CN108470626A - Electrode material and preparation method thereof - Google Patents

Electrode material and preparation method thereof Download PDF

Info

Publication number
CN108470626A
CN108470626A CN201810206006.2A CN201810206006A CN108470626A CN 108470626 A CN108470626 A CN 108470626A CN 201810206006 A CN201810206006 A CN 201810206006A CN 108470626 A CN108470626 A CN 108470626A
Authority
CN
China
Prior art keywords
metal
concentration
electrode material
chloride
electrode
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201810206006.2A
Other languages
Chinese (zh)
Inventor
符显珠
纪亚强
孙蓉
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.)
Shenzhen Institute of Advanced Technology of CAS
Original Assignee
Shenzhen Institute of Advanced Technology of CAS
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 Institute of Advanced Technology of CAS filed Critical Shenzhen Institute of Advanced Technology of CAS
Priority to CN201810206006.2A priority Critical patent/CN108470626A/en
Publication of CN108470626A publication Critical patent/CN108470626A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01GCAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/22Electrodes
    • H01G11/24Electrodes characterised by structural features of the materials making up or comprised in the electrodes, e.g. form, surface area or porosity; characterised by the structural features of powders or particles used therefor
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01GCAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/22Electrodes
    • H01G11/30Electrodes characterised by their material
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01GCAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/22Electrodes
    • H01G11/30Electrodes characterised by their material
    • H01G11/46Metal oxides
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01GCAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/84Processes for the manufacture of hybrid or EDL capacitors, or components thereof
    • H01G11/86Processes for the manufacture of hybrid or EDL capacitors, or components thereof specially adapted for electrodes
    • 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
    • Y02E60/13Energy storage using capacitors

Landscapes

  • Engineering & Computer Science (AREA)
  • Power Engineering (AREA)
  • Microelectronics & Electronic Packaging (AREA)
  • Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

Electrode material and preparation method thereof.The invention discloses a kind of three-dimensional high heat conduction electrochemical capacitance electrodes and preparation method thereof.The electrode has three-D space structure, using high-thermal conductive metal as heat conduction core, and powers on deposited porous metal structure back loading high capacitance active material in heat conduction core.There is higher specific capacitance, excellent energy and power density, and good cycle using ultracapacitor prepared by the three-dimensional high heat conduction electrode, cheap, in telecommunications, the fields such as mobile device have great application potential.

Description

Electrode material and preparation method thereof
Technical field
The present invention relates to a kind of three-dimensional high heat conduction electrochemical capacitance electrode materials and preparation method thereof more particularly to one kind to answer Electrode material and preparation method thereof for ultracapacitor.
Background technology
It is well known that the energy plays key player during the survival and development of human society.The world today is to changing Depending on unduly for stone fuel not only makes it i.e. will be exhausted, but also the danger of various aspects is brought to natural environment, animals and plants and the mankind Evil.Paid much attention to by researcher and business circles for this purpose, developing and producing renewable and clean energy resource.Currently, developed or New energy being developed includes wind energy, nuclear energy, solar energy, ocean energy, Hydrogen Energy etc..In order to fully develop and utilize these New energy needs the energy storage device to match therewith.There are many purposes as a kind of novel energy-storing element for ultracapacitor.It is not only Itself can serve as common power, moreover it is possible to merge use with common batteries or fuel cell.In addition, ultracapacitor is in energy storage The high power density shown with output facet can make up the defect of secondary cell.Research in relation to ultracapacitor at this stage It focuses mostly in electrode material.
The performance of entire electrochemical energy storing device depends mainly on electrode material.Currently, most of electrochemical energy storing devices Electrode preparation method it is as follows:By with electro-chemical activity metal oxide or bimetallic oxide, sulfide powder with Solvents N-methyl -2- pyrroles are added after polymer adhesive (PVDF, polyvinyladine floride) mixing in conductive agent (carbon black, acetylene carbon black) After pyrrolidone, uniform paste is stirred to get, is then coated in copper foil of affluxion body or nickel foam.But this preparation side The electrode that method makes due to the use of the very low polymer adhesive of thermal conductivity, all pay no attention to by the internal resistance of entire electrode and thermal conductivity Think, easy to produce huge heat in fast charging and discharging, and is difficult to be dispersed into environment, this stability for device All it is very unfavorable with cycle performance.For conventional power supply thermal management scheme as increased device air flowing nearby, use is heat sink Deng being all indirectly to take away the heat of device to play the role of cooling, however these are all without fundamentally solving devices Heat dissipation problem.
Currently, the heat conduction research about electrochemical capacitance electrode is less, and it is higher using cost mostly, prepares more complicated Graphene transmits heat, and at low cost, and the high-thermal conductive metal of technology maturation but rarely has people's research.
Invention content
In view of this, a kind of three-dimensional high heat conduction electrochemical capacitance electrode material and preparation method thereof, the electrode material with High thermal conductivity and high-ratio surface.
In order to achieve the above purpose, present invention employs the following technical solutions:
A kind of electrode material, wherein the electrode material includes metal heat-conducting matrix, porous metallic layers and electro-chemical activity Substance, for the porous metallic layers electroplating deposition on the surface of the metal heat-conducting matrix, the electroactive substance is in situ Growth is formed on the porous metallic layers.
Wherein, the metal heat-conducting matrix is the single metal simple-substance with high thermal conductivity or two or more metal lists The material of the alloy of matter composition, the porous metallic layers is any one in metallic copper, nickel, iron, aluminium or zinc.
Wherein, the electroactive substance is metal oxide, the metal hydroxides for including transition metal element Or bimetallic oxide.
Wherein, the metal oxide is Co3O4、MnO2, NiO or CuO, the metal hydroxides is Cu (OH)2、Co (OH)2Or Ni (OH)2, the bimetallic oxide is NiMn2O4、MnCo2O4、CuCo2O4、NiMnO3Or NiCo2O4
The present invention also provides a kind of preparation method of electrode material as described above, this method includes:
Metal heat-conducting matrix is provided;
Using the metal heat-conducting matrix as cathode, electroplating technology is carried out in basic electroplate liquid, in the metal heat-conducting base Deposition forms porous metallic layers on the surface of body;Include that the porous metallic layers correspond to metal material in the basis electroplate liquid Metal chlorination salt;
The metal heat-conducting matrix for being formed with porous metallic layers is positioned in the first reaction solution and carries out hydro-thermal reaction, described Growth in situ forms electroactive substance on porous metallic layers;It include the electro-chemical activity object in first reaction solution The corresponding metallic element of matter.
Wherein, include metal chlorination salt and ammonium chloride in the basic electroplate liquid, the metal chlorination salt be copper chloride, Nickel chloride, iron chloride, aluminium chloride or zinc chloride, a concentration of 0.1M~0.5M of the metal chlorination salt, the ammonium chloride it is dense Degree is 2M~3M;It is anode using the metal heat-conducting matrix as cathode, platinum plate electrode, current density is in the electroplating technology 2A/cm2~3A/cm2, the time is 40s~100s.
Wherein, first reaction solution is the mixed aqueous solution of chlorate, ammonium chloride and sodium hydroxide, shape after hydro-thermal reaction At electroactive substance be metal hydroxides;A concentration of 1mM~5mM of the chlorate, the concentration of the ammonium chloride For 4mM~8mM, a concentration of 1mM~3mM of the sodium hydroxide;The chlorate is nickel chloride, copper chloride or cobalt chloride.
Wherein, it carries out also carrying out the high temperature anneal in the atmosphere of nitrogen after hydro-thermal reaction, the electrification being correspondingly formed Active material is metal oxide.
Wherein, first reaction solution is the mixed aqueous solution of nitrate, acetate and methenamine, shape after hydro-thermal reaction At electroactive substance be bimetallic oxide;A concentration of 0.02M~0.05M of the nitrate, the acetate A concentration of 0.01M~0.03M, a concentration of 0.01M~0.03M of the methenamine;The nitrate is nickel nitrate, copper nitrate Or cobalt nitrate, the acetate are copper acetate or manganese acetate.
Wherein, first reaction solution is the mixed aqueous solution of two kinds of sulfate, and the electrochemistry formed after hydro-thermal reaction is lived Property substance be bimetallic oxide;A concentration of 0.01M~0.04M of the sulfate, described two sulfate be selected from nickel sulfate, Arbitrary two kinds in manganese sulfate, cobaltous sulfate and copper sulphate.
Compared with prior art, a kind of three-dimensional high heat conduction electrochemical capacitance electrode provided by the present invention and preparation method thereof, Method is simple and practicable, and yield is high, energy consumption is smaller.Material structure is three-dimensional porous, and larger ratio table is possessed while electric conductivity is high Area can not only provide quick electron transmission channel, also increase active material bond area, meanwhile, electrolyte and activity The contact area of substance also greatly increases, and can effectively shorten the diffusion length of ion, to obtain larger specific capacitance.This is three-dimensional High heat conduction electrode is a kind of ultracapacitor haveing excellent performance, and can be provided simultaneously with high power density and high-energy density, is one The novel electrode material of kind has great application potential in the field.
Description of the drawings
Fig. 1 is the flow diagram of the preparation method of electrode material provided in an embodiment of the present invention.
Specific implementation mode
To make the object, technical solutions and advantages of the present invention clearer, below in conjunction with the accompanying drawings to the specific reality of the present invention The mode of applying is described in detail.The example of these preferred embodiments is illustrated in the accompanying drawings.Shown in attached drawing and according to The embodiments of the present invention of attached drawing description are only exemplary, and the present invention is not limited to these embodiments.
Here, it should also be noted that, in order to avoid having obscured the present invention because of unnecessary details, in the accompanying drawings only It shows the structure and/or processing step closely related with scheme according to the present invention, and is omitted little with relationship of the present invention Other details.
The present embodiment provides firstly a kind of electrode material, wherein the electrode material includes metal heat-conducting matrix, porous Metal layer and electroactive substance, the porous metallic layers electroplating deposition are described on the surface of the metal heat-conducting matrix Electroactive substance growth in situ is formed on the porous metallic layers.
The present invention also provides a kind of preparation methods of electrode material as described above, and refering to fig. 1, this method includes step Suddenly:
S1, metal heat-conducting matrix 1 is provided.The metal heat-conducting matrix 1 is the single metal simple-substance with high thermal conductivity Or the alloy of two or more metal simple-substance compositions.Specifically, the metal heat-conducting matrix 1 can select to be that gold, silver, copper etc. are single One metal or two or more metal alloys.
S2, with the metal heat-conducting matrix 1 it is cathode, electroplating technology is carried out in basic electroplate liquid, is led in the metal Deposition forms porous metallic layers 2 on the surface of hot basal body 1.Specifically, the material of the porous metallic layers 2 can be selected as metal Any one in copper, nickel, iron, aluminium or zinc.Wherein, include that the porous metallic layers correspond to metal in the basic electroplate liquid The metal chlorination salt of material.
In the preferred scheme, include metal chlorination salt and ammonium chloride, the metal chlorination in the basic electroplate liquid A concentration of 0.1M~0.5M of salt, a concentration of 2M~3M of the ammonium chloride;In the electroplating technology, with the metal heat-conducting base Body is cathode, platinum plate electrode is anode, current density 2A/cm2~3A/cm2, the time is 40s~100s.Wherein, the metal Chlorate is copper chloride, nickel chloride, iron chloride, aluminium chloride or zinc chloride.
S3, it the metal heat-conducting matrix 1 for being formed with porous metallic layers 2 is positioned in the first reaction solution carries out hydro-thermal reaction, Growth in situ forms electroactive substance 3 on the porous metallic layers 2.Specifically, the electroactive substance is packet Metal oxide, metal hydroxides containing transition metal element or bimetallic oxide.For example, the metal oxide is Co3O4、MnO2, NiO or CuO, the metal hydroxides is Cu (OH)2、Co(OH)2Or Ni (OH)2, the bimetallic oxide For NiMn2O4、MnCo2O4、CuCo2O4、NiMnO3Or NiCo2O4.Wherein, include the electrochemistry in first reaction solution The corresponding metallic element of active material.
In the first preferred scheme, first reaction solution is the mixing water of chlorate, ammonium chloride and sodium hydroxide Solution, the electroactive substance formed after hydro-thermal reaction are metal hydroxides.Wherein, a concentration of 1mM of the chlorate ~5mM, a concentration of 4mM~8mM of the ammonium chloride, a concentration of 1mM~3mM of the sodium hydroxide;The chlorate is chlorine Change nickel, copper chloride or cobalt chloride.In the first preferred scheme, the temperature for carrying out hydro-thermal reaction is 40~80 DEG C, when reaction Between be 13~16 hours.
Further, it in the first preferred scheme, carries out carrying out height also in the atmosphere of nitrogen after hydro-thermal reaction Temperature annealing, the electroactive substance being correspondingly formed are metal oxide.Carry out the high temperature anneal temperature be 350~ 450 DEG C, annealing time is 1~2 hour.
In second of preferred scheme, first reaction solution is the mixing water of nitrate, acetate and methenamine Solution, the electroactive substance formed after hydro-thermal reaction are bimetallic oxide.Wherein, the nitrate is a concentration of 0.02M~0.05M, a concentration of 0.01M~0.03M of the acetate, a concentration of 0.01M~0.03M of the methenamine; The nitrate is nickel nitrate, copper nitrate or cobalt nitrate, and the acetate is copper acetate or manganese acetate.Second of preferred side In case, the temperature for carrying out hydro-thermal reaction is 60~100 DEG C, and the reaction time is 13~16 hours.
In the third preferred scheme, first reaction solution is the mixed aqueous solution of two kinds of sulfate, hydro-thermal reaction The electroactive substance formed afterwards is bimetallic oxide.Wherein, a concentration of 0.01M~0.04M of the sulfate, it is described Arbitrary two kinds in nickel sulfate, manganese sulfate, cobaltous sulfate and copper sulphate of two kinds of sulfate.In second of preferred scheme, The temperature for carrying out hydro-thermal reaction is 300~400 DEG C, and the reaction time is 13~16 hours.
The following provide some specific embodiments of the present invention.Illustrate to simplify, the metal heat-conducting in following embodiment Matrix is by taking copper foil as an example.
【Embodiment 1】
Copper sheet is cut into 1*4cm2Rectangle as metal heat-conducting matrix.Metal copper sheet is connect into cathode, platinum plate electrode Anode is connect, basic bath (the 0.1M NiCl of 100ml are taken2·6H2O+2M NH4Cl electroplating technology) is carried out, in 2.5A/cm2Electricity Electro-deposition 60s under current density obtains the porous metallic layers for including nickel, wherein the area deposited is 1cm2.It is anti-to prepare 20ml first It answers liquid and is transferred in hydro-thermal axe, wherein first reaction solution includes 0.03M Ni (NO3)2·6H2O、0.01M Mn (COOH)2·6H2O and 0.02M methenamines.The copper electrode that deposited porous nickel is put into hydro-thermal axe, 14 are kept the temperature at 80 DEG C Hour, active material NiMn is obtained on porous metallic layers2O4, prepare electrode material.After taking out electrode, deionized water is used Several times with ethyl alcohol cleaning, and it is dry.
Using the thermal conductivity that laser heat conducting instrument test calculates prepared metallic copper combination electrode is 300W m-1K-1, far Higher than thermal conductivity (the 1.7632W m of the comparison electrode prepared using traditional rubbing method-1K-1).What the present embodiment was prepared The conductivity of electrode is 1 × 10-6Ω·cm
【Embodiment 2】
Copper sheet is cut into 1*4cm2Rectangle as metal heat-conducting matrix.Metal copper sheet is connect into cathode, platinum plate electrode Anode is connect, basic bath (the 0.2M NiCl of 100ml are taken2·6H2O+2.5M NH4Cl electroplating technology) is carried out, in 3A/cm2Electricity Electro-deposition 40s under current density obtains the porous metallic layers for including nickel, wherein the area deposited is 1cm2.It is reacted with 20ml first Liquid is simultaneously transferred in hydro-thermal axe, wherein first reaction solution includes 0.05M Ni (NO3)2·6H2O、0.03M Mn (COOH)2·6H2O and 0.03M methenamines.The copper electrode that deposited porous nickel is put into hydro-thermal axe, 13 are kept the temperature at 70 DEG C Hour, active material NiMn is obtained on porous metallic layers2O4, prepare electrode material.
【Embodiment 3】
Copper sheet is cut into 1*4cm2Rectangle as metal heat-conducting matrix.Metal copper sheet is connect into cathode, platinum plate electrode Anode is connect, basic bath (the 0.5M NiCl of 100ml are taken2·6H2O+3M NH4Cl electroplating technology) is carried out, in 2A/cm2Electric current Electro-deposition 100s under density obtains the porous metallic layers for including nickel, wherein the area deposited is 1cm2.With the first reaction solutions of 20ml And be transferred in hydro-thermal axe, wherein first reaction solution includes 0.02M Ni (NO3)2·6H2O、0.01M Mn(COOH)2· 6H2O and 0.01M methenamines).The copper electrode that deposited porous nickel is put into hydro-thermal axe, 15 hours are kept the temperature at 60 DEG C, Active material NiMn is obtained on porous metallic layers2O4, prepare electrode material.
【Embodiment 4】
Copper sheet is cut into 1*4cm2Rectangle as metal heat-conducting matrix.Metal copper sheet is connect into cathode, platinum plate electrode Anode is connect, basic bath (the 0.1M FeCl of 100ml are taken3·6H2O+2M NH4Cl) carry out electroplating technology.In 3A/cm2Electric current Electro-deposition 100s under density is obtained and is wrapped iron-containing porous metallic layers, wherein the area deposited is 1cm2.With the first reaction solutions of 40ml And be transferred in hydro-thermal axe, wherein first reaction solution includes 1mM NiCl2、4mM NH4Cl and 1mmol NaOH.It will deposition Porous electrode is put into hydro-thermal axe, at 55 DEG C keeps the temperature 14 hours, and active material Ni (OH) is obtained on porous metallic layers2, Prepare electrode material.
【Embodiment 5】
Copper sheet is cut into 1*4cm2Rectangle as metal heat-conducting matrix.Metal copper sheet is connect into cathode, platinum plate electrode Anode is connect, basic bath (the 0.4M NiCl of 100ml are taken2·6H2O+3M NH4Cl electroplating technology) is carried out, in 2A/cm2Electric current Electro-deposition 60s under density obtains the porous metallic layers for including nickel, wherein the area deposited is 1cm2.With the first reaction solutions of 40ml And be transferred in hydro-thermal axe, wherein first reaction solution includes 2mM CuCl2、4mM NH4Cl and 2mmol NaOH.It will deposition The copper electrode of porous nickel is put into hydro-thermal axe, at 50 DEG C keeps the temperature 15 hours, and active material Cu is obtained on porous metallic layers (OH)2, prepare electrode material.
【Embodiment 6】
Copper sheet is cut into 1*4cm2Rectangle as metal heat-conducting matrix.Metal copper sheet is connect into cathode, platinum plate electrode Anode is connect, basic bath (the 0.5M FeCl of 100ml are taken3·6H2O+2M NH4Cl electroplating technology) is carried out, in 3A/cm2Electric current Electro-deposition 80s under density is obtained and is wrapped iron-containing porous metallic layers, wherein the area deposited is 1cm2.With the first reaction solutions of 40ml And be transferred in hydro-thermal axe, wherein first reaction solution includes 5mM CuCl2、6mM NH4Cl and 3mmol NaOH.It will deposition The copper electrode of porous nickel is put into hydro-thermal axe, at 80 DEG C keeps the temperature 14 hours, and substance C u is obtained on porous metallic layers (OH)2, fire is taken off at 400 DEG C in nitrogen atmosphere 2 hours, prepare the electrode material that active material is CuO.
【Embodiment 7】
Copper sheet is cut into 1*4cm2Rectangle as metal heat-conducting matrix.Metal copper sheet is connect into cathode, platinum plate electrode Anode is connect, basic bath (the 0.3M CuCl of 100ml are taken2·6H2O+2.5M NH4Cl electroplating technology) is carried out, in 3A/cm2Electricity Electro-deposition 100s under current density obtains the porous metallic layers for including copper, wherein the area deposited is 1cm2.It is reacted with 40ml first Liquid is simultaneously transferred in hydro-thermal axe, wherein first reaction solution includes 3mM NiCl2、8mM NH4Cl and 2mmol NaOH.It will sink The copper electrode for having accumulated Porous Cu is put into hydro-thermal axe, keeps the temperature 13 hours at 55 DEG C, active material is obtained on porous metallic layers Ni(OH)2.After taking out electrode, is cleaned and dried with deionized water and ethyl alcohol.Fire 1 is finally taken off at 450 DEG C in nitrogen atmosphere Hour, prepare the electrode material that active material is NiO.
【Embodiment 8】
Copper sheet is cut into 1*4cm2Rectangle as metal heat-conducting matrix.Metal copper sheet is connect into cathode, platinum plate electrode Anode is connect, basic bath (the 0.1M NiCl of 100ml are taken2·6H2O+2M NH4Cl electroplating technology) is carried out, in 3A/cm2Electric current Electro-deposition 40s under density obtains the porous metallic layers for including nickel, wherein the area deposited is 1cm2.With the first reaction solutions of 40ml And be transferred in hydro-thermal axe, wherein first reaction solution includes 4mM CuCl2、8mM NH4Cl and 3mmol NaOH.It will deposition The copper electrode of porous nickel is put into hydro-thermal axe, at 55 DEG C keeps the temperature 14 hours, and active material Cu is obtained on porous metallic layers (OH)2.After taking out electrode, is cleaned and dried with deionized water and ethyl alcohol.It is small that fire 2 is finally taken off at 350 DEG C in nitrogen atmosphere When, prepare the electrode material that active material is CuO.
【Embodiment 9】
Copper sheet is cut into 1*4cm2Rectangle as metal heat-conducting matrix.Metal copper sheet is connect into cathode, platinum plate electrode Anode is connect, basic bath (the 0.1M CuCl of 100ml are taken2·6H2O+2M NH4Cl electroplating technology) is carried out, in 3A/cm2Electric current Electro-deposition 80s under density obtains the porous metallic layers for including copper, wherein the area deposited is 1cm2.With the first reaction solutions of 40ml And be transferred in hydro-thermal axe, wherein first reaction solution includes 2mM CoCl2、5mM NH4Cl and 2mM NaOH.It will deposited The copper electrode of Porous Cu is put into hydro-thermal axe, and 15 hours are kept the temperature at 55 DEG C, and active material Co is obtained on porous metallic layers (OH)2.After taking out electrode, is cleaned and dried with deionized water and ethyl alcohol.It is small that fire 2 is finally taken off at 400 DEG C in nitrogen atmosphere When, it is Co to prepare active material3O4Electrode material.
【Embodiment 10】
Copper sheet is cut into 1*4cm2Rectangle as metal heat-conducting matrix.Metal copper sheet is connect into cathode, platinum plate electrode Anode is connect, basic bath (the 0.1M NiCl of 100ml are taken2·6H2O+2M NH4Cl electroplating technology) is carried out, in 3A/cm2Electric current Electro-deposition 60s under density obtains the porous metallic layers for including nickel, wherein the area deposited is 1cm2.With the first reaction solutions of 100ml And be transferred in hydro-thermal axe, wherein first reaction solution includes 0.02M MnSO4With 0.01M CoSO4.Porous nickel will be deposited Copper electrode put into hydro-thermal axe, keep the temperature 14 hours at 350 DEG C, active material MnCo obtained on porous metallic layers2O4, system It is standby to obtain electrode material.
【Embodiment 11】
Copper sheet is cut into 1*4cm2Rectangle as metal heat-conducting matrix.Metal copper sheet is connect into cathode, platinum plate electrode Anode is connect, basic bath (the 0.1M CuCl of 100ml are taken2·6H2O+2M NH4Cl electroplating technology) is carried out, in 2A/cm2Electric current Electro-deposition 80s under density obtains the porous metallic layers for including copper, wherein the area deposited is 1cm2.With the first reaction solutions of 100ml And be transferred in hydro-thermal axe, wherein first reaction solution includes 0.02M NiSO4With 0.04M CoSO4.Porous Cu will be deposited Copper electrode put into hydro-thermal axe, keep the temperature 13 hours at 400 DEG C, active material NiCo obtained on porous metallic layers2O4, system It is standby to obtain electrode material.
【Embodiment 12】
Copper sheet is cut into 1*4cm2Rectangle as metal heat-conducting matrix.Metal copper sheet is connect into cathode, platinum plate electrode Anode is connect, basic bath (the 0.1M NiCl of 100ml are taken2·6H2O+2M NH4Cl electroplating technology) is carried out, in 2A/cm2Electric current Electro-deposition 100s under density obtains the porous metallic layers for including nickel, wherein the area deposited is 1cm2.It is reacted with 100ml first Liquid is simultaneously transferred in hydro-thermal axe, wherein first reaction solution includes 0.01M CuSO4With 0.04M CoSO4.It will deposited porous The copper electrode of nickel is put into hydro-thermal axe, and 16 hours are kept the temperature at 300 DEG C, and active material CuCo is obtained on porous metallic layers2O4, Prepare electrode material.
【Embodiment 13】
Copper sheet is cut into 1*4cm2Rectangle as metal heat-conducting matrix.Metal copper sheet is connect into cathode, platinum plate electrode Anode is connect, basic bath (the 0.1M NiCl of 100ml are taken2·6H2O+2M NH4Cl electroplating technology) is carried out, in 2A/cm2Electric current Electro-deposition 100s under density obtains the porous metallic layers for including nickel, wherein the area deposited is 1cm2.It is reacted with 100ml first Liquid is simultaneously transferred in hydro-thermal axe, wherein first reaction solution includes 0.01M NiSO4With 0.03M MnSO4.It will deposited porous The copper electrode of nickel is put into hydro-thermal axe, and 15 hours are kept the temperature at 350 DEG C, and active material NiMn is obtained on porous metallic layers2O4, Prepare electrode material.
In conclusion a kind of three-dimensional high heat conduction electrochemical capacitance electrode provided by the present invention and preparation method thereof, method letter Single easy, yield is high, energy consumption is smaller.Material structure is three-dimensional porous, larger specific surface area is possessed while electric conductivity is high, no But quick electron transmission channel can be provided, active material bond area is also increased, meanwhile, electrolyte and active material connect Contacting surface product also greatly increases, and can effectively shorten the diffusion length of ion, to obtain larger specific capacitance.This three-dimensional high heat conduction electricity Pole is a kind of ultracapacitor haveing excellent performance, and can be provided simultaneously with high power density and high-energy density, is a kind of novel Electrode material has great application potential in the field.
It is pointed out that the technical concepts and features of above-described embodiment only to illustrate the invention, it is ripe its object is to allow The personage for knowing technique cans understand the content of the present invention and implement it accordingly, and the protection model of the present invention can not be limited with this It encloses.Any equivalent change or modification in accordance with the spirit of the invention should be covered by the protection scope of the present invention.

Claims (10)

1. a kind of electrode material, which is characterized in that including metal heat-conducting matrix, porous metallic layers and electroactive substance, institute Porous metallic layers electroplating deposition is stated on the surface of the metal heat-conducting matrix, the electroactive substance growth in situ is formed In on the porous metallic layers.
2. electrode material according to claim 1, which is characterized in that the metal heat-conducting matrix is with high thermal conductivity Single metal simple-substance or two or more metal simple-substances composition alloy, the materials of the porous metallic layers be metallic copper, nickel, Any one in iron, aluminium or zinc.
3. high heat conduction electrode according to claim 1 or 2, which is characterized in that the electroactive substance is to include Metal oxide, metal hydroxides or the bimetallic oxide of transition metal element.
4. high heat conduction electrode according to claim 3, which is characterized in that the metal oxide is Co3O4、MnO2、NiO Or CuO, the metal hydroxides are Cu (OH)2、Co(OH)2Or Ni (OH)2, the bimetallic oxide is NiMn2O4、 MnCo2O4、CuCo2O4、NiMnO3Or NiCo2O4
5. a kind of preparation method of electrode material as described in claim 1-4 is any, which is characterized in that this method includes:
Metal heat-conducting matrix is provided;
Using the metal heat-conducting matrix as cathode, electroplating technology is carried out in basic electroplate liquid, in the metal heat-conducting matrix Deposition forms porous metallic layers on surface;It include the gold that the porous metallic layers correspond to metal material in the basis electroplate liquid Belong to chlorate;
The metal heat-conducting matrix for being formed with porous metallic layers is positioned in the first reaction solution and carries out hydro-thermal reaction, described porous Growth in situ forms electroactive substance on metal layer;Include the electroactive substance pair in first reaction solution The metallic element answered.
6. the preparation method of electrode material according to claim 5, which is characterized in that include in the basis electroplate liquid Metal chlorination salt and ammonium chloride, the metal chlorination salt are copper chloride, nickel chloride, iron chloride, aluminium chloride or zinc chloride, the gold Belong to a concentration of 0.1M~0.5M, a concentration of 2M~3M of the ammonium chloride of chlorate;In the electroplating technology, with the metal Heat conduction substrate is cathode, platinum plate electrode is anode, current density 2A/cm2~3A/cm2, the time is 40s~100s.
7. the preparation method of electrode material according to claim 5, which is characterized in that first reaction solution is chlorination The mixed aqueous solution of salt, ammonium chloride and sodium hydroxide, the electroactive substance formed after hydro-thermal reaction are metal hydroxides; A concentration of 1mM~5mM of the chlorate, a concentration of 4mM~8mM of the ammonium chloride, a concentration of 1mM of the sodium hydroxide ~3mM;The chlorate is nickel chloride, copper chloride or cobalt chloride.
8. the preparation method of electrode material according to claim 5, which is characterized in that carry out hydro-thermal reaction later also in nitrogen The high temperature anneal is carried out in the atmosphere of gas, the electroactive substance being correspondingly formed is metal oxide.
9. the preparation method of electrode material according to claim 5, which is characterized in that first reaction solution is nitric acid The mixed aqueous solution of salt, acetate and methenamine, the electroactive substance formed after hydro-thermal reaction are bimetallic oxide; A concentration of 0.02M~0.05M of the nitrate, a concentration of 0.01M~0.03M of the acetate, the methenamine A concentration of 0.01M~0.03M;The nitrate is nickel nitrate, copper nitrate or cobalt nitrate, and the acetate is copper acetate or acetic acid Manganese.
10. the preparation method of electrode material according to claim 5, which is characterized in that first reaction solution is two kinds The mixed aqueous solution of sulfate, the electroactive substance formed after hydro-thermal reaction are bimetallic oxide;The sulfate A concentration of 0.01M~0.04M, described two sulfate in nickel sulfate, manganese sulfate, cobaltous sulfate and copper sulphate arbitrary two Kind.
CN201810206006.2A 2018-03-13 2018-03-13 Electrode material and preparation method thereof Pending CN108470626A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810206006.2A CN108470626A (en) 2018-03-13 2018-03-13 Electrode material and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810206006.2A CN108470626A (en) 2018-03-13 2018-03-13 Electrode material and preparation method thereof

Publications (1)

Publication Number Publication Date
CN108470626A true CN108470626A (en) 2018-08-31

Family

ID=63265271

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810206006.2A Pending CN108470626A (en) 2018-03-13 2018-03-13 Electrode material and preparation method thereof

Country Status (1)

Country Link
CN (1) CN108470626A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110323081A (en) * 2019-06-14 2019-10-11 电子科技大学 Nickel hydroxide/basic carbonate cobalt composite material method is prepared on a current collector
CN110676063A (en) * 2019-08-19 2020-01-10 深圳职业技术学院 High-conductivity cobalt hydroxide electrode material, preparation method thereof, electrode and capacitor
CN112397318A (en) * 2020-10-15 2021-02-23 南京大学 Foamed nickel Cu (OH)2@Ni3S2Core-shell nanowire composite capacitor material and preparation method thereof
CN112875765A (en) * 2021-01-18 2021-06-01 欣旺达电动汽车电池有限公司 NiMnO3Preparation method of bimetal oxide and energy storage device

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1767259A (en) * 2000-09-29 2006-05-03 株式会社东芝 Battery pack and portable electronic appliance
CN101728037A (en) * 2008-10-28 2010-06-09 信昌电子陶瓷股份有限公司 Chip resistor with heat-conducting layer
CN102842629A (en) * 2011-06-21 2012-12-26 张国生 Thin-film solar cell with metal substrate as cell film substrate or packaging material
CN203242722U (en) * 2013-04-12 2013-10-16 安徽德擎电池科技有限公司 Zinc-air battery with microporous membrane
CN106847529A (en) * 2017-01-21 2017-06-13 中国科学院深圳先进技术研究院 Combination electrode material and preparation method thereof

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1767259A (en) * 2000-09-29 2006-05-03 株式会社东芝 Battery pack and portable electronic appliance
CN101728037A (en) * 2008-10-28 2010-06-09 信昌电子陶瓷股份有限公司 Chip resistor with heat-conducting layer
CN102842629A (en) * 2011-06-21 2012-12-26 张国生 Thin-film solar cell with metal substrate as cell film substrate or packaging material
CN203242722U (en) * 2013-04-12 2013-10-16 安徽德擎电池科技有限公司 Zinc-air battery with microporous membrane
CN106847529A (en) * 2017-01-21 2017-06-13 中国科学院深圳先进技术研究院 Combination electrode material and preparation method thereof

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110323081A (en) * 2019-06-14 2019-10-11 电子科技大学 Nickel hydroxide/basic carbonate cobalt composite material method is prepared on a current collector
CN110323081B (en) * 2019-06-14 2021-02-05 电子科技大学 Method for preparing nickel hydroxide/basic cobaltous carbonate composite material on current collector
CN110676063A (en) * 2019-08-19 2020-01-10 深圳职业技术学院 High-conductivity cobalt hydroxide electrode material, preparation method thereof, electrode and capacitor
CN112397318A (en) * 2020-10-15 2021-02-23 南京大学 Foamed nickel Cu (OH)2@Ni3S2Core-shell nanowire composite capacitor material and preparation method thereof
CN112875765A (en) * 2021-01-18 2021-06-01 欣旺达电动汽车电池有限公司 NiMnO3Preparation method of bimetal oxide and energy storage device
CN112875765B (en) * 2021-01-18 2023-05-05 欣旺达电动汽车电池有限公司 NiMnO 3 Preparation method of bimetal oxide and energy storage device

Similar Documents

Publication Publication Date Title
CN108470626A (en) Electrode material and preparation method thereof
Li et al. A novel bifunctional oxygen GDE for alkaline secondary batteries
JP7345858B2 (en) Metal-hydrogen batteries for large-scale energy storage
CN103325999B (en) Preparation method of seamlessly integrated metal substrate/nanoporous metal/metal oxide composite electrode material, and application of compound electrode material
CN106030899A (en) Tri-electrode zinc-air battery with flowing electrolyte
CN108598431A (en) Grapheme foam-nickel oxide combination electrode material and preparation method thereof
CN102013527A (en) Rechargeable zinc ion battery
Xiong et al. Sequentially electrodeposited MnOX/Co-Fe as bifunctional electrocatalysts for rechargeable zinc-air batteries
CN104167540A (en) Negative electrode active material and preparation method thereof and lithium ion battery
Choi et al. Fibrous MnO2 electrode electrodeposited on carbon fiber for a fuel cell/battery system
Li et al. Three-dimensional nanoporous gold–cobalt oxide electrode for high-performance electroreduction of hydrogen peroxide in alkaline medium
CN101222047A (en) Cathode material of thin film lithium ion battery and method for producing the same
CN102097661A (en) Rechargeable zinc ion battery using zinc manganate as anode
CN106129361A (en) A kind of lithium ion battery anode active material and preparation method
CN112331933A (en) Long-cycle-life cathode of aqueous zinc secondary battery and preparation and application thereof
CN111403678B (en) Three-dimensional flexible metal cathode and preparation method thereof
CN107731552B (en) A kind of nickel nano wire collector and preparation method thereof
CN109301255A (en) A kind of 3D porous current collector and its preparation method and application
CN108364806A (en) A kind of tree-shaped three-dimensional structure metal material and preparation method thereof and application in the battery
CN108172407A (en) Composite electrode, preparation method and application thereof
Zhang et al. A novel alkaline Zn/MnO2 cell with alkaline solid polymer electrolyte
CN103199272A (en) Simple preparation method of integrated metal-air cathode for metal-air battery
JP5557385B2 (en) Energy storage device with proton as insertion species
CN115881915A (en) Large-scale preparation method for in-situ construction of zinc cathode metal composite protective layer by ultrafast microwave technology and application thereof
CN103579614B (en) Preparation method of lithium ion battery cathode material composited by in-situ synthesis Fe-Fe3O4

Legal Events

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

Application publication date: 20180831