CN102332596B - All-iron redox energy storage cell, electrolyte of battery and preparation method of electrolyte - Google Patents
All-iron redox energy storage cell, electrolyte of battery and preparation method of electrolyte Download PDFInfo
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- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims abstract description 74
- 239000003792 electrolyte Substances 0.000 title claims abstract description 56
- 229910052742 iron Inorganic materials 0.000 title claims abstract description 50
- 238000004146 energy storage Methods 0.000 title claims abstract description 29
- 238000002360 preparation method Methods 0.000 title claims abstract description 7
- 210000000352 storage cell Anatomy 0.000 title claims 4
- -1 iron ion Chemical class 0.000 claims abstract description 15
- 239000000654 additive Substances 0.000 claims abstract description 7
- 239000003115 supporting electrolyte Substances 0.000 claims abstract description 7
- 239000007864 aqueous solution Substances 0.000 claims abstract description 4
- 239000000243 solution Substances 0.000 claims description 20
- 239000008367 deionised water Substances 0.000 claims description 16
- 229910021641 deionized water Inorganic materials 0.000 claims description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 claims description 12
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 claims description 10
- 238000003756 stirring Methods 0.000 claims description 8
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 claims description 6
- 235000019270 ammonium chloride Nutrition 0.000 claims description 6
- 235000002639 sodium chloride Nutrition 0.000 claims description 6
- 239000011592 zinc chloride Substances 0.000 claims description 5
- 235000005074 zinc chloride Nutrition 0.000 claims description 5
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 4
- 230000000996 additive effect Effects 0.000 claims description 4
- 229910021380 Manganese Chloride Inorganic materials 0.000 claims description 3
- GLFNIEUTAYBVOC-UHFFFAOYSA-L Manganese chloride Chemical compound Cl[Mn]Cl GLFNIEUTAYBVOC-UHFFFAOYSA-L 0.000 claims description 3
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical group [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims description 3
- 239000011565 manganese chloride Substances 0.000 claims description 3
- 235000002867 manganese chloride Nutrition 0.000 claims description 3
- 229940099607 manganese chloride Drugs 0.000 claims description 3
- 239000001103 potassium chloride Substances 0.000 claims description 3
- 235000011164 potassium chloride Nutrition 0.000 claims description 3
- OTYBMLCTZGSZBG-UHFFFAOYSA-L potassium sulfate Chemical compound [K+].[K+].[O-]S([O-])(=O)=O OTYBMLCTZGSZBG-UHFFFAOYSA-L 0.000 claims description 3
- 229910052939 potassium sulfate Inorganic materials 0.000 claims description 3
- 235000011151 potassium sulphates Nutrition 0.000 claims description 3
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical group [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 claims description 3
- 229910000368 zinc sulfate Inorganic materials 0.000 claims description 3
- 229960001763 zinc sulfate Drugs 0.000 claims description 3
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims description 2
- 229910021555 Chromium Chloride Inorganic materials 0.000 claims description 2
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 claims description 2
- 229910002651 NO3 Inorganic materials 0.000 claims description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 2
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 claims description 2
- 229910052921 ammonium sulfate Inorganic materials 0.000 claims description 2
- 235000011130 ammonium sulphate Nutrition 0.000 claims description 2
- 239000001110 calcium chloride Substances 0.000 claims description 2
- 229910001628 calcium chloride Inorganic materials 0.000 claims description 2
- 235000011148 calcium chloride Nutrition 0.000 claims description 2
- QSWDMMVNRMROPK-UHFFFAOYSA-K chromium(3+) trichloride Chemical compound [Cl-].[Cl-].[Cl-].[Cr+3] QSWDMMVNRMROPK-UHFFFAOYSA-K 0.000 claims description 2
- GRWVQDDAKZFPFI-UHFFFAOYSA-H chromium(III) sulfate Chemical compound [Cr+3].[Cr+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O GRWVQDDAKZFPFI-UHFFFAOYSA-H 0.000 claims description 2
- 239000011790 ferrous sulphate Substances 0.000 claims description 2
- 235000003891 ferrous sulphate Nutrition 0.000 claims description 2
- 229910000359 iron(II) sulfate Inorganic materials 0.000 claims description 2
- 229940099596 manganese sulfate Drugs 0.000 claims description 2
- 239000011702 manganese sulphate Substances 0.000 claims description 2
- 235000007079 manganese sulphate Nutrition 0.000 claims description 2
- SQQMAOCOWKFBNP-UHFFFAOYSA-L manganese(II) sulfate Chemical compound [Mn+2].[O-]S([O-])(=O)=O SQQMAOCOWKFBNP-UHFFFAOYSA-L 0.000 claims description 2
- 239000011780 sodium chloride Substances 0.000 claims description 2
- 229910052938 sodium sulfate Inorganic materials 0.000 claims description 2
- 235000011152 sodium sulphate Nutrition 0.000 claims description 2
- 150000003839 salts Chemical class 0.000 claims 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims 1
- 239000011449 brick Substances 0.000 claims 1
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 claims 1
- 229910052720 vanadium Inorganic materials 0.000 abstract description 14
- 239000011149 active material Substances 0.000 abstract description 7
- 229910017053 inorganic salt Inorganic materials 0.000 abstract description 6
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 abstract description 6
- 231100000419 toxicity Toxicity 0.000 abstract description 3
- 230000001988 toxicity Effects 0.000 abstract description 3
- 238000002848 electrochemical method Methods 0.000 abstract description 2
- 231100000252 nontoxic Toxicity 0.000 abstract description 2
- 230000003000 nontoxic effect Effects 0.000 abstract description 2
- 230000033116 oxidation-reduction process Effects 0.000 abstract 1
- 239000008151 electrolyte solution Substances 0.000 description 6
- 229960002089 ferrous chloride Drugs 0.000 description 6
- NMCUIPGRVMDVDB-UHFFFAOYSA-L iron dichloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 description 6
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 3
- 238000003487 electrochemical reaction Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000002243 precursor Substances 0.000 description 3
- VTLYFUHAOXGGBS-UHFFFAOYSA-N Fe3+ Chemical compound [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- SURQXAFEQWPFPV-UHFFFAOYSA-L iron(2+) sulfate heptahydrate Chemical compound O.O.O.O.O.O.O.[Fe+2].[O-]S([O-])(=O)=O SURQXAFEQWPFPV-UHFFFAOYSA-L 0.000 description 2
- BNOODXBBXFZASF-UHFFFAOYSA-N [Na].[S] Chemical compound [Na].[S] BNOODXBBXFZASF-UHFFFAOYSA-N 0.000 description 1
- XHCLAFWTIXFWPH-UHFFFAOYSA-N [O-2].[O-2].[O-2].[O-2].[O-2].[V+5].[V+5] Chemical class [O-2].[O-2].[O-2].[O-2].[O-2].[V+5].[V+5] XHCLAFWTIXFWPH-UHFFFAOYSA-N 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000011262 electrochemically active material Substances 0.000 description 1
- 238000003411 electrode reaction Methods 0.000 description 1
- 229910001447 ferric ion Inorganic materials 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000012705 liquid precursor Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 150000003681 vanadium Chemical class 0.000 description 1
- 229910001935 vanadium oxide Inorganic materials 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Classifications
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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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- Hybrid Cells (AREA)
Abstract
本发明公开一种全铁氧化还原储能电池和该电池电解液及其制备方法,所述全铁氧化还原储能电池包含一种2价铁离子电解液,由2价铁离子的无机盐以及支持电解质和添加剂的水溶液所组成。本发明全铁氧化还原储能电池,采用无毒无害的铁的无机盐作为活性物质,正负极的活性物质全部为相同的铁元素,只是根据不同的价态,构成不同的氧化还原电位,用电化学的方法,实现电能的储存和释放,避免了钒电解液的毒性,同时也大大降低了电解液的价格,有望在大规模的储能电站中得到广泛应用。The invention discloses an all-iron redox energy storage battery, an electrolyte of the battery and a preparation method thereof. The all-iron redox energy storage battery comprises a divalent iron ion electrolyte, which consists of an inorganic salt of divalent iron ions and It consists of an aqueous solution of supporting electrolytes and additives. The all-iron redox energy storage battery of the present invention adopts non-toxic and harmless iron inorganic salt as the active material, and the active materials of the positive and negative electrodes are all the same iron element, but different oxidation-reduction potentials are formed according to different valence states , using the electrochemical method to realize the storage and release of electric energy, avoiding the toxicity of the vanadium electrolyte, and also greatly reducing the price of the electrolyte, it is expected to be widely used in large-scale energy storage power stations.
Description
技术领域 technical field
本发明涉及二次电池技术领域的氧化还原储能电池,尤其是一种全铁氧化还原储能电池和该电池电解液及其制备方法。 The invention relates to a redox energy storage battery in the technical field of secondary batteries, in particular to an all-iron redox energy storage battery, an electrolyte solution of the battery and a preparation method thereof.
背景技术 Background technique
随着全球环保呼声的不断高涨,洁净能源的开发热度不断升温,与可再生能源如风能,太阳能等配套使用的大型储能电池的需求也在不断提升。比如,接近商业化应用的全钒氧化还原液流电池,钠硫电池等。 With the increasing calls for global environmental protection, the development of clean energy continues to heat up, and the demand for large-scale energy storage batteries used in conjunction with renewable energy such as wind energy and solar energy is also increasing. For example, all-vanadium redox flow batteries and sodium-sulfur batteries that are close to commercial applications.
作为智能电网不可或缺的组成系统——储能电池,大容量,低成本,长寿命以及绿色环保等是储能电池必须具备的基本特点,比如中国专利申请号200910148218.0《用于全钒液流电池的电解液及其制备方法、以及包括该电解液的全钒液流电池》,介绍了用于全钒液流电池的电解液,并介绍了全钒液流电池的工作原理。该专利自述为:“本发明的用于全钒液流电池的电解液,包括含有含钒的离子和硫酸根离子的正极电解液和负极电解液,正极电解液中的硫酸根离子浓度大于负极电解液中的硫酸根离子浓度,正极电解液和负极电解液中的总钒浓度均为2.0-8.0MOL/L。本发明的用于全钒液流电池的电解液的制备方法,包括:分别将一种或多种钒氧化物和可选的还原剂溶解于具有第一浓度和第二浓度的硫酸溶液中获得总钒浓度均为2.0-8.0MOL/L的正极电解液前驱体和负极电解液前驱体,其中第一浓度大于第二浓度;以及分别电解正极电解液前驱体和负极电解液前驱体以获得全钒液流电池的正极电解液和负极电解液。”虽然该专利的技术方案能够带来一定的效果,但由于全钒液流电池所用的金属钒盐价格还是比较贵,且具有一定的毒性,因此,研究者正在努力寻找合适的氧化还原电对,价格便宜的电解液,而且对环境友好,为储能电池的研究开辟一个新的方向。 As an indispensable component system of smart grid - energy storage battery, large capacity, low cost, long life and green environmental protection are the basic characteristics that energy storage battery must possess, such as Chinese patent application number 200910148218.0 "for all vanadium liquid flow Electrolyte for battery and its preparation method, and all-vanadium redox flow battery including the electrolyte", which introduces the electrolyte used for all-vanadium redox flow battery and introduces the working principle of all-vanadium redox flow battery. The patent reads: "The electrolytic solution for an all-vanadium redox flow battery of the present invention includes a positive electrode electrolyte and a negative electrode electrolyte containing vanadium-containing ions and sulfate ions, and the concentration of sulfate ions in the positive electrode electrolyte is greater than that of the negative electrode. The sulfate ion concentration in the electrolyte, the total vanadium concentration in the positive electrode electrolyte and the negative electrode electrolyte are both 2.0-8.0MOL/L.The preparation method of the electrolyte for the all-vanadium redox flow battery of the present invention comprises: respectively One or more vanadium oxides and an optional reducing agent are dissolved in a sulfuric acid solution with a first concentration and a second concentration to obtain a positive electrode electrolyte precursor and a negative electrode electrolytic solution with a total vanadium concentration of 2.0-8.0MOL/L liquid precursor, wherein the first concentration is greater than the second concentration; and respectively electrolyzing the positive electrode electrolyte precursor and the negative electrode electrolyte precursor to obtain the positive electrode electrolyte and the negative electrode electrolyte of the all-vanadium redox flow battery.” Although the technical solution of the patent It can bring a certain effect, but because the metal vanadium salt used in the all-vanadium redox flow battery is still relatively expensive and has certain toxicity, researchers are working hard to find a suitable redox couple and a cheap electrolyte. Moreover, it is environmentally friendly and opens up a new direction for the research of energy storage batteries.
发明内容 Contents of the invention
本发明针对现有技术的不足,提供一种全铁氧化还原储能电池和该电池电解液及其制备方法,该电池采用铁离子电解液,价格便宜,而且对环境友好。 Aiming at the deficiencies of the prior art, the present invention provides an all-iron redox energy storage battery, an electrolyte of the battery and a preparation method thereof. The battery adopts the electrolyte of iron ions, which is cheap and environmentally friendly.
为实现上述的目的,本发明采用以下技术方案: To achieve the above-mentioned purpose, the present invention adopts the following technical solutions:
本发明提供一种全铁氧化还原储能电池的电解液,是一种含有2价铁离子电解液,由2价铁离子的无机盐以及支持电解质的水溶液所组成。 The invention provides an electrolyte solution for an all-iron redox energy storage battery, which is an electrolyte solution containing divalent iron ions, and is composed of an inorganic salt of the divalent iron ions and an aqueous solution of a supporting electrolyte.
所述的2价铁离子的无机盐可以为硫酸亚铁,氯化亚铁,硝酸亚铁等,浓度在0.1~4M之间。其作用是构成全铁氧化还原储能电池的电化学活性物质。初始的活性物质,全部由2价铁组成,在第一次充电时,2价铁在负极被还原成单质铁,沉积在负极的电极表面上,形成Fe2+ / Fe的活性物质电对;而在正极,2价铁被氧化成3价铁,形成Fe3+ / Fe2+ 的活性物质电对。这样,就可以构成电池的充放电循环,实现储能电池的功效。 The inorganic salt of divalent iron ion can be ferrous sulfate, ferrous chloride, ferrous nitrate, etc., and the concentration is between 0.1-4M. Its function is to constitute the electrochemically active material of the all-iron redox energy storage battery. The initial active material is all composed of divalent iron. When charging for the first time, the divalent iron is reduced to elemental iron at the negative electrode and deposited on the electrode surface of the negative electrode to form an active material pair of Fe 2+ /Fe; On the positive electrode, 2-valent iron is oxidized to 3-valent iron, forming an active material pair of Fe 3+ /Fe 2+ . In this way, the charging and discharging cycle of the battery can be formed to realize the function of the energy storage battery.
所述支持电解质为硫酸钠,硫酸钾,硫酸铵,氯化钠,氯化钾,氯化铵,氯化钙,浓度在0.05~5M之间。其作用为增加电解液的导电性,减少电池的内阻,提高电池的性能。特别是在负极充电状态的末期,多数2价铁被还原成金属铁沉积在多孔电极上,此时,主要依赖支持电解质,实现离子的内部传导。 The supporting electrolyte is sodium sulfate, potassium sulfate, ammonium sulfate, sodium chloride, potassium chloride, ammonium chloride, calcium chloride, and the concentration is between 0.05-5M. Its function is to increase the conductivity of the electrolyte, reduce the internal resistance of the battery, and improve the performance of the battery. Especially at the end of the charge state of the negative electrode, most of the divalent iron is reduced to metallic iron and deposited on the porous electrode. At this time, it mainly depends on the supporting electrolyte to realize the internal conduction of ions.
进一步的,为了得到更好的效果,上述电解液中还可以增加添加剂,所述的添加剂为硫酸锌,硫酸锰,硫酸铬,氯化锌,氯化锰,氯化铬中一种,浓度在0.01~0.10M之间。其作用是减少电池的自放电,提高电池效率。 Further, in order to obtain a better effect, additives can also be added in the above-mentioned electrolyte, and the additives are one of zinc sulfate, manganese sulfate, chromium sulfate, zinc chloride, manganese chloride, and chromium chloride, with a concentration of Between 0.01 and 0.10M. Its function is to reduce the self-discharge of the battery and improve the efficiency of the battery.
本发明提供一种全铁氧化还原储能电池的电解液的制备方法,包括如下步骤: The invention provides a method for preparing an electrolyte of an all-iron redox energy storage battery, comprising the following steps:
第一步,称取2价铁离子的无机盐和电解质,或者和添加剂; The first step, weighing the inorganic salt and electrolyte of divalent iron ion, or and additive;
第二步,加入去离子水,搅拌,直至溶液全部溶解; In the second step, add deionized water and stir until the solution is completely dissolved;
第三步,再滴加去离子水直至溶液的体积达到设定值。 In the third step, add deionized water dropwise until the volume of the solution reaches the set value.
本发明还提供一种全铁氧化还原储能电池,该电池包含上述的含有2价铁离子电解液。 The present invention also provides an all-iron redox energy storage battery, which comprises the above-mentioned electrolyte solution containing divalent iron ions.
本发明中,全铁氧化还原储能电池活性物质为含有2价铁离子电解液,在充电状态:含有2价铁离子的电解液在负极还原为金属铁,在正极氧化为3价铁;在放电状态:负极的金属铁,氧化成2价铁离子,正极的3价铁,还原成2价铁。如此循环往复,就可以根据铁的不同氧化还原状态,将电能储存和释放。电池的工作温度在20~80℃之间。 In the present invention, the active material of the all-iron redox energy storage battery is an electrolyte containing divalent iron ions. In the charging state: the electrolyte containing divalent iron ions is reduced to metallic iron at the negative electrode and oxidized to trivalent iron at the positive electrode; Discharge state: the metallic iron at the negative electrode is oxidized to ferric ions, and the trivalent iron at the positive electrode is reduced to ferric iron. By repeating this cycle, electrical energy can be stored and released according to the different redox states of iron. The operating temperature of the battery is between 20 and 80°C.
上述电化学反应,所对应的电极电位如反应式(1),(2),(3): For the above electrochemical reactions, the corresponding electrode potentials are shown in the reaction formulas (1), (2), (3):
负极电化学反应: Fe2+ + 2e- = Fe E = -0.44V vs. SHE (1) Negative electrode electrochemical reaction: Fe 2+ + 2e - = Fe E = -0.44V vs. SHE (1)
正极电化学反应: 2Fe2+ = 2Fe3+ + 2e- E = 0.77V vs. SHE (2) Positive electrochemical reaction: 2Fe 2+ = 2Fe 3+ + 2e - E = 0.77V vs. SHE (2)
总的电极反应: 3Fe2+ = 2Fe3+ + Fe △V=1.21V (3) Total electrode reaction: 3Fe 2+ = 2Fe 3+ + Fe △V=1.21V (3)
本发明提出的全铁氧化还原储能电池,采用无毒无害的铁的无机盐作为活性物质,正负极的活性物质全部为相同的铁元素,只是根据不同的价态,构成不同的氧化还原电位,用电化学的方法,实现电能的储存和释放,避免了钒电解液的毒性,同时也大大降低了电解液的价格,有望在大规模的储能电站中得到广泛应用。 The all-iron redox energy storage battery proposed by the present invention adopts non-toxic and harmless iron inorganic salt as the active material. Reduction potential, using electrochemical methods, realizes the storage and release of electric energy, avoids the toxicity of vanadium electrolyte, and also greatly reduces the price of electrolyte, and is expected to be widely used in large-scale energy storage power stations.
具体实施方式 Detailed ways
下面对本发明的实施例作详细说明:本实施例在以本发明技术方案为前提下进行实施,给出了详细的实施方式和具体的操作过程,但本发明的保护范围不限于下述的实施例。 The embodiments of the present invention are described in detail below: the present embodiment is implemented under the premise of the technical solution of the present invention, and detailed implementation and specific operation process are provided, but the protection scope of the present invention is not limited to the following implementation example. the
实施例1 Example 1
称取25.02克七水硫酸亚铁,0.87克硫酸钾,0.287克硫酸锌一起放入1500mL的容器中,加入600mL的去离子水,搅拌,直至溶液全部溶解后,再滴加去离子水直至溶液的体积达到900mL。 Weigh 25.02 grams of ferrous sulfate heptahydrate, 0.87 grams of potassium sulfate, and 0.287 grams of zinc sulfate into a 1500mL container, add 600mL of deionized water, stir until the solution is completely dissolved, then add deionized water dropwise until the solution is The volume reaches 900mL.
把上述电解液300mL放入全铁氧化还原储能电池的负极电解液储槽中,600mL放入正极电解液储槽中,以30mL/min的速率,进入活性面积为9cm2的单电池中,以200mA的电流进行充放电,电池容量为1.28Ah,电流效率91%,电压效率55%。 Put 300mL of the above-mentioned electrolyte into the negative electrode electrolyte storage tank of the all-iron redox energy storage battery, put 600mL into the positive electrode electrolyte storage tank, and enter the single cell with an active area of 9cm2 at a rate of 30mL/min. The current of 200mA is charged and discharged, the battery capacity is 1.28Ah, the current efficiency is 91%, and the voltage efficiency is 55%.
实施例2 Example 2
称取974.99克四水氯化亚铁,335.48克氯化钾,17.81克氯化锰一起放入1500mL的容器中,加入600mL的去离子水,搅拌,直至溶液全部溶解后,再滴加去离子水直至溶液的体积达到900mL。 Weigh 974.99 grams of ferrous chloride tetrahydrate, 335.48 grams of potassium chloride, and 17.81 grams of manganese chloride into a 1500mL container, add 600mL of deionized water, stir until the solution is completely dissolved, and then add deionized water until the volume of the solution reaches 900 mL.
把上述电解液300mL放入全铁氧化还原储能电池的负极电解液储槽中,600mL放入正极电解液储槽中,以30mL/min的速率,进入活性面积为9cm2的单电池中,以200mA的电流进行充放电,电池容量为51.46Ah,电流效率95%,电压效率58%。 Put 300mL of the above-mentioned electrolyte into the negative electrode electrolyte storage tank of the all-iron redox energy storage battery, put 600mL into the positive electrode electrolyte storage tank, and enter the single cell with an active area of 9cm2 at a rate of 30mL/min. Charge and discharge at a current of 200mA, the battery capacity is 51.46Ah, the current efficiency is 95%, and the voltage efficiency is 58%.
实施例3 Example 3
称取466.77克四水氯化亚铁,120.36克氯化铵,6.13克氯化锌一起放入1500mL的容器中,加入600mL的去离子水,搅拌,直至溶液全部溶解后,再滴加去离子水直至溶液的体积达到900mL。 Weigh 466.77 grams of ferrous chloride tetrahydrate, 120.36 grams of ammonium chloride, and 6.13 grams of zinc chloride into a 1500mL container, add 600mL of deionized water, stir until the solution is completely dissolved, and then add deionized water until the volume of the solution reaches 900 mL.
把上述电解液300mL放入全铁氧化还原储能电池的负极电解液储槽中,600mL放入正极电解液储槽中,以30mL/min的速率,进入活性面积为9cm2的单电池中,以200mA的电流进行充放电,电池容量为25.73Ah,电流效率93%,电压效率53%。 Put 300mL of the above-mentioned electrolyte into the negative electrode electrolyte storage tank of the all-iron redox energy storage battery, put 600mL into the positive electrode electrolyte storage tank, and enter the single cell with an active area of 9cm2 at a rate of 30mL/min. The current of 200mA is charged and discharged, the battery capacity is 25.73Ah, the current efficiency is 93%, and the voltage efficiency is 53%.
实施例4 Example 4
称取466.77克四水氯化亚铁,120.36克氯化铵,一起放入1500mL的容器中,加入600mL的去离子水,搅拌,直至溶液全部溶解后,再滴加去离子水直至溶液的体积达到900mL。 Weigh 466.77 grams of ferrous chloride tetrahydrate and 120.36 grams of ammonium chloride, put them together into a 1500mL container, add 600mL of deionized water, stir until the solution is completely dissolved, then add deionized water dropwise until the volume of the solution reaches up to 900mL.
把上述电解液300mL放入全铁氧化还原储能电池的负极电解液储槽中,600mL放入正极电解液储槽中,以30mL/min的速率,进入活性面积为9cm2的单电池中,以200mA的电流进行充放电,电池容量为25.73Ah,电流效率93%,电压效率53%。 Put 300mL of the above-mentioned electrolyte into the negative electrode electrolyte storage tank of the all-iron redox energy storage battery, put 600mL into the positive electrode electrolyte storage tank, and enter the single cell with an active area of 9cm2 at a rate of 30mL/min. The current of 200mA is charged and discharged, the battery capacity is 25.73Ah, the current efficiency is 93%, and the voltage efficiency is 53%.
实施例5 Example 5
称取4667.7克四水氯化亚铁,1203.6克氯化铵,61.3克氯化锌一起放入15L的容器中,加入6L的去离子水,搅拌,直至溶液全部溶解后,再滴加去离子水直至溶液的体积达到9L。 Weigh 4667.7 grams of ferrous chloride tetrahydrate, 1203.6 grams of ammonium chloride, and 61.3 grams of zinc chloride into a 15L container, add 6L of deionized water, stir until the solution is completely dissolved, and then dropwise add deionized water until the volume of the solution reaches 9 L.
把上述电解液3L放入全铁氧化还原储能电池的负极电解液储槽中,6L放入正极电解液储槽中,以300mL/min的速率,进入活性面积为90cm2的单电池中,以200mA的电流进行充放电,电池容量为257.3Ah,电流效率93%,电压效率55%。 Put 3L of the above-mentioned electrolyte into the negative electrode electrolyte storage tank of the all-iron redox energy storage battery, put 6L into the positive electrode electrolyte storage tank, and enter the single cell with an active area of 90cm2 at a rate of 300mL/min. The current of 200mA is charged and discharged, the battery capacity is 257.3Ah, the current efficiency is 93%, and the voltage efficiency is 55%.
实施例6 Example 6
称取46677克四水氯化亚铁,12036克氯化铵,613克氯化锌一起放入150L的容器中,加入60L的去离子水,搅拌,直至溶液全部溶解后,再滴加去离子水直至溶液的体积达到90L。 Weigh 46677 grams of ferrous chloride tetrahydrate, 12036 grams of ammonium chloride, and 613 grams of zinc chloride into a 150L container, add 60L of deionized water, stir until the solution is completely dissolved, and then add deionized water until the volume of the solution reaches 90 L.
把上述电解液30L放入全铁氧化还原储能电池的负极电解液储槽中,60L放入正极电解液储槽中,以3L/min的速率,进入由10个单电池活性面积为90cm2所组成的电池堆中,以200mA的电流进行充放电,电池容量为2573Ah,电流效率95%,电压效率60%。 Put 30L of the above-mentioned electrolyte into the negative electrode electrolyte storage tank of the all-iron redox energy storage battery, and put 60L into the positive electrode electrolyte storage tank. In the formed battery stack, charge and discharge are carried out at a current of 200mA, the battery capacity is 2573Ah, the current efficiency is 95%, and the voltage efficiency is 60%.
尽管本发明的内容已经通过上述优选实施例作了详细介绍,但应当认识到上述的描述不应被认为是对本发明的限制。在本领域技术人员阅读了上述内容后,对于本发明的多种修改和替代都将是显而易见的。因此,本发明的保护范围应由所附的权利要求来限定。 Although the content of the present invention has been described in detail through the above preferred embodiments, it should be understood that the above description should not be considered as limiting the present invention. Various modifications and alterations to the present invention will become apparent to those skilled in the art upon reading the above disclosure. Therefore, the protection scope of the present invention should be defined by the appended claims.
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