CN104078695A - Full-sedimentary type lead acid liquid current battery energy storing device - Google Patents
Full-sedimentary type lead acid liquid current battery energy storing device Download PDFInfo
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- CN104078695A CN104078695A CN201410347663.0A CN201410347663A CN104078695A CN 104078695 A CN104078695 A CN 104078695A CN 201410347663 A CN201410347663 A CN 201410347663A CN 104078695 A CN104078695 A CN 104078695A
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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
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/18—Regenerative fuel cells, e.g. redox flow batteries or secondary fuel cells
- H01M8/184—Regeneration by electrochemical means
- H01M8/188—Regeneration by electrochemical means by recharging of redox couples containing fluids; Redox flow type batteries
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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
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/04694—Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
- H01M8/04858—Electric variables
- H01M8/04865—Voltage
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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
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/04694—Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
- H01M8/04858—Electric variables
- H01M8/04895—Current
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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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
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- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
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Abstract
The invention discloses a full-sedimentary type lead acid liquid current battery energy storing device. The device comprises a liquid storing tank, a circulating pump, a flowmeter, an infusion tube, a reactor and an alternating current-direct current converter, wherein a guide wire, a battery lead plate, and other accessory devices are arranged on the reactor; an electrolyte in the liquid storing tank flows into the reactor under the function of the circulating pump and flows back to the liquid storage tank after the electrolyte is subjected to a redox reaction. According to the device, during charging, Pb ions in the electrolyte are subjected to a redox reaction resulting in the sedimentation of PbO2 on a positive plate and the sedimentation of Pb on a negative plate while during discharging, the sediments, namely the PbO2 on the positive plate and the Pb on the negative plate, are subject to the redox reaction so as to generate Pb ions for dissolving in the electrolyte, wherein during the charging and discharging processes, the magnitude of the electrolyte current is regulated through the flowmeter according to the differences in the aspects of charging and discharging current, the size of voltage or the number of the batter lead plate in the reactor.
Description
Technical field
The present invention relates to a kind of redox flow batteries energy storage device, particularly a kind of full appositional pattern lead-acid flow battery energy storage device, belongs to energy science and technology new forms of energy and energy-saving field.
Background technology
Energy crisis and environmental pollution have threatened the mankind's survival and development, and large-scale development and the carbon-free clean distributed energy of application have become the current and theme of human society life from now on.In carbon-free clean distributed energy, the abundantest and on the largest scaleization application prospect of reserves be solar energy and the wind energy distributed energy.But the solar energy of occurring in nature and wind energy energy density are low, extremely inhomogeneous in time and Regional Distribution, very large with seasonal fluctuations, regional differences in time, these are all the bottlenecks that limits its scale Application and Development.
Redox flow batteries is as novel electric power storage energy storage device, there is many potential premium properties, as large in stored energy capacitance, can to surpass deep discharge, long service life, concentration polarization little etc., and not limited by geographical conditions, can be used as the supporting energy storage device of solar energy, wind energy distributed clean energy resource, can also improve transmission of electricity quality as the peak adjusting device of electrical network, ensure power grid security.
Because the kind of redox flow batteries is different, its reaction mechanism is different.In the redox flow batteries such as traditional full vanadium system, sodium polysulfide/bromine system and iron/chromium system, there are two main weak points: one is key component barrier film, its performance is not very stable, and barrier film is expensive, and this is the bottleneck of traditional liquid flow energy storage battery development.Another one needs two cover transfusion systems, makes system configuration complicated, and cost increases.
Summary of the invention
For overcoming the problem of barrier film and the two cover transfusion systems of expensive and unstable properties, the object of this invention is to provide a kind of full appositional pattern lead-acid flow battery energy storage device, both positive and negative polarity is used same liquid, the plumbous mixed liquor of pyrovinic acid and pyrovinic acid of all take is electrolyte, has avoided the cross pollution of electrolyte and expensive amberplex problem.Make it compared with prior art, with traditional the same storage that realizes the energy of redox flow batteries, avoid the complexity of two cover transfusion systems and the expensive shortcoming of barrier film simultaneously.
Technical scheme of the present invention is as follows.
A full appositional pattern lead-acid flow battery energy storage device, is characterized in that: described full appositional pattern lead-acid flow battery energy storage device is comprised of fluid reservoir, circulating pump, flowmeter, woven hose, reactor, alterating and direct current converter, electric energy and load; Described reactor has the auxiliary devices such as wire, battery lead plate.
The present invention compared with prior art, has the following advantages and high-lighting effect.
Full appositional pattern lead-acid flow battery energy storage device is usingd soluble pyrovinic acid lead as the matrix solution of both positive and negative polarity, and reduction-state and the oxidation state of positive negative electricity centering are all present in electrolyte with soluble lead(II) ion, and its corresponding oxidation state PbO
2be insoluble to electrolyte with reduction-state Pb, and be deposited on positive and negative electrode surface.In reactor in full appositional pattern lead-acid flow battery energy storage device, with the electrolyte in the He Ji chamber, utmost point chamber between two pole plates, two-plate, form a charge/discharge unit, electrolyte is connected and realizes circulation with circulating pump, fluid reservoir outside reactor by liquid-transport pipe-line, completes energy storage and with can process.
Full appositional pattern lead-acid flow battery energy storage device provided by the invention, due to the parallel join of realizing between each electrode, there is larger unit volume electrode reaction area and electrode current distribution uniformly and electrolyte flow field, positive-negative electrode plate alternative arrangement, positive-negative electrode plate number is determined by battery capacity size.Thereby can obtain obtaining larger battery charging and discharging electric current and voltage and more stable charge-discharge performance in identical reactor volume.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of full appositional pattern lead-acid flow battery energy storage device of the present invention.
In figure: 1-circulating pump; 2-flowmeter; 3-woven hose; 4-reactor; 5-alterating and direct current transducer; 6-fluid reservoir; 7-battery lead plate; 8-wire; 9-electric energy; 10-load.
Embodiment
Below in conjunction with accompanying drawing, the present invention is described further with concrete case study on implementation.
Fig. 1 is the schematic diagram of full appositional pattern lead-acid flow battery energy storage device of the present invention.Described full appositional pattern lead-acid flow battery energy storage device is comprised of circulating pump 1, flowmeter 2, woven hose 3, reactor 4, alterating and direct current transducer 5, fluid reservoir 6, electric energy 9 and load 10; Described reactor has the auxiliary devices such as battery lead plate 7 and wire 8.
Operation logic of the present invention is: after mains switch is connected, circulating pump 1 flow into the electrolyte in fluid reservoir 6 in reactor 4 by woven hose 3, and the liquid level of electrolyte in reactor constantly raises and arrive outlet and from reactor, flow out through woven hose 4 and flow in fluid reservoir 7 and realize circulating of electrolyte.During charging, the gear in alterating and direct current transducer 5 is adjusted to charging shift.At this moment, electric current passes in battery lead plate 7 through wire 8, under the condition that has electric current to pass through, and the Pb ion generation redox reaction in electrolyte and deposit on positive plate on PbO2 and negative plate and deposit Pb.During electric discharge, the gear in alterating and direct current transducer 5 is adjusted to electric discharge shelves.At this moment, the PbO2 on positive/negative plate and Pb deposit generation redox reaction generate Pb ion and are added in electrolyte, simultaneously generation current and flow to load 10 on whole loop.In charge and discharge process, need to be according to the different sizes of adjusting flow of electrolyte by flowmeter 2 of the number of battery lead plate 7 in the size of charging and discharging currents, voltage or reactor 4.
Embodiment.
Full appositional pattern lead-acid flow battery energy storage device provided by the invention is on probation on small-sized device of solar generating, is arranged on the electricity consumption position of device of solar generating.Electrolyte is the mixed liquor of the pyrovinic acid lead of 1.5mol/L and the pyrovinic acid of 0.9mol/L; The volume of fluid reservoir is 10L, and the flow of electrolyte is 2L/min; Battery lead plate number is 50, and wherein positive/negative plate is respectively 25; Charging and discharging currents is 20A, and the time of discharging and recharging is 10h.
Energy storage device has moved 100 charge and discharge cycles, stable in charge and discharge process, reliable, does not occur that deposit comes off or deposit adhesion causes opening circuit or the phenomenon of short circuit in running.After stopping discharging and recharging, deposit on battery lead plate is dense and even, illustrate that flow battery energy storage device of the present invention is under this flow of electrolyte and structure of reactor design condition, electrolyte distributes very evenly at reactor flow field, and with battery lead plate between contact very fully, make flow battery energy storage device there is stable charge-discharge performance.
The above, be only the specific embodiment of the present invention, and when not limiting with this scope of enforcement of the present invention, all equivalent variations of doing according to the present invention and modification, all should belong to protection scope of the present invention.
Claims (2)
1. a full appositional pattern lead-acid flow battery energy storage device, is characterized in that: described full appositional pattern lead-acid flow battery energy storage device is comprised of circulating pump (1), flowmeter (2), woven hose (3), reactor (4), alterating and direct current transducer (5), fluid reservoir (6), electric energy (9) and load (10); Described reactor has the auxiliary devices such as battery lead plate (7) and wire (8).
2. according to full appositional pattern lead-acid flow battery energy storage device claimed in claim 1, it is characterized in that positive-negative electrode plate alternative arrangement in described reactor, positive-negative electrode plate number is determined by battery capacity size.
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105845960A (en) * | 2016-05-06 | 2016-08-10 | 华中科技大学 | Lead liquid flow battery and electrolytic cell thereof |
CN106684420A (en) * | 2016-12-20 | 2017-05-17 | 华中科技大学 | Lead redox flow battery with flow field design |
CN106711486A (en) * | 2016-12-13 | 2017-05-24 | 华中科技大学 | Lead redox flow battery electrolyte |
CN110140250A (en) * | 2017-11-28 | 2019-08-16 | 住友电气工业株式会社 | Redox flow batteries |
CN110718709A (en) * | 2019-10-18 | 2020-01-21 | 大连大学 | Single-liquid film-free full-deposition type lead-acid flow battery device and working method thereof |
RU2809218C1 (en) * | 2023-06-19 | 2023-12-07 | Федеральное государственное казенное военное образовательное учреждение высшего образования "Рязанское гвардейское высшее воздушно-десантное ордена Суворова дважды Краснознаменное командное училище имени генерала армии В.Ф. Маргелова" Министерства обороны Российской Федерации | Lead acid battery |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101853956A (en) * | 2010-06-12 | 2010-10-06 | 江苏华富控股集团有限公司 | Lead-acid flow battery |
CN102290588A (en) * | 2011-07-25 | 2011-12-21 | 中国东方电气集团有限公司 | Flow cell system and control method and device thereof |
CN103715447A (en) * | 2013-11-20 | 2014-04-09 | 浩源科技有限公司 | Efficient soluble lead-acid flow battery |
-
2014
- 2014-07-22 CN CN201410347663.0A patent/CN104078695A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101853956A (en) * | 2010-06-12 | 2010-10-06 | 江苏华富控股集团有限公司 | Lead-acid flow battery |
CN102290588A (en) * | 2011-07-25 | 2011-12-21 | 中国东方电气集团有限公司 | Flow cell system and control method and device thereof |
CN103715447A (en) * | 2013-11-20 | 2014-04-09 | 浩源科技有限公司 | Efficient soluble lead-acid flow battery |
Non-Patent Citations (1)
Title |
---|
牛微 等: "无膜单液全沉积型铅酸液流电池研究进展", 《沈阳工程学院学报(自然科学版)》, vol. 7, no. 4, 31 October 2011 (2011-10-31) * |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105845960A (en) * | 2016-05-06 | 2016-08-10 | 华中科技大学 | Lead liquid flow battery and electrolytic cell thereof |
CN106711486A (en) * | 2016-12-13 | 2017-05-24 | 华中科技大学 | Lead redox flow battery electrolyte |
CN106711486B (en) * | 2016-12-13 | 2020-05-19 | 华中科技大学 | Lead flow battery electrolyte |
CN106684420A (en) * | 2016-12-20 | 2017-05-17 | 华中科技大学 | Lead redox flow battery with flow field design |
CN106684420B (en) * | 2016-12-20 | 2019-05-31 | 华中科技大学 | A kind of lead flow battery with flow Field Design |
CN110140250A (en) * | 2017-11-28 | 2019-08-16 | 住友电气工业株式会社 | Redox flow batteries |
CN110140250B (en) * | 2017-11-28 | 2022-07-08 | 住友电气工业株式会社 | Redox flow battery |
CN110718709A (en) * | 2019-10-18 | 2020-01-21 | 大连大学 | Single-liquid film-free full-deposition type lead-acid flow battery device and working method thereof |
RU2809218C1 (en) * | 2023-06-19 | 2023-12-07 | Федеральное государственное казенное военное образовательное учреждение высшего образования "Рязанское гвардейское высшее воздушно-десантное ордена Суворова дважды Краснознаменное командное училище имени генерала армии В.Ф. Маргелова" Министерства обороны Российской Федерации | Lead acid battery |
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