CN107740099A - A kind of chlorine salt corrosion agent for being used to prepare micropore aluminium foil - Google Patents

A kind of chlorine salt corrosion agent for being used to prepare micropore aluminium foil Download PDF

Info

Publication number
CN107740099A
CN107740099A CN201710930884.4A CN201710930884A CN107740099A CN 107740099 A CN107740099 A CN 107740099A CN 201710930884 A CN201710930884 A CN 201710930884A CN 107740099 A CN107740099 A CN 107740099A
Authority
CN
China
Prior art keywords
aluminium foil
salt corrosion
corrosion agent
chlorine salt
battery
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.)
Withdrawn
Application number
CN201710930884.4A
Other languages
Chinese (zh)
Inventor
王宥宏
刘忆恩
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 Voight Alzheimer New Material Polytron Technologies Inc
Original Assignee
Shanxi Voight Alzheimer New Material Polytron Technologies Inc
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 Shanxi Voight Alzheimer New Material Polytron Technologies Inc filed Critical Shanxi Voight Alzheimer New Material Polytron Technologies Inc
Priority to CN201710930884.4A priority Critical patent/CN107740099A/en
Publication of CN107740099A publication Critical patent/CN107740099A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23FNON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
    • C23F1/00Etching metallic material by chemical means
    • C23F1/10Etching compositions
    • C23F1/14Aqueous compositions
    • 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
    • H01M4/64Carriers or collectors
    • H01M4/70Carriers or collectors characterised by shape or form
    • H01M4/72Grids
    • H01M4/74Meshes or woven material; Expanded metal
    • H01M4/742Meshes or woven material; Expanded metal perforated material
    • 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)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Electrochemistry (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Cell Electrode Carriers And Collectors (AREA)
  • Secondary Cells (AREA)

Abstract

A kind of chlorine salt corrosion agent for being used to prepare micropore aluminium foil of the present invention, more particularly to a kind of corrosive agent of high-performance lithium cell positive material, overcome the deficiencies in the prior art of the present invention, purpose is to provide a kind of corrosive agent of high-performance lithium battery plus plate current-collecting body material, in order to solve the above technical problems, the technical solution adopted in the present invention is:A kind of chlorine salt corrosion agent for being used to prepare micropore aluminium foil, described chlorine salt corrosion agent are salting liquid, and described chlorine salt corrosion agent comprises only the salting liquid of chlorion, Cl for anionMolar concentration be 0.1 3mol/L, cation contains the Fe that molar concentration is 0.1 3mol/L3+And Cu2+, the present invention can be widely applied in battery aluminium foil manufacturing field.

Description

A kind of chlorine salt corrosion agent for being used to prepare micropore aluminium foil
Technical field
A kind of a kind of chlorine salt corrosion agent for being used to prepare micropore aluminium foil of the present invention, and in particular to high-performance lithium anode material The corrosive agent of material.
Background technology
New material and clean energy resource are all the prior development directions of State-level, and lithium ion battery is in current energy storage technology Most widely used energy storage battery core, it is the target that the whole world is pursued to improve battery core energy storage density, and battery core energy density carries Height depends on the progress of its positive and negative electrode material, but also the both positive and negative polarity collector with lithium ion battery, both positive and negative polarity bond The progress of the material such as agent, electrolyte and barrier film is relevant.
The positive mix that the collector that the positive pole of lithium ion battery uses is generally aluminium foil and is coated on(Ferric phosphate Lithium, cobalt acid lithium or ternary material)Formed.Traditional current collector material is pure using 99.7% typically from the smooth aluminium foil in surface The aluminium foil of degree directly applies and is covered with active material, but the combination between the smooth aluminium foil and active material in surface more relaxes, to original Material and auxiliary material quality and technological requirement are high, and active material easily occurs in processing and charge and discharge process and comes off or dry linting phenomenon, Cycle charge discharge electrical efficiency and battery life are reduced, improves the contact resistance between component, causes positive plate electric conductivity to decline, So as to have impact on the combination property of battery.The serious combination property that have impact on lithium ion.People are generally using roughening aluminium at present The method on paper tinsel surface increases the cohesion between aluminium foil and positive mix, but the technique can not reach intended effect.Just Pole powder and aluminium foil separation problem can all occur when winding prismatic battery and during cycle charge-discharge, and then cause product to close Lattice rate first mate reduces, service life first mate shortens and battery capacity decay is obvious, on being influenceed the most using the battery of ternary material Seriously.
In order to improve positive pole aluminium foil collector, the bond state between anode sizing agent, prior art discloses micropore copper Paper tinsel and micropore aluminium foil, are all prepared for nine through holes on both both positive and negative polarity collector foils are every square centimeter, each through hole it is straight Footpath is about 1mm.But the aluminium foil and copper foil prepared by them must use special battery automatic assembly line, its reason is in original On some battery automatic assembly lines, using such a through-hole diameter in 1mm copper foil or aluminium foil, it may appear that slurry phenomenon is oozed at the back side, Influence the coating of another side.
Han Wei et al. utilizes acid, alkali electroless reagent in patent CN 103618090A and CN 103617894A, right Aluminium foil carries out soda acid etching processing.Obtained alumina foil contact resistance reduces unobvious, and is reduced during corrosion removal The mechanical strength of aluminium foil.The method of other countries' pore-forming on aluminium foil, employ rolling or laser ablation, and the present invention aluminium Paper tinsel pore-forming is using salt compounds etch, and technology path is entirely different, and it is special that resulting micropore aluminium foil also has Structure and performance.
The content of the invention
Overcome the deficiencies in the prior art of the present invention, it is therefore an objective to which a kind of corruption of high-performance lithium battery plus plate current-collecting body material is provided Lose agent.
In order to solve the above technical problems, the technical solution adopted in the present invention is:A kind of chlorine for being used to prepare micropore aluminium foil Salt corrosion agent, described chlorine salt corrosion agent are salting liquid, and the salt that described chlorine salt corrosion agent comprises only chlorion for anion is molten Liquid, Cl-Molar concentration be 0.1-3mol/L, cation contains the Fe that molar concentration is 0.1-3mol/L3+And Cu2+
Further, described chlorine salt corrosion agent also includes the Na that molar concentration is 0.5-1.5mol/L+
Further, described chlorine salt corrosion agent also includes the Ba that molar concentration is 0.1-0.3mol/L2+
Further, described chlorine salt corrosion agent also includes the Ca that molar concentration is 0.1-0.5mol/L2+
Further, described chlorine salt corrosion agent is 0.1-0.5mol/L NH also including molar concentration4 +
Compared with prior art the invention has the advantages that:
1st, a kind of chemical mordant for being used to prepare micropore aluminium foil, described chlorine salt corrosion agent are salting liquid, and described villaumite is rotten Erosion agent comprises only the salting liquid of chlorion, Cl for anion-Molar concentration be 0.1-3mol/L, cation contains molar concentration For 0.1-3mol/L Fe3+And Cu2+.Not acid-containing solution and/or aqueous slkali, environmental pollution is small, and reaction speed is easy to control. Micropore aluminium foil after corrosion can be used as anode current collector of lithium ion battery,
With the present invention corrosive agent corrosion after micropore aluminium foil it is every square centimeter on be distributed with 1000-1500 a diameter of 10- 50 μm of through hole, and it is every square centimeter on 1000-3000 a diameter of 10-50 μm of blind hole is distributed with, in the micropore The upper and lower surface of aluminium foil is dispersed with indentation, and indentation is wide 1-5 μm to be deep 1-3 μm, and length is 100-1000 μm so that aluminium foil two Individual surface both not completely through and also not completely isolated, can effectively by the ion of smaller less than 10-50 μm of diameter and/or Person's particle, and prevent major diameter ion or particle by, while do not influence the performance of material, such as:Average resistivity increase 1-3%, average tensile strength lifting 0-2%, averagely it is broken breaking elongation lifting 0-21%.
If there are 1000-1500 on its is every square centimeter directly as lithium battery anode collector using micropore aluminium foil Footpath had made inside and outside micropore aluminium foil two surfaces both in the blind hole of 10-50 μm of through hole and 1000-3000 diameters at 10-50 μm It is not completely isolated completely through yet, can be by lithium particle, and other particles or particle are prevented by the way that lithium ion passes through just It after the collector of pole, can be moved about in whole lithium battery, improve lithium ion activity, improve battery capacity, coating is superincumbent just Pole material and aluminium foil are integral, and its adhesive force significantly improves, and Li dendrite will not be grown at through hole and blind hole.
The present invention can also use chloride salt using being different from general acid & alkali liquid corrosive liquid in caustic solution of the present invention Compound is as corrosive liquid, the extent of reaction milder during corrosion, when aluminium foil is put into treatment fluid, in the protection of chlorion Under, copper ion or iron ion react with aluminium surface, aluminium surface is formed the structure of micropore, calcium ion, sodium in treatment fluid Ion and barium ions enter in perforated membrane and can be fixed in subsequent process, play a part of improvement to aluminium surface performance.
The size of the hole of micropore aluminium foil of the present invention is much smaller than the aperture of the micropore aluminium foil prepared by prior art, while again Avoid hole it is too small caused by positive electrode the problem of appearance can not penetrate in aluminium foil, micropore aluminium foil of the invention due to The hole and indentation of particular size, make micropore aluminium foil surface smoothness higher, without overlap, burr, and hole and aluminium foil surface Junction is irregular arc transition, in the absence of 90 ° of right angles, can effectively prevent the appearance of Li dendrite in charge and discharge process, prolong The service life of long battery;In addition, micro-pore shape is also different, the hole on micropore aluminium foil obtained by chemical corrosion method is not in Regular shape, aperture size change within the specific limits, and the diameter of each hole is also varied from different directions, it is this not The hole of regular shape is more beneficial for improving the cohesive force between aluminium foil and anode sizing agent.And existing production technology is varied without, Easy to spread, it is not only suitable for one side coating and is also applied for dual coating.
Compared with galvanic cell aluminium foil, the tensile strength of micropore aluminium foil is close with the tensile strength of primary aluminum paper tinsel;Micropore aluminium foil Resistivity increase only can make the capacity of lithium ion battery improve 8-10% less than 3%.When positive electrode uses ternary material, Because micropore aluminium foil makes the positive electrode on aluminium foil two sides be connected as an entirety, the property such as capacity and charge-discharge characteristics of battery can be made The uniformity of energy is substantially improved, and battery production yield rate improves 15-20%.
Described chlorine salt corrosion agent also includes the Na that molar concentration is 0.5-1.5mol/L+.Described chlorine salt corrosion agent is also Including the Ba that molar concentration is 0.1-0.3mol/L2+.Described chlorine salt corrosion agent is 0.1-0.5mol/L also including molar concentration Ca2+.Described chlorine salt corrosion agent is 0.1-0.5mol/L NH also including molar concentration4 +.It can further help to corrode Pore-forming or indentation.
Brief description of the drawings
Fig. 1 is the micro image of micropore aluminium foil prepared by the present invention.
Fig. 2 is the stress strain curve figure of micropore aluminium foil prepared by the present invention.
Embodiment
Embodiment 1
A kind of chemical mordant for being used to prepare micropore aluminium foil, using the corrosive agent corrosion cell aluminium foil, enters according to following steps OK:
1)Surface clean is carried out to the battery aluminium foil after rolling and dispels lubricant:The composition of first cleaning fluid be 5g/L NaOH, 70g/L Na2CO3, 40g/L Na3PO4, by the aluminium foil after rolling by the first cleaning fluid, kept in the first cleaning fluid Time be 6s.
2)The aluminium foil cleaned is pressed into chemical corrosion liquid:The composition of chemical corrosion liquid is:0.5mol/L NaCl, 0.1mol/L BaCl2, 0.1mol/L CaCl2, 0.1mol/L NH4Cl, 0.1mol/L CuCl2, 0.1mol/L FeCl3, residence time of the aluminium foil in the corrosive agent in 20s, in this stage, it is ensured that aluminium foil upper and lower surface is immersed in corrosion simultaneously In liquid, and the type of flow for circulating corrosive liquid flows in aluminium foil upper and lower surface, makes upper and lower surface corrosion uniform to reach.
3)Aluminium foil after corrosion is cleaned:The composition of second cleaning fluid is to take 0.4-0.8g/LNa2SO4、0.5— 1g/LCaSO4, 0.1-0.3g/L citric acids, aluminium foil upper and lower surface using shower nozzle spray the second cleaning fluid cleaned.
4)Brightization processing:The composition of brightening liquid is 2g/L CrO3, 1g/L Na2Cr2O7•2H2O, 0.1g/L NaF, Surface brightening processing is carried out to the aluminium foil after cleaning.
5)Aluminium foil after brightening is cleaned again:The aluminium foil after brightening is cleaned again using the second cleaning fluid.
6)Drying and processing:The aluminium foil cleaned again is dried, temperature is 200 DEG C.
7)Finished product is wound.
Fig. 1 is the micro image after corrosion cell aluminium foil of the present invention, from Fig. 1 as can be seen that two inside and outside micropore aluminium foil Surface both not completely through and also not completely isolated, it is integral with aluminium foil to coat superincumbent positive electrode, its adhesive force Significantly improve.
Fig. 2 is the stress strain curve figure after corrosion cell aluminium foil of the present invention, and curve 1 is bent for the stretching of galvanic cell aluminium foil in figure Line, curve 2 are the stress strain curve of micropore aluminium foil, and the micropore aluminium foil after chemical attack, its tensile property is compared with galvanic cell aluminium foil Do not reduce, it is close on the contrary or increase.
Using a kind of micropore aluminium foil for the chemical mordant preparation for being used to prepare micropore aluminium foil of the present invention, as lithium-ion electric The plus plate current-collecting body in pond, and assemble them into lithium ion battery:Weigh 8.5g LiFePO4s, 1.0g acetylene blacks and 0.5g PVDF, and 20g NMP are added, it is sufficiently stirred the slurry for making well mixed.Then scratched and implemented in through the present invention In the micropore aluminum foil current collector that example 1 is handled well, under 0.01MPa vacuum 80 DEG C of dryings to constant weight, and in 10-15MPa press Power lower roll is pressed into iron phosphate lithium electrode, and is cut into positive pole disk.Equally, weigh 4.25g graphite, 0.5g acetylene blacks and 0.25g butadiene-styrene rubber binding agents, and 10g NMP are added, the slurry for making well mixed is sufficiently stirred, is then scraped It is applied on the common copper foil cleaned through ethanol, is pressed into negative plate.By positive plate, celgard2400 polypropylene porous films every Lamination assembling is into battery core in sequence for film, negative plate, then with battery housing seal battery core, toward battery container in inject 1mol/L LiBF4/ diethyl carbonate electrolyte, seal liquid injection port after being full of, obtain lithium ion battery.
At a temperature of 60 DEG C, using charge-discharge test instrument to being assembled in the present embodiment in 2.5-4.2V voltage range Lithium ion battery carry out 1C charge-discharge tests, the specific discharge capacity of the 3rd time be 179mAh/g, progress 300 discharge and recharges follow After ring, capability retention 95.6%.
To further illustrate the lithium ion battery beneficial effect, spy sets following comparative example:
8.5g LiFePO4s, 1.0g acetylene blacks and 0.5g PVDF are weighed, and adds 20g NMP, is sufficiently stirred and makes mixed Close uniform slurry.Then scratched in the normal aluminium foil cleaned through ethanol, done for 80 DEG C under 0.01MPa vacuum It is dry to be pressed into iron phosphate lithium electrode to constant weight, and in 10-15MPa pressure lower rolls, and it is cut into positive pole disk.Equally, weigh 4.25g graphite, 0.5g acetylene blacks and 0.25g butadiene-styrene rubber binding agents, and 10g NMP are added, it is sufficiently stirred and makes mixed Uniform slurry is closed, is then scratched on the common copper foil cleaned through ethanol, is pressed into negative plate.By positive plate, Lamination assembling is electric into battery core, then with battery housing seal in sequence for celgard2400 polypropylene porous films barrier film, negative plate Core, toward battery container in inject 1mol/L LiBF4/ diethyl carbonate electrolyte, seal liquid injection port after filling, obtain lithium from Sub- battery.
After testing, after 300 charge and discharge cycles, capability retention is lithium ion battery obtained by the comparative example 82.5%.As can be seen here, micropore aluminum foil current collector made from the present embodiment, because the hole of this irregular shape thereon more has Beneficial to the cohesive force improved between aluminium foil and anode sizing agent, coming off for positive electrode can be avoided, so as to improve lithium ion battery Cyclical stability and the life-span.
Hole and quarter of a kind of micropore aluminium foil of lithium battery anode made of the present invention due to specific 10-50 μm of sizes Trace, can be by lithium ion, and other adiaphorous particles or ion can not be by adding lithium battery capacity, making micropore aluminium foil Surface flatness is higher, is irregular arc transition without overlap, burr, and hole and aluminium foil surface junction, in the absence of 90 ° Right angle, the appearance of Li dendrite in charge and discharge process can be effectively prevented, extend the service life of battery;In addition, micro-pore shape Different, the hole on micropore aluminium foil obtained by chemical corrosion method is in irregular shape, and aperture size becomes within the specific limits Change, the diameter of each hole is also varied from different directions, and the hole of this irregular shape is more beneficial for improving aluminium foil Cohesive force between anode sizing agent.And existing production technology is varied without, easy to spread, it is not only suitable for one side coating and also fitted For dual coating.
Compared with galvanic cell aluminium foil, the tensile strength of micropore aluminium foil is close with the tensile strength of primary aluminum paper tinsel;Micropore aluminium foil Resistivity increase only can make the capacity of lithium ion battery improve 8-10% less than 3%.When positive electrode uses ternary material, Because micropore aluminium foil makes the positive electrode on aluminium foil two sides be connected as an entirety, the property such as capacity and charge-discharge characteristics of battery can be made The uniformity of energy is substantially improved, and battery production yield rate improves 15-20%.
In above-mentioned second step, chemical mordant can also be following several formulas:
Second:0. 1mol/L CuCl2, 0. 1mol/L FeCl3
The third:0.5mol/L NaCl, 0.3mol/L BaCl2, 0.1mol/L CaCl2, 0.5mol/L NH4Cl、 0.1mol/L CuCl2, 0.2mol/L FeCl3
4th kind:0.5mol/L NaCl, 0.2mol/L BaCl2, 0.2mol/L CaCl2, 0.5mol/L CuCl2、 0.3mol/L FeCl3
5th kind:1.0mol/L NaCl, 0.3mol/L CaCl2, 0.1mol/L CuCl2, 0.2mol/L FeCl3
6th kind:0.1mol/L BaCl2, 0.2mol/L CaCl2, 0.3mol/L CuCl2, 0.2mol/L FeCl3
7th kind:1.2mol/L NaCl, 0.5mol/L CaCl2, 0.3mol/L NH4Cl, 0.5mol/L CuCl2、 0.2mol/L FeCl3,;
8th kind:0.1mol/L CuCl2, 2mol/L FeCl3
9th kind:1.5mol/L CuCl2, 0. 5mol/L FeCl3
Tenth kind:1.5mol/L NaCl, 0.1mol/L CaCl2, 0.1mol/L NH4Cl, 0.5mol/L CuCl2、 0.5mol/L FeCl3,
Tenth is a kind of:1.0mol/L NaCl, 0.1mol/L BaCl2, 0.1mol/L NH4Cl, 0.1mol/L CuCl2、 0.1mol/L FeCl3,
12nd kind:The composition of chemical corrosion liquid is:0.5mol/L NaCl, 0.1mol/L BaCl2, 0.1mol/L CaCl2, 0.5mol/L CuCl2, 0.5mol/L FeCl3,
13rd kind:0.3mol/L BaCl2, 0.3mol/L CaCl2, 0.3mol/L CuCl2, 0.5mol/L FeCl3
14th kind:The composition of chemical corrosion liquid is:0.5mol/L NaCl, 0.1mol/L BaCl2, 0.3mol/L CaCl2, 1mol/L CuCl2, 0.5 mol/L FeCl3,
15th kind:The composition of chemical corrosion liquid is:0.8mol/L NaCl, 0.1mol/L BaCl2, 0.1mol/L NH4Cl, 0.2mol/L CuCl2, 0.3mol/L FeCl3,
The caustic solution and embodiment of 15 kinds of corrosive agent of the above are same or like, can also be entered using conventional chemical industry caustic solution OK.
Table 1 is being compared as follows for micropore aluminium foil and primary aluminum paper tinsel resistivity:
Table 2 is as follows for the contrast of micropore aluminium foil and primary aluminum foil dynamic performance:
Above content is to combine the further description that specific preferred embodiment is done to the present invention, it is impossible to assert this hair Bright embodiment is only limitted to this, for general technical staff of the technical field of the invention, is not departing from this On the premise of invention, some simple deduction or replace can also be made, should all be considered as belonging to the power of the invention by being submitted Sharp claim determines scope of patent protection.

Claims (5)

  1. A kind of 1. chlorine salt corrosion agent for being used to prepare micropore aluminium foil, it is characterised in that:Described chlorine salt corrosion agent is salting liquid, institute The chlorine salt corrosion agent stated comprises only the salting liquid of chlorion, Cl for anion-Molar concentration be 0.1-3mol/L, cation contains There is the Fe that molar concentration is 0.1-3mol/L3+And Cu2+
  2. A kind of 2. chlorine salt corrosion agent for being used to prepare micropore aluminium foil according to claim 1, it is characterised in that:Described chlorine Salt corrosion agent also includes the Na that molar concentration is 0.5-1.5mol/L+
  3. A kind of 3. chlorine salt corrosion agent for being used to prepare micropore aluminium foil according to claim 1 or 2, it is characterised in that:It is described Chlorine salt corrosion agent also include molar concentration be 0.1-0.3mol/L Ba2+
  4. A kind of 4. chlorine salt corrosion agent for being used to prepare micropore aluminium foil according to claim 3, it is characterised in that:Described chlorine Salt corrosion agent also includes the Ca that molar concentration is 0.1-0.5mol/L2+
  5. A kind of 5. chlorine salt corrosion agent for being used to prepare micropore aluminium foil according to claim 4, it is characterised in that:Described chlorine Salt corrosion agent is 0.1-0.5mol/L NH also including molar concentration4 +
CN201710930884.4A 2017-10-09 2017-10-09 A kind of chlorine salt corrosion agent for being used to prepare micropore aluminium foil Withdrawn CN107740099A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710930884.4A CN107740099A (en) 2017-10-09 2017-10-09 A kind of chlorine salt corrosion agent for being used to prepare micropore aluminium foil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710930884.4A CN107740099A (en) 2017-10-09 2017-10-09 A kind of chlorine salt corrosion agent for being used to prepare micropore aluminium foil

Publications (1)

Publication Number Publication Date
CN107740099A true CN107740099A (en) 2018-02-27

Family

ID=61236770

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710930884.4A Withdrawn CN107740099A (en) 2017-10-09 2017-10-09 A kind of chlorine salt corrosion agent for being used to prepare micropore aluminium foil

Country Status (1)

Country Link
CN (1) CN107740099A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108611676A (en) * 2018-07-04 2018-10-02 山西沃特海默新材料科技股份有限公司 A kind of the electrochemical corrosion preparation method and its micropore copper foil of micropore battery copper foil

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101445932A (en) * 2008-12-25 2009-06-03 绍兴华立电子有限公司 Etching solution
CN102888608A (en) * 2012-11-02 2013-01-23 上海锅炉厂有限公司 Corrosive for displaying austenitic stainless steel grain boundary of fine grains and method for preparing corrosive
CN102906914A (en) * 2010-03-31 2013-01-30 东洋铝株式会社 Metal foil for negative electrode collector
CN107502936A (en) * 2017-08-04 2017-12-22 西北工业大学 A kind of method for obtaining large aperture doubled via AAO films

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101445932A (en) * 2008-12-25 2009-06-03 绍兴华立电子有限公司 Etching solution
CN102906914A (en) * 2010-03-31 2013-01-30 东洋铝株式会社 Metal foil for negative electrode collector
CN102888608A (en) * 2012-11-02 2013-01-23 上海锅炉厂有限公司 Corrosive for displaying austenitic stainless steel grain boundary of fine grains and method for preparing corrosive
CN107502936A (en) * 2017-08-04 2017-12-22 西北工业大学 A kind of method for obtaining large aperture doubled via AAO films

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108611676A (en) * 2018-07-04 2018-10-02 山西沃特海默新材料科技股份有限公司 A kind of the electrochemical corrosion preparation method and its micropore copper foil of micropore battery copper foil

Similar Documents

Publication Publication Date Title
CN107740177A (en) A kind of electrochemical heat corrosion preparation method of micropore battery aluminium foil
CN102332572B (en) Anode material and manufacturing method thereof as well as lithium ion battery and negative plate thereof
WO2016107564A1 (en) Composite positive material for lithium-sulphur battery with high rate performance and preparation method
KR20140039022A (en) Battery
CN108630446A (en) Positive plate and water system Asymmetric Supercapacitor for Asymmetric Supercapacitor
CN107403968A (en) Aqoue seconary battery
CN106803593B (en) A kind of complex function conductive coating and preparation method thereof
CN107768683A (en) A kind of high-performance lithium battery plus plate current-collecting body and its preparation method and application
CN111916709B (en) Preparation method of electrode material for water system zinc ion hybrid energy storage device
CN110048104A (en) A kind of water system battery and preparation method thereof based on cyaniding frame material
CN107256946A (en) Battery
CN112635698B (en) Negative pole piece of zinc secondary battery and preparation method and application thereof
CN105375034B (en) A kind of affluxion body in lithium ion batteries and preparation method thereof and a kind of lithium ion battery
CN107740100A (en) A kind of chemical mordant for being used to prepare micropore aluminium foil
CN107658470A (en) A kind of electrochemical corrosion preparation method of micropore battery aluminium foil
CN107768144A (en) A kind of micropore metal material and its preparation method and application
CN109904434A (en) A kind of porous lithium salts aeroge coated graphite composite material and preparation method
CN102969486A (en) Preparation method of tin-copper hollow nano-particles and application of nano-particles serving as negative pole material of lithium ion battery
CN107740099A (en) A kind of chlorine salt corrosion agent for being used to prepare micropore aluminium foil
CN207409587U (en) A kind of lithium battery anode
CN108172754A (en) A kind of preparation method of lithium ion battery aluminium foil, micropore aluminium foil and micropore aluminium foil
CN107768684A (en) A kind of lithium battery anode and its preparation method and application
CN107658471A (en) A kind of chemical heat erosion preparation method of micropore battery aluminium foil
CN117410437A (en) Antimony-based electrode and preparation method and application thereof
CN113140808B (en) Water-based battery

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
WW01 Invention patent application withdrawn after publication
WW01 Invention patent application withdrawn after publication

Application publication date: 20180227