CN106783212A - A kind of preparation method of porous carbon electrode - Google Patents

A kind of preparation method of porous carbon electrode Download PDF

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Publication number
CN106783212A
CN106783212A CN201611026419.XA CN201611026419A CN106783212A CN 106783212 A CN106783212 A CN 106783212A CN 201611026419 A CN201611026419 A CN 201611026419A CN 106783212 A CN106783212 A CN 106783212A
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China
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preparation
foil
bonding agent
porous
agent
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CN201611026419.XA
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Inventor
程杰
姚寿广
申亚举
杨裕生
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ZHANGJIAGANG SMARTGRID FANGHUA ELECTRICAL ENERGY STORAGE RESEARCH INSTITUTE Co Ltd
Marine Equipment and Technology Institute Jiangsu University of Science and Technology
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ZHANGJIAGANG SMARTGRID FANGHUA ELECTRICAL ENERGY STORAGE RESEARCH INSTITUTE Co Ltd
Marine Equipment and Technology Institute Jiangsu University of Science and Technology
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Priority to CN201611026419.XA priority Critical patent/CN106783212A/en
Publication of CN106783212A publication Critical patent/CN106783212A/en
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01GCAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES OR LIGHT-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
    • H01G11/32Carbon-based
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/469Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/469Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
    • C02F1/4691Capacitive deionisation
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01GCAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES OR LIGHT-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
    • H01G11/26Electrodes characterised by their structure, e.g. multi-layered, porosity or surface features
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01GCAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES OR LIGHT-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

Abstract

The present invention relates to a kind of preparation method of porous carbon electrode, it is comprised the following steps:(a)After conductive agent, bonding agent and porous charcoal are mixed, solvent and to starch to obtain electrode slurry;The mass ratio of the conductive agent, bonding agent and porous charcoal is 3 ~ 15:2~10:75~95;(b)The electrode slurry is overlayed on conducting matrix grain, is dried and is removed solvent;(c)By step(b)Product be placed in make bonding agent be in melting or semi-molten state at a temperature of, pressurization make the conductive agent, bonding agent and porous charcoal that active layer is formed on the conducting matrix grain.In can so avoiding conventional electrodes from preparing the problems such as incident shedding, poor adhesion, expansion;The method has the advantages that process is simple, steady quality, is particularly suitable for the activated carbon electrodes application and preparation in the directions such as ultracapacitor, condenser type sea water desalination.

Description

A kind of preparation method of porous carbon electrode
Technical field
The invention belongs to energy device electrode material field, and in particular to a kind of preparation method of porous carbon electrode.
Background technology
Many advantages, such as porous carbon material has considerable specific surface area, cheap and high commercial, is to make at present It is the ultracapacitor and the electrode material of condenser type sea water desalination commonly used.Porous carbon material mainly includes activated carbon, carbon airsetting Glue, active carbon fibre peacekeeping cellular glass state carbon etc..Traditional electrode of super capacitor is with the powdery porous charcoal of micron particles Material is main body active material, and a certain proportion of additional conductive agent is added in addition(Such as carbon black, CNT)And binding agent(Such as Polytetrafluoroethylene PTFE, Kynoar PVDF etc.)Prepared by way of sizing mixing-covering;But this method covered compares appearance , there is layer of charcoal peeling, expansion, obscission sometimes in the electrolytic solution in easy shedding, has a strong impact on electrode performance.Or roll and be pressed into charcoal Piece, is then compressed on conductive current collector(Skeleton)Go up or be bonded in conductive current collector, this method has used high level PTFE etc., their energy-storage properties to electrode are not almost contributed, and cause electrode performance to decline yet.
The content of the invention
A kind of preparation method of porous carbon electrode is provided the invention aims to overcome the deficiencies in the prior art.
To solve above technical problem, a kind of technical scheme that the present invention takes is:A kind of preparation side of porous carbon electrode Method, it is comprised the following steps:
(a)After conductive agent, bonding agent and porous charcoal are mixed, solvent and to starch to obtain electrode slurry;The conductive agent, bonding agent and The mass ratio of porous charcoal is 3 ~ 15:2~10:75~95;
(b)The electrode slurry is overlayed on conducting matrix grain, is dried and is removed solvent;
(c)By step(b)Product be placed in make bonding agent be in melting or semi-molten state at a temperature of, pressurization make the conduction Agent, bonding agent and porous charcoal form active layer on the conducting matrix grain.
Optimally, the bonding agent is selected from polypropylene, polyethylene, polyvinyl chloride, styrene acrylic, Ludox, silicon Sour potassium, sodium metasilicate, phosphate, animal glue, casein, gum arabic, water-soluble poly vinyl acetate, water-soluble poly styrene, water One or more composition in dissolubility phenolic resin, polyisobutene, polystyrene, polyacrylate, polyacrylonitrile and polyamide Mixture.
Optimally, the ratio of the gross mass of the conductive agent, bonding agent and porous charcoal and the solvent quality is 1:0.5~ 10。
Further, the viscosity of the electrode slurry is 1500 ~ 3500mPa s.
Further, the viscosity of the electrode slurry is adjusted by being added thereto to thickener, and the thickener is Selected from carboxymethylcellulose calcium, sodium carboxymethylcellulose, potassium carboxymethylcellulose, alginic acid, sodium alginate, potassium alginate, hydroxypropyl One or more mixing of composition in ylmethyl cellulose, hydroxypropyl methyl cellulose sodium and hydroxypropyl methyl cellulose potassium Thing.
Optimally, the conductive agent be selected from graphite powder, acetylene black, chopped carbon fiber, CNT, Graphene, bronze, One or more mixture of composition of silver powder, tantalum powder, conductive titanium oxide and ramet.
Optimally, the solvent is selected from water, methyl alcohol, ethanol, propyl alcohol, butanol, N-METHYLFORMAMIDE, N- crassitudes Ketone, benzene, toluene, acetonitrile, Ethyl formate, ethyl acetate, acetone, butanone, cyclohexanone, fourth lactones, paraxylene, trichloro-benzenes, second One or more mixture of composition in isoamyl valerate, decane, Carbon tetrachloride, chloroform and dimethyl sulfoxide.
Optimally, the conducting matrix grain is titanium net, covers carbon titanium net, stainless (steel) wire, covers carbon stainless steel net, stainless steel foil, punching Hole stainless steel foil, nickel foil, punching nickel foil, nickel screen, aluminium foil, punching aluminium foil, aluminium net, Copper Foil, punching Copper Foil, copper mesh, silver foil, punching Silver foil, silver-colored net, punching titanium-nickel alloy foil, Ti-Ni alloy, Ti-Ni alloy net, lead alloy-foil, punching lead alloy-foil, metal net, Lead net, nickel foam or foam copper.
Optimally, the step(c)In, cooling down during pressurization or after pressurization makes the conductive agent, bonding agent, porous charcoal and leads Electric skeleton secure bond.
Optimally, the step(c)In, bonding agent is in the temperature of melting or semi-molten state in the bonding agent Between softening temperature and its highest melt temperature.
Because above-mentioned technical proposal is used, the present invention has following advantages compared with prior art:Porous charcoal electricity of the present invention The preparation method of pole, slurry is blended into porous charcoal addition conductive agent, bonding agent, slurry is overlayed on conducting matrix grain, then profit Make slurry mix that the active layer being firmly combined with is formed on conducting matrix grain with the mode of bonding agent welding, can so avoid routine In electrode preparation the problems such as incident shedding, poor adhesion, expansion;The method have process is simple, steady quality it is excellent Point, is particularly suitable for the activated carbon electrodes application and preparation in the directions such as ultracapacitor, condenser type sea water desalination.
Specific embodiment
The preparation method of porous carbon electrode of the present invention, it is comprised the following steps:(a)By conductive agent, bonding agent and porous charcoal After mixing, solvent and to starch to obtain electrode slurry;The mass ratio of the conductive agent, bonding agent and porous charcoal is 3 ~ 15:2~10:75~ 95;(b)The electrode slurry is overlayed on conducting matrix grain, is dried and is removed solvent;(c)By step(b)Product be placed in and make bonding At a temperature of agent is in melting or semi-molten state, pressurization makes the conductive agent, bonding agent and porous charcoal in the conducting matrix grain Upper formation active layer.Slurry is blended into porous charcoal addition conductive agent, bonding agent, slurry is overlayed on conducting matrix grain, with Make slurry mix that the active layer being firmly combined with is formed on conducting matrix grain using the mode of bonding agent welding afterwards, can so avoid In conventional electrodes preparation the problems such as incident shedding, poor adhesion, expansion;The method has process is simple, steady quality Advantage, be particularly suitable for the activated carbon electrodes application and preparation in the directions such as ultracapacitor, condenser type sea water desalination.
The bonding agent is preferably selected from polypropylene, polyethylene, polyvinyl chloride, styrene acrylic, Ludox, silicic acid It is potassium, sodium metasilicate, phosphate, animal glue, casein, gum arabic, water-soluble poly vinyl acetate, water-soluble poly styrene, water-soluble Property phenolic resin, polyisobutene, polystyrene, polyacrylate, polyacrylonitrile and polyamide in one or more composition Mixture.The ratio of the gross mass of the conductive agent, bonding agent and porous charcoal and the solvent quality is preferably 1:0.5 ~ 10, with Ensure that the viscosity of electrode slurry is in the preferred scopes of 1500 ~ 3500mPa s.The viscosity of the electrode slurry can by Thickener is wherein added to be adjusted, the thickener is such as selected from carboxymethylcellulose calcium, carboxymethyl from those conventional Sodium cellulosate, potassium carboxymethylcellulose, alginic acid, sodium alginate, potassium alginate, hydroxypropyl methyl cellulose, hydroxypropyl methyl One or more mixture of composition in sodium cellulosate and hydroxypropyl methyl cellulose potassium.
The conductive agent is preferably selected from graphite powder, acetylene black, chopped carbon fiber, CNT, Graphene, bronze, silver One or more mixture of composition of powder, tantalum powder, conductive titanium oxide and ramet, has with the porous carbon electrode for ensuring final Good electric conductivity, to ensure performance when ultracapacitor, condenser type sea water desalination etc. are applied.And the solvent is using conventional Those, such as selected from water, methyl alcohol, ethanol, propyl alcohol, butanol, N-METHYLFORMAMIDE, 1-METHYLPYRROLIDONE, benzene, toluene, Acetonitrile, Ethyl formate, ethyl acetate, acetone, butanone, cyclohexanone, fourth lactones, paraxylene, trichloro-benzenes, isoamyl acetate, the last of the ten Heavenly stems One or more mixture of composition in alkane, Carbon tetrachloride, chloroform and dimethyl sulfoxide, for dissolving or disperseing above-mentioned Conductive agent, bonding agent, porous charcoal and thickener.
The conducting matrix grain is also those conventional, such as titanium net, cover carbon titanium net, stainless (steel) wire, cover carbon stainless steel net, stainless Steel foil, punching stainless steel foil, nickel foil, punching nickel foil, nickel screen, aluminium foil, punching aluminium foil, aluminium net, Copper Foil, punching Copper Foil, copper mesh, silver Paper tinsel, punching silver foil, silver-colored net, punching titanium-nickel alloy foil, Ti-Ni alloy, Ti-Ni alloy net, lead alloy-foil, punching lead alloy-foil, lead Alloy network, lead net, nickel foam or foam copper, thickness are preferably 0.005 ~ 2mm.
Step(c)In, make bonding agent be in melting or semi-molten state temperature be in the bonding agent softening temperature with And its between highest melt temperature, preferably 180 ~ 350 DEG C, can specifically be selected according to the material of bonding agent so that bonding Agent is in melting and/or semi-molten state, such porous charcoal(Or referred to as activated carbon), the bonding agent particle around conductive agent fills Divide welding, make have sufficient cementation between bonding agent and activated carbon granule, conductive agent particle and conducting matrix grain.During pressurization or Cooling makes the conductive agent, bonding agent, porous charcoal and conducting matrix grain secure bond after pressurization, such as can use normal temperature when pressurizeing Air is cooled down, or pressurized equipment is kept for 15 ~ 95 DEG C(Such as the transfer roller of water-cooled roll squeezer), or pressurization after be placed into normal temperature environment immediately In, such chilling makes bonding agent reply solid-state, be also beneficial to keep while keeping its abundant welding to act on bonding agent with it is many Hole charcoal particle, the well-bonded effect between conductive agent particle and conducting matrix grain.It is pre- that pressurization can reach the active layer to be formed Fixed thickness, to reduce stomata, reduce the porosity that solvent volatilization is caused, gives full play to conductive agent between porous charcoal particle And the electronics conduction between porous charcoal particle and conducting matrix grain.
The present invention is further described below in conjunction with embodiment.
Embodiment 1
The present embodiment provides a kind of preparation method of porous carbon electrode, comprises the following steps:
(a)Took the powdered activated carbon 95g of 400 mesh sieves, conductive agent acetylene black 3g, binding agent 2g(By polyethylene, styrene-acrylonitrile copolymer Acid and Ludox in mass ratio 1:1:1 mixes)After mixing, with 50g paraxylene and the mixed liquor of trichloro-benzenes(Volume ratio 1: 1)Sized mixing as solvent ball milling mixing, obtain slurry;
(b)The carbon titanium net of covering that thickness is 0.2mm is pulled through above-mentioned slurry with pulp feeder, the slurry that thickness starches load is adjusted with scraper Tape thickness is in 0.6mm or so;Slurry band dries more than 2h at 150 DEG C, removes solvent;
(c)Above-mentioned dried slurry band is heated to 200 DEG C, binding agent is in semi-molten state, then passed through water Chilling roller press(Transfer roller temperature is kept for 95 DEG C)0.45mm or so is arrived in roll-in, obtains final product the porous carbon electrode for covering active layer.
The porous carbon electrode of above-mentioned preparation can be directly used as condenser type sea water desalination electrode, to cover carbon titanium net as leading The activated carbon electrodes of electric skeleton can tolerate seawater corrosion and electrochemical corrosion.The condenser type sea water desalination experiment of the electrode assembling Model machine, the condenser type sea water desalination that the electrode preparation method that carbon plate Nian Jie with PTFE is used is compressed on conductive current collector is assembled is tested Model machine is compared, internal resistance reduction about more than 25%, and Seawater Treatment ability is significantly improved.
Embodiment 2
The present embodiment provides a kind of preparation method of porous carbon electrode, comprises the following steps:
(a)Powdered activated carbon 75g, the conductive agent acetylene black 15g and binding agent polypropylene 10g of 400 mesh sieves were taken, after three's mixing Thickener sodium carboxymethylcellulose 0.2g is added, is sized mixing as solvent ball milling mixing with 500g isoamyl acetates and is obtained slurry, then Viscosity to 1500mPa s is adjusted with sodium alginate;
(b)The nickel foam of thickness 2mm is pulled through above-mentioned slurry with pulp feeder, the slurry tape thickness that thickness starches load is adjusted with scraper In 2.0mm or so;Slurry band is vacuum dried more than 12h at 60 DEG C, removes solvent;
(c)The above-mentioned disposed slurry band that dries is heated to 250 DEG C, binding agent is in semi-molten state, then passed through water-cooled Roll squeezer(Transfer roller temperature is kept for 45 DEG C)0.7mm or so is arrived in roll-in, obtains final product the porous carbon electrode for covering active layer;
The activated carbon electrodes of above-mentioned preparation can be directly used as ultracapacitor carbon resistance rod, and with potassium hydroxide aqueous solution system As electrolyte.The button ultracapacitor of the electrode assembling, carbon plate Nian Jie with PTFE is used is compressed on the electricity of conductive current collector The button ultracapacitor of pole preparation method assembling is compared, internal resistance reduction about more than 50%.
Embodiment 3
The present embodiment provides a kind of preparation method of porous carbon electrode, comprises the following steps:
(a)Took activated carbon 95g, conductive agent acetylene black 3g and the binding agent 2g of 400 mesh sieves(By polystyrene, polyacrylate In mass ratio 1:1 mixes)Mixing, with 100g chloroforms, cyclohexanone as mixed solvent(Volume ratio 1:1)As solvent Ball milling mixing is sized mixing, and obtains slurry;Viscosity to 3500mPa s is adjusted with sodium alginate;
(b)The carbon titanium net of covering that thickness is 0.1mm is pulled through above-mentioned slurry with pulp feeder, the slurry that thickness starches load is adjusted with scraper Tape thickness is in 0.5mm or so;Slurry band dries more than 2h in 110 DEG C of degree, removes solvent;
(c)Dried slurry band is heated to 200 DEG C, binding agent is in semi-molten state, then passed through water cooled rolls Press(Transfer roller temperature is kept for 15 DEG C)Roll-in obtains final product the porous carbon electrode for covering active layer to 0.4mm or so;
The activated carbon electrodes of above-mentioned preparation can be directly used as condenser type sea water desalination electrode, to cover carbon titanium net as conductive bone The activated carbon electrodes of frame can tolerate seawater corrosion and electrochemical corrosion.The condenser type sea water desalination experiment sample of the electrode assembling Machine, the condenser type sea water desalination that the electrode preparation method that carbon plate Nian Jie with PTFE is used is compressed on conductive current collector is assembled tests sample Machine is compared, internal resistance reduction about more than 30%, and Seawater Treatment ability is significantly improved.
Embodiment 4
The present embodiment provides a kind of preparation method of porous carbon electrode, comprises the following steps:
(a)Took the powdered activated carbon 85g of 400 mesh sieves, conductive agent acetylene black 9g and binding agent 6g(By polystyrene, polychlorostyrene second Alkene, Ludox in mass ratio 1:1:1 mixes)Mixing, with 100g cyclohexanone and the mixed solvent of dimethylformamide(Volume Than 8:2)Sized mixing as solvent ball milling mixing, obtain slurry;Viscosity is adjusted with thickener hydroxypropyl methyl cellulose sodium to arrive 2500mPa•s;
(b)The carbon titanium net of covering of thickness 0.2mm is pulled through above-mentioned slurry with pulp feeder, the slurry band that thickness starches load is adjusted with scraper Thickness is in 0.6mm or so;Slurry band dries more than 2h at 120 DEG C, removes solvent;
(c)Dried slurry is heated to 180 DEG C, binding agent is in semi-molten state;Then passed through water-cooled roll-in Machine(Transfer roller temperature is kept for 15 DEG C)0.4mm or so is arrived in roll-in, obtains final product the porous carbon electrode for covering active layer;
The activated carbon electrodes of above-mentioned preparation can be directly used as condenser type sea water desalination electrode, to cover carbon titanium net as conductive bone The activated carbon electrodes of frame can tolerate seawater corrosion and electrochemical corrosion.The condenser type sea water desalination experiment sample of the electrode assembling Machine, the condenser type sea water desalination that the electrode preparation method that carbon plate Nian Jie with PTFE is used is compressed on conductive current collector is assembled tests sample Machine is compared, internal resistance reduction about more than 50%, and Seawater Treatment ability is significantly improved.
The above embodiments merely illustrate the technical concept and features of the present invention, its object is to allow person skilled in the art Scholar will appreciate that present disclosure and implement according to this that it is not intended to limit the scope of the present invention, all according to the present invention The equivalent change or modification that Spirit Essence is made, should all be included within the scope of the present invention.

Claims (10)

1. a kind of preparation method of porous carbon electrode, it is characterised in that it is comprised the following steps:
(a)After conductive agent, bonding agent and porous charcoal are mixed, solvent and to starch to obtain electrode slurry;The conductive agent, bonding agent and The mass ratio of porous charcoal is 3 ~ 15:2~10:75~95;
(b)The electrode slurry is overlayed on conducting matrix grain, is dried and is removed solvent;
(c)By step(b)Product be placed in make bonding agent be in melting or semi-molten state at a temperature of, pressurization make the conduction Agent, bonding agent and porous charcoal form active layer on the conducting matrix grain.
2. the preparation method of porous carbon electrode according to claim 1, it is characterised in that:The bonding agent is selected from poly- third Alkene, polyethylene, polyvinyl chloride, styrene acrylic, Ludox, potassium silicate, sodium metasilicate, phosphate, animal glue, casein, I Uncle's natural gum, water-soluble poly vinyl acetate, water-soluble poly styrene, water soluble phenol resin, polyisobutene, polystyrene, poly- third One or more mixture of composition in olefin(e) acid ester, polyacrylonitrile and polyamide.
3. the preparation method of porous carbon electrode according to claim 1, it is characterised in that:The conductive agent, bonding agent and The ratio of the gross mass of porous charcoal and the solvent quality is 1:0.5~10.
4. the preparation method of the porous carbon electrode according to claim 1 or 3, it is characterised in that:The electrode slurry it is viscous It is 1500 ~ 3500mPa s to spend.
5. the preparation method of porous carbon electrode according to claim 4, it is characterised in that:The viscosity of the electrode slurry is led to Cross and be added thereto to thickener and be adjusted, the thickener is selected from carboxymethylcellulose calcium, sodium carboxymethylcellulose, carboxymethyl Cellulose potassium, alginic acid, sodium alginate, potassium alginate, hydroxypropyl methyl cellulose, hydroxypropyl methyl cellulose sodium and hydroxypropyl One or more mixture of composition in methylcellulose potassium.
6. the preparation method of porous carbon electrode according to claim 1, it is characterised in that:The conductive agent is selected from graphite One kind of powder, acetylene black, chopped carbon fiber, CNT, Graphene, bronze, silver powder, tantalum powder, conductive titanium oxide and ramet Or the mixture of various compositions.
7. the preparation method of porous carbon electrode according to claim 1, it is characterised in that:The solvent is selected from water, first Alcohol, ethanol, propyl alcohol, butanol, N-METHYLFORMAMIDE, 1-METHYLPYRROLIDONE, benzene, toluene, acetonitrile, Ethyl formate, ethyl acetate, Acetone, butanone, cyclohexanone, fourth lactones, paraxylene, trichloro-benzenes, isoamyl acetate, decane, Carbon tetrachloride, chloroform and two One or more mixture of composition in first sulfoxide.
8. the preparation method of porous carbon electrode according to claim 1, it is characterised in that:The conducting matrix grain be titanium net, Cover carbon titanium net, stainless (steel) wire, cover carbon stainless steel net, stainless steel foil, punching stainless steel foil, nickel foil, punching nickel foil, nickel screen, aluminium foil, Punching aluminium foil, aluminium net, Copper Foil, punching Copper Foil, copper mesh, silver foil, punching silver foil, silver-colored net, punching titanium-nickel alloy foil, Ti-Ni alloy, Ti-Ni alloy net, lead alloy-foil, punching lead alloy-foil, metal net, lead net, nickel foam or foam copper.
9. the preparation method of porous carbon electrode according to claim 1, it is characterised in that:The step(c)In, during pressurization Or cooling makes the conductive agent, bonding agent, porous charcoal and conducting matrix grain secure bond after pressurization.
10. the preparation method of porous carbon electrode according to claim 1, it is characterised in that:The step(c)In, make to glue Connect agent and be in the temperature of melting or semi-molten state between the bonding agent softening temperature and its highest melt temperature.
CN201611026419.XA 2016-11-22 2016-11-22 A kind of preparation method of porous carbon electrode Pending CN106783212A (en)

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CN109721137A (en) * 2019-02-22 2019-05-07 辽宁科技大学 Electric Fenton combination electrode and preparation method thereof
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