WO2011051997A1 - 鉛蓄電池の運用方法及び該運用方法により運用される鉛蓄電池を備えた蓄電装置 - Google Patents
鉛蓄電池の運用方法及び該運用方法により運用される鉛蓄電池を備えた蓄電装置 Download PDFInfo
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- WO2011051997A1 WO2011051997A1 PCT/JP2009/005633 JP2009005633W WO2011051997A1 WO 2011051997 A1 WO2011051997 A1 WO 2011051997A1 JP 2009005633 W JP2009005633 W JP 2009005633W WO 2011051997 A1 WO2011051997 A1 WO 2011051997A1
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
- H01M10/44—Methods for charging or discharging
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
- H01M10/425—Structural combination with electronic components, e.g. electronic circuits integrated to the outside of the casing
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
- H01M10/44—Methods for charging or discharging
- H01M10/443—Methods for charging or discharging in response to temperature
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
- H01M10/44—Methods for charging or discharging
- H01M10/448—End of discharge regulating measures
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
- H01M10/46—Accumulators structurally combined with charging apparatus
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
- H01M10/48—Accumulators combined with arrangements for measuring, testing or indicating the condition of cells, e.g. the level or density of the electrolyte
- H01M10/486—Accumulators combined with arrangements for measuring, testing or indicating the condition of cells, e.g. the level or density of the electrolyte for measuring temperature
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/60—Heating or cooling; Temperature control
- H01M10/61—Types of temperature control
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/60—Heating or cooling; Temperature control
- H01M10/63—Control systems
- H01M10/635—Control systems based on ambient temperature
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- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J3/00—Circuit arrangements for ac mains or ac distribution networks
- H02J3/28—Arrangements for balancing of the load in a network by storage of energy
- H02J3/32—Arrangements for balancing of the load in a network by storage of energy using batteries with converting means
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- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J3/00—Circuit arrangements for ac mains or ac distribution networks
- H02J3/38—Arrangements for parallely feeding a single network by two or more generators, converters or transformers
- H02J3/381—Dispersed generators
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- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J3/00—Circuit arrangements for ac mains or ac distribution networks
- H02J3/38—Arrangements for parallely feeding a single network by two or more generators, converters or transformers
- H02J3/46—Controlling of the sharing of output between the generators, converters, or transformers
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- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J7/00—Circuit arrangements for charging or depolarising batteries or for supplying loads from batteries
- H02J7/0047—Circuit arrangements for charging or depolarising batteries or for supplying loads from batteries with monitoring or indicating devices or circuits
- H02J7/0048—Detection of remaining charge capacity or state of charge [SOC]
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- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J7/00—Circuit arrangements for charging or depolarising batteries or for supplying loads from batteries
- H02J7/007—Regulation of charging or discharging current or voltage
- H02J7/007188—Regulation of charging or discharging current or voltage the charge cycle being controlled or terminated in response to non-electric parameters
- H02J7/007192—Regulation of charging or discharging current or voltage the charge cycle being controlled or terminated in response to non-electric parameters in response to temperature
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- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J7/00—Circuit arrangements for charging or depolarising batteries or for supplying loads from batteries
- H02J7/007—Regulation of charging or discharging current or voltage
- H02J7/007188—Regulation of charging or discharging current or voltage the charge cycle being controlled or terminated in response to non-electric parameters
- H02J7/007192—Regulation of charging or discharging current or voltage the charge cycle being controlled or terminated in response to non-electric parameters in response to temperature
- H02J7/007194—Regulation of charging or discharging current or voltage the charge cycle being controlled or terminated in response to non-electric parameters in response to temperature of the battery
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- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J7/00—Circuit arrangements for charging or depolarising batteries or for supplying loads from batteries
- H02J7/02—Circuit arrangements for charging or depolarising batteries or for supplying loads from batteries for charging batteries from ac mains by converters
- H02J7/04—Regulation of charging current or voltage
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- H—ELECTRICITY
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- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
- H01M10/425—Structural combination with electronic components, e.g. electronic circuits integrated to the outside of the casing
- H01M2010/4271—Battery management systems including electronic circuits, e.g. control of current or voltage to keep battery in healthy state, cell balancing
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2220/00—Batteries for particular applications
- H01M2220/10—Batteries in stationary systems, e.g. emergency power source in plant
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- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J2300/00—Systems for supplying or distributing electric power characterised by decentralized, dispersed, or local generation
- H02J2300/20—The dispersed energy generation being of renewable origin
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- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J2300/00—Systems for supplying or distributing electric power characterised by decentralized, dispersed, or local generation
- H02J2300/20—The dispersed energy generation being of renewable origin
- H02J2300/22—The renewable source being solar energy
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- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J2300/00—Systems for supplying or distributing electric power characterised by decentralized, dispersed, or local generation
- H02J2300/20—The dispersed energy generation being of renewable origin
- H02J2300/22—The renewable source being solar energy
- H02J2300/24—The renewable source being solar energy of photovoltaic origin
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- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J2300/00—Systems for supplying or distributing electric power characterised by decentralized, dispersed, or local generation
- H02J2300/20—The dispersed energy generation being of renewable origin
- H02J2300/28—The renewable source being wind energy
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/50—Photovoltaic [PV] energy
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/50—Photovoltaic [PV] energy
- Y02E10/56—Power conversion systems, e.g. maximum power point trackers
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
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- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/70—Wind energy
- Y02E10/76—Power conversion electric or electronic aspects
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- Y—GENERAL 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
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E70/00—Other energy conversion or management systems reducing GHG emissions
- Y02E70/30—Systems combining energy storage with energy generation of non-fossil origin
Definitions
- the present invention relates to a method of operating a lead storage battery installed in a power generation facility equipped with a power generation device using natural energy such as a solar power generation device or a wind power generation device, and a storage battery provided with a lead storage battery operated according to this operation method. It relates to an apparatus.
- Patent Document 1 proposes that a battery of an electric vehicle be charged with power obtained from a solar cell.
- the natural energy power generation apparatus is also linked to the electric power system of the electric power company (hereinafter, referred to as "system"). There is.
- a secondary battery is connected to the power generation system, and charging of the secondary battery by the output of the power generation system and discharge from the secondary battery to the system are performed.
- the fluctuation of the power generation amount of the power generation device is compensated, and the fluctuation of the power supplied from the power generation device to the grid is suppressed.
- secondary batteries lead-acid batteries, which are low in cost, safe and reliable, are often used.
- the AC power generated by the natural energy power generation apparatus is converted into appropriate DC power by a converter or the like, and the lead-acid battery is charged with this DC power, and lead is used.
- the direct current power obtained from the storage battery is converted again into alternating current power by the inverter to supply stable power to the grid.
- the lead storage battery has a state of charge (hereinafter sometimes referred to as "SOC".
- SOC is an abbreviation of State Of Charge.
- the lead storage battery is in an overdischarged state (for example, an SOC of 30% or less) or an overcharged state (SOC)
- SOC overcharged state
- Wind power generators and solar power generators can be designed to have a life of 17 to 20 years, and converters and inverters can also have approximately the same durability. No matter how long the life of the lead-acid battery is, if the life of the lead-acid battery is around five years, it will be necessary to replace the lead-acid battery frequently, resulting in an increase in the overall cost of the system. I will.
- the present invention is the operation of a lead storage battery that is optimal for prolonging the life of a lead storage battery charged by the power generation device to compensate for fluctuations in the output of a natural energy power generation device such as a solar power generation device or wind power generation device. Intended to provide a method.
- Another object of the present invention is to provide a storage device for a natural energy utilization power generation facility which can prolong the life of a lead storage battery.
- the first invention is connected to a power generation device to compensate for fluctuations in the amount of power generation of a natural energy power generation device such as a solar cell or a wind power generator, and charging by the output of the power generation device and discharge to an external circuit are performed.
- a natural energy power generation device such as a solar cell or a wind power generator
- the fully charged state of the lead storage battery is 100%
- the charged state of the lead storage battery is maintained in the range of 30 to 90%
- the battery voltage is 1.80 to 2.42 V / cell.
- the lead-acid battery is discharged and charged while maintaining the regulation range of
- the second invention is applied to the first invention, and in the present invention, the battery temperature is determined as the reference temperature when the ambient temperature of the lead-acid battery is the reference temperature, with 25.degree. C. as the reference temperature. Discharge and charge the lead-acid battery while maintaining the voltage between 1.80 and 2.42 V / cell).
- the upper limit value and the lower limit value of the regulation range were selected in the range of 4mV / ° C to 6mV / ° C per cell according to the amount of rise from the reference temperature of the ambient temperature.
- the corrected voltage range is determined by performing correction to decrease by the correction amount, and the battery voltage is maintained in the corrected voltage range to discharge and charge the lead storage battery, and when the ambient temperature is lower than the reference temperature After correction by raising the upper limit value and lower limit value of the regulation range by a correction amount selected in the range of 4mV / ° C to 6mV / ° C per cell according to the amount of decrease from the reference temperature of the ambient temperature
- the voltage range is determined, and the battery voltage is maintained in the corrected voltage range, and the lead storage battery is operated by discharging and charging the lead storage battery.
- the third invention is applied to the first invention or the second invention, and in the present invention, the maximum discharge current of the lead storage battery at the time of operation is 0.4 CA (C is a rated capacity of the lead storage battery) [Ah] is shown.) Maintain below.
- the fourth invention is applied to the first invention, the second invention or the third invention, and in the present invention, the maximum charging current of the lead storage battery at the time of operation is 0.3 CA (C is Indicate the rated capacity [Ah] of the lead storage battery.
- the fifth invention is applied to any one of the first to fourth inventions, and in the present invention, after the operation of the lead storage battery is started, the operation is interrupted each time a set period passes. Then, refresh charging is performed to equally charge the lead storage battery to the full charge state.
- the sixth invention is applied to any of the first invention to the fifth invention, and in the present invention, the lead storage battery at the time of operation by integrating the charge quantity and the discharge quantity [Ah]. Calculate the charge status of
- a seventh invention is a storage battery including a lead storage battery connected to the power generation device to compensate for fluctuations in the output of the natural energy power generation device, and in which charging by the power generation device and discharging to the outside are performed.
- the charge and discharge control device is provided to control the charge and discharge of the lead storage battery so as to operate the lead storage battery by the operation methods described in the first to sixth aspects.
- the SOC is maintained in the range of 30 to 90%, and the discharge and charge of the lead storage battery during operation are maintained in the range of 1.80 to 2.42 V / cell. Since the lead storage battery is discharged and charged, the lead storage battery can be operated in an undercharged state, and the life of the lead storage battery can be significantly extended.
- the ambient temperature of the lead storage battery is the reference temperature
- 25 ° C. is defined as the reference temperature
- the battery voltage is maintained within the specified range (range 1.80 to 2.42 V / cell).
- the upper limit value and lower limit value of the above regulation range according to the amount of increase or decrease from the reference temperature of the ambient temperature
- the corrected voltage range is determined by performing correction to decrease or increase the correction amount in the range of 4mV / ° C to 6mV / ° C per cell, and lead is held with the battery voltage kept in this corrected voltage range.
- the lead storage battery When the storage battery is discharged and charged, the lead storage battery is prevented from being overcharged when the ambient temperature is high, and the progress of the corrosion of the positive electrode grid and the decrease of the electrolyte are suppressed, It can be extended. That is, at high temperatures, even if the voltage is low, the efficiency of charging is good, and by operating the battery voltage range to the negative side, it is possible to prevent the lead storage battery from being overcharged. Conversely, when the temperature is low, the charging efficiency is very poor, so temperature correction of the battery voltage during operation is performed to shift the battery voltage range to the positive side, thereby suppressing the occurrence of the sulfation phenomenon due to insufficient charging. Can.
- the present invention by setting the maximum discharge current of the lead-acid battery to 0.4 CA or less and / or the maximum charge current to 0.3 CA or less, generation of Joule heat due to charge and discharge current is suppressed to reduce the battery. It can be used, and the life of the lead storage battery can be extended by minimizing the temperature rise inside the lead storage battery.
- heat may be concentrated on members other than the electrode plate (e.g., pole post, terminal, strap, etc.) by melting and discharging lead or resin battery case by limiting charge and discharge current. Can also be obtained.
- members other than the electrode plate e.g., pole post, terminal, strap, etc.
- the present invention by limiting the charge / discharge current, it is possible to suppress instantaneous voltage fluctuations and prevent the battery voltage from deviating from the voltage range in which the lead-acid battery can be used safely. There is also an effect that system control can be easily performed to perform an operation for extending the life of the battery without complicating the structure of the battery.
- the SOC of the lead storage battery when the SOC of the lead storage battery is calculated by integrating the charge and discharge electric charge, the SOC of the lead storage battery is always grasped, and the electric charge and discharge are possible for instantaneous charge acceptance. Because the amount of electricity can be predicted, it is possible to cope with random changes in the amount of power generation of natural energy power generation devices such as wind power generation devices and solar power generation devices.
- a solar power generation device means a power generation device using a power generation element that generates power using sunlight as an energy source.
- a specific example of a power generation element that generates power using sunlight as an energy source is a solar cell (Solar cell).
- Solar cells are power generation elements that convert light energy directly into electric power by using the photovoltaic effect.
- a pn junction type in which a p-type semiconductor and an n-type semiconductor are joined, a dye-sensitized type in which electrons in a dye adsorbed to titanium dioxide are excited, or the like can be used.
- a wind power generation device means a power generation device that generates power using wind power as an energy source.
- a typical example of a wind power generator is a wind power generator that drives a power generator using a wind turbine.
- the type of wind turbine is not particularly limited, and a lift type horizontal axis wind turbine, a drag type horizontal axis wind turbine, a lift vertical axis wind turbine, or a drag type Any suitable type of wind turbine can be used, such as a vertical axis wind turbine.
- Propeller windmills, ribbon-type windmills, etc. can be used as the lift-type horizontal-axis windmill, and cell-wing windmills, Dutch-type windmills, multi-wing-type windmills, pinwheel-type windmills, etc. can be used as the drag-type horizontal-axis windmills.
- Darrieus windmill, Gyromill windmill, etc. can be used as a lift vertical axis windmill, and Savonius windmill, cross flow windmill, S-type windmill, paddle windmill, etc. can be used as a drag type vertical axis windmill. .
- the wind power generation device that can be used as a natural energy power generation device is not limited to a wind power generator using a wind turbine, and power can be obtained by installing a piezoelectric element on a diaphragm that vibrates by applying wind. It is also possible to use one of the above.
- the above-described solar power generation device generates power in a daytime with a certain amount of sunlight, and the amount of power generation changes with time, weather, and regions. In addition, the amount of power generation of the wind power generator changes with the strength of the wind.
- the power generation apparatus for charging a lead storage battery operated by the method of the present invention is not limited to a solar power generation device or a wind power generation device, and may be one using tidal power or wave power.
- a storage device for storing the electric power generated by the power generation unit in the secondary battery is provided. It is necessary to supply stable power.
- a lead storage battery is used as a secondary battery provided in the power storage device.
- the lead-acid battery operated by the operation method according to the present invention has a structure in which an electrode plate having an active material supported on a lead or lead alloy substrate is immersed in an electrolytic solution.
- an electrode plate As the electrode plate, a clad type, a paste type or a tudle type is used, but a paste type which has good manufacturability and can easily increase the electrode plate area is preferable.
- the substrate used for the electrode plate is called a lattice substrate.
- a gravity casting method GDC: Gravity Die Casting
- the grid substrate used for the electrode plate of the lead storage battery operated by the operation method of the present invention is It is preferable that it manufactures using a gravity casting system.
- the grid substrate manufactured by the gravity casting method has no theoretical limit on the thickness of the castable grid, and is excellent in current collection characteristics and corrosion resistance.
- the material metal (alloy) forming the lattice substrate is melted, and the molten metal (alloy) is poured into a heat resistant mold by gravity and cast. According to this casting method, a grid substrate excellent in current collection characteristics and corrosion resistance can be manufactured efficiently at high speed.
- an alloy material in which tin, calcium, antimony or the like is added to lead as a main raw material can be used.
- lead in which both tin and calcium are added.
- the addition of calcium to lead can reduce the rate of self-discharge.
- the addition of calcium to lead causes a problem that bone corrosion is likely to occur, but the addition of tin to both calcium and lead can suppress bone corrosion.
- the paste type electrode plate it is necessary to support the paste-like active material on the substrate, but in this operation, the paste-like active material is pressed against the substrate under pressure, and then the roller is used. This can be done by further pushing the active material into the lattice of the substrate.
- the bones forming the lattice of the substrate are not all made the same as in FIG. 1 (a), but the major bone 1 and the bone bone 2 are mixed as in FIG. 1 (b), Preferably, one or more bones 2 are arranged between the large bone 1 and the large bone 1.
- the active material pushed from the one surface of the substrate between the lattice bones is likely to move to the back surface portion of the large bone 1 more easily than the fine bone 2 portion,
- the entire grid of the substrate can be covered with the active material, and the grid can be prevented from being exposed.
- the active material of the electrode plate is not particularly limited, but it is preferable to prepare by mixing lead powder containing lead monoxide, water, sulfuric acid and the like.
- the active material may be added with additives such as cut fiber, carbon powder, lignin, barium sulfate, and red lead according to the characteristics of the positive electrode and the negative electrode.
- the electrolyte solution is not particularly limited, but diluted dilute sulfuric acid with purified water and prepared to about 30% by mass as mass percent concentration, and adjusted to an appropriate concentration considering battery capacity, life, etc.
- the solution is poured into the battery case.
- an additive such as magnesium sulfate or silica gel may be added to the electrolyte prepared by diluting dilute sulfuric acid with purified water.
- a power storage device configured by combining a large number of the above lead storage batteries is connected to the power generation device, and charging of the lead storage battery by the output of the power generation device And discharging the lead storage battery to the external circuit under a predetermined condition to operate the lead storage battery in the undercharged state.
- the “external circuit” is usually a power system, but may be a circuit connected to a load in a specific customer such as a factory.
- the fully charged state of the lead storage battery is set to 100%, and the state of charge (SOC) of the lead storage battery is maintained in the range of 30 to 90%,
- SOC state of charge
- the lead-acid battery is discharged and charged while keeping the battery voltage within the specified range of 1.80 to 2.42 V / cell.
- the reference range of the battery voltage is the above range, and when the ambient temperature of the lead storage battery is other than 25 ° C., according to the ambient temperature. Correct the battery voltage range.
- the maximum discharge current of the lead storage battery during operation is maintained at 0.4 CA (C indicates the rated capacity [Ah] of the lead storage battery) or less, and the lead storage battery during operation is The maximum charging current is maintained below 0.3 CA (C indicates the rated capacity [Ah] of the lead storage battery).
- the lead-acid battery operated by the method of the present invention preferably has a life equal to or longer than that of each component used in the power generation device.
- the battery in order to extend the life of the battery, the battery is operated by maintaining the SOC in the range of 30 to 90% and performing charging and discharging.
- the lead storage battery In order to operate the lead storage battery while maintaining the SOC within the range of 30 to 90%, first, the lead storage battery is fully charged (a state in which all of the positive electrode active material is charged by the positive electrode capacity control), By defining the SOC in that state as 100% and discharging the lead storage battery at a constant discharge current, the SOC is reduced to an appropriate value in the range of 30 to 90%. Assuming that the SOC at this time is an initial value, the charge amount of charge is added thereafter and the discharge amount of charge is subtracted to integrate the charge / discharge amount of electricity and successively calculate the SOC at each time, and the calculated SOC is 30 Operate the battery while controlling the charge and discharge of the lead storage battery so that it does not deviate from the range of 90%.
- the discharge is forcibly stopped and the SOC is 90%. If it exceeds, the SOC is maintained in the range of 30 to 90% by forcibly stopping charging.
- the lead storage battery is operated with the SOC outside the above range, the lead storage battery is likely to be overcharged in the region where the SOC exceeds 90%, and corrosion of the positive electrode grid is promoted or water in the electrolyte is There is a high possibility of shortening the life, for example, due to the fact that the electrode is electrolyzed and reduced due to the high potential.
- the lead storage battery is likely to be in the overdischarged state and tends to be insufficiently charged, so that sulfation of the negative electrode active material may occur, and the life may be shortened.
- charge and discharge of the lead storage battery are controlled so that the SOC does not deviate from the range of 30 to 90%, but in the present invention, the lead is prevented so that the SOC does not deviate from the range of 30 to 90%.
- the charging and discharging of the storage battery may be controlled, and the charging and discharging of the lead storage battery may be controlled so that the SOC falls within a narrower range set in the range of 30 to 90%, for example 30 to 60%. .
- the value of SOC is calculated by sequentially adding and subtracting the amount of charge and the amount of discharge (Ah) of the lead storage battery, with 100% being the state where the capacity of the battery is the rated capacity (the fully charged state). For example, an integrated wattmeter for measuring the amount of charged electricity and the amount of discharged electricity is provided, and the amount of charged electricity measured by the integrated wattmeter while charging is being performed is calculated immediately before the charging is started.
- the capacity in a fully charged state (SOC: 100%) is 100 Ah. Then, when discharge is performed at 10 A for 6 minutes (0.1 hours), the discharge capacity is 1 Ah, and the remaining capacity is 99 Ah. Calculate this as SOC: 99%.
- the SOC of the lead storage battery is calculated as described above. By performing such calculation, the SOC of the lead storage battery at any time can be grasped, and the lead storage battery is instantaneously determined from the grasped SOC Since it is possible to predict the amount of electricity that can be charged and the amount of electricity that can be discharged from the lead storage battery, the external circuit connected to the generator corresponding to the change in the random generation amount of the natural energy generator The control to suppress the fluctuation of the power supplied to (for example, the power system) can be properly performed.
- the integrated value of the discharge quantity (total discharge quantity, which is an important factor in estimating the life of the lead storage battery By grasping)
- total discharge quantity which is an important factor in estimating the life of the lead storage battery By grasping
- the system control accurately based on the estimation result. That is, if the state of the SOC is known, it is possible to determine what kind of control the system should perform on the storage battery with respect to the fluctuation of the power generation output estimated from the predicted wind state. Since the discharge current and the charge / discharge time can be accurately calculated, system control can be accurately performed.
- the voltage range of 1.80 to 2.42 V / cell is set as the regulation range of the battery voltage (battery terminal voltage), and the battery voltage is maintained within this regulation range.
- the lead storage battery is operated by discharging and charging the lead storage battery.
- the battery voltage falls within the above-mentioned prescribed range (range of 1.80 to 2.42 V / cell). Discharge and charge the lead storage battery, and when the ambient temperature is higher or lower than the reference temperature (25.degree. C.), according to the amount of increase or decrease of the ambient temperature from the reference temperature, Lower or raise the upper and lower limit values. That is, when the ambient temperature is higher than the reference temperature (25.degree. C.), the upper limit value and the lower limit value of the standard range are 4 mV / .degree. C.
- the corrected voltage range is determined by performing correction to decrease by the correction amount selected in the range of ° C., and the battery voltage is maintained in the corrected voltage range, and the lead storage battery is discharged and charged.
- the ambient temperature is lower than the reference temperature, select the upper limit value and lower limit value of the regulation range in the range of 4mV / ° C to 6mV / ° C per cell according to the amount of decrease from the reference temperature of the ambient temperature.
- the corrected voltage range is determined by performing correction to increase by the correction amount as described above, and the battery voltage is maintained in the corrected voltage range, and the lead storage battery is discharged and charged.
- the atmosphere is based on the battery voltage at 25 ° C. (reference operating voltage) Every time the temperature rises by 1 ° C., the corrected voltage range is determined by lowering the upper limit value and the lower limit value of the specified range of the battery voltage by 5 mV per cell.
- the battery voltage regulation range each time the atmosphere temperature decreases by 1 ° C.
- the lead storage battery is operated in a more appropriate voltage range by setting the battery voltage range to the above-mentioned after-correction voltage range, and as the battery voltage deviates from the after-correction voltage range, the influence of deterioration due to temperature It becomes easy to receive.
- a temperature sensor is installed in the vicinity of a part of the lead storage batteries, and the lead storage battery is converted by converting the signal obtained from this temperature sensor into a temperature value.
- the ambient temperature is detected, and the amount of deviation of the detected ambient temperature from the reference temperature (25.degree. C.) is calculated.
- the upper limit (2.42 V / cell) and the lower limit (1.80 V / cell) of the reference range are corrected based on the amount of deviation of the atmospheric temperature from the reference temperature to obtain a corrected voltage range.
- an error in the range of ⁇ 1 mV / ° C. is an allowable range.
- the range of 5 mV / ° C. ⁇ 1 mV / ° C. is an allowable range.
- equal charge in order to refresh the lead storage battery periodically to suppress deterioration of the lead storage battery, equal charge (refresh charge) until the lead storage battery is fully charged.
- the equal charge is a charge that is performed to equalize the state of charge by eliminating variations in the state of charge between the cells when a large number of secondary batteries are used as one set and used for a long time.
- constant current charging is performed until the battery voltage of each battery reaches a predetermined voltage, and then charging is performed for a fixed time with a constant voltage.
- the charge quantity at the time of uniform charge execution is counted in integration of charge and discharge quantity of electricity, and clears the integrated value of charge and discharge current from the end of the previous equal charge end after the equal charge end.
- constant current discharge is performed to return to a low state of about 60 to 65% SOC and then resume the operation of the lead storage battery.
- the state at the time of operation refers to connecting the power generation device to the grid after smoothing random fluctuations of the power generation amount of natural energy power generation devices such as solar power generation devices or wind power generation devices as much as possible. Therefore, the lead storage battery is charged and discharged as needed, and states other than the operation state mean that the power generation has been stopped due to a failure or inspection of the power generator, and furthermore, the lead storage battery should be refreshed. It refers to the state where equal charge (constant current charge) is performed.
- the maximum discharge current during operation is preferably 0.4 CA or less.
- C described here is the rated capacity (Ah: ampere hour) of the lead storage battery, and the amount of electricity that can be taken out from the fully charged state (SOC: 100%) under the specified temperature, discharge current and termination voltage conditions.
- the maximum discharge current during operation is an important factor affecting the life of the lead-acid battery, and using at a discharge current of 0.4 CA or less can suppress the temperature rise inside the lead-acid battery due to Joule heat . Thereby, the deterioration by the temperature of lead acid battery can be minimized.
- the lead storage battery when the lead storage battery is continuously used at a discharge current exceeding 0.4 CA, the temperature of the electrode plate inside the lead storage battery, the members such as the pole post, the strap, the battery case made of resin, and the electrolyte Not only the corrosion of the positive electrode plate is promoted but also the deterioration of each member proceeds.
- the maximum charge current during operation is preferably 0.3 CA or less.
- the maximum charge current during operation affects the life of the lead-acid battery. By charging with a maximum charging current of 0.3 CA or less, it is possible to avoid a rapid voltage rise of the lead storage battery and to suppress the temperature rise of the battery body and the corrosion of the positive electrode grid.
- the charging voltage of the lead storage battery is constantly measured, and then charging is performed when the battery voltage reaches the specified voltage (charging voltage when charging current of 0.3 CA). It is possible to control at 0.3 CA or less by performing charging according to a charging method for narrowing the current, so-called constant voltage charging method.
- the storage device in which the lead storage battery is operated by the operation method of the present invention is provided with a charge / discharge control device for controlling the charge and discharge of each lead storage battery so that the lead storage battery is operated by the operation method according to the present invention.
- the charge / discharge control device controls the charge and discharge of the lead storage battery so as to detect the SOC, the battery voltage, the maximum discharge current, and the maximum charge current, and keep the detected values in the target range in the operation method of the present invention.
- means for The method of controlling the charge and discharge of the lead storage battery may be a known method.
- lignin 0.2% by mass
- barium sulfate 0.1% by mass
- carbon powder such as ordinary commercially available graphite: 0.2 %
- polyester fiber 0.1% by mass
- the positive electrode plate and the negative electrode plate described above are alternately laminated one by one while interposing a separator between them, and the same electrode plates are connected by straps, and a positive electrode plate: 24 / negative electrode plate: 25 A plate group was produced.
- the electrode plate group was placed in a battery case, diluted sulfuric acid was injected, and formation was performed to prepare a 2V-1500 Ah control valve type lead-acid battery.
- Example 1 An operation test was conducted to understand the influence of SOC.
- the SOC is 60%
- the charge current is 0.2 CA
- the discharge current is 0.2 CA
- the 1-second discharge and the 1-second charge are repeated without any pause period
- the test temperature is 25 ° C.
- the voltage was controlled so as to be maintained in the range of 1.80 V to 2.42 V / cell, and the degree of progress of deterioration was compared with each test.
- the SOC was maintained at 60% throughout the period of the operation test.
- Example 2 As a test of operation to grasp the influence of SOC, 30% of SOC, 0.2 CA of charge current, 0.2 CA of discharge current, repeat 1 second discharge and 1 second charge without putting a pause period, The test was conducted at a test temperature of 25 ° C. and controlled so as to keep the battery voltage in the range of 1.80 V to 2.42 V / cell, and the degree of deterioration progress was compared with each test. In this example, the SOC was maintained at 30% throughout the operation test period. The difference between the present embodiment and the first embodiment is only the SOC.
- Example 3 As a test of operation to grasp the influence of SOC, 90% of SOC, 0.2 CA of charge current, 0.2 CA of discharge current, repeat 1 second discharge and 1 second charge without putting a pause period, The test was conducted at a test temperature of 25 ° C. and controlled so as to keep the battery voltage in the range of 1.80 V to 2.42 V / cell, and the degree of deterioration progress was compared with each test. In this example, the SOC was maintained at 90% throughout the period of the operation test. The difference between the present embodiment and the first embodiment is only the SOC.
- Comparative Example 1 As a test of operation to grasp the influence of SOC, repeat 20 seconds of SOC, 0.2 CA of charging current, 0.2 CA of discharging current, and 1 sec of discharging and 1 sec of charging without putting a pause period, The test was conducted at a test temperature of 25 ° C. and controlled so as to keep the battery voltage in the range of 1.80 V to 2.42 V / cell, and the degree of deterioration progress was compared with each test. In this comparative example, SOC was maintained at 20% throughout the period of the operation test. The only difference between this comparative example and Example 1 is the SOC.
- Comparative Example 2 As a test of operation to grasp the influence of SOC, 100% of SOC, 0.2 CA of charge current, 0.2 CA of discharge current, repeat 1 second discharge and 1 second charge without putting a pause period, The test was conducted at a test temperature of 25 ° C. and controlled so as to keep the battery voltage in the range of 1.80 V to 2.42 V / cell, and the degree of deterioration progress was compared with each test. In this comparative example, the SOC was maintained at 100% throughout the period of the operation test. The only difference between this comparative example and Example 1 is the SOC.
- Reference Example 1 As a test of operation to grasp the influence of voltage, 30% of SOC, 0.2 CA of charge current, 0.2 CA of discharge current, repeat the discharge for 1 second and the charge for 1 second without any pause period and test Tests were conducted at a temperature of 25 ° C. and a battery voltage controlled to be in the range of 1.70 V to 2.42 V / cell, and the degree of deterioration progress was compared with each test. In this reference example, the SOC was maintained at 30% throughout the operation test period. The present embodiment is different from the second embodiment only in voltage control.
- Reference Example 2 As a test of operation to grasp the influence of voltage, 90% of SOC, 0.2 CA of charging current and 0.2 CA of discharging current, repeat 1 second discharge and 1 second charge without putting a pause period, The test was conducted at a test temperature of 25 ° C. and controlled so as to keep the battery voltage in the range of 1.80 V to 2.52 V / cell, and the degree of deterioration progress was compared with each test. In this reference example, the SOC was maintained at 90% throughout the period of the operation test. The present embodiment is different from the third embodiment only in voltage control.
- Example 4 As a test of operation to grasp the influence of temperature correction, SOC is 90%, charge current is 0.2 CA, discharge current is 0.2 CA, discharge for 1 second and charge for 1 second are repeated without any pause period. The In addition, the test is performed by controlling the test so that the test temperature is 40 ° C. and the battery voltage is in the range of 1.725 V to 2.345 V / cell (the temperature correction of -5 mV / ° C. is performed per cell). The degree of deterioration progress was compared with each test. In this example, the SOC was maintained at 90% throughout the period of the operation test.
- Example 5 As a test of operation to grasp the influence of temperature correction, SOC is 90%, charge current is 0.2 CA, discharge current is 0.2 CA, discharge for 1 second and charge for 1 second are repeated without any pause period. A test was conducted at a test temperature of 40 ° C. and controlled to keep the battery voltage in the range of 1.80 V to 2.42 V / cell (without temperature correction), and the degree of deterioration progress was compared with each test. In this example, the SOC was maintained at 90% throughout the period of the operation test. The present embodiment is different from the fourth embodiment only in that the temperature correction in the battery voltage range is not performed.
- Example 6 As a test of operation to grasp the influence of temperature correction, 30% SOC, 0.2 CA charge current, 0.2 CA discharge current, 1 second discharge and 1 second charge repeated without pause period
- the test temperature is 40 ° C.
- the battery voltage is in the range of 1.725 V to 2.345 V / cell (temperature correction of -5 mV / ° C. per cell is performed for the upper limit value and the lower limit value of the voltage range)
- the control test was carried out so as to keep the above and the degree of deterioration progress was compared with each test. In this example, the SOC was maintained at 30% throughout the operation test period.
- Example 7 As a test of operation to grasp the influence of temperature correction, 30% SOC, 0.2 CA charge current, 0.2 CA discharge current, 1 second discharge and 1 second charge repeated without pause period
- the test temperature is 40 ° C
- the battery voltage is in the range of 1.65V to 2.27V / cell (the temperature correction of -10mV / ° C per cell is performed for the upper limit value and the lower limit value of the voltage range)
- Tests to control were conducted to compare the degree of deterioration progress with each test. In this example, the SOC was maintained at 30% throughout the operation test period.
- the present embodiment is different from the sixth embodiment only in voltage control based on temperature correction.
- Example 8 As a test of operation to grasp the influence of discharge current, SOC is 60%, charge current is 0.2 CA, discharge current is 0.4 CA, charge for 2 seconds and discharge for 1 second are repeated without pause period. A test was conducted at a test temperature of 25 ° C. and controlled so as to keep the battery voltage in the range of 1.80 V to 2.42 V / cell, and the degree of deterioration progress was compared with each test. In the present embodiment, the SOC was maintained at 60% throughout the period of the operation test.
- Example 9 As a test of operation to understand the influence of discharge current, SOC is 60%, charge current is 0.2 CA, discharge current is 0.6 CA, charging for 3 seconds and discharging for 3 seconds are repeated without pause period. A test was conducted at a test temperature of 25 ° C. and controlled so as to keep the battery voltage in the range of 1.80 V to 2.42 V / cell, and the degree of deterioration progress was compared with each test. In the present embodiment, the SOC was maintained at 60% throughout the period of the operation test. The present embodiment is different from the eighth embodiment in discharge current and charge time.
- Example 10 As a test of operation to understand the influence of charge current, SOC with 60%, charge current with 0.3 CA, and discharge current with 0.2 CA, charge for 1 second and discharge for 1.5 seconds without pause period The test was repeated at a test temperature of 25 ° C., and a test was performed to control the battery voltage in the range of 1.80 V to 2.42 V / cell, and the degree of deterioration progress was compared with each test. In the present embodiment, the SOC was maintained at 60% throughout the period of the operation test.
- Example 11 As a test of operation to understand the influence of charge current, SOC is 60%, charge current is 0.4 CA, discharge current is 0.2 CA, and 1 second charge and 2 second discharge are repeated without putting a pause period. A test was conducted at a test temperature of 25 ° C. and controlled so as to keep the battery voltage in the range of 1.80 V to 2.42 V / cell, and the degree of deterioration progress was compared with each test. In the present embodiment, the SOC was maintained at 60% throughout the period of the operation test. The present embodiment is different from the tenth embodiment only in charge current and discharge time. The conditions of the above-described Examples 1 to 11 and Comparative Examples 1 and 2 and Reference Examples 1 and 2 are summarized in Table 1 below.
- Example 8 since the charge and discharge cycle is longer than the above example, the magnification of each accelerated life test is as follows.
- Example 8: 28800/5000 5.7 times
- Example 9: 21600/5000 4.3 times
- Example 10: 34560/5000 6.9 times
- Example 11: 28800/5000 5.7 times
- FIG. 2 shows the change in capacity of the 0.1 CA discharge test.
- the initial capacity was maintained during the test period of 24 months, while in Comparative Example 1, the lifetime reached about 18 months.
- Comparative Example 1 it was found that a large amount of lead sulfate was accumulated on the negative electrode plate, which was the cause of the life. That is, in Comparative Example 1, it can be determined that the battery life is shortened due to the long insufficient charge state. Furthermore, in the comparative example 2, it became a life in about 12 months.
- FIG. 3 shows the capacity transition of the 0.1 CA discharge test.
- the initial capacity was maintained during the test period of 24 months, while in Reference Example 1, the life was about 21 months.
- a large amount of lead sulfate has accumulated on the negative electrode plate, which has been found to be the cause of the life. That is, in the reference example 1, it can be judged that the battery life is shortened due to the long state of the insufficient charge.
- the life was about 18 months.
- the battery which became the life was dismantled, the growth of the positive electrode plate by corrosion was intense, and it turned out that this is the life cause. That is, in the reference example 2, it can be determined that the battery life is shortened due to the long overcharge state.
- FIG. 4 shows the capacity transition of the 0.1 CA discharge test.
- Example 4 the initial capacity was maintained for 24 months in the test period, whereas in Example 5, the life was about 22 months.
- the battery which became the life was dismantled, activation of the chemical reaction by high temperature environment occurred, growth of the positive electrode plate by corrosion advanced, and it turned out that this is the life cause. That is, in the fifth embodiment, since the temperature correction is not added, it can be determined that the battery life has become short due to the continued overcharge state.
- Example 6 the initial capacity was maintained for 24 months in the test period, whereas in Example 7, the life was about 23 months.
- a large amount of lead sulfate has accumulated on the negative electrode plate, which has been found to be the cause of the life. That is, in the seventh embodiment, since the value of the temperature correction is increased, it can be determined that the battery life is shortened due to the continued insufficient charge state.
- FIG. 5 shows the capacity transition of the 0.1 CA discharge test.
- Example 1 and Example 8 while the initial capacity was maintained for 24 months in the test period, in Example 9 the life became about 23 months.
- the battery which became the life was disassembled, it was found that a large amount of lead sulfate was accumulated in the negative electrode plate due to the decrease of the battery voltage due to the increase of the discharge current, which was the cause of the life. That is, in Example 9, it can be judged that the battery life has become short due to repeated deep deep discharges.
- FIG. 6 shows the capacity transition of the 0.1 CA discharge test.
- Example 1 and Example 10 the initial capacity was maintained for 24 months in the test period, while in Example 11 the life became about 24 months.
- the expansion of the positive electrode plate due to corrosion was progressing due to the increase of the cell voltage due to the increase of the charging current, which was the cause of the life. That is, in Example 11, it can be judged that the battery life has become short due to the repetition of the momentary overcharging.
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Abstract
Description
また自然エネルギー発電装置を系統と連系させる場合に、発電装置から系統に供給される電力が大きく変動すると、電力会社が要求する連系要件を満たさなくなるおそれがある。
第1の発明は、太陽電池や風力発電機等の自然エネルギー発電装置の発電量の変動を補償するために発電装置に接続されて、発電装置の出力による充電と外部回路への放電とが行われる鉛蓄電池を運用する鉛蓄電池の運用方法に係わるものである。本発明の運用方法では、鉛蓄電池の満充電状態を100%として、該鉛蓄電池の充電状態を30~90%の範囲内に維持し、かつ、電池電圧を1.80~2.42V/セルの規程範囲に保って鉛蓄電池の放電及び充電を行う。
<太陽光発電機器>
本明細書において、太陽光発電機器とは、太陽光をエネルギー源として発電を行う発電要素を用いた発電機器を意味する。太陽光をエネルギー源として発電を行う発電要素の具体例は、太陽電池(Solar cell)である。
本明細書において、風力発電機器とは、風力をエネルギー源として発電を行う発電機器を意味する。風力発電機器の代表的なものは、風車を用いて発電機を駆動する風力発電機である。
本発明に係わる運用方法により運用する鉛蓄電池は、鉛又は鉛合金製の基板に活物質を担持させた極板を、電解液に浸漬した構造を有する。極板としては、クラッド式、ペースト式又はチュードル式のもの等が用いられているが、製造性が良く、極板面積を容易に増やすことができるペースト式のものが好ましい。
本実施形態では、自然エネルギー発電装置の発電量の変動を補償するために、上記の鉛蓄電池を多数組み合わせることにより構成した蓄電装置を発電装置に接続し、該発電装置の出力による鉛蓄電池の充電と、該鉛蓄電池から外部回路への放電とを所定の条件で行わせて、鉛蓄電池を不足充電状態で運用する。
<鉛蓄電池のSOC>
本発明の方法により運用する鉛蓄電池は、発電機器に用いられる各部品と同等以上の寿命を有することが好ましい。本発明では、電池の寿命を延ばすために、SOCを30~90%の範囲内に維持して充電及び放電を行うことにより電池を運用する。
SOCの値は、電池の容量が定格容量である状態(満充電された状態)を100%として、鉛蓄電池の充電電気量及び放電電気量(Ah)を逐次加算及び減算することにより演算する。例えば、充電電気量及び放電電気量を計測する積算電力計を設けて、充電が行われている間に該積算電力計により計測された充電電気量をその充電が開始される直前に演算されていた電気量の積算値に加算し、放電が行われている間に積算電力計により計測された放電電気量を、その放電が開始される直前に演算されていた電気量から減算することにより、充電電気量及び放電電気量を逐次積算して、各時刻で演算されている電気量の定格容量に対する百分率(%)を、その時刻でのSOCとする。
鉛蓄電池のより長寿命化を図るため、本発明では、1.80~2.42V/セルの電圧範囲を電池電圧(電池の端子電圧)の規程範囲として、電池電圧をこの規程範囲に保って鉛蓄電池の放電と充電とを行うことにより鉛蓄電池を運用する。
本発明の運用方法を実施するに当っては、鉛蓄電池の劣化を抑制するために、定期的に、鉛蓄電池をリフレッシュさせるために、鉛蓄電池を満充電状態にするまで、均等充電(リフレッシュ充電)を行うのが好ましい。均等充電は、多数個の二次電池を一組にして長時間使用した場合に生じる電池間の充電状態のバラツキをなくし、充電状態を均一にするために行なう充電である。均等充電では、各電池の電池電圧が所定電圧になるまでは定電流充電を行ない、その後定電圧で一定時間充電を行う。
運用時の最大放電電流は、0.4CA以下とすることが好ましい。尚、ここで述べる「C」とは、鉛蓄電池の定格容量(Ah:アンペアアワー)であり、規定の温度、放電電流及び終止電圧条件で、満充電状態(SOC:100%)から取り出せる電気量を示す。
運用時の最大充電電流は、0.3CA以下とすることが好ましい。運用時の最大充電電流は、鉛蓄電池の寿命に影響を及ぼす。最大充電電流を0.3CA以下として充電を行うことにより、鉛蓄電池の急激な電圧上昇を避け、電池本体の温度上昇及び正極格子の腐食を抑制することができる。
本発明の運用方法により鉛蓄電池が運用される蓄電装置には、本発明に係わる運用方法で鉛蓄電池を運用するように各鉛蓄電池の充電及び放電を制御する充放電制御装置を設けておく。この充放電制御装置は、SOC、電池電圧、最大放電電流及び最大充電電流を検出する手段と、これらの検出値を本発明の運用方法における目標範囲に保つように鉛蓄電池の充電及び放電を制御する手段とにより構成することができる。鉛蓄電池の充放電を制御する手法は公知の方法によればよい。
鉛に、スズ:1.6質量%、カルシウム:0.08質量%を添加混合して混合物全体を100質量%とした鉛合金を溶融し、重力鋳造方式によって縦:385mm、横:140mm、厚み:5.8mmの格子基板を作製した。ここで、骨の断面形状は、縦骨、横骨ともに六角形とし、それぞれの骨の高さを3.2mm、幅を2.4mmとした。この格子基板に、一酸化鉛を主成分とする鉛粉の質量に対して、ポリエステル繊維を0.1質量%加えて混合し、次に水を12質量%、希硫酸を16質量%加えて再び混練したペースト状活物質を充填した。格子基板に活物質を充填した後は、熟成及び乾燥を行って正極板とした。
鉛に、スズ:0.2質量%、カルシウム:0.1質量%を添加混合して混合物全体を100質量%として作製した鉛合金を溶融し、重力鋳造方式によって縦:385mm、横:140mm、厚み:3.0mmの格子基板を作製した。ここで骨の断面形状は、縦骨及び横骨ともに六角形とし、それぞれの骨の高さを2.6mm、幅を1.8mmとした。また、一酸化鉛を主成分とする鉛粉の質量に対して、リグニン:0.2質量%、硫酸バリウム:0.1質量%、通常の市販されている黒鉛等のカーボン粉末:0.2質量%、ポリエステル繊維:0.1質量%を加えて混合した。次に、これに水:12質量%を加えて混練した後、更に希硫酸:13質量%を加えて再び混練して得たペースト状活物質を上記格子基板に充填した。格子基板に活物質を充填した後、熟成及び乾燥を行って負極板とした。
上述した正極板と負極板とを、間にセパレータを介在させながら1枚ずつ交互に積層し、同極板同士をストラップで連結して、正極板:24枚/負極板:25枚からなる極板群を作製した。この極板群を電槽の中に入れ、希硫酸を注液し、化成を行って2V-1500Ahの制御弁式鉛蓄電池を作製した。
上記のようにして作製した鉛蓄電池を用い、25℃の環境温度において運用試験を行った。また試験に供した電池に対しては、1カ月毎に25℃環境下にて0.1CA放電容量(0.1CA=150A)で定電流放電を実施し、電池電圧が放電終止電圧1.80V/セルになった時点で試験を終了して、その放電時間からAhを計算して放電容量とした。このようにして測定した放電容量の推移を確認した。尚、電池が寿命に到るまで劣化が進んだか否かを判断する目安として、初期の電池容量の70%の容量を寿命判定容量とし、電池容量が初期の容量に対し70%以下となった状態を寿命に達した状態として、劣化の進行度合いを判定した。
SOCの影響を把握する運用の試験を行った。この試験では、SOCを60%、充電電流を0.2CA、放電電流を0.2CAとして、1秒間の放電と1秒間の充電とを休止期間をおかずに繰り返し、試験温度を25℃として、電池電圧を、1.80V~2.42V/セルの範囲に保つように制御して試験を行い、各試験との劣化進行度合いを比較した。本実施例では、運用試験の期間を通じて、SOCを60%に維持した。
SOCの影響を把握する運用の試験として、SOCを30%、充電電流を0.2CA、放電電流を0.2CAとして、1秒間の放電と1秒間の充電とを休止期間を置かずに繰り返し、試験温度を25℃として、電池電圧を、1.80V~2.42V/セルの範囲に保つように制御して試験を行い、各試験との劣化進行度合いを比較した。本実施例では、運用試験の期間を通じて、SOCを30%に維持した。本実施例と実施例1との相違点は、SOCのみである。
SOCの影響を把握する運用の試験として、SOCを90%、充電電流を0.2CA、放電電流を0.2CAとして、1秒間の放電と1秒間の充電とを休止期間を置かずに繰り返し、試験温度を25℃として、電池電圧を、1.80V~2.42V/セルの範囲に保つように制御して試験を行い、各試験との劣化進行度合いを比較した。本実施例では、運用試験の期間を通じて、SOCを90%に維持した。本実施例と実施例1との相違点は、SOCのみである。
SOCの影響を把握する運用の試験として、SOCを20%、充電電流を0.2CA、放電電流を0.2CAとして、1秒間の放電と1秒間の充電とを休止期間を置かずに繰り返し、試験温度を25℃として、電池電圧を、1.80V~2.42V/セルの範囲に保つように制御して試験を行い、各試験との劣化進行度合いを比較した。本比較例では、運用試験の期間を通じて、SOCを20%に維持した。本比較例と実施例1との相違点は、SOCのみである。
SOCの影響を把握する運用の試験として、SOCを100%、充電電流を0.2CA、放電電流を0.2CAとして、1秒間の放電と1秒間の充電とを休止期間を置かずに繰り返し、試験温度を25℃として、電池電圧を、1.80V~2.42V/セルの範囲に保つように制御して試験を行い、各試験との劣化進行度合いを比較した。本比較例では、運用試験の期間を通じて、SOCを100%に維持した。本比較例と実施例1との相違点は、SOCのみである。
電圧の影響を把握する運用の試験として、SOCを30%、充電電流を0.2CA、放電電流を0.2CAとして、1秒間の放電と1秒間の充電とを休止期間をおかずに繰り返し、試験温度を25℃として、電池電圧を、1.70V~2.42V/セルの範囲に保つように制御して試験を行い、各試験との劣化進行度合いを比較した。本参考例では、運用試験の期間を通じて、SOCを30%に維持した。本参考例は電圧制御のみが実施例2と相違する。
電圧の影響を把握する運用の試験として、SOCを90%、充電電流を0.2CA、放電電流を0.2CAとして、1秒間の放電と1秒間の充電とを休止期間を置かずに繰り返し、試験温度を25℃として、電池電圧を、1.80V~2.52V/セルの範囲に保つように制御して試験を行い、各試験との劣化進行度合いを比較した。本参考例では、運用試験の期間を通じて、SOCを90%に維持した。本参考例は、電圧制御のみが実施例3と相違する。
温度補正の影響を把握する運用の試験として、SOCを90%、充電電流を0.2CA、放電電流を0.2CAとして、1秒間の放電と1秒間の充電とを休止期間を置かずに繰り返した。また試験温度を40℃とし、電池電圧を1.725V~2.345V/セルの範囲(1つのセル当たり、-5mV/℃の温度補正を行った)に保つように電圧制御を行って試験を行い、各試験との劣化進行度合いを比較した。本実施例では、運用試験の期間を通じて、SOCを90%に維持した。
温度補正の影響を把握する運用の試験として、SOCを90%、充電電流を0.2CA、放電電流を0.2CAとして、1秒間の放電と1秒間の充電とを休止期間を置かずに繰り返し、試験温度を40℃として、電池電圧を1.80V~2.42V/セル(温度補正なし)の範囲に保つように制御する試験を行い、各試験との劣化進行度合いを比較した。本実施例では、運用試験の期間を通じて、SOCを90%に維持した。本実施例は、電池電圧の範囲の温度補正を行わなかった点のみが実施例4と相違する。
温度補正の影響を把握する運用の試験として、SOCを30%、充電電流を0.2CA、放電電流を0.2CAとして、1秒間の放電と1秒間の充電とを休止期間を置かずに繰り返し、試験温度を40℃として、電池電圧を1.725V~2.345V/セルの範囲(電圧範囲の上限値及び下限値に対して1つのセル当たり、-5mV/℃の温度補正を行った)に保つように制御する試験を行い、各試験との劣化進行度合いを比較した。本実施例では、運用試験の期間を通じて、SOCを30%に維持した。
温度補正の影響を把握する運用の試験として、SOCを30%、充電電流を0.2CA、放電電流を0.2CAとして、1秒間の放電と1秒間の充電とを休止期間を置かずに繰り返し、試験温度を40℃として、電池電圧を1.65V~2.27V/セルの範囲(電圧範囲の上限値及び下限値に対し1つのセル当たり、-10mV/℃の温度補正を行った)に保つように制御する試験を行い、各試験との劣化進行度合いを比較した。本実施例では、運用試験の期間を通じて、SOCを30%に維持した。本実施例は、温度補正に基づく電圧制御のみが実施例6と相違する。
放電電流の影響を把握する運用の試験として、SOCを60%、充電電流を0.2CA、放電電流を0.4CAとして、2秒間の充電と1秒間の放電とを休止期間を置かずに繰り返し、試験温度を25℃として、電池電圧を1.80V~2.42V/セルの範囲に保つように制御する試験を行い、各試験との劣化進行度合いを比較した。本実施例では、運用試験の期間を通じて、SOCを60%に維持した。
放電電流の影響を把握する運用の試験として、SOCを60%、充電電流を0.2CA、放電電流を0.6CAとして、3秒間の充電と3秒間の放電とを休止期間を置かずに繰り返し、試験温度を25℃として、電池電圧を1.80V~2.42V/セルの範囲に保つように制御する試験を行い、各試験との劣化進行度合いを比較した。本実施例では、運用試験の期間を通じて、SOCを60%に維持した。本実施例は、放電電流及び充電時間が実施例8と相違する。
充電電流の影響を把握する運用の試験として、SOCを60%、充電電流を0.3CA、放電電流を0.2CAとして、1秒間の充電と1.5秒間の放電とを休止期間を置かずに繰り返し、試験温度を25℃として、電池電圧を1.80V~2.42V/セルの範囲に保つように制御する試験を行い、各試験との劣化進行度合いを比較した。本実施例では、運用試験の期間を通じて、SOCを60%に維持した。
充電電流の影響を把握する運用の試験として、SOCを60%、充電電流を0.4CA、放電電流を0.2CAとして、1秒間の充電と2秒間の放電とを休止期間を置くことなく繰り返し、試験温度を25℃として、電池電圧を1.80V~2.42V/セルの範囲に保つように制御する試験を行い、各試験との劣化進行度合いを比較した。本実施例では、運用試験の期間を通じて、SOCを60%に維持した。本実施例は、充電電流及び放電時間のみが実施例10と相違する。
前述した実施例1~11、比較例1,2及び参考例1,2について、各条件を下記の表1に纏めて記載する。
実施例8:28800/5000=5.7倍
実施例9:21600/5000=4.3倍
実施例10:34560/5000=6.9倍
実施例11:28800/5000=5.7倍
<SOCの影響把握:実施例1~3、比較例1、2>
図2に0.1CA放電試験の容量推移を示す。実施例1~3では、試験期間24ヶ月の間初期容量を維持しているのに対し、比較例1では約18ヶ月で寿命となった。寿命となった電池を解体したところ、負極板に硫酸鉛が多く蓄積しており、これが寿命原因であることが判った。即ち、比較例1においては、充電不足の状態が長く続いたことにより、電池寿命が短くなったと判断できる。更に、比較例2では約12ヶ月で寿命となった。寿命となった電池を解体したところ、腐食による正極板の伸びが激しく、これが寿命原因であることが判った。即ち、比較例2においては、SOCが100%に維持されている状態で0.2CA充電を行った結果、瞬間的に電池の電圧が上昇し、正極が酸化されやすい電位におかれる状態が繰り返されたことにより、電池寿命が短くなったと判断できる。
図3に0.1CA放電試験の容量推移を示す。実施例2~3は、試験期間24ヶ月の間初期容量を維持しているのに対し、参考例1では約21ヶ月で寿命となった。寿命となった電池を解体したところ、負極板に硫酸鉛が多く蓄積しており、これが寿命原因であるとわかった。即ち、参考例1においては、充電不足の状態が長く続いたことにより、電池寿命が短くなったと判断できる。更に、参考例2では約18ヶ月で寿命となった。寿命となった電池を解体したところ、腐食による正極板の伸びが激しく、これが寿命原因であるとわかった。即ち、参考例2においては、過充電の状態が長く続いたことにより、電池寿命が短くなったと判断できる。
図4に0.1CA放電試験の容量推移を示す。実施例4では、試験期間24ヶ月の間初期容量を維持しているのに対し、実施例5では約22ヶ月で寿命となった。寿命となった電池を解体したところ、高温環境下による化学反応の活性化が起こり、腐食による正極板の伸びが進んでおり、これが寿命原因であることがわかった。即ち、実施例5においては、温度補正を加えていないので過充電の状態が続いたことにより、電池寿命が短くなったと判断できる。
図5に0.1CA放電試験の容量推移を示す。実施例1及び実施例8では、試験期間24ヶ月の間初期容量を維持しているのに対し、実施例9では約23ヶ月で寿命となった。寿命となった電池を解体したところ、放電電流を大きくしたことによる電池電圧の低下のため、負極板に硫酸鉛が多く蓄積しており、これが寿命原因であることがわかった。即ち、実施例9においては、瞬間的な深い放電が繰り返されることにより、電池寿命が短くなったと判断できる。
図6に0.1CA放電試験の容量推移を示す。実施例1及び実施例10では、試験期間24ヶ月の間初期容量を維持しているのに対し、実施例11では約24ヶ月で寿命となった。寿命となった電池を解体したところ、充電電流を大きくしたことによる電池電圧の上昇のため、腐食による正極板の伸びが進んでおり、これが寿命原因であるとわかった。即ち、実施例11においては、瞬間的な過充電が繰り返されることにより、電池寿命が短くなったと判断できる。
2…細骨
Claims (7)
- 自然エネルギー発電装置の発電量の変動を補償するために前記発電装置に接続されて、前記発電装置の出力による充電と外部回路への放電とが行われる鉛蓄電池を運用する鉛蓄電池の運用方法であって、
前記鉛蓄電池の満充電状態を100%として、前記鉛蓄電池の充電状態を、30~90%の範囲内に維持し、
かつ、電池電圧を1.80~2.42V/セルの規程範囲に保って前記鉛蓄電池の放電及び充電を行うことにより前記鉛蓄電池を運用する、
鉛蓄電池の運用方法。 - 請求項1に記載された鉛蓄電池の運用方法において、
25℃を基準温度として、前記鉛蓄電池の雰囲気温度が前記基準温度であるときに電池電圧を前記規程範囲に保って前記鉛蓄電池の放電及び充電を行い、
前記雰囲気温度が前記基準温度よりも上昇しているときには、前記雰囲気温度の基準温度からの上昇量に応じて、前記規程範囲の上限値及び下限値を1セル当たり4mV/℃~6mV/℃の範囲に選定した補正量だけ低下させる補正を行うことにより補正後電圧範囲を求めて、前記電池電圧を前記補正後電圧範囲に保って、前記鉛蓄電池の放電及び充電を行い、
前記雰囲気温度が前記基準温度よりも低下しているときには、前記雰囲気温度の基準温度からの低下量に応じて、前記規程範囲の上限値及び下限値を1セル当たり4mV/℃~6mV/℃の範囲に選定した補正量だけ上昇させる補正を行うことにより補正後電圧範囲を求めて、前記電池電圧を前記補正後電圧範囲に保って、前記鉛蓄電池の放電及び充電を行うことにより前記鉛蓄電池を運用する、
鉛蓄電池の運用方法。 - 請求項1又は2に記載された鉛蓄電池の運用方法において、
運用時の鉛蓄電池の最大放電電流を、0.4CA(Cは、鉛蓄電池の定格容量[Ah]を示す。)以下に維持する、
鉛蓄電池の運用方法。 - 請求項1乃至3の何れかに記載された鉛蓄電池の運用方法において、
運用時の鉛蓄電池の最大充電電流を、0.3CA(Cは、鉛蓄電池の定格容量[Ah]を示す。)以下に維持する、
鉛蓄電池の運用方法。 - 請求項1ないし4の何れかに記載された鉛蓄電池の運用方法において、
前記鉛蓄電池の運用が開始された後、設定された期間が経過する毎に運用を中断して、前記鉛蓄電池を満充電状態まで均等充電するリフレッシュ充電を行う鉛蓄電池の運用方法。 - 請求項1乃至5の何れかに記載された鉛蓄電池の運用方法において、
運用時の鉛蓄電池の充電状態を、充電電気量及び放電電気量(Ah)を積算することにより演算する、
鉛蓄電池の運用方法。 - 自然エネルギー発電装置の出力の変動を補償するために前記発電装置に接続されて、前記発電装置による充電と、外部への放電とが行われる鉛蓄電池を備えた蓄電装置であって、
請求項1乃至6の何れかに記載された運用方法で前記鉛蓄電池を運用するように前記鉛蓄電池の充電及び放電を制御する充放電制御装置を備えている、
自然エネルギー発電設備用蓄電装置。
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