygen Copper powder after change carries out the second reduction treatment:Under conditions of hydrogen atmosphere, temperature are 550 DEG C, 1h is carried out to copper powder Reduction treatment.Remaining condition, step are identical with parameter embodiment 1.
Embodiment 6
The different copper powder of particle diameter and silica flour are chosen as raw material;First oxidation processes are carried out to copper powder;After oxidation Copper powder carries out the first reduction treatment, and the porous steel structure of Lacking oxygen type, the aperture of its mesoporous are formed to reduce CuO particle surfaces In 100nm, porosity 15%;Second oxidation processes are carried out to copper powder;Second reduction treatment is carried out to the copper powder after oxidation, with Reduction CuO particle surfaces are so as to form the porous steel structure of Lacking oxygen type, and the aperture of its mesoporous is in 350nm, porosity 30%;It is right Copper powder carries out the first oxidation processes:Under conditions of 500 DEG C, the oxidation processes of 1h are carried out to copper powder.After oxidation Copper powder carries out the first reduction treatment:Under conditions of hydrogen atmosphere, temperature are 500 DEG C, the reduction of 1h is carried out to copper powder Processing.Carrying out the second oxidation processes to copper powder is specially:Under conditions of 700 DEG C, the oxidation processes of 3h are carried out to copper powder.To oxygen Copper powder after change carries out the second reduction treatment:Under conditions of hydrogen atmosphere, temperature are 700 DEG C, 3h is carried out to copper powder Reduction treatment.Remaining condition, step are identical with parameter embodiment 1.
Embodiment 7
The different copper powder of particle diameter and silica flour are chosen as raw material;First oxidation processes are carried out to copper powder;After oxidation Copper powder carries out the first reduction treatment, and the porous steel structure of Lacking oxygen type, the aperture of its mesoporous are formed to reduce CuO particle surfaces In 200nm, porosity 25%;Second oxidation processes are carried out to copper powder;Second reduction treatment is carried out to the copper powder after oxidation, with Reduction CuO particle surfaces are so as to form the porous steel structure of Lacking oxygen type, and the aperture of its mesoporous is in 250nm, porosity 35%;It is right Copper powder carries out the first oxidation processes:Under conditions of 500 DEG C, the oxidation processes of 2h are carried out to copper powder.After oxidation Copper powder carries out the first reduction treatment:Under conditions of hydrogen atmosphere, temperature are 500 DEG C, the reduction of 2h is carried out to copper powder Processing.Carrying out the second oxidation processes to copper powder is specially:Under conditions of 550 DEG C, the oxidation processes of 1.5h are carried out to copper powder.It is right Copper powder after oxidation carries out the second reduction treatment:Under conditions of hydrogen atmosphere, temperature are 550 DEG C, copper powder is carried out The reduction treatment of 1.5h.Remaining condition, step are identical with parameter embodiment 1.
Embodiment 8
The different copper powder of particle diameter and silica flour are chosen as raw material;First oxidation processes are carried out to copper powder;After oxidation Copper powder carries out the first reduction treatment, and the porous steel structure of Lacking oxygen type, the aperture of its mesoporous are formed to reduce CuO particle surfaces In 600nm, porosity 40%;Second oxidation processes are carried out to copper powder;Second reduction treatment is carried out to the copper powder after oxidation, with Reduction CuO particle surfaces are so as to form the porous steel structure of Lacking oxygen type, and the aperture of its mesoporous is in 800nm, porosity 50%;It is right Copper powder carries out the first oxidation processes:Under conditions of 900 DEG C, the oxidation processes of 20h are carried out to copper powder.After oxidation Copper powder carries out the first reduction treatment:Under conditions of hydrogen atmosphere, temperature are 900 DEG C, the reduction of 25h is carried out to copper powder Processing.Carrying out the second oxidation processes to copper powder is specially:Under conditions of 8500 DEG C, the oxidation processes of 10h are carried out to copper powder.It is right Copper powder after oxidation carries out the second reduction treatment:Under conditions of hydrogen atmosphere, temperature are 900 DEG C, copper powder is carried out The reduction treatment of 10h.Remaining condition, step are identical with parameter embodiment 1.
Embodiment 9
The mass ratio of copper powder and silica flour after reduction is 5:1, remaining condition, step are identical with parameter embodiment 1.
Embodiment 10
The mass ratio of copper powder and silica flour after reduction is 2:1, remaining condition, step are identical with parameter embodiment 1.
Embodiment 11
Ball-milling Time control is 5h, remaining condition, step are identical with parameter embodiment 1.
Embodiment 12
Obtained alloying powder is subjected to sieving processing;Then directly using dust technology to the alloying after sieving Powder is corroded, without the 3rd reduction treatment.Remaining condition, step are identical with parameter embodiment 1.
Embodiment 13
Copper powder size is 4um, remaining condition, step are identical with parameter embodiment 1.
Embodiment 14
Copper powder size is 12um, remaining condition, step are identical with parameter embodiment 1.
Embodiment 15
Silica flour particle diameter is 80nm, remaining condition, step are identical with parameter embodiment 1.
Embodiment 16
Silica flour particle diameter is 170nm, remaining condition, step are identical with parameter embodiment 1.
Embodiment 17
After the 3rd reduction treatment is carried out to alloying powder, dust technology is not used to the alloy after the 3rd reduction Change powder to be corroded, remaining condition, step are identical with parameter embodiment 1.
Battery cathode is assembled into using the material prepared by embodiment 1-17, tests the battery capacity of battery, tests battery The method of capacity is method well known in the art, unit mAh/g.Test content includes first circle capacity, capacity after stablizing, 50 circles Capacity after capacity and 300 circles circulate after circulation.For the ease of comparing, as a result all on the basis of the first circle capacity of embodiment 1 into Row normalization.
Table 1
It is foregoing to the present invention specific exemplary embodiment description be in order to illustrate and illustration purpose.These descriptions It is not wishing to limit the invention to disclosed precise forms, and it will be apparent that according to the above instruction, can be much changed And change.The purpose of selecting and describing the exemplary embodiment is that explain that the certain principles of the present invention and its reality should With so that those skilled in the art can realize and utilize the present invention a variety of exemplaries and Various chooses and changes.The scope of the present invention is intended to be limited by claims and its equivalents.

Claims (9)

  1. A kind of 1. method for preparing Porous Cu silicon lithium ion battery cathode, it is characterised in that:The described method includes:
    The different copper powder of particle diameter and silica flour are chosen as raw material;
    First oxidation processes are carried out to the copper powder;
    First reduction treatment is carried out to the copper powder after oxidation, Lacking oxygen type Porous Cu knot is formed to reduce CuO particle surfaces Structure, wherein the aperture in the hole is between 200nm-500nm, porosity 20-35%;
    Second oxidation processes are carried out to the copper powder;
    Second reduction treatment is carried out to the copper powder after oxidation, Lacking oxygen type Porous Cu knot is formed to reduce CuO particle surfaces Structure, wherein the aperture in the hole is between 300nm-600nm, porosity 25-45%;
    Copper powder after reduction is mixed with the silica flour, then carries out ball milling, wherein copper powder and silica flour after the reduction Mass ratio be 4:1-1:1, Ball-milling Time control is 10h-15h, so as to obtain the powder of alloying;
    Obtained alloying powder is subjected to sieving processing;
    Then the 3rd reduction treatment is carried out to the alloying powder after sieving.
  2. 2. the method as described in claim 1, it is characterised in that:The copper powder size is 5-10um, and the silica flour particle diameter is 100-150nm。
  3. 3. the method as described in claim 1, it is characterised in that:Carrying out the first oxidation processes to the copper powder is specially: Under conditions of 500-600 DEG C, the oxidation processes of 2-3h are carried out to the copper powder.
  4. 4. the method as described in claim 1, it is characterised in that:Carrying out the first reduction treatment to the copper powder after oxidation is specially: Under conditions of hydrogen atmosphere, temperature are 500-600 DEG C, the reduction treatment of 2-3h is carried out to the copper powder.
  5. 5. the method as described in claim 1, it is characterised in that:Carrying out the second oxidation processes to the copper powder is specially: Under conditions of 550-650 DEG C, the oxidation processes of 2-3h are carried out to the copper powder.
  6. 6. the method as described in claim 1, it is characterised in that:Carrying out the second reduction treatment to the copper powder after oxidation is specially: Under conditions of hydrogen atmosphere, temperature are 550-650 DEG C, the reduction treatment of 2-3h is carried out to the copper powder.
  7. 7. the method as described in claim 1, it is characterised in that:The method further includes:Carried out to the alloying powder After 3rd reduction treatment, the alloying powder after the 3rd reduction is corroded using dust technology.
  8. A kind of 8. Porous Cu silicon lithium ion battery cathode, it is characterised in that:The Porous Cu silicon lithium ion battery cathode is to pass through Prepared by the method as described in one of claim 1-7.
  9. A kind of 9. lithium ion battery, it is characterised in that:The lithium ion battery includes Porous Cu silicon lithium ion battery cathode, described Porous Cu silicon lithium ion battery cathode is being prepared by the method as described in one of claim 1-7.
CN201711256708.3A 2017-12-03 2017-12-03 Method for preparing lithium ion battery cathode, battery cathode prepared by method and lithium ion battery Active CN108011090B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711256708.3A CN108011090B (en) 2017-12-03 2017-12-03 Method for preparing lithium ion battery cathode, battery cathode prepared by method and lithium ion battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711256708.3A CN108011090B (en) 2017-12-03 2017-12-03 Method for preparing lithium ion battery cathode, battery cathode prepared by method and lithium ion battery

Publications (2)

Publication Number Publication Date
CN108011090A true CN108011090A (en) 2018-05-08
CN108011090B CN108011090B (en) 2020-06-05

Family

ID=62056106

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711256708.3A Active CN108011090B (en) 2017-12-03 2017-12-03 Method for preparing lithium ion battery cathode, battery cathode prepared by method and lithium ion battery

Country Status (1)

Country Link
CN (1) CN108011090B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110635103A (en) * 2019-08-29 2019-12-31 天津工业大学 Flexible nano porous metal oxide cathode for secondary battery and preparation method thereof

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102324501A (en) * 2011-09-09 2012-01-18 中国科学院过程工程研究所 Silicon-based cathode composite material for lithium ion battery and preparation method thereof
CN103247792A (en) * 2013-03-22 2013-08-14 济南大学 Nano porous silicon alloy material and preparation method thereof
CN103311523A (en) * 2013-06-04 2013-09-18 清华大学深圳研究生院 Silicon-carbon composite material with nano micropores and preparation method as well as application thereof
US20140248543A1 (en) * 2011-10-05 2014-09-04 Oned Material Llc Silicon Nanostructure Active Materials for Lithium Ion Batteries and Processes, Compositions, Components and Devices Related Thereto
CN105047892A (en) * 2015-08-03 2015-11-11 中国科学院宁波材料技术与工程研究所 Porous silicon material, and preparation method and application thereof
CN105506336A (en) * 2015-12-23 2016-04-20 哈尔滨工业大学 Method for preparing porous metal through high-temperature oxidation and reduction

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102324501A (en) * 2011-09-09 2012-01-18 中国科学院过程工程研究所 Silicon-based cathode composite material for lithium ion battery and preparation method thereof
US20140248543A1 (en) * 2011-10-05 2014-09-04 Oned Material Llc Silicon Nanostructure Active Materials for Lithium Ion Batteries and Processes, Compositions, Components and Devices Related Thereto
CN103247792A (en) * 2013-03-22 2013-08-14 济南大学 Nano porous silicon alloy material and preparation method thereof
CN103311523A (en) * 2013-06-04 2013-09-18 清华大学深圳研究生院 Silicon-carbon composite material with nano micropores and preparation method as well as application thereof
CN105047892A (en) * 2015-08-03 2015-11-11 中国科学院宁波材料技术与工程研究所 Porous silicon material, and preparation method and application thereof
CN105506336A (en) * 2015-12-23 2016-04-20 哈尔滨工业大学 Method for preparing porous metal through high-temperature oxidation and reduction

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
左朋建等: ""锂离子电池硅铜复合负极材料的研究"", 《第十三次全国电化学会议》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110635103A (en) * 2019-08-29 2019-12-31 天津工业大学 Flexible nano porous metal oxide cathode for secondary battery and preparation method thereof

Also Published As

Publication number Publication date
CN108011090B (en) 2020-06-05

Similar Documents

Publication Publication Date Title
Zhang et al. High performance of electrochemical lithium storage batteries: ZnO-based nanomaterials for lithium-ion and lithium–sulfur batteries
Cheng et al. CeO2 decorated graphene as separator modification material for capture and boost conversion of polysulfide in lithium-sulfur batteries
Zhang et al. Fabrication of Cu2O‐based materials for lithium‐ion batteries
CN103022437B (en) Silicon alloy and graphene composite material and preparation method thereof
Rahman et al. Lithium germanate (Li2GeO3): a high‐performance anode material for lithium‐ion batteries
KR20140031953A (en) Three-dimensional porous silicon-based composite negative electrode material of lithium ion cell and preparation method thereof
CN103346307B (en) A kind of lithium ion battery negative material and preparation method thereof
CN102082262A (en) Method for preparing nano-carbon coated lithium battery anode material
CN103326023A (en) High-performance lithium ion battery silicon-carbon cathode material and preparation method thereof
CN103236528B (en) A kind of germanium carbon graphite alkene composite material and its preparation method and application
CN106784752A (en) Lithium ion battery loose structure Si/Cu combination electrodes and its manufacture method
Wang et al. Post‐lithium‐ion battery era: Recent advances in rechargeable potassium‐ion batteries
CN104538585B (en) Hollow porous micron order silicon ball, silicon based anode material and preparation method of lithium ion battery
Wang et al. A rational design to buffer volume expansion of CoSn intermetallic in lithium and sodium storage: Multicore-shell versus monocore-shell
CN107317002B (en) A kind of prussian blue comprehensive silicon negative electrode material and preparation method thereof
CN106159277A (en) Porous current collector and preparation method thereof
CN107256946A (en) Battery
CN107579233A (en) A kind of metal-doped silicon oxide molecular sieve/sulphur carbon complex and its preparation method and application
CN107528063A (en) A kind of preparation method and applications of core shell structure silicon/carbon material of cornstarch porous carbon encapsulation
JP2010161076A (en) Anode material for lithium ion secondary battery, and fabricating method thereof
CN104715931A (en) Energy storage element and super capacitor element
Qi et al. MCo2O4 (M= Co, Mn, Ni, Zn) nanosheet arrays constructed by two-dimension metal-organic frameworks as binder-free electrodes for lithium-ion batteries
CN102163711A (en) Method for preparing lithium ion battery negative material by utilizing mesoporous carbon supported nano particles
CN107958992A (en) Porous binary NiMn oxide lithium cell negative pole materials and preparation method thereof
Liang et al. Three-dimensionally ordered macro/mesoporous TiO2 matrix to immobilize sulfur for high performance lithium/sulfur batteries

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
TA01 Transfer of patent application right

Effective date of registration: 20200414

Address after: 030000 second floor, No.98 Tanghuai Road, Tanghuai Park, Shanxi comprehensive reform demonstration zone, Taiyuan City, Shanxi Province

Applicant after: SHANXI CHANGHAN NEW ENERGY TECHNOLOGY Co.,Ltd.

Address before: 518101 23 Xin'an Lake Garden, Xin'an Street, Baoan District, Shenzhen City, Guangdong Province 203

Applicant before: SHENZHEN WANJIA INTERDYNAMIC TECHNOLOGY Co.,Ltd.

TA01 Transfer of patent application right
GR01 Patent grant
GR01 Patent grant