CN109841832A - Positive plate and electrochemical cell - Google Patents

Positive plate and electrochemical cell Download PDF

Info

Publication number
CN109841832A
CN109841832A CN201711226486.0A CN201711226486A CN109841832A CN 109841832 A CN109841832 A CN 109841832A CN 201711226486 A CN201711226486 A CN 201711226486A CN 109841832 A CN109841832 A CN 109841832A
Authority
CN
China
Prior art keywords
positive
positive plate
prussian blue
diaphragm
blue material
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
CN201711226486.0A
Other languages
Chinese (zh)
Other versions
CN109841832B (en
Inventor
王莹
郭永胜
梁成都
苏硕剑
刘倩
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.)
Contemporary Amperex Technology Co Ltd
Original Assignee
Contemporary Amperex 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 Contemporary Amperex Technology Co Ltd filed Critical Contemporary Amperex Technology Co Ltd
Priority to CN201711226486.0A priority Critical patent/CN109841832B/en
Publication of CN109841832A publication Critical patent/CN109841832A/en
Application granted granted Critical
Publication of CN109841832B publication Critical patent/CN109841832B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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

  • Battery Electrode And Active Subsutance (AREA)
  • Secondary Cells (AREA)

Abstract

The application provides a positive plate and an electrochemical cell. The positive plate comprises a positive current collector and a positive diaphragm, wherein the positive diaphragm is arranged on the positive current collector and comprises a positive active material, a conductive agent and a binder. The positive active material comprises a Prussian blue material, and the molecular formula of the Prussian blue material is AxMz[M′(CN)6]yWherein, A is one or more of alkali metal ions and alkaline earth metal ions, M is transition metal, M' is transition metal, x is more than 0 and less than or equal to 2, y is more than 0 and less than or equal to 1, z is more than 0 and less than or equal to 1, the particle size D50 of the Prussian blue material is 50 nm-10 mu M, and the porosity of the anode membrane is 10-50%. The positive plate can ensure that the electrochemical cell has better cycle performance and higher volume energy density, and is suitable for large-scale production.

Description

Positive plate and electrochemical cell
Technical field
This application involves field of batteries more particularly to a kind of positive plates and electrochemical cell.
Background technique
Prussian blue (Prussian Blue Analogue, PBA) material because have specific capacity is high, voltage platform is high, The advantages such as at low cost are the positive electrodes for obtaining extensive concern in recent years.Prussian blue material is during the preparation process because of ion Reaction speed is fast, and the particle size generally yielded is smaller (generally nanoscale or micron order), thus makes to be difficult to press between particle It is real, the foundation not only bad for conductive network between particle in this way, while the volume energy density of battery can be also reduced, thus not Conducive to the whole design of product, thus how to take into account the volume energy density of battery and performance to be that prussian blue material is practical answer With one of problem in need of consideration.
Summary of the invention
In view of the problems in the background art, the application is designed to provide a kind of positive plate and electrochemical cell, The electrochemical cell volume energy density with higher and preferable cycle performance.
In order to achieve the above object, in the one side of the application, this application provides a kind of positive plates comprising anode collection Fluid and positive diaphragm, the anode diaphragm are set on the plus plate current-collecting body and including positive electrode active materials, conductive agent And binder.The positive electrode active materials include prussian blue material, and the molecular formula of the prussian blue material is AxMz [M′(CN)6]y, wherein A is one or more of alkali metal ion, alkaline-earth metal ions, and M is transition metal, and M ' is transition Metal, 0 < x≤2,0 < y≤1,0 z≤1 <, the partial size D50 of the prussian blue material is 50nm~10 μm, the anode The porosity of diaphragm is 10%~50%.
In the another aspect of the application, this application provides a kind of electrochemical cells comprising described in the application one side Positive plate.
Compared with the existing technology, the application include at least it is following the utility model has the advantages that
The positive plate of the application is taken into account while can guaranteeing electrochemical cell with preferable cycle performance with higher Volume energy density, be suitble to large-scale production.
Detailed description of the invention
Fig. 1 is the cycle performance curve of embodiment 1 and comparative example 2;
Fig. 2 is the cycle performance curve of embodiment 1 and comparative example 4.
Specific embodiment
The following detailed description of the positive plate and electrochemical cell according to the application.
Illustrate the positive plate according to the application first aspect first.
Positive plate according to the application first aspect includes plus plate current-collecting body and positive diaphragm, the anode diaphragm setting In on the plus plate current-collecting body and including positive electrode active materials, conductive agent and binder, the positive electrode active materials include general Shandong scholar's indigo plant class material, the molecular formula of the prussian blue material are AxMz[M′(CN)6]y, wherein A be alkali metal cation, One or more of alkaline earth metal cation, M are transition metal, and M ' is transition metal, 0 < x≤2,0 < y≤1,0 < z≤ 1, the porosity of the anode diaphragm is 10%~50%, and the partial size D50 of the prussian blue material is 50nm~10 μm.
In the positive plate according to the application first aspect, it is preferable that A can be selected from Li+、Na+、K+、Mg2+、Ca2+In One or more, it is further preferred that A can be selected from Li+、Na+、K+One or more of;It is further preferred that A is optional From Li+、Na+One or both of.Preferably, M can be selected from one of Mn, Fe, Co, Ni, Cu, Zn, V, Cr.Preferably, M ' It can be selected from one of Mn, Fe, Co, Ni, Cu, Zn, V, Cr.
In the positive plate according to the application first aspect, when the porosity of positive diaphragm is larger, electrolyte can Adequately to be infiltrated to prussian blue material granule, this plays the performance of electrochemical cell advantageous.But positive diaphragm Porosity it is excessive when, in the long-term cyclic process of electrochemical cell, more prussian blue material granules surface is direct Exposure in the electrolytic solution, increases the probability that side reaction occurs with electrolyte, poor so as to cause the cycle performance of electrochemical cell. In addition, when the porosity of positive diaphragm is excessive, the volume energy density of electrochemical cell is lower, simultaneously because prussian blue Contact between material granule is not close, and conduction of the electronics between prussian blue material granule is obstructed, and can also make to performance At adverse effect.Therefore, the porosity of positive diaphragm preferably controls below 50%.It is general when the porosity of positive diaphragm It is contacted between the scholar's indigo plant class material granule of Shandong relatively closely, is conducive to conduction of the electronics between prussian blue material granule, simultaneously The volume energy density of electrochemical cell increases.If but porosity is too small, on the one hand, electrolyte is to prussian blue material granule Wellability be deteriorated, ion transmit in positive plate and is obstructed, and the cycle performance that will lead to electrochemical cell declines;On the other hand, When porosity is too small, positive plate usually requires larger pressure in cold pressure procedure, and positive plate may cause because of over-voltage in electrochemistry It is broken at folding line in the rolling step of cell production process or in electrochemical cell charge and discharge process, thus to electrification The performance for learning battery causes to deteriorate.Therefore, the porosity of positive diaphragm is preferably controlled 10% or more.The porosity of positive diaphragm can To be controlled by the partial size for adjusting the cold pressing pressure in pole piece preparation process, active material and content etc..
In the positive plate according to the application first aspect, it is preferable that the porosity of the anode diaphragm is 15% ~35%.
In the positive plate according to the application first aspect, when the partial size of prussian blue material is smaller, electrolysis Liquid can sufficiently infiltrate it, while ion can also free deintercalation.But partial size is too small, prussian blue material granule it Between stacking gap it is larger, cause the porosity of positive diaphragm larger, on the one hand can reduce volume energy density, on the other hand also The contact between prussian blue material granule can be made not close, while because of prussian blue material poorly conductive itself, can be made Good conductive network is formed at being difficult between prussian blue material granule, so that the capacity for influencing electrochemical cell plays. Therefore, the partial size D50 of prussian blue material is preferably controlled in 50nm or more.And the partial size for increasing prussian blue material can subtract The porosity of small anode diaphragm, keeps the contact between prussian blue material granule closer, increases volume energy density, simultaneously It also helps and establishes good conductive network between prussian blue material granule, so that the electronics be conducive between particle passes It leads, makes electrochemical cell that there is preferable cycle performance.But the partial size of prussian blue material is excessive, and ion is in diffusion wherein Path extends, and is unfavorable for the deintercalation of ion, the performance of electrochemical cell is caused to decline.Therefore, the partial size of prussian blue material D50 is preferably controlled at 10 μm or less.
In the positive plate according to the application first aspect, it is preferable that the partial size D50 of the prussian blue material For 500nm~5 μm.
In the positive plate according to the application first aspect, if the content of prussian blue material is less, on the one hand It will affect the volume energy density of electrochemical cell, on the other hand also will affect the porosity of positive diaphragm.Preferably, described general The content of Shandong scholar's indigo plant class material is more than or equal to the 70% of the positive diaphragm gross mass, it is further preferred that described Prussian blue The content of class material is more than or equal to the 80% of the positive diaphragm gross mass.
In the positive plate according to the application first aspect, it is described anode diaphragm in may also include it is other it is conventional just Pole active material.
In the positive plate according to the application first aspect, the compacted density of positive diaphragm is too low to will cause electrochemistry The volume energy density of battery is too low, is unfavorable for the whole design of product and is difficult to meet the actual needs, positive diaphragm Compacted density is excessive, then causes positive plate by over-voltage, influence infiltration of the electrolyte to prussian blue material.Preferably, described The compacted density of positive diaphragm is 0.8g/cm3~2.0g/cm3, it is further preferred that the compacted density of the anode diaphragm is 1.0g/cm3~1.5g/cm3
In the positive plate according to the application first aspect, the type of the binder is not limited specifically, can It is selected according to actual needs.Specifically, the binder can be selected from one of oil-soluble binder, water-soluble binder Or it is several.
In the positive plate according to the application first aspect, the type of the oil-soluble binder is not limited specifically System, can be selected according to actual needs.Preferably, the oil-soluble binder can be selected from vinylidene fluoride monomer homopolymers, One or more of the copolymer of vinylidene fluoride monomer and fluorine-containing vinyl monomer.The vinylidene fluoride monomer with it is fluorine-containing The type of the copolymer of vinyl monomer does not limit specifically, can be selected according to actual needs.Specifically, the inclined fluorine The copolymer of vinyl monomer and fluorine-containing vinyl monomer can be selected from vinylidene fluoride-hexafluoropropylene copolymer, vinylidene-trifluoro Ethylene copolymer, vinylidene-chlorotrifluoroethylene, skewed segregation, vinylidene-trifluoro second One or more of alkene-chloro vinylidene fluoride copolymers, hexafluoropropylene (HFP)/tetrafluoroethylene (TFE)-vinylidene fluoride copolymers.
In the positive plate according to the application first aspect, the type of the water-soluble binder is not limited specifically System, can be selected according to actual needs.Preferably, the water-soluble binder can be selected from butadiene-styrene rubber, carboxymethyl cellulose One or more of sodium, sodium alginate, polyacrylic acid, polytetrafluoroethylene (PTFE).
In the positive plate according to the application first aspect, the type of the conductive agent is not limited specifically, can It is selected according to actual needs.Specifically, the conductive agent can be selected from conductive black (SuperP, Super S), Ketjen black, One or more of acetylene black, electrically conductive graphite, carbon nanotube, carbon nano-fiber.
In the positive plate according to the application first aspect, the type of the plus plate current-collecting body is not limited specifically System, can be selected according to actual needs.Specifically, the plus plate current-collecting body can be selected from aluminium foil, porous aluminium foil, stainless steel foil, One of porous stainless steel foil.
In the positive plate according to the application first aspect, the preparation method of the positive plate is not limited particularly System, using the preparation method of conventional cathode piece.Specifically, can in a solvent by prussian blue material, conductive agent and Binder, which is mixed in a certain ratio, is prepared into anode sizing agent, then presses anode sizing agent and is coated on plus plate current-collecting body, most passes through afterwards It crosses the processes such as drying, cold pressing and is prepared into the positive plate.
Secondly explanation electrochemical cell according to the application second aspect.
Electrochemical cell according to the application second aspect includes the positive plate according to the application first aspect.
In the electrochemical cell according to the application second aspect, the electrochemical cell may also include negative electrode tab, Electrolyte and isolation film etc..
In the electrochemical cell according to the application second aspect, the electrochemical cell can for lithium ion battery, Sodium-ion battery, kalium ion battery, Zinc ion battery or aluminium ion battery.In embodiments herein, electrochemistry is only shown Battery is the embodiment of sodium-ion battery, but the application is without being limited thereto.
In sodium-ion battery, negative electrode tab may include negative current collector and be set on negative current collector and contain cathode The cathode membrane of active material.The negative electrode active material can be selected from carbon material, alloy material, transition metal oxide and vulcanization One or more of object, phosphorous-based materials, titanate material.Specifically, the carbon material can be selected from hard carbon, soft carbon, amorphous One or more of carbon, nanostructured carbon material;The alloy material can be selected from one of Si, Ge, Sn, Pb, Sb or several The alloy material that kind is formed;The general formula of the transition metal oxide and sulfide is MxNy, wherein M be Fe, Co, Ni, Cu, Mn, The one or more of Sn, Mo, Sb, V, N are O or S;The phosphorous-based materials can be selected from one of red phosphorus, white phosphorus, black phosphorus or several Kind;The titanate material can be selected from Na2Ti3O7、Na2Ti6O13、Na4Ti5O12、Li4Ti5O12、NaTi2(PO4)3One of or It is several.
In sodium-ion battery, the negative electrode tab further includes conductive agent and binder, the kind of the conductive agent and binder Class does not limit specifically, can be selected according to actual needs.
In sodium-ion battery, the electrolyte can be liquid electrolyte, and the electrolyte may include sodium salt, organic solvent And optional additive.The type of the sodium salt does not limit specifically, can be selected according to actual needs.Specifically, The sodium salt can be selected from sodium hexafluoro phosphate (NaPF6), sodium perchlorate (NaClO4), hexafluoro Boratex (NaBF6), trifluoromethyl sulphur One or more of sour sodium, trifluoromethane sulfonic acid imines sodium (NaTFSI).The type of the organic solvent does not limit specifically System, can be selected according to actual needs.Specifically, the organic solvent can be selected from ethylene carbonate (EC), propene carbonate (PC), one of dimethyl carbonate (DMC), diethyl carbonate (DEC), methyl ethyl carbonate (EMC) or and several.The addition The type of agent does not limit specifically, can selectively add according to actual needs.
In sodium-ion battery, the material of the isolation film is unrestricted, can be selected according to actual needs.Specifically Ground, isolation film can be selected from polypropylene screen, polyethylene film, polyethylene/polypropylene/polyethylene composite membrane, non-woven membrane, glass fibers Tie up one or more of film.
Below with reference to embodiment, the application is further described.It should be understood that these embodiments be merely to illustrate the application without For limiting scope of the present application.
The sodium-ion battery of embodiment 1-9 and comparative example 1-4 are prepared by the following method.
(1) preparation of positive plate
By prussian blue material Na2MnFe(CN)6, conductive agent conductive carbon black, oil-soluble binder polyvinylidene fluoride (PVDF) it by weight being sufficiently mixed for 80:10:10, is then added in organic solvent N-Methyl pyrrolidone (NMP), stirs Anode sizing agent is prepared into after uniformly;Anode sizing agent is then coated uniformly on to the surface of plus plate current-collecting body aluminium foil, later again 100 It is dried at DEG C, obtains initial positive plate;Finally obtained initial positive plate is cold-pressed using cold press, obtains positive plate.
(2) preparation of negative electrode tab
By negative electrode active material hard carbon, binder butadiene-styrene rubber (SBR), conductive agent conductive carbon black according to weight ratio be 90: 5:5 is mixed with solvent deionized water, obtains negative electrode slurry after mixing evenly;Then negative electrode slurry is coated uniformly on negative pole currect collecting On body copper foil, negative electrode tab is obtained by drying, cold pressing, slitting later.
(3) preparation of electrolyte
Ethylene carbonate (EC), dimethyl carbonate (DMC) are mixed according to volume ratio for 1:1, then will sufficiently be done Dry sodium salt NaClO4It is dissolved in mixed organic solvents, obtains electrolyte, wherein NaClO4Concentration be 1mol/L.
(4) preparation of isolation film
Using conventional polypropylene (PP) film as isolation film.
(5) preparation of sodium-ion battery
Battery core is made by winding in positive plate, negative electrode tab and isolation film, then battery core is fitted into battery packages shell, it After inject electrolyte, using chemical conversion, stand etc. techniques be made sodium-ion battery.
The test process of sodium-ion battery will be illustrated next.
(1) porosity test of positive diaphragm
Respectively referring to national standard " measurement of GB/T 24586-2009 iron ore apparent density, real density and porosity " The apparent density and real density of positive diaphragm are tested, the porosity of positive diaphragm, test and specific calculation method are then calculated It is as follows: to calculate the apparent density of positive diaphragm according to Archimedes's drainage principle first, be denoted as ρa;Then real density is used Instrument equipment tests the real density of positive diaphragm, is denoted as ρ.
Porosity P=(ρ-the ρ of positive diaphragma)/ρ × 100%.
(2) the cycle performance test of sodium-ion battery
It with 1C multiplying power constant-current charge to voltage is 4.0V by sodium-ion battery, later with 4.0V constant-voltage charge at 25 DEG C It is 0.2C to electric current, stands 5min later, be 1.9V with 1C multiplying power constant-current discharge to voltage, then stand 5min, this is followed for one Ring charge and discharge process, this discharge capacity are denoted as the discharge capacity of sodium-ion battery the 1st time circulation.By sodium-ion battery according to The above method carries out 100 cyclic charging and discharging tests, and detection obtains the discharge capacity of the 100th circulation.4 sodium of every group of test from Sub- battery, is averaged.
Capacity retention ratio (%)=sodium-ion battery the 100th time electric discharge recycled after sodium-ion battery recycles 100 times is held Discharge capacity × 100% of amount/lithium ion battery the 1st time circulation.
(3) the volume energy density test of sodium-ion battery
The capacity of sodium-ion battery is set as 1Ah, then tests sodium-ion battery according to Archimedes's drainage principle Actual volume, and it is recorded as V, the average working voltage U of sodium-ion battery is 3.4V.
The volume energy density (Wh/L) of sodium-ion battery=(capacity (Ah) × sodium-ion battery of sodium-ion battery is flat Equal operating voltage (V))/sodium-ion battery actual volume V (L).
The parameter and the performance test results of table 1 embodiment 1-9 and comparative example 1-4
When embodiment 1-5, comparative example 1-2 are that the partial size of prussian blue material is fixed, the porosity of positive diaphragm is to sodium The influence of ion battery performance.In comparative example 1, the porosity of positive diaphragm is too low, although sodium-ion battery has higher volumes Energy density, but the cycle performance of sodium-ion battery is poor, is integrally difficult to meet the actual needs, the reason is that, cathode film The porosity of piece is too low to be meaned to stack in a manner of more close between prussian blue material granule, therefore identical battery core is held Occupied volume is smaller under amount design, sodium-ion battery volume energy density with higher, but the porosity of positive diaphragm When too low, electrolyte is slower to the infiltration of prussian blue material granule, and transmission of the sodium ion in positive plate is obstructed, to lead Cause sodium-ion battery cycle performance poor.In addition, prussian blue material is needed in cold pressing when the porosity of positive diaphragm is too low Larger pressure is born, causes positive plate easily by over-voltage, after being wound into battery core, folding line, which is in charge and discharge process, is easy hair Raw local fracture, to further deteriorate cycle performance.With the increase of the porosity of positive diaphragm, in embodiment 1-5, sodium The cycle performance of ion battery is improved, but it is understood that, the volume energy density of sodium-ion battery slightly reduces, Entirety can satisfy the demand of actual use.If but the porosity of positive diaphragm is excessively high, such as comparative example 2, can seriously affect sodium The volume energy density and cycle performance of ion battery, the reason is that, when the porosity of positive diaphragm is excessive, although electrolyte can Contact defective tightness adequately to be infiltrated to prussian blue material granule, but between prussian blue material granule, It will affect conduction of the electronics between prussian blue material granule.In addition, in long-term cyclic process, the hole of positive diaphragm Rate is excessive, has more prussian blue material granules surface and is directly exposed in electrolyte, increases and pair occurs with electrolyte The probability of reaction.In conjunction with Fig. 1 analysis it is found that in embodiment 1, the capacity protective rate after sodium-ion battery recycles 100 times is 93%, And in comparative example 2, the capacity retention ratio after sodium-ion battery recycles 100 times is only 78%.
When embodiment 1, embodiment 6-9, comparative example 3-4 are that the porosity of positive diaphragm is fixed, prussian blue material Influence of the partial size to sodium-ion battery performance.In comparative example 3, the partial size of prussian blue material is too small, the body of sodium-ion battery Product energy density is lower, and the cycle performance of sodium-ion battery is poor, the reason is that, the partial size of prussian blue material is too small When, specific surface area is usually larger, therefore the surface of exposure in the electrolytic solution is more, and the probability that side reaction occurs with electrolyte increases Add, deteriorate the cycle performance of sodium-ion battery, at the same between the prussian blue material of small particle can not Close stack, although cold Pressure is already close to the pressure limit under the partial size when pressure, but the volume energy density of sodium-ion battery is still lower.When general Shandong When the partial size of scholar's indigo plant class material is gradually increased, such as in embodiment 1, embodiment 6-9, Pu Lu can be made by increasing cold pressing pressure It is closer that scholar's indigo plant carrys out the stacking between material granule, is conducive to establish good conductive network, to be conducive between particle Electronics conduction, makes sodium-ion battery have preferable cycle performance, while keeping sodium-ion battery volume energy with higher close Degree.But when the partial size of prussian blue material is excessive, such as comparative example 4, due to the partial size ruler of single prussian blue material Very little larger, sodium ion diffusion path in prussian blue material extends, and deteriorates so as to cause the cycle performance of sodium-ion battery. It is analyzed in conjunction with Fig. 2 it is found that the capacity retention ratio after sodium-ion battery recycles 100 times is 93%, and comparative example 4 in embodiment 1 In, the capacity retention ratio after sodium-ion battery recycles 100 times is only 82%.
In conclusion the positive plate of the application can guarantee to take into account while sodium-ion battery has preferable cycle performance Volume energy density with higher is suitble to large-scale production.

Claims (10)

1. a kind of positive plate, comprising:
Plus plate current-collecting body;And
Positive diaphragm is set on the plus plate current-collecting body and including positive electrode active materials, conductive agent and binder;
It is characterized in that,
The positive electrode active materials include prussian blue material, and the molecular formula of the prussian blue material is AxMz[M′ (CN)6]y, wherein A is one or more of alkali metal ion, alkaline-earth metal ions, and M is transition metal, and M ' is transition gold Belong to, 0 < x≤2,0 < y≤1,0 z≤1 <;
The partial size D50 of the prussian blue material is 50nm~10 μm;
The porosity of the anode diaphragm is 10%~50%.
2. positive plate according to claim 1, which is characterized in that
A is selected from Li+、Na+、K+、Mg2+、Ca2+One or more of;
M is selected from one of Mn, Fe, Co, Ni, Cu, Zn, V, Cr;
M ' is selected from one of Mn, Fe, Co, Ni, Cu, Zn, V, Cr.
3. positive plate according to claim 1, which is characterized in that the porosity of the anode diaphragm is 15%~35%.
4. positive plate according to claim 1, which is characterized in that the partial size D50 of the Prussian blue material be 500nm~ 5μm。
5. positive plate according to claim 1, which is characterized in that the compacted density of the anode diaphragm is 0.8g/cm3~ 2.0g/cm3
6. positive plate according to claim 4, which is characterized in that the compacted density of the anode diaphragm is 1.0g/cm3~ 1.5g/cm3
7. positive plate according to claim 1, which is characterized in that the binder is selected from oil-soluble binder, water solubility One or more of binder.
8. positive plate according to claim 1, which is characterized in that the conductive agent is selected from conductive black, Ketjen black, acetylene One or more of black, electrically conductive graphite, carbon nanotube, carbon nano-fiber.
9. positive plate according to claim 1, which is characterized in that the content of the prussian blue material is more than or equal to institute State the 70% of positive diaphragm gross mass, it is preferable that the content of the prussian blue material is more than or equal to greatly the positive diaphragm The 80% of gross mass.
10. a kind of electrochemical cell, which is characterized in that including positive plate according to claim 1 to 9.
CN201711226486.0A 2017-11-29 2017-11-29 Positive plate and electrochemical cell Active CN109841832B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711226486.0A CN109841832B (en) 2017-11-29 2017-11-29 Positive plate and electrochemical cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711226486.0A CN109841832B (en) 2017-11-29 2017-11-29 Positive plate and electrochemical cell

Publications (2)

Publication Number Publication Date
CN109841832A true CN109841832A (en) 2019-06-04
CN109841832B CN109841832B (en) 2021-05-04

Family

ID=66882103

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711226486.0A Active CN109841832B (en) 2017-11-29 2017-11-29 Positive plate and electrochemical cell

Country Status (1)

Country Link
CN (1) CN109841832B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112259730A (en) * 2020-12-08 2021-01-22 江苏时代新能源科技有限公司 Prussian blue transition metal cyanide, preparation method thereof, and related positive electrode plate, secondary battery, battery pack and device
CN113437261A (en) * 2021-06-22 2021-09-24 中国电力科学研究院有限公司 Prussian blue positive plate, sodium ion battery and preparation method
CN113488611A (en) * 2021-06-24 2021-10-08 东莞塔菲尔新能源科技有限公司 Electrode assembly and secondary battery

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101826634A (en) * 2010-05-17 2010-09-08 江西省福斯特新能源有限公司 Lithium ion battery and manufacturing method thereof
CN102299307A (en) * 2011-09-03 2011-12-28 深圳市贝特瑞新能源材料股份有限公司 Electrode anode material and preparation method thereof
CN104716314A (en) * 2015-03-18 2015-06-17 上海中聚佳华电池科技有限公司 Prussian blue/reduced graphene oxide composite material as well as preparation method and application thereof
CN105789690A (en) * 2014-12-23 2016-07-20 宁德时代新能源科技股份有限公司 Rechargeable magnesium battery and preparation method thereof
CN105990567A (en) * 2015-02-09 2016-10-05 中国科学院宁波材料技术与工程研究所 Preparation method of prussian blue analogue nano-material and use of prussian blue analogue in sodium-ion battery
CN106960956A (en) * 2017-04-01 2017-07-18 上海中聚佳华电池科技有限公司 Modified Prussian blue material, sodium-ion battery positive plate and preparation method
CN107026283A (en) * 2017-02-28 2017-08-08 东莞市联洲知识产权运营管理有限公司 A kind of preparation method of nanometer Prussian Blue/chitosan complex film of low defect and its application in sodium-ion battery
CN107253731A (en) * 2017-07-13 2017-10-17 大连民族大学 A kind of high-performance super capacitance electrode material Co Fe Prussian blue analogue nano cubics and its preparation method and application
CN107394113A (en) * 2017-06-07 2017-11-24 天津中科先进技术研究院有限公司 Surface coating for improving safety performance of power lithium ion battery, surface coating application and power lithium ion battery

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101826634A (en) * 2010-05-17 2010-09-08 江西省福斯特新能源有限公司 Lithium ion battery and manufacturing method thereof
CN102299307A (en) * 2011-09-03 2011-12-28 深圳市贝特瑞新能源材料股份有限公司 Electrode anode material and preparation method thereof
CN105789690A (en) * 2014-12-23 2016-07-20 宁德时代新能源科技股份有限公司 Rechargeable magnesium battery and preparation method thereof
CN105990567A (en) * 2015-02-09 2016-10-05 中国科学院宁波材料技术与工程研究所 Preparation method of prussian blue analogue nano-material and use of prussian blue analogue in sodium-ion battery
CN104716314A (en) * 2015-03-18 2015-06-17 上海中聚佳华电池科技有限公司 Prussian blue/reduced graphene oxide composite material as well as preparation method and application thereof
CN107026283A (en) * 2017-02-28 2017-08-08 东莞市联洲知识产权运营管理有限公司 A kind of preparation method of nanometer Prussian Blue/chitosan complex film of low defect and its application in sodium-ion battery
CN106960956A (en) * 2017-04-01 2017-07-18 上海中聚佳华电池科技有限公司 Modified Prussian blue material, sodium-ion battery positive plate and preparation method
CN107394113A (en) * 2017-06-07 2017-11-24 天津中科先进技术研究院有限公司 Surface coating for improving safety performance of power lithium ion battery, surface coating application and power lithium ion battery
CN107253731A (en) * 2017-07-13 2017-10-17 大连民族大学 A kind of high-performance super capacitance electrode material Co Fe Prussian blue analogue nano cubics and its preparation method and application

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112259730A (en) * 2020-12-08 2021-01-22 江苏时代新能源科技有限公司 Prussian blue transition metal cyanide, preparation method thereof, and related positive electrode plate, secondary battery, battery pack and device
CN112259730B (en) * 2020-12-08 2021-05-04 江苏时代新能源科技有限公司 Prussian blue transition metal cyanide and preparation method and application thereof
WO2022121570A1 (en) * 2020-12-08 2022-06-16 宁德时代新能源科技股份有限公司 Prussian blue transition metal cyanide, preparation method therefor, and positive electrode pole piece, secondary battery, battery module, battery pack, and apparatus related to prussian blue transition metal cyanide
JP2023519589A (en) * 2020-12-08 2023-05-11 寧徳時代新能源科技股▲分▼有限公司 Prussian blue transition metal cyanide, manufacturing method thereof, and related positive plate, secondary battery, battery module, battery pack and device
CN113437261A (en) * 2021-06-22 2021-09-24 中国电力科学研究院有限公司 Prussian blue positive plate, sodium ion battery and preparation method
CN113488611A (en) * 2021-06-24 2021-10-08 东莞塔菲尔新能源科技有限公司 Electrode assembly and secondary battery
WO2022268153A1 (en) * 2021-06-24 2022-12-29 江苏正力新能电池技术有限公司 Electrode assembly and secondary battery

Also Published As

Publication number Publication date
CN109841832B (en) 2021-05-04

Similar Documents

Publication Publication Date Title
CN104681797B (en) A kind of preparation method of silicon-carbon composite cathode electrode, lithium ion battery
CN109728252A (en) Positive plate, preparation method thereof and sodium ion battery
CN101207197B (en) Lithium ion battery anode material and lithium ion battery and anode containing the material
CN109935784A (en) Positive plate and electrochemical cell
CN110767880A (en) Lithium supplement slurry for lithium secondary battery and preparation method of lithium secondary battery
CN101271972B (en) Lithium ion battery sandwich electrode piece and method for producing the same
CN108183209A (en) A kind of polyaniline-coated method of modifying of nickel-cobalt lithium manganate cathode material
CN114665065B (en) Positive electrode plate and preparation method and application thereof
CN101192682A (en) Lithium-ion secondary cell and manufacture method thereof
CN101192662A (en) Battery cathode and lithium ion secondary battery comprising same
CN110265626B (en) Positive pole piece, preparation method thereof and lithium ion secondary battery
CN101212070A (en) Laminated Li-ion secondary battery and method for producing the battery
CN107925057A (en) Anode of secondary cell, its preparation method and the lithium secondary battery for including the cathode
CN101399337B (en) Negative pole active material, preparing method thereof and negative pole and battery using the material
JPWO2011001666A1 (en) Non-aqueous electrolyte secondary battery positive electrode, method for producing the same, and non-aqueous electrolyte secondary battery
CN103427113B (en) Gel polymer electrolyte and polymer battery and preparation method thereof
CN105932329B (en) A kind of gel polymer electrolyte diaphragm and its preparation method and application
CN109841832A (en) Positive plate and electrochemical cell
CN100449824C (en) Battery pole piece and manufacturing method of lithium ion secordary battery containing the pole piece
CN102386439B (en) Lithium ion secondary battery
CN109461935A (en) Electrode slice and electrochemical energy storage device
CN1971980A (en) Anode of battery and lithium ion battery using the same and their preparation method
CN108598483A (en) Anti-overcharge metal ion battery and preparation method thereof
CN107534186A (en) Lithium rechargeable battery
CN109841806A (en) Positive plate and electrochemical cell

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
GR01 Patent grant
GR01 Patent grant