WO2014101863A1 - Battery electrode having auxiliary electrode structure, and high-power battery - Google Patents

Battery electrode having auxiliary electrode structure, and high-power battery Download PDF

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Publication number
WO2014101863A1
WO2014101863A1 PCT/CN2013/090851 CN2013090851W WO2014101863A1 WO 2014101863 A1 WO2014101863 A1 WO 2014101863A1 CN 2013090851 W CN2013090851 W CN 2013090851W WO 2014101863 A1 WO2014101863 A1 WO 2014101863A1
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WIPO (PCT)
Prior art keywords
electrode
battery
auxiliary
auxiliary electrode
negative electrode
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PCT/CN2013/090851
Other languages
French (fr)
Chinese (zh)
Inventor
刘军
陈勇
Original Assignee
Liu Jun
Chen Yong
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Publication of WO2014101863A1 publication Critical patent/WO2014101863A1/en

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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M16/00Structural combinations of different types of electrochemical generators
    • H01M16/003Structural combinations of different types of electrochemical generators of fuel cells with other electrochemical devices, e.g. capacitors, electrolysers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04313Processes for controlling fuel cells or fuel cell systems characterised by the detection or assessment of variables; characterised by the detection or assessment of failure or abnormal function
    • H01M8/04537Electric variables
    • H01M8/04604Power, energy, capacity or load
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04694Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
    • H01M8/04858Electric variables
    • H01M8/04895Current
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/20Indirect fuel cells, e.g. fuel cells with redox couple being irreversible
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/425Structural combination with electronic components, e.g. electronic circuits integrated to the outside of the casing
    • H01M2010/4271Battery management systems including electronic circuits, e.g. control of current or voltage to keep battery in healthy state, cell balancing
    • 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
    • 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
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Definitions

  • the invention belongs to the technical field of new energy batteries, and relates to a battery electrode with an auxiliary electrode structure and a high power battery thereof for increasing the power density of a liquid flow battery.
  • the fluid battery can directly convert the chemical energy in the liquid stream into electrical energy by discharging the reducing agent and the oxidizing agent on the electrodes on both sides of the battery. Since the energy is stored in the electrolyte of the battery, it can be stored separately by energy. To achieve unlimited battery capacity, which is suitable for large-scale energy storage, peaking of the power grid is a very promising technology relative to air energy storage and storage energy storage.
  • the main flow batteries are multi-gram sodium/bromo batteries and all-vanadium flow batteries and the like. However, due to the characteristics of the electrode itself, the discharge power density is very low.
  • the output current per unit area of the electrode of the vanadium redox flow battery is only 80 mA/cm 2 , and the output power is only 0.08 ⁇ 0.1 W/CM 2 .
  • the hydrogen fuel cell has an output power of 0.4 to 0.6 W/cm 2 in the case of a platinum catalyst.
  • These batteries have to be used because of the use of expensive perfluorinated S-resin membranes and precious metal catalysts. Further, the flow battery and the fuel battery cannot be applied on a large scale. However, in the case where the cost of other materials cannot be rapidly reduced, it is important to increase the power density per unit area of the same battery electrode to reduce the cost of the battery system. Summary of the invention
  • the present invention provides a battery electrode having an auxiliary electrode structure and a high power battery thereof which improve battery power density and reduce battery cost.
  • a battery electrode having an auxiliary electrode structure includes a positive electrode, a negative electrode, an electrode separator disposed between the positive electrode and the negative electrode, and an auxiliary electrode;
  • the auxiliary electrode includes a positive electrode auxiliary Electrode and/or negative auxiliary electrode;
  • the positive electrode auxiliary electrode is disposed on an inner side of the positive electrode side, and the positive electrode and the positive electrode are assisted a first diaphragm is disposed between the electrodes;
  • the negative electrode auxiliary electrode is disposed inside the negative electrode side, and a second separator is disposed between the negative electrode and the negative electrode auxiliary electrode.
  • the present invention provides a high-power battery, including a battery case, a positive electrode electrolytic solution, a negative electrode electrolytic solution, and a battery electrode according to the above technical solution, which are disposed in a cavity surrounded by the battery case;
  • the electrode separator is disposed between the positive electrode electrolytic solution and the negative electrode electrolytic solution, and further includes a battery system parameter sensor and a battery control system.
  • the pole, the battery system parameter sensor and the battery control system, the battery working interval is divided into two sections.
  • the battery working output current is supplied to the battery control system and stored by the control system.
  • the internal circuit of the battery control system divides the stored energy into two parts.
  • the energy ratio of the two parts is adjusted by the controller software or manually adjusted; some of them are rectified and outputted externally, and the other part is reduced by the internal battery active substance conversion circuit to obtain a low voltage current for feedback to the electrodes of the battery and Corresponding auxiliary electrode; when the battery outputs for a certain period of time, the external output current is stopped, and the stored part of the stored electric energy is supplied to the corresponding auxiliary electrode and the electrode of the battery with a certain low voltage current, so that the electrode active in the negative electrode region of the battery
  • the substance is oxidized on the negative electrode while obtaining a higher discharge activity on the auxiliary electrode and a positive electrode material having higher discharge activity at the auxiliary electrode, thereby realizing conversion of the electrode active material during discharge of the battery; when the active substance is converted in the system controller Circuit After completion of the storage of the power consumption, the battery enters the discharging state again, so the cycle to continue; work cell belonging to the intermittent output, the entire battery system is continuously output.
  • the battery has a positive electrode, a negative electrode, a positive electrode auxiliary electrode, a negative electrode auxiliary electrode, a battery separator, a battery state sensor, and a battery system controller; a first porous diaphragm is disposed between the positive electrode and the positive electrode auxiliary electrode, a second porous diaphragm is disposed between the negative electrode and the negative electrode auxiliary electrode; the battery state sensor is configured to convert an operating state of the battery; and the battery system controller is configured to control the positive electrode, the negative electrode, the positive electrode auxiliary electrode, and the negative electrode auxiliary The electrode works.
  • the battery system controller includes an active material conversion circuit, an external discharge circuit, an energy storage module, and a sensor circuit;
  • the sensor includes a temperature sensor, an electrolyte flow rate sensor, an electrolyte concentration sensor, and electricity Deconstruction component sensor.
  • a first porous separator that is in contact with each other, a positive electrode auxiliary electrode that is in contact with the first porous membrane, an ion exchange membrane that is in contact with the positive electrode auxiliary electrode, a negative electrode auxiliary electrode that is in contact with the ion exchange membrane, a second porous separator that is in contact with the negative electrode auxiliary electrode, and a negative electrode that is in contact with the second porous membrane;
  • the battery having the auxiliary electrode structure includes a positive electrode, a first porous separator that is in contact with the positive electrode, a positive electrode auxiliary electrode that is in contact with the first porous separator, and a positive electrode auxiliary electrode.
  • the battery having the auxiliary electrode structure may be in the form of only the positive electrode region adopting the auxiliary auxiliary structure electrode, or only the negative electrode region may be in the form of adding the auxiliary structure electrode, or the positive electrode and the negative electrode region may be in the form of adding the auxiliary structure electrode.
  • both the positive electrode auxiliary electrode and the negative electrode auxiliary electrode have an extremely large microscopic surface area and are suitable for high-power discharge.
  • the electrode potential of the negative electrode auxiliary electrode is similar to the electrode potential of the fluid battery active material in the electrolyte system and the negative electrode region, and the discharge power of the electrode can be greatly improved after the electrode active material is converted.
  • the anode auxiliary electrode is Pb/PbS0 4
  • the electrode potential is similar to the V(II)/V(III) electrode potential of the negative vanadium flow battery, but the metal lead electrode discharge power is Greatly accelerated.
  • the electrode potential of the pole auxiliary electrode of the positive electrode is similar to the electrode potential of the active material of the fluid itself in the electrolyte system, for example, in the all-vanadium flow battery, the positive electrode auxiliary electrode can be adsorbed by the porous carbon electrode.
  • a certain concentration of [3 ⁇ 4 prime element forms Br 2 /Br_, or forms a low concentration of ci 2 /cr.
  • the positive electrode auxiliary electrode and the positive electrode are separated by a porous separator between the negative electrode auxiliary electrode and the negative electrode.
  • the battery having the auxiliary electrode structure has an ion exchange membrane or a porous membrane between the positive electrode and the negative electrode for isolating the electrolyte in the positive electrode and the negative electrode region.
  • the battery with the auxiliary electrode structure can cooperate in the control system and the auxiliary electrode
  • the liquid active material flowing through the surface of the electrode is completely discharged, so that a porous membrane can be used instead of the ion exchange membrane between the positive electrode and the negative electrode of the full flow battery.
  • the current supplied to the electrode/auxiliary electrode has a current voltage of 0.1 to 0.5V.
  • the active material conversion circuit charges the electrode/auxiliary electrode for 0.1 second to 60 minutes.
  • liquid flow rechargeable battery liquid flow fuel cell, metal air fuel cell, direct oxime fuel cell, hydrogen fuel cell, etc.
  • the power supply of the battery pack automatic control system is provided by the battery itself.
  • the positive effects of the present invention are: using a battery pack having an auxiliary electrolytic electrode structure to greatly increase the output power of the battery by changing the real discharge electrode of the battery, thereby reducing the flow charging battery, the liquid flow fuel cell, and the metal under other conditions.
  • the cost of an air fuel cell, a battery such as a direct fuel cell fuel cell or a hydrogen fuel cell; the application of this type of electrode structure to a fuel cell fueled by reforming hydrogen gas can reduce a small amount of CO in a conventional reformer and lead to a catalyst containing a precious metal.
  • Electrolyte poisoning problem this type of electrode structure is applied to a fuel cell fueled by direct sterol, which can prevent the intermediate product generated in the catalytic oxidation of sterol of the noble metal catalyst from causing poisoning of the noble metal catalytic electrode.
  • the invention provides a battery electrode with an auxiliary electrode structure and a high-power battery thereof, and belongs to the technical field of new energy batteries, and relates to a battery electrode for improving the power density of a liquid flow battery, and the liquid flow using the electrode structure
  • Both the secondary battery and the fuel cell can increase the output power and reduce the cost of the secondary fluid battery and the fuel cell for energy storage; using the electrode structure can also improve the direct sterol fuel cell and hydrogen The output power of the fuel cell.
  • the invention adopts an auxiliary electrode and a battery control system to increase the discharge power of the flow battery and the fuel cell electrode, and increase the power density of the battery, thereby reducing the battery cost.
  • the present invention provides a battery electrode having an auxiliary electrode structure including a positive electrode, a negative electrode, an electrode separator disposed between the positive electrode and the negative electrode, and an auxiliary electrode;
  • the auxiliary electrode includes a positive electrode auxiliary electrode and/or a negative electrode auxiliary electrode;
  • the positive electrode auxiliary electrode is disposed on an inner side of the positive electrode side, and a first porous separator is disposed between the positive electrode and the positive electrode auxiliary electrode;
  • the negative electrode auxiliary electrode is disposed inside the negative electrode side, and a second porous separator is disposed between the negative electrode and the negative electrode auxiliary electrode.
  • Schematic diagram wherein 11 is the negative electrode, 13 is the negative electrode auxiliary electrode, 6 is the positive electrode, 7 is the positive electrode auxiliary electrode, 10 is the second porous separator, 14 is the negative electrode auxiliary electrode, and 15 is the ion exchange membrane.
  • the type and source of the positive electrode, the negative electrode and the electrode separator are not particularly limited, and the battery positive electrode, the negative electrode and the electrode separator which are well known to those skilled in the art may be used, such as a positive electrode in a flow battery or a fuel cell, Negative electrode and electrode separator.
  • the graphite sheet collector when the battery is a vanadium flow battery, the graphite sheet collector may be used, and the polypropylene fiber carbon felt electrode is used as a negative electrode, and the positive electrode may be a collector obtained from a metal titanium mesh.
  • a zinc electrode such as a porous metal zinc plate, may be used as a negative electrode; the positive electrode may be a slurry obtained by mixing carbon black, activated carbon, ⁇ 11 0 2 and polytetrafluoroethylene resin.
  • the positive electrode obtained by spraying onto the nickel collecting electrode preferably has a mass ratio of carbon black, activated carbon, MnO 2 and polytetrafluoroethylene resin of 30:40:25:5.
  • the electrode separator is used to isolate the electrolyte body of the positive electrode region and the negative electrode region, and the electrode separator is preferably an ion exchange membrane or a porous separator.
  • the porous separator between the separator and the electrode and the auxiliary electrode the porous membrane used as the electrode separator in the present invention is named as the third porous membrane.
  • the battery electrode having the auxiliary electrode structure includes, in order, a positive electrode, a first porous separator that is in contact with the positive electrode, and the first porous membrane. a positive electrode auxiliary electrode that is in contact with each other, an ion exchange membrane that is in contact with the positive electrode auxiliary electrode, a negative electrode auxiliary electrode that is in contact with the ion exchange membrane, a second porous separator that is in contact with the negative electrode auxiliary electrode, and The second porous membrane is connected to the negative electrode.
  • the structural arrangement therein is a positive electrode, a first porous separator, a positive electrode auxiliary electrode, an ion exchange membrane, a negative electrode auxiliary electrode, a second porous membrane, and a negative electrode;
  • the battery electrode having the auxiliary electrode structure preferably includes a positive electrode, a first porous membrane that is in contact with the positive electrode, and a first porous membrane.
  • the structural arrangement therein is a positive electrode, a first porous separator, a positive electrode auxiliary electrode, a third porous separator, a negative electrode auxiliary electrode, a second porous separator, and a negative electrode.
  • the negative electrode auxiliary electrode when the battery is a vanadium flow electrode, the negative electrode auxiliary electrode may be a lead electrode, such as porous metal foam, and the positive electrode auxiliary electrode may be a polypropylene fiber carbon felt;
  • the positive electrode auxiliary electrode When the battery is a zinc-air battery, the positive electrode auxiliary electrode may be sprayed on a nickel collector by a mixture of carbon black, activated carbon, NiO and polytetrafluoroethylene resin, dried at 80 ° C, and then rolled.
  • the positive electrode auxiliary electrode preferably has a mass ratio of carbon black, activated carbon, NiO, and polytetrafluoroethylene resin of 30:40:25:5.
  • the first porous membrane, the second porous membrane, and the third porous membrane are preferably independently selected from the group consisting of porous fibers, as in the embodiment of the invention, the first porous membrane, the second porous membrane, and the first
  • the three porous membrane may be a polypropylene carbon fiber felt.
  • the battery electrode having the auxiliary electrode structure may be a battery electrode obtained by adding only the positive electrode auxiliary electrode and the first porous separator, or may be a negative electrode auxiliary electrode and a second porous separator.
  • the battery electrode may be a battery electrode in which a positive electrode auxiliary electrode, a first porous separator, a negative electrode auxiliary electrode, and a second porous separator are simultaneously added, which is not particularly limited in the present invention.
  • the present invention provides a high-power battery, comprising a battery case, a positive electrode electrolytic solution, a negative electrode electrolytic solution, and a battery electrode disposed in the above-mentioned technical solution and a cavity surrounded by the battery case, the battery electrode One end is led out by a wire; an electrode separator in the battery electrode is disposed between the positive electrode electrolytic solution and the negative electrode electrolytic solution, and further includes a battery system parameter sensor and a battery control system.
  • the high power battery provided by the invention is in the positive electrode region and/or the negative electrode of the flow battery or fuel cell
  • the area is provided with an auxiliary electrode, a battery state sensor and a battery control system.
  • the battery operation interval is divided into two sections. First, the battery operation output current is supplied to the battery control system and stored by the control system. The energy stored in the internal circuit of the battery control system is stored. Divided into two parts, the energy ratio of the two parts is controlled by the battery control system software or manually adjusted; some of them are rectified and outputted externally, and the other part is reduced by the internal battery active substance conversion circuit to obtain a low voltage current.
  • the external output current is stopped, and the stored part of the electric energy is supplied to the auxiliary electrode and the electrode corresponding to the battery with a certain low voltage current, so that the electrode active material in the negative electrode region of the battery is oxidized on the negative electrode.
  • an electrode active material with higher discharge activity is obtained on the auxiliary electrode; similarly, the electrode active material with low discharge activity in the positive electrode region of the battery is reduced on the positive electrode and a positive electrode material with higher discharge activity is obtained at the auxiliary electrode, thereby realizing battery discharge.
  • FIG. 2 is a cross-sectional view of the battery having the auxiliary electrode structure shown in FIG. 1. In FIG. 1
  • 1, 1 is a pump, 2 is an inlet, 3 is an outlet, 4 is a negative electrode region, and 5 is a positive electrode region;
  • 6 is the positive electrode
  • 7 is the positive electrode auxiliary electrode
  • 8 is the positive electrode electrolytic solution
  • 9 is the positive electrode auxiliary electrode
  • 10 is the separator
  • 11 is the negative electrode
  • 12 is the negative electrode electrolytic solution
  • 13 is the negative electrode auxiliary electrode
  • 14 is the negative electrode auxiliary electrode
  • 15 is an ion exchange membrane.
  • the high-power battery provided by the present invention includes a battery case.
  • the shape, size and material of the battery case are not particularly limited in the present invention, and a battery case known to those skilled in the art may be used, such as the battery case.
  • the material may be an ABS plastic plate, and the battery case may have a rectangular parallelepiped shape.
  • the battery has a positive electrode, a negative electrode, a positive electrode auxiliary electrode, a negative electrode auxiliary electrode, a battery separator, a positive electrode electrolytic solution, a negative electrode electrolytic solution, a battery state sensor, and a battery system controller; and the battery system controller includes An active material conversion circuit, an external discharge circuit, an energy storage module, and a sensor circuit; in the present invention, the battery system controller receives a current outputted by the battery, and the received current is stored by the energy storage module, and is stored The energy is divided into two parts, the energy ratio of the two parts is adjusted by the battery control system software or manually adjusted; A portion of the energy is rectified and outputted to the outside through the external discharge circuit, and another portion is reduced in voltage by the active material conversion circuit to obtain a low voltage current, and the low voltage current is supplied to the electrode and the corresponding auxiliary electrode, and the active material is converted.
  • the circuit charges the electrode/auxiliary electrode.
  • the positive electrode is connected to a positive terminal of the battery system controller
  • the negative electrode is connected to a negative terminal of the battery system controller
  • the positive auxiliary electrode and the battery system are controlled.
  • a positive auxiliary electrode terminal is connected to the negative electrode auxiliary electrode and a negative auxiliary electrode terminal in the battery system controller.
  • the current supplied to the electrode/auxiliary electrode is preferably 0.1 V to 0.5 V, more preferably 0.2 V to 0.4 V; and the time during which the active material conversion circuit charges the electrode/auxiliary electrode is preferably It is from 0.1 second to 60 minutes, more preferably from 1 second to 55 minutes, and most preferably from 10 seconds to 50 minutes.
  • the battery state sensor includes a temperature sensor, an electrolyte flow rate sensor, an electrolyte concentration sensor, and an electrolyte composition sensor for sensing and adjusting an operating temperature of the battery, a flow rate of the electrolyte, a concentration of the electrolyte, and a composition of the electrolyte, Thereby adjusting the working state of the battery.
  • the electrode system in the battery having the auxiliary electrode structure is the battery electrode having the auxiliary electrode structure described in the above technical solution, and the battery having the auxiliary electrode structure may be only the positive electrode region adopting the auxiliary structure.
  • the negative electrode region may be in the form of an auxiliary structure electrode, or the positive electrode and the negative electrode region may be in the form of an auxiliary structure electrode, and no particular limitation is imposed on the invention.
  • the type of the positive electrode electrolyte body and the negative electrode electrolyte body of the present invention is not particularly limited, and an electrolyte solution well known to those skilled in the art may be used.
  • the positive electrode electrolyte body and the negative electrode electrolyte body may be a potassium hydroxide solution having a mass concentration of 30%; when the battery is a vanadium flow battery
  • the positive electrode electrolyte body includes V0 2 + , 2 mol/L of sulphuric acid and 0.5 mol/L in a molar concentration of 2 mol/L. ⁇
  • the negative electrode electrolyte body includes V 2+ , 2 mol/L sulfuric acid, and 0.5 mol/L Cl_ at a molar concentration of 2 mol/L.
  • the battery case may be provided with an opening, which is an inlet of an electrolyte and an outlet of an electrolyte.
  • a positive electrode region of the battery case is provided with an electrolyte inlet of a positive electrode region.
  • a positive electrode region electrolyte outlet; the negative electrode region of the battery case is provided with a negative electrode region electrolyte inlet and a negative electrode region electrolyte outlet.
  • the positive electrode region electrolyte is advanced An electrolyte outlet of the port and the positive electrode region is disposed on a sidewall on the same side of the battery case, the electrolyte inlet of the positive electrode region is disposed below the electrolyte outlet of the positive electrode region; and the electrolyte inlet and the negative electrode region of the negative electrode region are electrolyzed
  • the liquid outlet is disposed on a side wall of the same side of the battery case, and the negative electrode area electrolyte inlet is disposed below the electrolyte outlet of the negative electrode area.
  • a pump is installed at the inlet of the electrolyte. Specifically, a first pump is installed at the inlet of the electrolyte in the positive electrode region, and an electrolyte is disposed in the negative electrode region. A second pump is installed at the inlet.
  • both the positive electrode auxiliary electrode and the negative electrode auxiliary electrode have an extremely large microscopic surface area and are suitable for high-power discharge.
  • the electrode potential of the negative electrode auxiliary electrode is similar to the electrode potential of the fluid battery active material in the negative electrode region, and the discharge of the electrode can be improved after the electrode active material is converted. power.
  • the negative auxiliary electrode pair is Pb/PbS0 4
  • the electrode potential of the electrode pair Pb/PbS0 4 and the total vanadium flow battery negative electrode region electrode pair V The electrode potentials of (II)/V(III) are similar, and the discharge power of the metal lead electrode is greatly accelerated.
  • the electrode potential of the positive electrode auxiliary electrode is close to the electrode potential of the active material of the fluid itself, and the discharge power of the electrode can be provided after the electrode active material is converted.
  • the positive electrode auxiliary electrode may adsorb a certain concentration of halogen element to form a Br 2 /Br- or a low concentration of C1 2 /C1_ for the porous carbon electrode.
  • the electrode potential pair and the V(IV)/V(V) potential are similar to the electrode potential, and the former has a much higher discharge power than the latter.
  • a porous separator is isolated between the negative electrode auxiliary electrode and the negative electrode.
  • the battery having the auxiliary electrode structure has an ion exchange membrane or a porous separator between the positive electrode and the negative electrode for isolating the electrolyte in the positive electrode and the negative electrode region.
  • the battery with the auxiliary electrode structure can completely discharge the liquid active material flowing through the electrode surface under the joint action of the control system and the auxiliary electrode, so a porous diaphragm can be used instead of the positive electrode and the negative electrode of the full flow battery.
  • Ion exchange membrane The output power of batteries, liquid fuel cells, metal air fuel cells, direct methanol fuel cells, hydrogen fuel cells, etc.
  • the battery control system in the high power battery having the auxiliary electrode structure provided by the present invention is preferably an automatic control system, and the power supply of the automatic control system is preferably provided by the battery itself.
  • the invention uses the battery pack with the auxiliary electrolysis electrode structure to greatly increase the output power of the battery by changing the real discharge electrode of the battery, thereby reducing the flow charging battery, the liquid flow fuel cell, the metal air fuel cell directly under other conditions.
  • the cost of a battery such as a sterol fuel cell or a hydrogen fuel cell; applying this type of electrode structure to a fuel cell fueled by reforming hydrogen can reduce the problem of electrode poisoning of a noble metal-containing catalyst caused by a small amount of CO in a conventional reformer;
  • This type of electrode structure is applied to a fuel cell fueled by direct sterol, which can prevent the noble metal catalyst from poisoning problems caused by intermediate products generated in the catalytic oxidation of sterol.
  • the battery electrode having the auxiliary electrode structure and the high power battery thereof provided by the present invention are described in detail below with reference to the embodiments, but they are not to be construed as limiting the scope of the present invention.
  • the following embodiment employs the structure shown in Figs. 1 to 3 to prepare a battery having an auxiliary electrode structure.
  • a plastic groove of 20 mm long x 100 mm x 20 is made of ABS plastic plate and a proton exchange membrane is installed in the middle of the groove as a separator for the fluid battery, and the plastic tank is divided into 10 X 100 X 150 mm.
  • the two parts are respectively a negative electrode region and a positive electrode region, and the side walls of the two portions are respectively opened to form an inlet and outlet of the fluid battery electrolyte, and the corresponding micro pump is connected as a circulating pump of the electrolyte;
  • a graphite sheet having a length X width of 100 X 150 mm and a thickness of 1 mm was used as a collecting electrode, and was cut into a 150 150 electrode by heat treatment at 400 ° C for 24 hours.
  • a porous fiber cloth having a length X and a width of 105 X 155 mm was cut as a separator.
  • a porous metal foam lead having a length x width of 100 X 150 mm and a thickness of 1 mm was used as the negative electrode auxiliary electrode.
  • the graphite collector, the polypropylene carbon fiber felt electrode, the separator, and the auxiliary lead electrode are pressed in order and placed in the negative electrode region of the processed plastic tank.
  • a metal titanium mesh having a length X width of 100 X 150 mm and a thickness of 1 mm is used as a collector to The polypropylene carbon fiber felt was heat-treated at 400 ° C for 24 hours, and then heat-treated and then cut into 100 150, which were a positive electrode and a positive electrode auxiliary electrode, respectively.
  • a porous fiber cloth having a length X width of 105 X 155 mm was cut as a separator.
  • the titanium mesh collector, the polyacrylonitrile carbon fiber felt positive auxiliary electrode, the separator, and the polypropylene carbon fiber felt positive electrode are pressed in order and placed in the positive electrode region of the processed plastic tank.
  • the electrolyte component in the negative electrode region is 2 mol/L of V 2+ , 2 mol/L of sulphuric acid, and 0.5 mol/L of CT; the electrolyte in the positive electrode region is 2 mol/L of V0 2 + , 2 mol/L of sulfuric acid, 0.5 mol/L of Cr.
  • the auxiliary electrodes in the battery are respectively connected to the terminals of the corresponding auxiliary electrodes of the control system, and the electrodes are respectively connected with the corresponding terminals of the control system, and connected to the electrolyte circulation system to obtain the auxiliary electrode structure.
  • the voltage output from the control system to the positive/positive auxiliary electrode is 0.2 volts.
  • the reaction in the positive electrode region is vo 2 + +cr- - vo 2+ + ci 2 (adsorbed by the polypropylene-based carbon felt electrode).
  • the ci 2 in the adsorbed state at the time of discharge is discharged through the positive electrode of the polypropylene fiber carbon fiber felt.
  • the output voltage of the control system to the negative/negative auxiliary electrode is 0.1 volt, and the reaction occurs at this time as PbS0 4 + 2V 2+ - Pb + S0 4 2 " + 2V 3+ , which is discharged by the metal lead electrode during discharge.
  • the charging and discharging time of the control system to the battery pack is intelligently controlled by the magnitude of the load power, so that the battery operates at the maximum efficiency.
  • the operation of the auxiliary electrode makes the average output power of the entire vanadium flow battery more than the vanadium without the auxiliary electrode.
  • the output power of the flow battery is increased by 5 times.
  • the electrode structure of the battery is changed from a common all-vanadium flow battery structure to a metal lead/chlorine battery structure.
  • a plastic groove of length X width X height 100 X 50 X 70 mm is made of ABS plastic plate and a hole of 80 60 is opened in one side wall of the groove.
  • the foamed nickel with a length X width of 90 60 mm and a thickness of 1 mm is used as a collector, and then carbon black, activated carbon, NiO, and polytetrafluoroethylene resin are arranged in a ratio of 35:35:15:15.
  • the material was uniformly sprayed onto the foamed nickel collector by spraying, and dried at 80 ° C and then rolled to obtain a positive electrode auxiliary electrode.
  • the same processing size length X width is 90 X 60mm, the thickness of lmm foam nickel is the collector, and then (3 crystal carbon black, activated carbon and Mn0 2 , polytetrafluoroethylene resin according to 30:30: 15: 25
  • the ratio is configured such that the slurry is uniformly sprayed onto the foamed nickel collector by spraying, and is sufficiently dried after being dried at 80 ° C to obtain a positive electrode.
  • the porous fiber cloth having a length X width of 90 X 60 mm is cut.
  • the positive electrode auxiliary electrode, the separator, and the positive electrode are pressed in order and fixed at the opening of the plastic tank and will be positive.
  • the gap between the pole and the plastic groove is sealed so that the positive electrode auxiliary electrode faces the inside of the plastic groove.
  • the porous metal zinc plate is a negative electrode.
  • the auxiliary electrodes in the battery are respectively connected to the corresponding auxiliary electrode terminals of the control system, and the positive and negative electrodes are respectively connected to the electrode terminals corresponding to the control system to obtain the zinc air fuel cell having the auxiliary electrode structure.
  • the voltage output from the control system to the positive/positive auxiliary electrode is 0.2 volts.
  • the reaction in the positive electrode region is NiO + MnO(OH) - NiO(OH) + ⁇ , 0 2 (from air) + MnO MnO(OH) is discharged through the positive electrode auxiliary electrode during discharge.
  • the zinc-air battery has an output voltage of 1.7V, which is about 0.3V higher than the direct output voltage of a normal zinc-air battery.
  • the charging and discharging time of the control system to the battery pack is intelligently controlled by the magnitude of the load power.
  • the battery electrode structure is converted from a common metal zinc electrode/air electrode structure to a metal zinc electrode/hydroxyl group. Nickel oxide electrode structure.

Abstract

The present invention relates to a battery electrode having an auxiliary electrode structure, and a high-power battery. An auxiliary electrode, a battery system parameter sensor and a battery control system are provided in an anode area and/or a cathode area of a flow battery or a fuel cell, and the working time interval of the battery is divided into two sections. First, the battery works to output current to the battery control system and the current is stored by the control system, the stored energy is divided into two parts by a circuit inside the battery control system, and the energy ratio of the two parts is adjusted in a braked way by controller software or manually adjusted; the battery reenters a discharging state after electric energy stored in an active material conversion circuit in the system controller is used up, and the above process is repeated continuously; the battery in working belongs to intermittent output and the whole battery system belongs to continuous output. The power density of the battery is increased, and the battery cost is reduced.

Description

一种具有辅助电极结构的电池电极及其高功率电池  Battery electrode with auxiliary electrode structure and high power battery thereof
本申请要求于 2012 年 12 月 31 日提交中国专利局、 申请号为 201210588983.6、 发明名称为 "一种具有辅助电极结构的电池电极及其高功率 电池" 的中国专利申请的优先权, 其全部内容通过引用结合在本申请中。 技术领域  This application claims priority to Chinese Patent Application No. 201210588983.6, entitled "A Battery Electrode with Auxiliary Electrode Structure and Its High Power Battery", filed on December 31, 2012, the entire contents of which is hereby incorporated by reference. This is incorporated herein by reference. Technical field
本发明属于新能源电池技术领域,涉及一种用来提高液流电池功率密度的 具有辅助电极结构的电池电极及其高功率电池。  The invention belongs to the technical field of new energy batteries, and relates to a battery electrode with an auxiliary electrode structure and a high power battery thereof for increasing the power density of a liquid flow battery.
背景技术 Background technique
流体电池能通过把还原剂和氧化剂分别在电池的两侧电极上放电实现将 液流中的化学能直接转变为电能, 由于能量是存储在电池的电解液中, 所以它 能通过将能量分别存储而达到无限制提高电池容量的方法,从而适合大规模能 量存储, 对电网的调峰相对于空气能储能和蓄水储能是一个非常有前景的技 术。 目前主要的液流电池有多石克化钠 /溴电池和全钒液流电池等类型的流体电 池。 然而由于液流电池由于电极本身的特点导致放电功率密度很低,如全钒液 流电池电极上单位面积上的输出电流只有 80mA/CM2, 输出功率只有 0.08 ~ 0.1W/CM2。 而氢燃料电池在使用白金催化剂的情况下只有 0.4 ~ 0.6 W/CM2的 输出功率。这些电池由于都要使用昂贵的全氟横 S史树脂膜,及贵金属催化剂的 原因, 导致电池成本无法降低。 进而使得液流电池, 燃料电池并不能大规模的 应用。 而在其他材料成本不能快速降低的情况下,提高同等电池电极单位面积 上的功率密度对降低电池系统的成本就意义重大。 发明内容 The fluid battery can directly convert the chemical energy in the liquid stream into electrical energy by discharging the reducing agent and the oxidizing agent on the electrodes on both sides of the battery. Since the energy is stored in the electrolyte of the battery, it can be stored separately by energy. To achieve unlimited battery capacity, which is suitable for large-scale energy storage, peaking of the power grid is a very promising technology relative to air energy storage and storage energy storage. At present, the main flow batteries are multi-gram sodium/bromo batteries and all-vanadium flow batteries and the like. However, due to the characteristics of the electrode itself, the discharge power density is very low. For example, the output current per unit area of the electrode of the vanadium redox flow battery is only 80 mA/cm 2 , and the output power is only 0.08 ~ 0.1 W/CM 2 . The hydrogen fuel cell has an output power of 0.4 to 0.6 W/cm 2 in the case of a platinum catalyst. These batteries have to be used because of the use of expensive perfluorinated S-resin membranes and precious metal catalysts. Further, the flow battery and the fuel battery cannot be applied on a large scale. However, in the case where the cost of other materials cannot be rapidly reduced, it is important to increase the power density per unit area of the same battery electrode to reduce the cost of the battery system. Summary of the invention
为了克服现有技术的上述缺点,本发明提供一种提高电池功率密度、 降低 电池成本的具有辅助电极结构的电池电极及其高功率电池。  In order to overcome the above disadvantages of the prior art, the present invention provides a battery electrode having an auxiliary electrode structure and a high power battery thereof which improve battery power density and reduce battery cost.
本发明解决其技术问题所采用的技术方案是:一种具有辅助电极结构的电 池电极包括正极、负极、设置在所述正极和负极之间的电极隔膜以及辅助电极; 所述辅助电极包括正极辅助电极和 /或负极辅助电极;  The technical solution adopted by the present invention to solve the technical problem is that a battery electrode having an auxiliary electrode structure includes a positive electrode, a negative electrode, an electrode separator disposed between the positive electrode and the negative electrode, and an auxiliary electrode; the auxiliary electrode includes a positive electrode auxiliary Electrode and/or negative auxiliary electrode;
所述正极辅助电极设置在所述正极一侧的内侧,所述正极与所述正极辅助 电极之间设置有第一隔膜; The positive electrode auxiliary electrode is disposed on an inner side of the positive electrode side, and the positive electrode and the positive electrode are assisted a first diaphragm is disposed between the electrodes;
所述负极辅助电极设置在所述负极一侧的内侧 ,所述负极与所述负极辅助 电极之间设置有第二隔膜。  The negative electrode auxiliary electrode is disposed inside the negative electrode side, and a second separator is disposed between the negative electrode and the negative electrode auxiliary electrode.
本发明提供了一种高功率电池, 包括电池壳体, 正极电解溶液、 负极电解 溶液和上述技术方案所述的电池电极设置于所述电池壳体围成的腔体中;所述 电池电极中的电极隔膜设置于所述正极电解溶液和负极电解溶液之间,还包括 电池系统参数传感器和电池控制系统。 极、 电池系统参数传感器及电池控制系统, 电池工作时区间被分成两段, 首先 让电池工作输出电流给电池控制系统并被控制系统存储起来,电池控制系统内 部电路将存储的能量分成两部分,这两部分的能量比例由控制器软件制动调节 或由人工调节; 其中一部分整流后对外输出, 另外一部分被内部的电池活性物 质转换电路将电压降低后得到低压电流用来反馈给电池的电极和对应的辅助 电极; 当电池输出一定时间后, 停止对外输出电流, 由系统控制器将存储的部 分电能以一定的低压电流提供给电池对应的辅助电极和电极上,使得电池中负 极区域的电极活性物质在负极上氧化同时在辅助电极上得到放电活性更高的 原同时在辅助电极得到放电活性更高的正极材料,从而实现电池放电时电极活 性物质的转换; 当系统控制器内的活性物质转换电路存储的电能消耗完毕后, 电池重新进入放电状态, 如此不断的循环; 工作中电池是属于间断性的输出, 而整个电池系统属于连续输出。  The present invention provides a high-power battery, including a battery case, a positive electrode electrolytic solution, a negative electrode electrolytic solution, and a battery electrode according to the above technical solution, which are disposed in a cavity surrounded by the battery case; The electrode separator is disposed between the positive electrode electrolytic solution and the negative electrode electrolytic solution, and further includes a battery system parameter sensor and a battery control system. The pole, the battery system parameter sensor and the battery control system, the battery working interval is divided into two sections. First, the battery working output current is supplied to the battery control system and stored by the control system. The internal circuit of the battery control system divides the stored energy into two parts. The energy ratio of the two parts is adjusted by the controller software or manually adjusted; some of them are rectified and outputted externally, and the other part is reduced by the internal battery active substance conversion circuit to obtain a low voltage current for feedback to the electrodes of the battery and Corresponding auxiliary electrode; when the battery outputs for a certain period of time, the external output current is stopped, and the stored part of the stored electric energy is supplied to the corresponding auxiliary electrode and the electrode of the battery with a certain low voltage current, so that the electrode active in the negative electrode region of the battery The substance is oxidized on the negative electrode while obtaining a higher discharge activity on the auxiliary electrode and a positive electrode material having higher discharge activity at the auxiliary electrode, thereby realizing conversion of the electrode active material during discharge of the battery; when the active substance is converted in the system controller Circuit After completion of the storage of the power consumption, the battery enters the discharging state again, so the cycle to continue; work cell belonging to the intermittent output, the entire battery system is continuously output.
优选的, 所述电池具有正极、 负极、 正极辅助电极、 负极辅助电极、 电池 隔膜、 电池状态传感器和电池系统控制器; 所述正极和正极辅助电极之间设置 有第一多孔隔膜, 所述负极和所述负极辅助电极之间设置有第二多孔隔膜; 所 述电池状态传感器用于转换电池的工作状态;所述电池系统控制器用于控制所 述正极、 负极、 正极辅助电极和负极辅助电极的工作。  Preferably, the battery has a positive electrode, a negative electrode, a positive electrode auxiliary electrode, a negative electrode auxiliary electrode, a battery separator, a battery state sensor, and a battery system controller; a first porous diaphragm is disposed between the positive electrode and the positive electrode auxiliary electrode, a second porous diaphragm is disposed between the negative electrode and the negative electrode auxiliary electrode; the battery state sensor is configured to convert an operating state of the battery; and the battery system controller is configured to control the positive electrode, the negative electrode, the positive electrode auxiliary electrode, and the negative electrode auxiliary The electrode works.
优选的, 所述的电池系统控制器包括活性物质转换电路、 对外放电电路、 能量存储模块和传感器电路;  Preferably, the battery system controller includes an active material conversion circuit, an external discharge circuit, an energy storage module, and a sensor circuit;
所述传感器包括温度传感器、 电解液流速传感器、 电解质浓度传感器和电 解质成分传感器。 相接的第一多孔隔膜、所述第一多孔隔膜相接的正极辅助电极、与所述正极辅 助电极相接的离子交交换膜、与所述离子交换膜相接的负极辅助电极、与所述 负极辅助电极相接的第二多孔隔膜、 与所述第二多孔隔膜相接的负极; The sensor includes a temperature sensor, an electrolyte flow rate sensor, an electrolyte concentration sensor, and electricity Deconstruction component sensor. a first porous separator that is in contact with each other, a positive electrode auxiliary electrode that is in contact with the first porous membrane, an ion exchange membrane that is in contact with the positive electrode auxiliary electrode, a negative electrode auxiliary electrode that is in contact with the ion exchange membrane, a second porous separator that is in contact with the negative electrode auxiliary electrode, and a negative electrode that is in contact with the second porous membrane;
或所述具有辅助电极结构的电池依次包括正极、与所述正极相接的第一多 孔隔膜、与所述第一多孔隔膜相接的正极辅助电极、与所述正极辅助电极相接 的第三多孔隔膜、与所述第三多孔隔膜相接的负极辅助电极、与所述负极辅助 电极相接的第二多孔隔膜、 与所述第二多孔隔膜相接的负极。  Or the battery having the auxiliary electrode structure includes a positive electrode, a first porous separator that is in contact with the positive electrode, a positive electrode auxiliary electrode that is in contact with the first porous separator, and a positive electrode auxiliary electrode. a third porous separator, a negative electrode auxiliary electrode that is in contact with the third porous separator, a second porous separator that is in contact with the negative electrode auxiliary electrode, and a negative electrode that is in contact with the second porous separator.
优选的,所述的具有辅助电极结构的电池可以是只有正极区域采用添加辅 助结构电极形式,也可以是只有负极区域采用添加辅助结构电极形式, 或者正 极与负极区域都采用添加辅助结构电极形式。  Preferably, the battery having the auxiliary electrode structure may be in the form of only the positive electrode region adopting the auxiliary auxiliary structure electrode, or only the negative electrode region may be in the form of adding the auxiliary structure electrode, or the positive electrode and the negative electrode region may be in the form of adding the auxiliary structure electrode.
在本发明中,所述的正极辅助电极和负极辅助电极都具有超大的微观表面 积, 适合大功率放电。  In the present invention, both the positive electrode auxiliary electrode and the negative electrode auxiliary electrode have an extremely large microscopic surface area and are suitable for high-power discharge.
优选的,所述的负极辅助电极的电极电位要在电解液体系中和负极区域流 体电池活性物质的电极电位要相近,且进行电极活性物质转换后能够大大提高 电极的放电功率。 例如在全钒液流电池中负极辅助电极电对为 Pb/PbS04, 该 电极电位和全钒液流电池负极区域 V(II)/V(III)电极电位相近 ,但金属铅电极放 电功率却大大加快。 Preferably, the electrode potential of the negative electrode auxiliary electrode is similar to the electrode potential of the fluid battery active material in the electrolyte system and the negative electrode region, and the discharge power of the electrode can be greatly improved after the electrode active material is converted. For example, in the all-vanadium redox flow battery, the anode auxiliary electrode is Pb/PbS0 4 , and the electrode potential is similar to the V(II)/V(III) electrode potential of the negative vanadium flow battery, but the metal lead electrode discharge power is Greatly accelerated.
优选的,所述的正极的极辅助电极的电极电位要在电解液体系中和流体本 身活性物质的电极电位要相近,例如在全钒液流电池中正极极辅助电极可以为 多孔碳素电极吸附一定浓度的[¾素单质形成 Br2/Br_ , 或者形成低浓度的 ci2/cr , 在该电极电位对和 ν(ιν)/ν(ν)电位对电极电位相近的情况下, 前者 的放电功率大大高于后者。 Preferably, the electrode potential of the pole auxiliary electrode of the positive electrode is similar to the electrode potential of the active material of the fluid itself in the electrolyte system, for example, in the all-vanadium flow battery, the positive electrode auxiliary electrode can be adsorbed by the porous carbon electrode. A certain concentration of [3⁄4 prime element forms Br 2 /Br_, or forms a low concentration of ci 2 /cr. When the electrode potential pair and the ν(ιν)/ν(ν) potential are close to the electrode potential, the former discharge The power is much higher than the latter.
优选的, 所述的正极辅助电极与正极, 所述负极辅助电极与负极之间存在 多孔隔膜进行隔离。  Preferably, the positive electrode auxiliary electrode and the positive electrode are separated by a porous separator between the negative electrode auxiliary electrode and the negative electrode.
优选的,所述的具有辅助电极结构的电池在正极和负极之间存在离子交换 膜或者多孔隔膜, 用来隔离正极和负极区域的电解液。  Preferably, the battery having the auxiliary electrode structure has an ion exchange membrane or a porous membrane between the positive electrode and the negative electrode for isolating the electrolyte in the positive electrode and the negative electrode region.
所述的具有辅助电极结构的电池可以在控制系统和辅助电极的共同作用 下使得流过电极表面的液态活性物质完全放电完毕,因此对于全液流电池正极 和负极之间也可使用多孔隔膜代替离子交换膜。 The battery with the auxiliary electrode structure can cooperate in the control system and the auxiliary electrode The liquid active material flowing through the surface of the electrode is completely discharged, so that a porous membrane can be used instead of the ion exchange membrane between the positive electrode and the negative electrode of the full flow battery.
优选的, 所述的提供给电极 /辅助电极的电流电压为 0.1 ~ 0.5V。 优选的, 所述的活性物质转换电路对电极 /辅助电极进行充电的时间为 0.1 秒 ~ 60分钟。 Preferably, the current supplied to the electrode/auxiliary electrode has a current voltage of 0.1 to 0.5V. Preferably, the active material conversion circuit charges the electrode/auxiliary electrode for 0.1 second to 60 minutes.
Figure imgf000005_0001
高,液流充电 电池, 液流燃料电池、 金属空气燃料电池, 直接曱醇燃料电池、 氢燃料电池等 电池的输出功率。
Figure imgf000005_0001
High, liquid flow rechargeable battery, liquid flow fuel cell, metal air fuel cell, direct oxime fuel cell, hydrogen fuel cell, etc.
优选的, 所述的电池组自动控制系统的电源都由电池本身提供。 本发明的积极效果是: 使用具有辅助电解电极结构的电池组通过改变电 池真实放电电极大大提高电池的输出功率,从而在其他条件不变的情况下降低 液流充电电池, 液流燃料电池、 金属空气燃料电池, 直接曱醇燃料电池、 氢燃 料电池等电池的成本; 将该类型电极结构应用于以重整氢气为燃料的燃料电 池, 能够降低普通重整器中少量的 CO 导致含有贵金属催化剂的电极中毒问 题; 将该类型电极结构应用于以直接曱醇为燃料的燃料电池, 能够防止贵金属 催化剂的对曱醇的催化氧化过程中产生的中间产物导致贵金属催化电极中毒  Preferably, the power supply of the battery pack automatic control system is provided by the battery itself. The positive effects of the present invention are: using a battery pack having an auxiliary electrolytic electrode structure to greatly increase the output power of the battery by changing the real discharge electrode of the battery, thereby reducing the flow charging battery, the liquid flow fuel cell, and the metal under other conditions. The cost of an air fuel cell, a battery such as a direct fuel cell fuel cell or a hydrogen fuel cell; the application of this type of electrode structure to a fuel cell fueled by reforming hydrogen gas can reduce a small amount of CO in a conventional reformer and lead to a catalyst containing a precious metal. Electrolyte poisoning problem; this type of electrode structure is applied to a fuel cell fueled by direct sterol, which can prevent the intermediate product generated in the catalytic oxidation of sterol of the noble metal catalyst from causing poisoning of the noble metal catalytic electrode.
Figure imgf000005_0002
Figure imgf000005_0002
具体实施方式 其高功率电池进一步说明。 DETAILED DESCRIPTION OF THE INVENTION Its high power battery is further illustrated.
本发明提供了一种具有辅助电极结构的电池电极及其高功率电池,它属于 新能源电池技术领域, 涉及一种用来提高液流电池功率密度的电池电极,使用 该电极结构的液流二次电池和燃料电池都能提高输出功率,降低储能用二次流 体电池和燃料电池的成本;使用该电极结构同样能提高直接曱醇燃料电池和氢 燃料电池的输出功率。 The invention provides a battery electrode with an auxiliary electrode structure and a high-power battery thereof, and belongs to the technical field of new energy batteries, and relates to a battery electrode for improving the power density of a liquid flow battery, and the liquid flow using the electrode structure Both the secondary battery and the fuel cell can increase the output power and reduce the cost of the secondary fluid battery and the fuel cell for energy storage; using the electrode structure can also improve the direct sterol fuel cell and hydrogen The output power of the fuel cell.
本发明采用增加辅助电极和电池控制系统器来提高液流电池和燃料电池 电极放电功率, 提高电池功率密度, 从而降低了电池成本。  The invention adopts an auxiliary electrode and a battery control system to increase the discharge power of the flow battery and the fuel cell electrode, and increase the power density of the battery, thereby reducing the battery cost.
本发明提供了一种具有辅助电极结构的电池电极包括正极、 负极、设置在 所述正极和负极之间的电极隔膜以及辅助电极;  The present invention provides a battery electrode having an auxiliary electrode structure including a positive electrode, a negative electrode, an electrode separator disposed between the positive electrode and the negative electrode, and an auxiliary electrode;
所述辅助电极包括正极辅助电极和 /或负极辅助电极;  The auxiliary electrode includes a positive electrode auxiliary electrode and/or a negative electrode auxiliary electrode;
所述正极辅助电极设置在所述正极一侧的内侧,所述正极与所述正极辅助 电极之间设置有第一多孔隔膜;  The positive electrode auxiliary electrode is disposed on an inner side of the positive electrode side, and a first porous separator is disposed between the positive electrode and the positive electrode auxiliary electrode;
所述负极辅助电极设置在所述负极一侧的内侧,所述负极与所述负极辅助 电极之间设置有第二多孔隔膜。 构示意图, 其中 11为负极, 13为负极辅助电极, 6为正极, 7为正极辅助电 极, 10为第二多孔隔膜, 14为负极辅助电极, 15为离子交换膜。 正极和负极之间的电极隔膜。本发明对所述正极、 负极和电极隔膜的种类和来 源没有特殊的限制, 采用本领域技术人员熟知的电池正极、 负极和电极隔膜即 可, 如可以为液流电池或燃料电池中的正极、 负极和电极隔膜。 具体的, 在本 发明实施例中, 当所述电池为钒液流电池时, 可以以石墨片集电极, 以聚丙烯 纤维碳毡电极为负极, 所述正极可以为金属钛网得到的集电极; 当所述电池为 锌空气电池时, 可以以锌电极, 如多孔金属锌板为负极; 所述正极可以为由碳 黑、 活性炭、 ^11 02和聚四氟乙烯树脂混合得到的浆料喷涂到镍集电极上得到 的正极, 所述碳黑、 活性炭、 Mn02和聚四氟乙烯树脂的质量比优选为 30:40:25:5。 The negative electrode auxiliary electrode is disposed inside the negative electrode side, and a second porous separator is disposed between the negative electrode and the negative electrode auxiliary electrode. Schematic diagram, wherein 11 is the negative electrode, 13 is the negative electrode auxiliary electrode, 6 is the positive electrode, 7 is the positive electrode auxiliary electrode, 10 is the second porous separator, 14 is the negative electrode auxiliary electrode, and 15 is the ion exchange membrane. An electrode separator between the positive electrode and the negative electrode. The type and source of the positive electrode, the negative electrode and the electrode separator are not particularly limited, and the battery positive electrode, the negative electrode and the electrode separator which are well known to those skilled in the art may be used, such as a positive electrode in a flow battery or a fuel cell, Negative electrode and electrode separator. Specifically, in the embodiment of the present invention, when the battery is a vanadium flow battery, the graphite sheet collector may be used, and the polypropylene fiber carbon felt electrode is used as a negative electrode, and the positive electrode may be a collector obtained from a metal titanium mesh. When the battery is a zinc-air battery, a zinc electrode, such as a porous metal zinc plate, may be used as a negative electrode; the positive electrode may be a slurry obtained by mixing carbon black, activated carbon, ^11 0 2 and polytetrafluoroethylene resin. The positive electrode obtained by spraying onto the nickel collecting electrode preferably has a mass ratio of carbon black, activated carbon, MnO 2 and polytetrafluoroethylene resin of 30:40:25:5.
在本发明中, 所述电极隔膜用来隔离正极区域和负极区域的电解液体, 所 述电极隔膜优选为离子交换膜或多孔隔膜,在本发明中, 为了区分此处的用过 电极隔膜的多孔隔膜与电极和辅助电极之间的多孔隔膜,本发明将用作电极隔 膜的多孔隔膜命名为第三多孔隔膜。  In the present invention, the electrode separator is used to isolate the electrolyte body of the positive electrode region and the negative electrode region, and the electrode separator is preferably an ion exchange membrane or a porous separator. In the present invention, in order to distinguish the porous membrane used here The porous separator between the separator and the electrode and the auxiliary electrode, the porous membrane used as the electrode separator in the present invention is named as the third porous membrane.
在本发明中, 当所述电极隔膜为离子交换膜时, 所述具有辅助电极结构的 电池电极依次包括正极、与所述正极相接的第一多孔隔膜、所述第一多孔隔膜 相接的正极辅助电极、与所述正极辅助电极相接的离子交交换膜、与所述离子 交换膜相接的负极辅助电极、 与所述负极辅助电极相接的第二多孔隔膜、与所 述第二多孔隔膜相接的负极。 也就是说, 从电池电极正极一侧看, 其中的结构 排布依次为正极、第一多孔隔膜、正极辅助电极、 离子交换膜、 负极辅助电极、 第二多孔隔膜和负极; In the present invention, when the electrode separator is an ion exchange membrane, the battery electrode having the auxiliary electrode structure includes, in order, a positive electrode, a first porous separator that is in contact with the positive electrode, and the first porous membrane. a positive electrode auxiliary electrode that is in contact with each other, an ion exchange membrane that is in contact with the positive electrode auxiliary electrode, a negative electrode auxiliary electrode that is in contact with the ion exchange membrane, a second porous separator that is in contact with the negative electrode auxiliary electrode, and The second porous membrane is connected to the negative electrode. That is, viewed from the positive side of the battery electrode, the structural arrangement therein is a positive electrode, a first porous separator, a positive electrode auxiliary electrode, an ion exchange membrane, a negative electrode auxiliary electrode, a second porous membrane, and a negative electrode;
当所述电极隔膜为第三多孔隔膜时,所述具有辅助电极结构的电池电极优 选依次包括正极、与所述正极相接的第一多孔隔膜、与所述第一多孔隔膜相接 的正极辅助电极、与所述正极辅助电极相接的第三多孔隔膜、与所述第三多孔 隔膜相接的负极辅助电极、与所述负极辅助电极相接的第二多孔隔膜、与所述 第二多孔隔膜相接的负极。 也就是说, 从电池电极正极一侧看, 其中的结构排 布依次为正极、第一多孔隔膜、正极辅助电极、第三多孔隔膜、 负极辅助电极、 第二多孔隔膜和负极。 在本发明的实施例中, 当所述电池为钒液流电极时, 所 述负极辅助电极可以为铅电极,如多孔泡沫金属铅, 所述正极辅助电极可以为 聚丙烯纤维碳毡;当所述电池为锌空气电池时,所述正极辅助电极可以由碳黑、 活性炭、 NiO和聚四氟乙烯树脂混合得到的浆料喷涂到镍集电极上、 80°C下烘 干后轧制得到的正极辅助电极, 所述碳黑、 活性炭、 NiO和聚四氟乙烯树脂的 质量比优选为 30:40:25:5。  When the electrode separator is a third porous membrane, the battery electrode having the auxiliary electrode structure preferably includes a positive electrode, a first porous membrane that is in contact with the positive electrode, and a first porous membrane. a positive electrode auxiliary electrode, a third porous separator that is in contact with the positive electrode auxiliary electrode, a negative electrode auxiliary electrode that is in contact with the third porous separator, and a second porous separator that is in contact with the negative electrode auxiliary electrode, a negative electrode that is in contact with the second porous membrane. That is, from the side of the positive electrode of the battery electrode, the structural arrangement therein is a positive electrode, a first porous separator, a positive electrode auxiliary electrode, a third porous separator, a negative electrode auxiliary electrode, a second porous separator, and a negative electrode. In an embodiment of the present invention, when the battery is a vanadium flow electrode, the negative electrode auxiliary electrode may be a lead electrode, such as porous metal foam, and the positive electrode auxiliary electrode may be a polypropylene fiber carbon felt; When the battery is a zinc-air battery, the positive electrode auxiliary electrode may be sprayed on a nickel collector by a mixture of carbon black, activated carbon, NiO and polytetrafluoroethylene resin, dried at 80 ° C, and then rolled. The positive electrode auxiliary electrode preferably has a mass ratio of carbon black, activated carbon, NiO, and polytetrafluoroethylene resin of 30:40:25:5.
所述第一多孔隔膜、第二多孔隔膜和第三多孔隔膜优选独立地选自多孔纤 维, 如在本发明实施例中, 所述第一多孔隔膜、 第二多孔隔膜和第三多孔隔膜 可以为聚丙烯碳纤维毡。  The first porous membrane, the second porous membrane, and the third porous membrane are preferably independently selected from the group consisting of porous fibers, as in the embodiment of the invention, the first porous membrane, the second porous membrane, and the first The three porous membrane may be a polypropylene carbon fiber felt.
在本发明的实施例中,所述具有辅助电极结构的电池电极可以为只添加正 极辅助电极和第一多孔隔膜得到的电池电极,也可以为只添加负极辅助电极和 第二多孔隔膜的电池电极, 还可以为同时添加正极辅助电极、 第一多孔隔膜、 负极辅助电极和第二多孔隔膜的电池电极, 本发明对此不作特殊的限定。  In an embodiment of the present invention, the battery electrode having the auxiliary electrode structure may be a battery electrode obtained by adding only the positive electrode auxiliary electrode and the first porous separator, or may be a negative electrode auxiliary electrode and a second porous separator. The battery electrode may be a battery electrode in which a positive electrode auxiliary electrode, a first porous separator, a negative electrode auxiliary electrode, and a second porous separator are simultaneously added, which is not particularly limited in the present invention.
本发明提供了一种高功率电池, 包括电池壳体, 正极电解溶液、 负极电解 溶液和上述技术方案所述的电池电极设置与所述电池壳体围成的腔体中,所述 电池电极的一端由导线引出;所述电池电极中的电极隔膜设置于所述正极电解 溶液和负极电解溶液之间, 还包括电池系统参数传感器和电池控制系统。  The present invention provides a high-power battery, comprising a battery case, a positive electrode electrolytic solution, a negative electrode electrolytic solution, and a battery electrode disposed in the above-mentioned technical solution and a cavity surrounded by the battery case, the battery electrode One end is led out by a wire; an electrode separator in the battery electrode is disposed between the positive electrode electrolytic solution and the negative electrode electrolytic solution, and further includes a battery system parameter sensor and a battery control system.
本发明提供的高功率电池, 在液流电池或燃料电池的正极区域和 /或负极 区域分别设有辅助电极、 电池状态传感器及电池控制系统, 电池工作时区间被 分成两段, 首先让电池工作输出电流给电池控制系统并被控制系统存储起来, 电池控制系统内部电路将存储的能量分成两部分,这两部分的能量比例由所述 电池控制系统软件制动调节或由人工调节; 其中一部分整流后对外输出, 另外 一部分被内部的电池活性物质转换电路将电压降低后得到低压电流用来反馈 给电池的电极和对应的辅助电极。当电池输出一定时间后,停止对外输出电流, 由电池控制系统将存储的部分电能以一定的低压电流提供给电池对应的辅助 电极和电极上,使得电池中负极区域的电极活性物质在负极上氧化同时在辅助 电极上得到放电活性更高的电极活性材料; 同理,在电池正极区域低放电活性 的电极活性物质在正极上还原同时在辅助电极得到放电活性更高的正极材料, 从而实现电池放电时电极活性物质的转换;当电池控制系统内的活性物质转换 电路存储的电能消耗完毕后, 电池重新进入放电状态, 如此不断的循环; 工作 中电池是属于间断性的输出, 而整个电池系统属于连续输出。通过这种方法来 实现电池输出更大的功率。 结构示意图, 图 2为本发明图 1所示的具有辅助电极结构的电池的剖视图, 图 1中, 1为泵, 2为进口, 3为出口, 4为负极区域, 5为正极区域; 图 2中, 6 为正极, 7为正极辅助电极, 8为正极电解溶液, 9为正极辅助电极, 10为隔 膜, 11为负极, 12为负极电解溶液, 13为负极辅助电极, 14为负极辅助电极, 15为离子交换膜。 The high power battery provided by the invention is in the positive electrode region and/or the negative electrode of the flow battery or fuel cell The area is provided with an auxiliary electrode, a battery state sensor and a battery control system. The battery operation interval is divided into two sections. First, the battery operation output current is supplied to the battery control system and stored by the control system. The energy stored in the internal circuit of the battery control system is stored. Divided into two parts, the energy ratio of the two parts is controlled by the battery control system software or manually adjusted; some of them are rectified and outputted externally, and the other part is reduced by the internal battery active substance conversion circuit to obtain a low voltage current. The feedback to the electrodes of the battery and the corresponding auxiliary electrodes. When the battery is output for a certain period of time, the external output current is stopped, and the stored part of the electric energy is supplied to the auxiliary electrode and the electrode corresponding to the battery with a certain low voltage current, so that the electrode active material in the negative electrode region of the battery is oxidized on the negative electrode. At the same time, an electrode active material with higher discharge activity is obtained on the auxiliary electrode; similarly, the electrode active material with low discharge activity in the positive electrode region of the battery is reduced on the positive electrode and a positive electrode material with higher discharge activity is obtained at the auxiliary electrode, thereby realizing battery discharge. When the electrode active material is converted; when the electric energy stored in the active substance conversion circuit in the battery control system is consumed, the battery re-enters the discharge state, and thus the cycle is continued; the battery is an intermittent output during operation, and the entire battery system belongs to Continuous output. In this way, the battery output is more powerful. 2 is a cross-sectional view of the battery having the auxiliary electrode structure shown in FIG. 1. In FIG. 1, 1 is a pump, 2 is an inlet, 3 is an outlet, 4 is a negative electrode region, and 5 is a positive electrode region; In the middle, 6 is the positive electrode, 7 is the positive electrode auxiliary electrode, 8 is the positive electrode electrolytic solution, 9 is the positive electrode auxiliary electrode, 10 is the separator, 11 is the negative electrode, 12 is the negative electrode electrolytic solution, 13 is the negative electrode auxiliary electrode, 14 is the negative electrode auxiliary electrode, 15 is an ion exchange membrane.
本发明提供的高功率电池包括电池壳体, 本发明对所述电池壳体的形状、 尺寸和材质没有特殊的限制, 采用本领域技术人员熟知的电池壳体即可,如所 述电池壳体的材质可以为 ABS塑料板, 所述电池壳体可以为长方体形。  The high-power battery provided by the present invention includes a battery case. The shape, size and material of the battery case are not particularly limited in the present invention, and a battery case known to those skilled in the art may be used, such as the battery case. The material may be an ABS plastic plate, and the battery case may have a rectangular parallelepiped shape.
在本发明中,所述的电池具有正极、 负极、正极辅助电极、 负极辅助电极、 电池隔膜、正极电解溶液、负极电解溶液、电池状态传感器和电池系统控制器; 所述的电池系统控制器包括活性物质转换电路、对外放电电路、 能量存储模块 和传感器电路; 在本发明中, 所述电池系统控制器接收电池工作输出的电流, 接收到的电流被所述能量储存模块存储起来, 并将储存的能量分成两部分, 这 两部分的能量比例由所述电池控制系统软件制动调节或由人工调节;存储起来 的一部分能量被整流后通过所述对外放电电路对外输出,另一部分被所述活性 物质转换电路降低电压后得到低压电流,将所述低压电流提供给电极和对应的 辅助电极, 所述活性物质转换电路对电极 /辅助电极进行充电。 在本发明中, 所述正极与所述电池系统控制器中的正极接线柱相连,所述负极与所述电池系 统控制器中的负极接线柱相连,所述正极辅助电极与所述电池系统控制器中的 正极辅助电极接线柱相连,所述负极辅助电极与所述电池系统控制器中的负极 辅助电极接线柱相连。 In the present invention, the battery has a positive electrode, a negative electrode, a positive electrode auxiliary electrode, a negative electrode auxiliary electrode, a battery separator, a positive electrode electrolytic solution, a negative electrode electrolytic solution, a battery state sensor, and a battery system controller; and the battery system controller includes An active material conversion circuit, an external discharge circuit, an energy storage module, and a sensor circuit; in the present invention, the battery system controller receives a current outputted by the battery, and the received current is stored by the energy storage module, and is stored The energy is divided into two parts, the energy ratio of the two parts is adjusted by the battery control system software or manually adjusted; A portion of the energy is rectified and outputted to the outside through the external discharge circuit, and another portion is reduced in voltage by the active material conversion circuit to obtain a low voltage current, and the low voltage current is supplied to the electrode and the corresponding auxiliary electrode, and the active material is converted. The circuit charges the electrode/auxiliary electrode. In the present invention, the positive electrode is connected to a positive terminal of the battery system controller, the negative electrode is connected to a negative terminal of the battery system controller, and the positive auxiliary electrode and the battery system are controlled. A positive auxiliary electrode terminal is connected to the negative electrode auxiliary electrode and a negative auxiliary electrode terminal in the battery system controller.
在本发明中, 所述的提供给电极 /辅助电极电流电压优选为 0.1 V〜0.5 V, 更优选为 0.2 V〜0.4 V; 所述的活性物质转换电路对电极 /辅助电极进行充电的 时间优选为 0.1秒〜 60分钟,更优选为 1秒〜 55分钟,最优选为 10秒〜 50分钟。  In the present invention, the current supplied to the electrode/auxiliary electrode is preferably 0.1 V to 0.5 V, more preferably 0.2 V to 0.4 V; and the time during which the active material conversion circuit charges the electrode/auxiliary electrode is preferably It is from 0.1 second to 60 minutes, more preferably from 1 second to 55 minutes, and most preferably from 10 seconds to 50 minutes.
在本发明中, 所述电池状态传感器包括温度传感器、 电解液流速传感器、 电解质浓度传感器和电解质成分传感器, 用于感知和调节电池的工作温度、 电 解液的流速、 电解质的浓度和电解质的成分, 从而调节电池的工作状态。  In the present invention, the battery state sensor includes a temperature sensor, an electrolyte flow rate sensor, an electrolyte concentration sensor, and an electrolyte composition sensor for sensing and adjusting an operating temperature of the battery, a flow rate of the electrolyte, a concentration of the electrolyte, and a composition of the electrolyte, Thereby adjusting the working state of the battery.
在本发明中,所述具有辅助电极结构的电池中的电极系统为上述技术方案 所述的具有辅助电极结构的电池电极,所述的具有辅助电极结构的电池可以是 只有正极区域采用添加辅助结构电极形式,也可以是只有负极区域采用添加辅 助结构电极形式, 或者正极与负极区域都采用添加辅助结构电极形式, 不发明 对此不作特殊的限制。 体, 本发明对所述正极电解液体和负极电解液体的种类没有特殊的限制, 采用 本领域技术人员熟知的电解液即可。在本发明的实施例中, 当所述电池为锌空 气电池时,所述正极电解液体和负极电解液体可以为质量浓度为 30%的氢氧化 钾溶液; 当所述电池为钒液流电池时, 所述正极电解液体包括摩尔浓度为 2 mol/L的 V02 +、 2 mol/L的石克酸和 0.5 mol/L的。Γ, 所述负极电解液体包括摩 尔浓度为 2 mol/L的 V2+、 2 mol/L硫酸和 0.5 mol/L的 Cl_。 In the present invention, the electrode system in the battery having the auxiliary electrode structure is the battery electrode having the auxiliary electrode structure described in the above technical solution, and the battery having the auxiliary electrode structure may be only the positive electrode region adopting the auxiliary structure. In the form of an electrode, only the negative electrode region may be in the form of an auxiliary structure electrode, or the positive electrode and the negative electrode region may be in the form of an auxiliary structure electrode, and no particular limitation is imposed on the invention. The type of the positive electrode electrolyte body and the negative electrode electrolyte body of the present invention is not particularly limited, and an electrolyte solution well known to those skilled in the art may be used. In an embodiment of the present invention, when the battery is a zinc-air battery, the positive electrode electrolyte body and the negative electrode electrolyte body may be a potassium hydroxide solution having a mass concentration of 30%; when the battery is a vanadium flow battery The positive electrode electrolyte body includes V0 2 + , 2 mol/L of sulphuric acid and 0.5 mol/L in a molar concentration of 2 mol/L.负极, the negative electrode electrolyte body includes V 2+ , 2 mol/L sulfuric acid, and 0.5 mol/L Cl_ at a molar concentration of 2 mol/L.
在本发明的实施例中, 所述电池壳体上可以设置有开孔, 分别为电解液的 进口和电解液的出口,具体的, 所述电池壳体的正极区域设置有正极区域电解 液进口和正极区域电解液出口;所述电池壳体的负极区域设置有负极区域电解 液进口和负极区域电解液出口。在本发明的实施例中, 所述正极区域电解液进 口和正极区域电解液出口设置在所述电池壳体同一侧的侧壁上,所述正极区域 电解液进口设置所述正极区域电解液出口的下方;所述负极区域电解液进口和 负极区域电解液出口设置在所述电池壳体同一侧的侧壁上,所述负极区域电解 液进口设置于所述负极区域电解液出口的下方。 In an embodiment of the present invention, the battery case may be provided with an opening, which is an inlet of an electrolyte and an outlet of an electrolyte. Specifically, a positive electrode region of the battery case is provided with an electrolyte inlet of a positive electrode region. And a positive electrode region electrolyte outlet; the negative electrode region of the battery case is provided with a negative electrode region electrolyte inlet and a negative electrode region electrolyte outlet. In an embodiment of the invention, the positive electrode region electrolyte is advanced An electrolyte outlet of the port and the positive electrode region is disposed on a sidewall on the same side of the battery case, the electrolyte inlet of the positive electrode region is disposed below the electrolyte outlet of the positive electrode region; and the electrolyte inlet and the negative electrode region of the negative electrode region are electrolyzed The liquid outlet is disposed on a side wall of the same side of the battery case, and the negative electrode area electrolyte inlet is disposed below the electrolyte outlet of the negative electrode area.
为了便于电解液的输送,在本发明的实施例中, 所述电解液进口处安装有 泵, 具体的, 在所述正极区域电解液进口处安装有第一泵, 在所述负极区域电 解液进口处安装有第二泵。  In order to facilitate the transportation of the electrolyte, in the embodiment of the present invention, a pump is installed at the inlet of the electrolyte. Specifically, a first pump is installed at the inlet of the electrolyte in the positive electrode region, and an electrolyte is disposed in the negative electrode region. A second pump is installed at the inlet.
在本发明中,所述的正极辅助电极和负极辅助电极都具有超大的微观表面 积, 适合大功率放电。  In the present invention, both the positive electrode auxiliary electrode and the negative electrode auxiliary electrode have an extremely large microscopic surface area and are suitable for high-power discharge.
在本发明提供的高功率电池中,在电解液体系中, 所述负极辅助电极的电 极电位要和负极区域流体电池活性物质的电极电位要相近,且进行电极活性物 质转换后能够提高电极的放电功率。在本发明的实施例中, 例如在全钒液流电 池中负极辅助电极电对为 Pb/PbS04 , 该电极电对 Pb/PbS04的电极电位和全钒 液流电池负极区域电极电对 V(II)/V(III)的电极电位相近 ,且金属铅电极放电功 率却大大加快。 In the high-power battery provided by the present invention, in the electrolyte system, the electrode potential of the negative electrode auxiliary electrode is similar to the electrode potential of the fluid battery active material in the negative electrode region, and the discharge of the electrode can be improved after the electrode active material is converted. power. In an embodiment of the invention, for example, in the all-vanadium redox flow battery, the negative auxiliary electrode pair is Pb/PbS0 4 , the electrode potential of the electrode pair Pb/PbS0 4 and the total vanadium flow battery negative electrode region electrode pair V The electrode potentials of (II)/V(III) are similar, and the discharge power of the metal lead electrode is greatly accelerated.
在本发明提供的高功率电池中,在电解液体系中, 所述正极辅助电极的电 极电位要和流体本身活性物质的电极电位要相近,且进行电极活性物质转换后 能够提供电极的放电功率。在本发明的实施例中, 例如在全钒液流电池中正极 辅助电极可以为多孔碳素电极吸附一定浓度的卤素单质形成 Br2/Br-,或者形成 低浓度的 C12/C1_ , 该类电极电位对和 V(IV)/V(V)电位对电极电位相近, 前者 的放电功率大大高于后者。 In the high-power battery provided by the present invention, in the electrolyte system, the electrode potential of the positive electrode auxiliary electrode is close to the electrode potential of the active material of the fluid itself, and the discharge power of the electrode can be provided after the electrode active material is converted. In an embodiment of the present invention, for example, in the all-vanadium redox flow battery, the positive electrode auxiliary electrode may adsorb a certain concentration of halogen element to form a Br 2 /Br- or a low concentration of C1 2 /C1_ for the porous carbon electrode. The electrode potential pair and the V(IV)/V(V) potential are similar to the electrode potential, and the former has a much higher discharge power than the latter.
在本发明提供的高功率电池中, 所述的正极辅助电极与正极之间, 所述负 极辅助电极与负极之间存在多孔隔膜进行隔离。  In the high-power battery provided by the present invention, between the positive electrode auxiliary electrode and the positive electrode, a porous separator is isolated between the negative electrode auxiliary electrode and the negative electrode.
所述的具有辅助电极结构的电池在正极和负极之间存在离子交换膜或者 多孔隔膜, 用来隔离正极和负极区域的电解液。  The battery having the auxiliary electrode structure has an ion exchange membrane or a porous separator between the positive electrode and the negative electrode for isolating the electrolyte in the positive electrode and the negative electrode region.
所述的具有辅助电极结构的电池可以在控制系统和辅助电极的共同作用 下使得流过电极表面的液态活性物质完全放电完毕,因此对于全液流电池正极 和负极之间也可使用多孔隔膜代替离子交换膜。 池, 液流燃料电池、 金属空气燃料电池, 直接曱醇燃料电池、 氢燃料电池等电 池的输出功率。 The battery with the auxiliary electrode structure can completely discharge the liquid active material flowing through the electrode surface under the joint action of the control system and the auxiliary electrode, so a porous diaphragm can be used instead of the positive electrode and the negative electrode of the full flow battery. Ion exchange membrane. The output power of batteries, liquid fuel cells, metal air fuel cells, direct methanol fuel cells, hydrogen fuel cells, etc.
本发明提供的具有辅助电极结构的高功率电池中的电池控制系统优选为 自动控制系统, 所述自动控制系统的电源优选由电池本身提供。  The battery control system in the high power battery having the auxiliary electrode structure provided by the present invention is preferably an automatic control system, and the power supply of the automatic control system is preferably provided by the battery itself.
本发明使用具有辅助电解电极结构的电池组通过改变电池真实放电电极 大大提高电池的输出功率, 从而在其他条件不变的情况下降低液流充电电池, 液流燃料电池、金属空气燃料电池, 直接曱醇燃料电池、 氢燃料电池等电池的 成本; 将该类型电极结构应用于以重整氢气为燃料的燃料电池, 能够降低普通 重整器中少量的 CO导致含有贵金属催化剂的电极中毒问题;将该类型电极结 构应用于以直接曱醇为燃料的燃料电池,能够防止贵金属催化剂的对曱醇的催 化氧化过程中产生的中间产物导致贵金属催化电极中毒问题。  The invention uses the battery pack with the auxiliary electrolysis electrode structure to greatly increase the output power of the battery by changing the real discharge electrode of the battery, thereby reducing the flow charging battery, the liquid flow fuel cell, the metal air fuel cell directly under other conditions. The cost of a battery such as a sterol fuel cell or a hydrogen fuel cell; applying this type of electrode structure to a fuel cell fueled by reforming hydrogen can reduce the problem of electrode poisoning of a noble metal-containing catalyst caused by a small amount of CO in a conventional reformer; This type of electrode structure is applied to a fuel cell fueled by direct sterol, which can prevent the noble metal catalyst from poisoning problems caused by intermediate products generated in the catalytic oxidation of sterol.
为了进一步说明本发明,下面结合实施例对本发明提供的具有辅助电极结 构的电池电极及其高功率电池进行详细地描述,但不能将它们理解为对本发明 保护范围的限定。  In order to further explain the present invention, the battery electrode having the auxiliary electrode structure and the high power battery thereof provided by the present invention are described in detail below with reference to the embodiments, but they are not to be construed as limiting the scope of the present invention.
下述实施例采用附图 1〜3 所示的结构, 制备得到具有辅助电极结构的电 池。  The following embodiment employs the structure shown in Figs. 1 to 3 to prepare a battery having an auxiliary electrode structure.
实施例 1:  Example 1:
按附图 1所示的结构, 采用 ABS塑料板制作长 20mm x宽 lOOmm x高 20 的塑料槽并在槽中间装上质子交换膜作为流体电池的隔膜, 将塑料槽分成 10 X 100 X 150mm的两部分, 分别为负极区和正极区域, 并在这两部分的侧壁分 别开孔形成流体电池电解液的进出口,并连接相应的微型泵作为电解液的循环 泵;  According to the structure shown in Figure 1, a plastic groove of 20 mm long x 100 mm x 20 is made of ABS plastic plate and a proton exchange membrane is installed in the middle of the groove as a separator for the fluid battery, and the plastic tank is divided into 10 X 100 X 150 mm. The two parts are respectively a negative electrode region and a positive electrode region, and the side walls of the two portions are respectively opened to form an inlet and outlet of the fluid battery electrolyte, and the corresponding micro pump is connected as a circulating pump of the electrolyte;
按照图 2示加工尺寸长 X宽为 100 X 150mm, 厚度为 1mm的石墨片为集 电极, 以聚丙婦碳纤维毡在 400 °C热处理 24小时后剪切成 100 150的电极。 裁切尺寸长 X宽为 105 X 155mm 的多孔纤维布作为隔膜。 加工尺寸长 x宽为 100 X 150mm,厚度为 1mm的多孔泡沫金属铅作为负极辅助电极。按顺序将石 墨集电极、 聚丙烯碳纤维毡电极、 隔膜、 辅助铅电极压紧后放入到加工好的塑 料槽的负极区域。  According to Fig. 2, a graphite sheet having a length X width of 100 X 150 mm and a thickness of 1 mm was used as a collecting electrode, and was cut into a 150 150 electrode by heat treatment at 400 ° C for 24 hours. A porous fiber cloth having a length X and a width of 105 X 155 mm was cut as a separator. A porous metal foam lead having a length x width of 100 X 150 mm and a thickness of 1 mm was used as the negative electrode auxiliary electrode. The graphite collector, the polypropylene carbon fiber felt electrode, the separator, and the auxiliary lead electrode are pressed in order and placed in the negative electrode region of the processed plastic tank.
加工尺寸长 X宽为 100 X 150mm, 厚度为 1mm的金属钛网为集电极, 以 聚丙烯碳纤维毡在 400°C热处理 24小时后热处理后剪切成 100 150, 分别为 正极和正极辅助电极。 裁切尺寸长 X宽为 105 X 155mm 的多孔纤维布作为隔 膜。 按顺序将钛网集电极、 聚丙婦碳纤维毡正极辅助电极、 隔膜、 聚丙烯碳纤 维毡正极压紧后放入到加工好的塑料槽的正极区域。 A metal titanium mesh having a length X width of 100 X 150 mm and a thickness of 1 mm is used as a collector to The polypropylene carbon fiber felt was heat-treated at 400 ° C for 24 hours, and then heat-treated and then cut into 100 150, which were a positive electrode and a positive electrode auxiliary electrode, respectively. A porous fiber cloth having a length X width of 105 X 155 mm was cut as a separator. The titanium mesh collector, the polyacrylonitrile carbon fiber felt positive auxiliary electrode, the separator, and the polypropylene carbon fiber felt positive electrode are pressed in order and placed in the positive electrode region of the processed plastic tank.
负极区域的电解液成分为 2mol/L的 V2+, 2mol/L的石克酸, 0.5mol/L的 CT; 正极区域的电解液成为 2mol/L的 V02 +, 2mol/L的硫酸, 0.5mol/L的 Cr。 The electrolyte component in the negative electrode region is 2 mol/L of V 2+ , 2 mol/L of sulphuric acid, and 0.5 mol/L of CT; the electrolyte in the positive electrode region is 2 mol/L of V0 2 + , 2 mol/L of sulfuric acid, 0.5 mol/L of Cr.
将电池中的辅助电极分别和控制系统的对应辅助电极的接线柱连接,电极 分别和和控制系统的对应的接线柱连接,并连接好电解液循环系统连接好后得 到所述的具有辅助电极结构的全钒液流流体电池。  The auxiliary electrodes in the battery are respectively connected to the terminals of the corresponding auxiliary electrodes of the control system, and the electrodes are respectively connected with the corresponding terminals of the control system, and connected to the electrolyte circulation system to obtain the auxiliary electrode structure. An all-vanadium flow fluid battery.
电池工作时 ,控制系统对正极 /正极辅助电极输出的电压为 0.2伏,此时正 极区域发生的反应为 vo2 + +cr— - vo2+ + ci2(被聚丙婦碳毡电极吸附)。放电时 吸附态的 ci2通过聚丙婦碳纤维毡正极电极来放电。控制系统对负极 /负极辅助 电极的输出电压为 0.1 伏特, 此时发生的反应为 PbS04+ 2V2+ -— Pb +S04 2" +2V3+, 放电时是通过金属铅电极来放电。 控制系统对电池组的充放时间比由 负载功率的大小来智能控制,使得电池工作在最大效率处。通过辅助电极的工 作使得整个钒液流电池的平均输出功率比未使用辅助电极的全钒液流电池输 出功率增大 5倍。 电池电极结构由普通全钒液流电池结构转变为金属铅 /氯气 电池结构。 When the battery is working, the voltage output from the control system to the positive/positive auxiliary electrode is 0.2 volts. At this time, the reaction in the positive electrode region is vo 2 + +cr- - vo 2+ + ci 2 (adsorbed by the polypropylene-based carbon felt electrode). The ci 2 in the adsorbed state at the time of discharge is discharged through the positive electrode of the polypropylene fiber carbon fiber felt. The output voltage of the control system to the negative/negative auxiliary electrode is 0.1 volt, and the reaction occurs at this time as PbS0 4 + 2V 2+ - Pb + S0 4 2 " + 2V 3+ , which is discharged by the metal lead electrode during discharge. The charging and discharging time of the control system to the battery pack is intelligently controlled by the magnitude of the load power, so that the battery operates at the maximum efficiency. The operation of the auxiliary electrode makes the average output power of the entire vanadium flow battery more than the vanadium without the auxiliary electrode. The output power of the flow battery is increased by 5 times. The electrode structure of the battery is changed from a common all-vanadium flow battery structure to a metal lead/chlorine battery structure.
实施例 2:  Example 2:
按附图说明的方案采用 ABS塑料板制作长 X宽 X高 100 X 50 X 70mm的塑 料槽并在槽其中一个侧壁开出 80 60的孔。 按照图示 3加工尺寸长 X宽为 90 60mm, 厚度为 1mm的泡沫镍为集电极, 然后将炭黑、 活性炭和 NiO、 聚四 氟乙烯树脂按照 35:35: 15: 15的比例配置成浆料利用喷涂的方法均匀的喷涂到 泡沫镍集电极上, 在 80 °C条件下充分烘干后进行轧制得到正极辅助电极。 同 样的加工尺寸长 X宽为 90 X 60mm, 厚度为 lmm的泡沫镍为集电极, 然后将 (3晶型的炭黑、 活性炭和 Mn02、 聚四氟乙烯树脂按照 30:30: 15: 25的比例配 置成浆料利用喷涂的方法均匀的喷涂到泡沫镍集电极上, 在 80°C条件下充分 烘干后进行轧制得到正极。裁切尺寸长 X宽为 90 X 60mm的多孔纤维布作为隔 膜。 按顺序将正极辅助电极、 隔膜、 正极压紧后固定在塑料槽的开口处并将正 极和塑料槽的接触的缝隙处进行密封, 让正极辅助电极面向塑料槽的内部。在 电解槽中以 30%的 KOH为电解液, According to the scheme described in the drawing, a plastic groove of length X width X height 100 X 50 X 70 mm is made of ABS plastic plate and a hole of 80 60 is opened in one side wall of the groove. According to Figure 3, the foamed nickel with a length X width of 90 60 mm and a thickness of 1 mm is used as a collector, and then carbon black, activated carbon, NiO, and polytetrafluoroethylene resin are arranged in a ratio of 35:35:15:15. The material was uniformly sprayed onto the foamed nickel collector by spraying, and dried at 80 ° C and then rolled to obtain a positive electrode auxiliary electrode. The same processing size length X width is 90 X 60mm, the thickness of lmm foam nickel is the collector, and then (3 crystal carbon black, activated carbon and Mn0 2 , polytetrafluoroethylene resin according to 30:30: 15: 25 The ratio is configured such that the slurry is uniformly sprayed onto the foamed nickel collector by spraying, and is sufficiently dried after being dried at 80 ° C to obtain a positive electrode. The porous fiber cloth having a length X width of 90 X 60 mm is cut. As a separator, the positive electrode auxiliary electrode, the separator, and the positive electrode are pressed in order and fixed at the opening of the plastic tank and will be positive. The gap between the pole and the plastic groove is sealed so that the positive electrode auxiliary electrode faces the inside of the plastic groove. 30% KOH as electrolyte in the electrolytic cell,
多孔金属锌板为负极。将电池中的辅助电极分别和控制系统的对应辅助电 极接线柱连接,正、 负电极分别和控制系统对应的电极接线柱连接后得到所述 的具有辅助电极结构的锌空气燃料电池。  The porous metal zinc plate is a negative electrode. The auxiliary electrodes in the battery are respectively connected to the corresponding auxiliary electrode terminals of the control system, and the positive and negative electrodes are respectively connected to the electrode terminals corresponding to the control system to obtain the zinc air fuel cell having the auxiliary electrode structure.
电池工作时,控制系统对正极 /正极辅助电极输出的电压为 0.2伏,此时正 极区域发生的反应为 NiO +MnO(OH) -— NiO(OH) + ΜηΟ , 02 (来自空 气) +MnO MnO(OH), 放电时通过正极辅助电极来放电。 该锌空气电池的输 出电压为 1.7V, 比普通锌空气电池直接输出电压高约 0.3V。 控制系统对电池 组的充放时间比由负载功率的大小来智能控制。通过辅助电极的工作使得整个 锌空气电池的平均输出功率比未使用辅助电极的锌空气电池输出功率增大 4 倍, 电池电极结构由普通的金属锌电极 /空气电极结构转变为金属锌电极 /羟基 氧化镍电极结构。 When the battery is working, the voltage output from the control system to the positive/positive auxiliary electrode is 0.2 volts. At this time, the reaction in the positive electrode region is NiO + MnO(OH) - NiO(OH) + ΜηΟ, 0 2 (from air) + MnO MnO(OH) is discharged through the positive electrode auxiliary electrode during discharge. The zinc-air battery has an output voltage of 1.7V, which is about 0.3V higher than the direct output voltage of a normal zinc-air battery. The charging and discharging time of the control system to the battery pack is intelligently controlled by the magnitude of the load power. Through the operation of the auxiliary electrode, the average output power of the entire zinc-air battery is increased by 4 times compared with the output of the zinc-air battery without the auxiliary electrode. The battery electrode structure is converted from a common metal zinc electrode/air electrode structure to a metal zinc electrode/hydroxyl group. Nickel oxide electrode structure.
以上实施例的说明只是用于帮助理解本发明的方法及其核心思想。应当指 出, 对于本技术领域的普通技术人员来说, 在不脱离本发明原理的前提下, 还 可以对本发明进行若干改进和修饰,这些改进和修饰也落入本发明权利要求的 保护范围内。对这些实施例的多种修改对本领域的专业技术人员来说是显而易 见的,本文中所定义的一般原理可以在不脱离本发明的精神或范围的情况下在 其它实施例中实现。 因此, 本发明将不会被限制于本文所示的这些实施例, 而 是要符合与本文所公开的原理和新颖特点相一致的最宽的范围。  The above description of the embodiments is merely to assist in understanding the method of the present invention and its core idea. It is to be understood that those skilled in the art can make various modifications and changes to the present invention without departing from the spirit and scope of the invention. Various modifications to these embodiments are obvious to those skilled in the art, and the general principles defined herein may be implemented in other embodiments without departing from the spirit or scope of the invention. Therefore, the present invention is not to be limited to the embodiments shown herein, but is to be accorded to the broadest scope of the principles and novel features disclosed herein.

Claims

权 利 要 求 Rights request
1. 一种具有辅助电极结构的电池电极及其高功率电池, 其特征是: 在液 数传感器及电池控制系统, 电池工作时区间被分成两段, 首先让电池工作输出 电流给电池控制系统并被控制系统存储起来,电池控制系统内部电路将存储的 能量分成两部分, 这两部分的能量比例由控制器软件制动调节或由人工调节; 其中一部分整流后对外输出,另外一部分被内部的电池活性物质转换电路将电 压降低后得到低压电流用来提供给电池的电极和对应的辅助电极;当电池输出 一定时间后,停止对外输出电流, 由系统控制器将存储的部分电能以一定的低 压电流提供给电池对应的辅助电极和电极上,使得电池中负极区域的电极活性 物质在负极上氧化同时在辅助电极上得到放电活性更高的电极活性材料; 同 得到放电活性更高的正极材料,从而实现电池放电时电极活性物质的转换; 当 系统控制器内的活性物质转换电路存储的电能消耗完毕后,电池重新进入放电 状态, 如此不断的循环; 工作中电池是属于间断性的输出, 而整个电池系统属 于连续输出。 1. A battery electrode having an auxiliary electrode structure and a high-power battery thereof, characterized in that: in the liquid number sensor and the battery control system, the interval of the battery is divided into two sections, first letting the battery work output current to the battery control system and Stored by the control system, the internal circuit of the battery control system divides the stored energy into two parts. The energy ratio of the two parts is adjusted by the controller software or manually adjusted; some of them are rectified and output externally, and the other part is internally charged. The active material conversion circuit reduces the voltage to obtain a low-voltage current for supplying the electrode of the battery and the corresponding auxiliary electrode; when the battery outputs for a certain period of time, stopping the external output current, the system controller uses the stored partial power to a certain low-voltage current. Providing to the auxiliary electrode and the electrode corresponding to the battery, so that the electrode active material in the negative electrode region of the battery is oxidized on the negative electrode and the electrode active material having higher discharge activity is obtained on the auxiliary electrode; and the positive electrode material having higher discharge activity is obtained, thereby Realize electrode live when discharging battery Conversion of the substance; when the stored energy stored in the active substance conversion circuit in the system controller is consumed, the battery re-enters the discharge state, and thus continues to cycle; the battery in operation is an intermittent output, and the entire battery system is a continuous output. .
2. 如权利要求 1 所述具有辅助电极结构的电池电极及其高功率电池, 其 特征是: 所述的电池具有正极、 负极、 正极辅助电极、 负极辅助电极、 电池隔 膜、电池状态传感器和电池系统控制器;从正极到负极的结构排布依次为正极、 多孔隔膜、 正极辅助电极、 离子交换膜、 负极辅助电极、 多孔隔膜、 负极或者 是正极、 多孔隔膜、 正极辅助电极、 多孔隔膜、 负极辅助电极、 多孔隔膜和负 极。  2. The battery electrode having an auxiliary electrode structure according to claim 1, and the high power battery thereof, wherein: the battery has a positive electrode, a negative electrode, a positive electrode auxiliary electrode, a negative electrode auxiliary electrode, a battery separator, a battery state sensor, and a battery. The system controller; the structure from the positive electrode to the negative electrode is sequentially a positive electrode, a porous separator, a positive electrode auxiliary electrode, an ion exchange membrane, a negative electrode auxiliary electrode, a porous separator, a negative electrode or a positive electrode, a porous separator, a positive electrode auxiliary electrode, a porous separator, and a negative electrode. Auxiliary electrode, porous separator and negative electrode.
3. 如权利要求 2所述具有辅助电极结构的电池电极及其高功率电池, 其 特征是: 所述的电池系统控制器具有活性物质转换电路、 对外放电电路、 能量 存储模块和传感器电路; 电池传感器具有温度传感器、 电解液流速传感器、 电 解质浓度和电解质成分传感器这类型的传感器。  3. The battery electrode having the auxiliary electrode structure and the high power battery thereof according to claim 2, wherein: the battery system controller has an active material conversion circuit, an external discharge circuit, an energy storage module, and a sensor circuit; The sensor has a sensor of the type such as a temperature sensor, an electrolyte flow rate sensor, an electrolyte concentration, and an electrolyte composition sensor.
4. 如权利要求 2所述具有辅助电极结构的电池电极及其高功率电池, 其 特征是: 所述的正极辅助电极和负极辅助电极都具有超大的微观表面积,适合 大功率放电;所述的负极辅助电极的电极电位要在电解液体系中和负极区域流 体电池活性物质的电极电位要相近,且进行电极活性物质转换后能够大大提高 电极的放电功率; 在全钒液流电池中负极辅助电极电对为 Pb/PbS04, 该电极 电位和全钒液流电池负极区域 ν(π)/ν(πι)电极电位相近,但金属铅电极放电功 率却大大加快;所述的正极辅助电极的电极电位要在电解液体系中和流体本身 活性物质的电极电位要相近;在全钒液流电池中正极辅助电极可以为多孔碳素 电极吸附一定浓度的卤素单质形成 Br2/Br_, 或者形成低浓度的 C12/C1_ , 在该 电极电位对和 V(IV)/V(V)电位对电极电位相近的情况下,前者的放电功率大大4. The battery electrode having the auxiliary electrode structure and the high power battery thereof according to claim 2, wherein: the positive electrode auxiliary electrode and the negative electrode auxiliary electrode both have an ultra-large micro surface area, which is suitable for High-power discharge; the electrode potential of the negative electrode auxiliary electrode should be similar to the electrode potential of the fluid battery active material in the electrolyte system and the negative electrode region, and the discharge power of the electrode can be greatly improved after the electrode active material is converted; In the flow battery, the negative electrode auxiliary electrode is Pb/PbS0 4 , and the electrode potential is similar to the ν(π)/ν(πι) electrode potential of the negative electrode region of the all-vanadium flow battery, but the discharge power of the metal lead electrode is greatly accelerated; The electrode potential of the positive electrode auxiliary electrode is similar to the electrode potential of the active material of the fluid itself in the electrolyte system; in the all-vanadium flow battery, the positive electrode auxiliary electrode can adsorb a certain concentration of halogen element to form a Br 2 for the porous carbon electrode. /Br_, or form a low concentration of C1 2 /C1_, in the case where the electrode potential pair and the V(IV)/V(V) potential are close to the electrode potential, the former has a large discharge power.
1¾于后者。 13⁄4 in the latter.
5. 如权利要求 2或 4所述具有辅助电极结构的电池电极及其高功率电池, 其特征是: 所述的正极辅助电极与正极, 负极辅助电极与负极之间存在多孔隔 膜进行隔离; 在正极和负极之间存在离子交换膜或者多孔隔膜, 用来隔离正极 和负极区域的电解液。  The battery electrode having the auxiliary electrode structure and the high-power battery thereof according to claim 2 or 4, wherein: the positive electrode auxiliary electrode and the positive electrode, and the negative electrode auxiliary electrode and the negative electrode are separated by a porous diaphragm; An ion exchange membrane or a porous membrane is present between the positive electrode and the negative electrode to isolate the electrolyte in the positive and negative electrode regions.
6. 如权利要求 1 所述具有辅助电极结构的电池电极及其高功率电池, 其 特征是:所述的具有辅助电极结构的电池在所述控制系统和辅助电极的共同作 用下使得流过电极表面的液态活性物质完全放电完毕,在全液流电池中,正极 和负极之间使用多孔隔膜代替离子交换膜。  6. The battery electrode having an auxiliary electrode structure and the high power battery thereof according to claim 1, wherein said battery having an auxiliary electrode structure is caused to flow through the electrode under the joint action of said control system and said auxiliary electrode The liquid active material on the surface is completely discharged. In the full-flow battery, a porous membrane is used instead of the ion exchange membrane between the positive electrode and the negative electrode.
7. 如权利要求 1 所述具有辅助电极结构的电池电极及其高功率电池, 其 特征是: 所述提供给电极 /辅助电极的电流电压为 0.1 ~ 0.5V。  7. The battery electrode having an auxiliary electrode structure according to claim 1, and a high-power battery thereof, wherein: the current supplied to the electrode/auxiliary electrode is 0.1 to 0.5V.
8. 如权利要求 1或 3所述具有辅助电极结构的电池电极及其高功率电池, 其特征是: 所述的活性物质转换电路对电极 /辅助电极进行充电的时间是指 0.1 秒 ~ 60分钟。  The battery electrode having the auxiliary electrode structure according to claim 1 or 3, and the high-power battery thereof, wherein: the active material conversion circuit charges the electrode/auxiliary electrode in a period of 0.1 second to 60 minutes. .
9. 如权利要求 1 所述具有辅助电极结构的电池电极及其高功率电池, 其 特征是: 具有辅助电极结构的大功率电池用于液流充电电池、 液流燃料电池、 金属空气燃料电池、直接曱醇燃料电池或氢燃料电池中,提高所述液流充电电 池、 液流燃料电池、 金属空气燃料电池、 直接曱醇燃料电池或氢燃料电池的输 出功率。  9. The battery electrode with an auxiliary electrode structure according to claim 1, and a high-power battery thereof, characterized in that: a high-power battery having an auxiliary electrode structure is used for a liquid flow rechargeable battery, a liquid flow fuel cell, a metal air fuel cell, In a direct methanol fuel cell or a hydrogen fuel cell, the output power of the liquid flow rechargeable battery, the liquid flow fuel cell, the metal air fuel cell, the direct methanol fuel cell or the hydrogen fuel cell is increased.
10. 如权利要求 1所述具有辅助电极结构的电池电极及其高功率电池, 其 特征是:所述具有辅助电极结构的电池中电池控制系统的电源由所述电池本身 十 10. The battery electrode having an auxiliary electrode structure according to claim 1, and a high power battery thereof, wherein: a power source of the battery control system in the battery having the auxiliary electrode structure is used by the battery itself Ten
.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11081712B2 (en) 2018-10-26 2021-08-03 Saudi Arabian Oil Company Method and system to modify the performance of a redox flow battery

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102983341A (en) * 2012-12-31 2013-03-20 刘军 Battery electrode with auxiliary electrode structure and high-power battery

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1090340A (en) * 1992-11-23 1994-08-03 帕马斯坎德公司 Battery
CN101071886A (en) * 2007-05-30 2007-11-14 李文华 Three-electrode electro Chemical cell
CN102983341A (en) * 2012-12-31 2013-03-20 刘军 Battery electrode with auxiliary electrode structure and high-power battery

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TW543230B (en) * 2001-04-24 2003-07-21 Reveo Inc Hybrid electrochemical cell system
JP2003157884A (en) * 2001-11-21 2003-05-30 Sumitomo Electric Ind Ltd Charging method of vanadium redox flow battery
JP2005216627A (en) * 2004-01-28 2005-08-11 Aisin Seiki Co Ltd Fuel cell power generation system and its control method
US8119269B2 (en) * 2007-05-10 2012-02-21 Enovix Corporation Secondary battery with auxiliary electrode

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1090340A (en) * 1992-11-23 1994-08-03 帕马斯坎德公司 Battery
CN101071886A (en) * 2007-05-30 2007-11-14 李文华 Three-electrode electro Chemical cell
CN102983341A (en) * 2012-12-31 2013-03-20 刘军 Battery electrode with auxiliary electrode structure and high-power battery

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11081712B2 (en) 2018-10-26 2021-08-03 Saudi Arabian Oil Company Method and system to modify the performance of a redox flow battery

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