CN111816890A - A kind of fluid seawater battery and preparation method - Google Patents
A kind of fluid seawater battery and preparation method Download PDFInfo
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- 239000013535 sea water Substances 0.000 title claims abstract description 125
- 239000012530 fluid Substances 0.000 title claims abstract description 68
- 238000002360 preparation method Methods 0.000 title claims abstract description 25
- 239000013078 crystal Substances 0.000 claims abstract description 79
- 229910052751 metal Inorganic materials 0.000 claims abstract description 29
- 239000002184 metal Substances 0.000 claims abstract description 29
- 239000003792 electrolyte Substances 0.000 claims abstract description 27
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 26
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 26
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims abstract description 24
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 23
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 23
- 239000001301 oxygen Substances 0.000 claims abstract description 23
- 238000000034 method Methods 0.000 claims abstract description 20
- 239000011780 sodium chloride Substances 0.000 claims abstract description 15
- 230000008569 process Effects 0.000 claims abstract description 13
- 238000003860 storage Methods 0.000 claims abstract description 12
- 238000010248 power generation Methods 0.000 claims abstract description 7
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims abstract description 3
- 239000011777 magnesium Substances 0.000 claims abstract description 3
- 229910052749 magnesium Inorganic materials 0.000 claims abstract description 3
- 238000004519 manufacturing process Methods 0.000 claims abstract description 3
- 230000010287 polarization Effects 0.000 claims abstract description 3
- 239000013225 prussian blue Substances 0.000 claims description 47
- DCYOBGZUOMKFPA-UHFFFAOYSA-N iron(2+);iron(3+);octadecacyanide Chemical compound [Fe+2].[Fe+2].[Fe+2].[Fe+3].[Fe+3].[Fe+3].[Fe+3].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-] DCYOBGZUOMKFPA-UHFFFAOYSA-N 0.000 claims description 45
- 229960003351 prussian blue Drugs 0.000 claims description 42
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 28
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 21
- 229910052799 carbon Inorganic materials 0.000 claims description 21
- 239000011734 sodium Substances 0.000 claims description 19
- 238000003756 stirring Methods 0.000 claims description 16
- 239000010949 copper Substances 0.000 claims description 15
- 235000002639 sodium chloride Nutrition 0.000 claims description 15
- 229910052802 copper Inorganic materials 0.000 claims description 13
- 238000001132 ultrasonic dispersion Methods 0.000 claims description 12
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 11
- 238000005341 cation exchange Methods 0.000 claims description 11
- 239000012528 membrane Substances 0.000 claims description 11
- 238000003760 magnetic stirring Methods 0.000 claims description 10
- 229910000838 Al alloy Inorganic materials 0.000 claims description 9
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 9
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 claims description 8
- 229910021645 metal ion Inorganic materials 0.000 claims description 8
- 239000002002 slurry Substances 0.000 claims description 8
- 230000008929 regeneration Effects 0.000 claims description 7
- 238000011069 regeneration method Methods 0.000 claims description 7
- 239000010936 titanium Substances 0.000 claims description 6
- 239000011701 zinc Substances 0.000 claims description 6
- 229910001415 sodium ion Inorganic materials 0.000 claims description 5
- 229910052719 titanium Inorganic materials 0.000 claims description 5
- 229910052725 zinc Inorganic materials 0.000 claims description 5
- 229910000861 Mg alloy Inorganic materials 0.000 claims description 4
- FKNQFGJONOIPTF-UHFFFAOYSA-N Sodium cation Chemical compound [Na+] FKNQFGJONOIPTF-UHFFFAOYSA-N 0.000 claims description 4
- 229910052783 alkali metal Inorganic materials 0.000 claims description 4
- 150000001340 alkali metals Chemical class 0.000 claims description 4
- 229910052742 iron Inorganic materials 0.000 claims description 4
- 229910052759 nickel Inorganic materials 0.000 claims description 4
- 239000001103 potassium chloride Substances 0.000 claims description 4
- 235000011164 potassium chloride Nutrition 0.000 claims description 4
- 229910052723 transition metal Inorganic materials 0.000 claims description 4
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 3
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 3
- 229910052744 lithium Inorganic materials 0.000 claims description 3
- 229910052700 potassium Inorganic materials 0.000 claims description 3
- 230000021148 sequestering of metal ion Effects 0.000 claims description 3
- 229910052708 sodium Inorganic materials 0.000 claims description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims description 2
- 229910001297 Zn alloy Inorganic materials 0.000 claims description 2
- SNAAJJQQZSMGQD-UHFFFAOYSA-N aluminum magnesium Chemical compound [Mg].[Al] SNAAJJQQZSMGQD-UHFFFAOYSA-N 0.000 claims description 2
- 229910052792 caesium Inorganic materials 0.000 claims description 2
- 229910052804 chromium Inorganic materials 0.000 claims description 2
- 239000011651 chromium Substances 0.000 claims description 2
- 125000004122 cyclic group Chemical group 0.000 claims description 2
- 230000000694 effects Effects 0.000 claims description 2
- 238000005485 electric heating Methods 0.000 claims description 2
- 239000004744 fabric Substances 0.000 claims description 2
- 239000011521 glass Substances 0.000 claims description 2
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 claims description 2
- 229910052738 indium Inorganic materials 0.000 claims description 2
- 229910052748 manganese Inorganic materials 0.000 claims description 2
- 239000011572 manganese Substances 0.000 claims description 2
- 229910052701 rubidium Inorganic materials 0.000 claims description 2
- 238000004506 ultrasonic cleaning Methods 0.000 claims description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims 4
- 229910052791 calcium Inorganic materials 0.000 claims 4
- 239000011575 calcium Substances 0.000 claims 4
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 claims 4
- 229910052753 mercury Inorganic materials 0.000 claims 4
- 238000002156 mixing Methods 0.000 claims 3
- JOUIQRNQJGXQDC-AXTSPUMRSA-N namn Chemical compound O1[C@@H](COP(O)([O-])=O)[C@H](O)[C@@H](O)[C@@H]1[N+]1=CC=CC(C(O)=O)=C1 JOUIQRNQJGXQDC-AXTSPUMRSA-N 0.000 claims 2
- MYLBTCQBKAKUTJ-UHFFFAOYSA-N 7-methyl-6,8-bis(methylsulfanyl)pyrrolo[1,2-a]pyrazine Chemical compound C1=CN=CC2=C(SC)C(C)=C(SC)N21 MYLBTCQBKAKUTJ-UHFFFAOYSA-N 0.000 claims 1
- 229910004589 Na2FeP2O7 Inorganic materials 0.000 claims 1
- 229910020344 Na2Zn Inorganic materials 0.000 claims 1
- 229910020620 Na3Fe2(PO4)3 Inorganic materials 0.000 claims 1
- 229910021271 NaCrO2 Inorganic materials 0.000 claims 1
- 229910021260 NaFe Inorganic materials 0.000 claims 1
- 229910021312 NaFePO4 Inorganic materials 0.000 claims 1
- 229910019338 NaMnO2 Inorganic materials 0.000 claims 1
- 239000003011 anion exchange membrane Substances 0.000 claims 1
- 239000008151 electrolyte solution Substances 0.000 claims 1
- 238000002347 injection Methods 0.000 claims 1
- 239000007924 injection Substances 0.000 claims 1
- 229910000155 iron(II) phosphate Inorganic materials 0.000 claims 1
- 239000004745 nonwoven fabric Substances 0.000 claims 1
- 239000010406 cathode material Substances 0.000 abstract description 6
- 239000010405 anode material Substances 0.000 abstract description 5
- 150000002500 ions Chemical class 0.000 abstract description 5
- 239000000463 material Substances 0.000 abstract description 3
- 230000002441 reversible effect Effects 0.000 abstract description 2
- 238000004064 recycling Methods 0.000 abstract 1
- 239000007787 solid Substances 0.000 description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 13
- 239000008367 deionised water Substances 0.000 description 12
- 229910021641 deionized water Inorganic materials 0.000 description 12
- 238000010586 diagram Methods 0.000 description 11
- 229920001296 polysiloxane Polymers 0.000 description 8
- 239000007788 liquid Substances 0.000 description 7
- 150000001768 cations Chemical class 0.000 description 6
- 230000002572 peristaltic effect Effects 0.000 description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- 229960002089 ferrous chloride Drugs 0.000 description 3
- NMCUIPGRVMDVDB-UHFFFAOYSA-L iron dichloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 125000000896 monocarboxylic acid group Chemical group 0.000 description 3
- NLJMYIDDQXHKNR-UHFFFAOYSA-K sodium citrate Chemical compound O.O.[Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NLJMYIDDQXHKNR-UHFFFAOYSA-K 0.000 description 3
- 229960000999 sodium citrate dihydrate Drugs 0.000 description 3
- GTSHREYGKSITGK-UHFFFAOYSA-N sodium ferrocyanide Chemical compound [Na+].[Na+].[Na+].[Na+].[Fe+2].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-] GTSHREYGKSITGK-UHFFFAOYSA-N 0.000 description 3
- 239000000264 sodium ferrocyanide Substances 0.000 description 3
- 235000012247 sodium ferrocyanide Nutrition 0.000 description 3
- 229910021591 Copper(I) chloride Inorganic materials 0.000 description 1
- 241000251729 Elasmobranchii Species 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 229910021607 Silver chloride Inorganic materials 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- OXBLHERUFWYNTN-UHFFFAOYSA-M copper(I) chloride Chemical compound [Cu]Cl OXBLHERUFWYNTN-UHFFFAOYSA-M 0.000 description 1
- 229940045803 cuprous chloride Drugs 0.000 description 1
- 238000009831 deintercalation Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 230000002687 intercalation Effects 0.000 description 1
- 238000009830 intercalation Methods 0.000 description 1
- HWSZZLVAJGOAAY-UHFFFAOYSA-L lead(II) chloride Chemical compound Cl[Pb]Cl HWSZZLVAJGOAAY-UHFFFAOYSA-L 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000006855 networking Effects 0.000 description 1
- -1 nickel ferricyanide Chemical compound 0.000 description 1
- 239000013110 organic ligand Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 239000013354 porous framework Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910001414 potassium ion Inorganic materials 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- HKZLPVFGJNLROG-UHFFFAOYSA-M silver monochloride Chemical compound [Cl-].[Ag+] HKZLPVFGJNLROG-UHFFFAOYSA-M 0.000 description 1
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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
- H01M6/00—Primary cells; Manufacture thereof
- H01M6/30—Deferred-action cells
- H01M6/32—Deferred-action cells activated through external addition of electrolyte or of electrolyte components
- H01M6/34—Immersion cells, e.g. sea-water cells
-
- 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)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Hybrid Cells (AREA)
Abstract
本发明公开了一种流体海水电池及制备方法,属于混合电池极其制造技术领域。该方法包含以下几个方面:1)以流体配位晶体为主,为海水中离子提供存储位点的阴极材料,展示出二次电池可逆充放电特性;2)以氧化还原势较低的金属镁、铝为主的阳极材料,用于提供电子,直至金属消耗完。这是典型的一次电池特征;3)以溶解氧至少1ppm和氯化钠至少0.35%的海水溶液作为电解液,用以平衡发电过程中带来的电极内离子浓度的极化,稳定发电装置的环境。当配位晶体中离子存储位点被完全占据后,通过使用海水中溶解氧与配位晶体反应,释放出存储位点中的离子,从而实现配位晶体的循环使用。本发明的方法操作简便,材料环保,可循环利用,可满足一般使用。
The invention discloses a fluid seawater battery and a preparation method, belonging to the technical field of hybrid batteries and manufacturing. The method includes the following aspects: 1) a cathode material dominated by fluid coordination crystals that provides storage sites for ions in seawater, and exhibits reversible charge-discharge characteristics of secondary batteries; 2) a metal with a lower redox potential Anode materials dominated by magnesium and aluminum are used to provide electrons until the metal is consumed. This is a typical primary battery feature; 3) A seawater solution with at least 1 ppm of dissolved oxygen and at least 0.35% of sodium chloride is used as the electrolyte to balance the polarization of the ion concentration in the electrode during the power generation process and stabilize the power generation device. surroundings. When the ion storage sites in the coordination crystals are completely occupied, the ions in the storage sites are released by using dissolved oxygen in seawater to react with the coordination crystals, thereby realizing the recycling of the coordination crystals. The method of the invention is easy to operate, the material is environmentally friendly, can be recycled, and can meet general use.
Description
技术领域technical field
本发明涉及混合电池及其制造技术领域,具体地说,是一种流体海水电池及制备方法。The invention relates to the technical field of hybrid batteries and their manufacture, in particular to a fluid seawater battery and a preparation method.
背景技术Background technique
随着我国海洋强国战略的提出,海洋用电与海岛供电问题亟待解决。现有的供电方式主要有联网和离网两种;联网型的电网主要通过海底电缆的方式,虽然联网工程能够确保海岛供电可靠性,但是其惊人的造价,及其后期维护困难等不足使得海岛离网供电成为海岛供电的核心技术。海岛离网供电体系中利用可再生能源,例如光伏发电,风能等,但是海岛环境高温、高湿、高盐雾,光伏发电的器件在这样的条件下需经过特殊的处理,经济适用型还是有待改善。针对以上一系列问题,近年来国内外的研究者将视角转移至海岛中最丰富的资源-海水。尝试使用天然海水作为电解质来进行发电,海水电池因此应运而生。海水电池其突出特点即不需要携带电解质,可在全海况的环境中工作。海水电池采用原电池的工作原理,阳极为活泼金属,阴极为氯化银、氯化亚铜、氯化铅的电极,这类海水电池的特点是能量密度大,功率高,但是在放电过程中,通过消耗正阳极材料,因此属于一次电池,经济性不佳,因此主要应用在军事方面,作为鱼雷的动力电源;另一类研究较多的金属-空气海水电池即阳极仍采用活泼金属,而阴极直接以海水中的溶解氧还原电极。这类海水电池较前一类电池相比,阳极仍需消耗活泼金属,而阴极则通过消耗海水中的溶解氧来发生氧化还原反应。这类电池即具有一次电池的特点,同时又具备燃料电池的特点。但由于其工作原理的限制,即阴极材料溶解氧浓度的限制,其电池的功率一直都存在很大问题,现有的电池体系只能适用于海上的小功率用电器,例如浮标,灯塔等。因此,寻求一种功效更好,效率更高的阴极材料,可以制造一种综合性能更好的海水电池。With the proposal of my country's marine power strategy, the problems of ocean power consumption and island power supply need to be solved urgently. The existing power supply methods are mainly networked and off-grid; the networked power grid is mainly through submarine cables. Although the networking project can ensure the reliability of the island’s power supply, its amazing cost and difficulties in subsequent maintenance make the island. Off-grid power supply has become the core technology of island power supply. The island off-grid power supply system uses renewable energy, such as photovoltaic power generation, wind energy, etc., but the island environment is high temperature, high humidity, high salt fog, photovoltaic power generation devices need to undergo special treatment under such conditions, economical and applicable type still needs to be improve. In response to the above series of problems, in recent years, researchers at home and abroad have shifted their perspectives to seawater, the most abundant resource in islands. Attempts to use natural seawater as an electrolyte to generate electricity led to the emergence of seawater batteries. The outstanding feature of seawater batteries is that they do not need to carry electrolytes and can work in the environment of all sea conditions. The seawater battery adopts the working principle of a primary battery. The anode is an active metal, and the cathode is an electrode of silver chloride, cuprous chloride and lead chloride. The characteristics of this type of seawater battery are high energy density and high power, but during the discharge process , by consuming the positive anode material, it belongs to a primary battery, and the economy is not good, so it is mainly used in the military as a power source for torpedoes; another type of metal-air seawater battery that is more researched, that is, the anode still uses active metals, while The cathode directly reduces the electrode with dissolved oxygen in seawater. Compared with the previous type of battery, the anode still needs to consume active metals, while the cathode consumes the dissolved oxygen in seawater for redox reactions. This type of battery not only has the characteristics of a primary battery, but also has the characteristics of a fuel cell. However, due to the limitation of its working principle, that is, the limitation of the dissolved oxygen concentration of the cathode material, the power of the battery has always been a big problem. The existing battery system can only be applied to low-power electrical appliances at sea, such as buoys, lighthouses, etc. Therefore, seeking a cathode material with better efficacy and higher efficiency can create a seawater battery with better comprehensive performance.
配位晶体是一类以金属离子或团簇作为节点,有机配体作为骨架,形成的三维周期性多孔骨架材料。配位晶体具有高孔隙率、低密度、大比表面积、孔径可调以及拓扑结构多样性和可裁剪性等优点,因此配位晶体可被用于金属离子(如钾离子、钠离子等)的可逆存储。除此之外,其晶体结构可在客体离子嵌入脱出过程中保持稳定。近年来,配位晶体以普鲁士蓝类化合物作为典型代表在锂、钠、钾等离子二次电池中展现出巨大的潜力。Coordination crystals are a kind of three-dimensional periodic porous framework materials formed by metal ions or clusters as nodes and organic ligands as frameworks. Coordination crystals have the advantages of high porosity, low density, large specific surface area, adjustable pore size, and topology diversity and tailorability. Therefore, coordination crystals can be used for metal ions (such as potassium ions, sodium ions, etc.). Reversible storage. In addition, its crystal structure can remain stable during the intercalation and deintercalation of guest ions. In recent years, coordination crystals, represented by Prussian blue compounds, have shown great potential in lithium, sodium, and potassium secondary batteries.
发明内容SUMMARY OF THE INVENTION
本发明的目的是为了优化针对特定海洋环境中能源持续供应的问题而提出的一种流体海水电池及制备方法,本发明操作简便,材料环保,可循环利用。The purpose of the present invention is to optimize a fluid seawater battery and a preparation method proposed for the problem of continuous energy supply in a specific marine environment. The present invention is easy to operate, environmentally friendly and recyclable.
实现本发明目的的具体技术方案是:The concrete technical scheme that realizes the object of the present invention is:
一种流体海水电池及制备方法,该方法包括以下具体步骤:A fluid seawater battery and a preparation method, the method comprising the following specific steps:
步骤1:阴极的选取与制备Step 1: Selection and Preparation of Cathode
A1:配位晶体的选取A1: Selection of coordination crystals
选取普鲁士蓝类晶体以及具有钠离子存储位点的晶体作为配位晶体,所述普鲁士蓝类晶体的分子通式为AaMⅠ bMⅡ c[MⅢ(CN)6]d·nH2O;其中,A为碱金属元素、氢离子或者铵根离子;MⅠ、MⅡ、MⅢ为相同或不同的过渡金属元素;a、b、c、d为[0,2]内的数值;n为[0,20]内的数值;所述碱金属元素为Li、Na、K、Rb或Cs;所述过渡金属元素为Fe、Co、Ni、Mn、Ti、Zn、Cr、Cu或In;Prussian blue crystals and crystals with sodium ion storage sites are selected as coordination crystals, and the general molecular formula of the Prussian blue crystals is A a M I b M II c [M III (CN) 6 ] d ·nH 2 O; wherein, A is an alkali metal element, hydrogen ion or ammonium ion; M I , M II , M III are the same or different transition metal elements; a, b, c, d are values in [0,2] ; n is a value within [0,20]; the alkali metal element is Li, Na, K, Rb or Cs; the transition metal element is Fe, Co, Ni, Mn, Ti, Zn, Cr, Cu or In;
所述具有钠离子存储位点的晶体为:Na2C6O6、Na4Fe3(PO4)2(P2O7)、NaVO2、NaCrO2、NaMnFe2(PO4)3、Na3Fe2(PO4)3、C24H8O6、C6Cl4O2、NaFePO4、Na2FeP2O7或NaMnO2;The crystals with sodium ion storage sites are: Na 2 C 6 O 6 , Na 4 Fe 3 (PO 4 ) 2 (P 2 O 7 ), NaVO 2 , NaCrO 2 , NaMnFe 2 (PO 4 ) 3 , Na 3 Fe 2 (PO 4 ) 3 , C 24 H 8 O 6 , C 6 Cl 4 O 2 , NaFePO 4 , Na 2 FeP 2 O 7 or NaMnO 2 ;
A2:阴极流体的制备A2: Preparation of Cathode Fluid
阴极流体的制备采用手动搅拌、磁力搅拌或超声分散方式;The preparation of cathode fluid adopts manual stirring, magnetic stirring or ultrasonic dispersion;
ⅰ)手动搅拌:将配位晶体与海水按照比例混合于容器中,配位晶体与海水的质量比例为1:10~8:10,利用工具搅拌5~50分钟,成为均匀连续的浆料,即可得到所述的阴极流体;其中,ⅰ) Manual stirring: Mix the coordination crystals and seawater in the container according to the proportion, the mass ratio of the coordination crystals and seawater is 1:10~8:10, use tools to stir for 5~50 minutes to become a uniform and continuous slurry, The cathode fluid can be obtained; wherein,
所述的工具为:玻璃棒、铁棒、铝合金棒、镁合金棒、刮刀或电动搅拌机;The tools are: glass rod, iron rod, aluminum alloy rod, magnesium alloy rod, scraper or electric mixer;
所述海水为溶解氧至少1ppm和氯化钠至少0.35%的天然海水、海盐配置海水、氯化钠或氯化钾配置的模拟海水;The seawater is natural seawater with at least 1ppm of dissolved oxygen and at least 0.35% of sodium chloride, seawater configured with sea salt, simulated seawater configured with sodium chloride or potassium chloride;
ⅱ)磁力搅拌:将配位晶体与海水按照比例混合于容器中,配位晶体与海水的质量比例为1:10~8:10,加入磁力搅拌子,利用磁力搅拌机驱动磁力搅拌子搅拌5~50分钟,成为均匀连续的浆料,即可得到所述的阴极流体;其中,ii) Magnetic stirring: Mix the coordination crystals and seawater in the container according to the proportion, the mass ratio of the coordination crystals and seawater is 1:10~8:10, add a magnetic stirring bar, and use a magnetic stirring machine to drive the magnetic stirring bar to stir for 5~ After 50 minutes, a uniform and continuous slurry can be obtained, and the cathode fluid can be obtained; wherein,
所述的磁力搅拌子为形状为圆柱形、椭圆形、十字型、双头型、三角柱形或八角柱形,尺寸为5mm×5mm~500mm×500mm的磁力搅拌子;The magnetic stirring bar is cylindrical, oval, cross, double-headed, triangular or octagonal, and the size is 5mm×5mm~500mm×500mm;
所述的磁力搅拌机为电热磁力搅拌套或平板型磁力搅拌机;Described magnetic force stirrer is electric heating magnetic force stirring sleeve or flat plate magnetic force stirring machine;
ⅲ)超声分散:将配位晶体与海水按照比例混合于容器中,配位晶体与海水的质量比例为1:10~8:10,利用超声分散仪进行超声分散5~50分钟,成为均匀连续的浆料,即可得到所述的阴极流体;其中,ⅲ) Ultrasonic dispersion: Mix the coordination crystals and seawater in the container according to the proportion, the mass ratio of the coordination crystals and seawater is 1:10~8:10, use the ultrasonic disperser to carry out ultrasonic dispersion for 5~50 minutes, and it becomes uniform and continuous. , the cathode fluid can be obtained; wherein,
所述超声分散仪为插入式的超声波分散仪、超声波振动子、超声波清洗仪或超声波震板;Described ultrasonic dispersing instrument is plug-in ultrasonic dispersing instrument, ultrasonic vibrator, ultrasonic cleaning instrument or ultrasonic vibration plate;
A3:阴极的制备A3: Preparation of cathode
将制备好的阴极流体用泵引导,流过集流体,再循环流回阴极流体的容器中,即可得到流体海水电池阴极;其中,The prepared cathode fluid is guided by a pump, flows through the current collector, and is recirculated back to the container of the cathode fluid to obtain a fluid seawater battery cathode; wherein,
所述的泵为离心泵、混流泵、轴流泵、旋涡泵、活塞泵、柱塞泵、隔膜泵、齿轮泵、螺杆泵、划片泵、喷射泵、水锤泵或真空泵;The pump is a centrifugal pump, a mixed flow pump, an axial flow pump, a vortex pump, a piston pump, a plunger pump, a diaphragm pump, a gear pump, a screw pump, a dicing pump, a jet pump, a water hammer pump or a vacuum pump;
所述的集流体为碳布、碳毡、金属钛、金属铜或金属镍;The current collector is carbon cloth, carbon felt, metal titanium, metal copper or metal nickel;
所述流过集流体的方式:从集流体外部流过或从集流体内部流过。The way of the current collector: flowing from the outside of the current collector or from the inside of the current collector.
步骤2:阳极的选取Step 2: Anode Selection
选取金属镁、金属铝、金属锌、汞和钙掺杂的镁合金、汞和钙掺杂的铝合金、汞和钙掺杂的锌合金或汞和钙掺杂镁铝合金为阳极;Selecting metal magnesium, metal aluminum, metal zinc, mercury- and calcium-doped magnesium alloys, mercury- and calcium-doped aluminum alloys, mercury- and calcium-doped zinc alloys, or mercury- and calcium-doped magnesium-aluminum alloys as anodes;
步骤3:电解液Step 3: Electrolyte
选用海水作为电解液,用于提供发电过程中所需的金属离子以及平衡电极极化效应;所述海水为溶解氧至少1ppm和氯化钠至少0.35%的天然海水、海盐配置海水、氯化钠或氯化钾配置的模拟海水;Seawater is selected as the electrolyte to provide metal ions required in the power generation process and to balance the electrode polarization effect; the seawater is natural seawater with at least 1ppm of dissolved oxygen and at least 0.35% of sodium chloride, sea salt configuration seawater, sodium chloride or simulated seawater configured with potassium chloride;
步骤4:恒定电流的产生Step 4: Generation of Constant Current
分别将阴极集流体和阳极放入用隔膜隔开的两个容器中,用导线把阴极集流体连接起来,再用导线把阳极连接起来;用电解液浸没阳极;打开泵,使阴极流体流过阴极集流体;便可产生恒定直流电流;Put the cathode current collector and the anode into two containers separated by a diaphragm, connect the cathode current collector with a wire, and then connect the anode with a wire; immerse the anode with the electrolyte; turn on the pump and let the cathode fluid flow through Cathode current collector; can generate constant DC current;
步骤5:阴极-配位晶体的循环再生Step 5: Cyclic Regeneration of Cathode-Coordination Crystals
当阴极配位晶体中金属离子存储位点被全部占据后,产生电流过程将停止;搅拌阴极流体,通过将阴极流体与海水或空气接触,利用海水中的溶解氧或空气的氧气氧化配位晶体,使配位晶体失去电子的同时,释放出存储位点中的金属离子;再通过泵引入阴极集流体,继续产生恒定直流电。When the metal ion storage sites in the cathode coordination crystal are fully occupied, the process of generating current will stop; stirring the cathode fluid, by contacting the cathode fluid with seawater or air, the coordination crystal is oxidized by the dissolved oxygen in the seawater or the oxygen in the air , while the coordination crystal loses electrons, the metal ions in the storage site are released; and then the cathode current collector is introduced through the pump to continue to generate constant direct current.
步骤1中所述的普鲁士蓝类化合物为:Fe4[Fe(CN)6]3(亚铁氰化铁,普鲁士蓝,CAS号14038-43-8)、Ni3[Fe(CN)6]2(铁氰化镍)、Na2Co[Fe(CN)6](亚铁氰化钴)、Ti[Fe(CN)6](亚铁氰化钛)、Na2Cu[Fe(CN)6](亚铁氰化铜)、Na2Zn[Fe(CN)6](亚铁氰化锌)。The Prussian blue compounds described in
本发明操作简便,材料环保,可循环利用。其中金属主要用于发电过程中提供电子,最终会变成离子态溶于海水中;配位晶体主要用于提供金属离子的可以存储位点。与现有技术相比,本发明可在保证工艺简单,环境友好的前提下,实现能量密度提高,可循环使用的海水电池。The invention has the advantages of simple operation, environment-friendly materials and recyclable utilization. Among them, metals are mainly used to provide electrons in the process of power generation, and will eventually become ionic and dissolved in seawater; coordination crystals are mainly used to provide storage sites for metal ions. Compared with the prior art, the present invention can realize a seawater battery with improved energy density and recyclable use on the premise of ensuring simple process and environmental friendliness.
附图说明Description of drawings
图1为本发明流体海水电池的结构示意图;1 is a schematic structural diagram of a fluid seawater battery of the present invention;
图2为本发明流体海水电池的阴极材料-配位晶体的循环再生侧面示意图;2 is a schematic side view of the cycle regeneration of the cathode material-coordination crystal of the fluid seawater battery of the present invention;
图3为本发明实施例1制得的海水电池的恒电流放电图;Fig. 3 is the galvanostatic discharge diagram of the seawater battery obtained in Example 1 of the present invention;
图4为本发明实施例2制得的海水电池的恒电流放电图;Fig. 4 is the galvanostatic discharge diagram of the seawater battery obtained in Example 2 of the present invention;
图5为本发明实施例3制得的海水电池的恒电流放电图。FIG. 5 is a galvanostatic discharge diagram of the seawater battery prepared in Example 3 of the present invention.
具体实施方式Detailed ways
以下结合附图及实施例对本发明进行详细描述。The present invention will be described in detail below with reference to the accompanying drawings and embodiments.
参阅图1,本发明的海水电池结构如图所示,将制备好的配位晶体1与天然海水2混合,形成阴极流体,放置于1 L的烧杯中。另一边用天然海水2作为电解液置于另一个烧杯中。在液流电解槽5中,用碳毡7作为阴极集流体,用工业牌号为1A99的金属铝片8作为阳极电极,并用型号为CMI 7000的阳离子交换膜6隔开。将碳毡7用铜导线引出来连接在以小灯泡为例的负载10的阴极,将工业牌号为1A99的金属铝片8用铜导线连接在负载10的阳极。再用泵3通过硅胶管9从液体进出口4引入阴极流体,再通过同一边的另一个液体进出口流回烧杯中,形成循环。用泵3通过硅胶管从液体进出口引入阳极电解液,再通过同一边的另一个液体进出口流回烧杯中,形成循环。构成本发明所述海水电池。Referring to FIG. 1 , the structure of the seawater battery of the present invention is shown in the figure. The
参阅图2,本发明的海水电池的阴极配位晶体的循环再生原理图,当配位晶体1的金属离子存储位点被全部占据后,产生电流过程将停止。在存储阴极流体的烧杯中,利用海水2中的溶解氧或空气的氧气氧化配位晶体1,使配位晶体1失去电子的同时,释放出存储位点中的金属离子;氧气被还原为氢氧根融入海水中,此过程一般为1天。Referring to FIG. 2 , the schematic diagram of the cycle regeneration of the cathode coordination crystal of the seawater battery of the present invention, when the metal ion storage sites of the
实施例1Example 1
手动搅拌hand stirring
本实施例中选择的阴极材料为普鲁士蓝配位晶体,其分子式Fe4[Fe(CN)6]3;阳极材料为牌照为1A99的工业纯铝;电解质为天然海水。The cathode material selected in this example is a Prussian blue coordination crystal with the molecular formula Fe 4 [Fe(CN) 6 ] 3 ; the anode material is industrial pure aluminum with a license plate of 1A99; and the electrolyte is natural seawater.
步骤1:普鲁士蓝配位晶体的制备Step 1: Preparation of Prussian Blue Coordination Crystal
将16.7 g氯化亚铁水合物(FeCl2·6H2O)及20 g柠檬酸钠二水合物(HOC(COOH)(CH2COONa)2·1.5H2O)溶于2.5 L去离子水形成透明澄清溶液A;将14.5 g亚铁氰化钠(Na4[Fe(CN)6])溶于2.5 L去离子水形成透明澄清溶液B,将溶液A和溶液B在室温下均匀混合得到灰白色浑浊液体,在室温(25℃)下反应24小时,得到深蓝色普鲁士蓝配位晶体溶液,将得到的普鲁士蓝配位晶体溶液用10000 rpm的速度离心分离得到普鲁士蓝配位晶体固体;a、将得到的普鲁士蓝配位晶体固体放入20 ml工业酒精中超声10 min分散,再用8000 rpm的速度离心分离得到普鲁士蓝配位晶体固体;b、将a得到的普鲁士蓝配位晶体固体放入20ml去离子水超声10min分散,再用10000rpm的速度离心分离得到普鲁士蓝配位晶体固体;重复a、b两步骤3次。把最后得到的固体置于室温下,真空干燥20 h,真空度小于0.1 Pa;Dissolve 16.7 g of ferrous chloride hydrate (FeCl 2 ·6H 2 O) and 20 g of sodium citrate dihydrate (HOC(COOH)(CH 2 COONa) 2 ·1.5H 2 O) in 2.5 L of deionized water A transparent and clear solution A was formed; 14.5 g of sodium ferrocyanide (Na 4 [Fe(CN) 6 ]) was dissolved in 2.5 L of deionized water to form a transparent and clear solution B, and the solution A and solution B were uniformly mixed at room temperature to obtain The gray-white turbid liquid was reacted at room temperature (25°C) for 24 hours to obtain a dark blue Prussian blue coordination crystal solution. The obtained Prussian blue coordination crystal solution was centrifuged at 10,000 rpm to obtain a Prussian blue coordination crystal solid; a , put the obtained Prussian blue coordination crystalline solid into 20 ml of industrial alcohol and disperse by ultrasonic for 10 min, and then centrifuge at a speed of 8000 rpm to obtain the Prussian blue coordination crystalline solid; b, the Prussian blue coordination crystalline solid obtained by a Put 20ml of deionized water into 20ml of deionized water for ultrasonic dispersion for 10min, and then centrifuge at 10000rpm to obtain a Prussian blue coordination crystal solid; repeat steps a and b three times. The final obtained solid was placed at room temperature, dried in vacuum for 20 h, and the degree of vacuum was less than 0.1 Pa;
步骤2:海水电池阴极流体的制备Step 2: Preparation of Cathode Fluid for Seawater Batteries
取50 g步骤1中的普鲁士蓝配位晶体固体500 ml 天然海水置于1 L容积的烧杯中,用电动搅拌机搅拌15分钟,成为均匀连续的浆料。得到的产品可作为海水电池的阴极流体;Take 50 g of the Prussian blue coordination crystal solid in
步骤3:海水电池阴极集流体的制备Step 3: Preparation of Seawater Battery Cathode Current Collector
把碳毡剪裁成1.5 cm×1.5 cm×1 cm 的块状,即可作为海水电池的阴极集流体。The carbon felt is cut into a block of 1.5 cm×1.5 cm×1 cm, which can be used as the cathode current collector of the seawater battery.
步骤4:海水电池阳极的制备Step 4: Preparation of Seawater Battery Anode
选择牌照为1A99的工业纯铝,将其分割成尺寸为2.5 cm×2.5 cm×0.5 cm的铝片,即可作为海水电池的阳极。Select industrial pure aluminum with a license plate of 1A99, and divide it into aluminum sheets with a size of 2.5 cm × 2.5 cm × 0.5 cm, which can be used as the anode of the seawater battery.
步骤5:海水电池的组装和恒定电流的产生Step 5: Assembly of Seawater Battery and Generation of Constant Current
将步骤3得到的碳毡和步骤4得到的金属铝片分别放于用型号为CMI 7000的阳离子交换膜分隔开的两个电解槽内。海水电解液和阴极流体分别放于两个1 L的烧杯中,用蠕动泵和硅胶管分别将海水电解液和阴极流体引入阳极电解槽和阴极电解槽。阴阳极分别用铜导线引出来,连接在用电器两极,即可输出稳定的直电流。The carbon felt obtained in
图3是本实施例的流体海水电池的恒电流放电图,测试条件为,将步骤3得到的碳毡和步骤4得到的金属铝片分别放于用型号为CMI 7000的阳离子交换膜分隔开的两个电解槽内。海水电解液和阴极流体分别放于两个1 L的烧杯中,用蠕动泵和硅胶管分别将海水电解液和阴极流体引入阳极电解槽和阴极电解槽。阴阳极分别用铜导线引出来,连接到蓝电电池测试系统的恒电流模式下以5 mA的电流进行放电,可得到图3所示的电压-时间关系图。Fig. 3 is the galvanostatic discharge diagram of the fluid seawater battery of the present embodiment, and the test condition is that the carbon felt obtained in
本实施例中,将海水电解液和阴极流体分别通入用型号为CMI 7000的阳离子交换膜分隔开的两个电解槽内中并浸没铝片和碳毡集流体时,由于1A99铝合金较低的氧化还原势,会驱动电子向碳毡端移动,并最终传递给阴极流体,普鲁士蓝配位晶体接受电子,同时吸收一个海水中的阳离子,形成普鲁士白配位晶体,金属铝会变成离子形式溶解于海水中,由于有电子的流动所以产生了电流。当阴极流体与被引出电解槽之后,与海水中的溶解氧或空气的氧气接触,会氧化普鲁士白配位晶体,同时放出一个阳离子,恢复成为普鲁士蓝配位晶体,此过程为配位晶体的循环再生。如此往复,可提供稳定的电流。整个工艺简便易行,对海水环境友好无污染。In this embodiment, when the seawater electrolyte and the cathode fluid are respectively passed into two electrolytic cells separated by a cation exchange membrane with a model of CMI 7000, and the aluminum sheet and the carbon felt current collector are immersed, the 1A99 aluminum alloy is relatively The low redox potential will drive the electrons to move to the carbon felt end, and finally transfer them to the cathode fluid. The Prussian blue coordination crystal accepts electrons and absorbs a cation in seawater at the same time to form a Prussian white coordination crystal. The metal aluminum will become The ionic form dissolves in seawater, and an electric current is generated due to the flow of electrons. When the cathode fluid comes into contact with the dissolved oxygen in seawater or oxygen in the air after being drawn out of the electrolytic cell, it will oxidize the Prussian white coordination crystal and release a cation at the same time, which will restore to the Prussian blue coordination crystal. Cycle regeneration. This reciprocation can provide a stable current. The whole process is simple and easy to implement, and is friendly to the seawater environment without pollution.
实施例2Example 2
磁力搅拌Magnetic stirring
本实施例中选择的阴极材料为普鲁士蓝配位晶体,其分子式Fe4[Fe(CN)6]3;阳极材料为牌照为1A99的工业纯铝;电解质为海盐配置的海水。The cathode material selected in this embodiment is a Prussian blue coordination crystal, and its molecular formula is Fe 4 [Fe(CN) 6 ] 3 ; the anode material is industrial pure aluminum with a license plate of 1A99; and the electrolyte is seawater prepared with sea salt.
步骤1:普鲁士蓝配位晶体的制备Step 1: Preparation of Prussian Blue Coordination Crystal
将16.7 g氯化亚铁水合物(FeCl2·6H2O)及20 g柠檬酸钠二水合物(HOC(COOH)(CH2COONa)2·1.5H2O)溶于2.5 L去离子水形成透明澄清溶液A;将14.5 g亚铁氰化钠(Na4[Fe(CN)6])溶于2.5 L去离子水形成透明澄清溶液B,将溶液A和溶液B在室温下均匀混合得到灰白色浑浊液体,在室温(25℃)下反应24小时,得到深蓝色普鲁士蓝配位晶体溶液,将得到的普鲁士蓝配位晶体溶液用10000 rpm的速度离心分离得到普鲁士蓝配位晶体固体;a、将得到的普鲁士蓝配位晶体固体放入20 ml工业酒精中超声10 min分散,再用8000 rpm的速度离心分离得到普鲁士蓝配位晶体固体;b、将a得到的普鲁士蓝配位晶体固体放入20ml去离子水超声10min分散,再用10000rpm的速度离心分离得到普鲁士蓝配位晶体固体;重复a、b两步骤3次。把最后得到的固体置于室温下,真空干燥20 h,真空度小于0.1 Pa;Dissolve 16.7 g of ferrous chloride hydrate (FeCl 2 ·6H 2 O) and 20 g of sodium citrate dihydrate (HOC(COOH)(CH 2 COONa) 2 ·1.5H 2 O) in 2.5 L of deionized water A transparent and clear solution A was formed; 14.5 g of sodium ferrocyanide (Na 4 [Fe(CN) 6 ]) was dissolved in 2.5 L of deionized water to form a transparent and clear solution B, and the solution A and solution B were uniformly mixed at room temperature to obtain The gray-white turbid liquid was reacted at room temperature (25°C) for 24 hours to obtain a dark blue Prussian blue coordination crystal solution. The obtained Prussian blue coordination crystal solution was centrifuged at 10,000 rpm to obtain a Prussian blue coordination crystal solid; a , put the obtained Prussian blue coordination crystalline solid into 20 ml of industrial alcohol and disperse by ultrasonic for 10 min, and then centrifuge at a speed of 8000 rpm to obtain the Prussian blue coordination crystalline solid; b, the Prussian blue coordination crystalline solid obtained by a Put 20ml of deionized water into 20ml of deionized water for ultrasonic dispersion for 10min, and then centrifuge at 10000rpm to obtain a Prussian blue coordination crystal solid; repeat steps a and b three times. The final obtained solid was placed at room temperature, dried in vacuum for 20 h, and the degree of vacuum was less than 0.1 Pa;
步骤2:海水电池阴极流体的制备Step 2: Preparation of Cathode Fluid for Seawater Batteries
取50 g步骤1中的普鲁士蓝配位晶体固体500 ml 天然海水置于容积为1 L的烧杯中,放入尺寸为120 mm×10 mm的圆柱型磁力搅拌子,用磁力搅拌机搅拌以400转每分钟的速度搅拌30分钟,成为均匀连续的浆料。得到的产品可作为海水电池的阴极流体;Take 50 g of the Prussian blue coordination crystal solid in
步骤3:海水电池阴极集流体的制备Step 3: Preparation of Seawater Battery Cathode Current Collector
把碳毡剪裁成2 cm×2 cm×1 cm 的块状,即可作为海水电池的阴极集流体。The carbon felt is cut into a block of 2 cm × 2 cm × 1 cm, which can be used as the cathode current collector of the seawater battery.
步骤4:海水电池阳极的制备Step 4: Preparation of Seawater Battery Anode
选择牌照为1A99的工业纯铝,将其分割成尺寸为1 cm×1 cm×0.5 cm的铝片,即可作为海水电池的阳极。Select industrial pure aluminum with a license plate of 1A99, and divide it into aluminum sheets with a size of 1 cm × 1 cm × 0.5 cm, which can be used as the anode of the seawater battery.
步骤5:海水电池的组装和恒定电流的产生Step 5: Assembly of Seawater Battery and Generation of Constant Current
将步骤3得到的碳毡和步骤4得到的金属铝片分别放于用型号为CMI 7000的阳离子交换膜分隔开的两个电解槽内。海水电解液和阴极流体分别放于两个1 L的烧杯中,用蠕动泵和硅胶管分别将海水电解液和阴极流体引入阳极电解槽和阴极电解槽。阴阳极分别用铜导线引出来,连接在用电器两极,即可输出稳定的直电流。The carbon felt obtained in
图4是本实施例的流体海水电池的恒电流放电图,测试条件为,将步骤3得到的碳毡和步骤4得到的金属铝片分别放于用型号为CMI 7000的阳离子交换膜分隔开的两个电解槽内。海水电解液和阴极流体分别放于两个1 L的烧杯中,用蠕动泵和硅胶管分别将海水电解液和阴极流体引入阳极电解槽和阴极电解槽。阴阳极分别用铜导线引出来,连接到蓝电电池测试系统的恒电流模式下以5 mA的电流进行放电,可得到图4所示的电压-时间关系图。Fig. 4 is the galvanostatic discharge diagram of the fluid seawater battery of the present embodiment, and the test conditions are that the carbon felt obtained in
本实施例中,将海水电解液和阴极流体分别通入用型号为CMI 7000的阳离子交换膜分隔开的两个电解槽内中并浸没铝片和碳毡集流体时,由于1A99铝合金较低的氧化还原势,会驱动电子向碳毡端移动,并最终传递给阴极流体,普鲁士蓝配位晶体接受电子,同时吸收一个海水中的阳离子,形成普鲁士白配位晶体,金属铝会变成离子形式溶解于海水中,由于有电子的流动所以产生了电流。当阴极流体与被引出电解槽之后,与海水中的溶解氧或空气的氧气接触,会氧化普鲁士白配位晶体,同时放出一个阳离子,恢复成为普鲁士蓝配位晶体,此过程为配位晶体的循环再生。如此往复,可提供稳定的电流。整个工艺简便易行,对海水环境友好无污染。In this embodiment, when the seawater electrolyte and the cathode fluid are respectively passed into two electrolytic cells separated by a cation exchange membrane with a model of CMI 7000, and the aluminum sheet and the carbon felt current collector are immersed, the 1A99 aluminum alloy is relatively The low redox potential will drive the electrons to move to the carbon felt end, and finally transfer them to the cathode fluid. The Prussian blue coordination crystal accepts electrons and absorbs a cation in seawater at the same time to form a Prussian white coordination crystal. The metal aluminum will become The ionic form dissolves in seawater, and an electric current is generated due to the flow of electrons. When the cathode fluid comes into contact with the dissolved oxygen in seawater or oxygen in the air after being drawn out of the electrolytic cell, it will oxidize the Prussian white coordination crystal and release a cation at the same time, which will restore to the Prussian blue coordination crystal. Cycle regeneration. This reciprocation can provide a stable current. The whole process is simple and easy to implement, and is friendly to the seawater environment without pollution.
实施例3Example 3
超声分散Ultrasonic dispersion
本实施例中选择的阴极材料为普鲁士蓝配位晶体,其分子式Fe4[Fe(CN)6]3;阳极材料为牌照为1A99的工业纯铝;电解质为海盐配置的海水。The cathode material selected in this embodiment is a Prussian blue coordination crystal, and its molecular formula is Fe 4 [Fe(CN) 6 ] 3 ; the anode material is industrial pure aluminum with a license plate of 1A99; and the electrolyte is seawater prepared with sea salt.
步骤1:普鲁士蓝配位晶体的制备Step 1: Preparation of Prussian Blue Coordination Crystal
将16.7 g氯化亚铁水合物(FeCl2·6H2O)及20 g柠檬酸钠二水合物(HOC(COOH)(CH2COONa)2·1.5H2O)溶于2.5 L去离子水形成透明澄清溶液A;将14.5 g亚铁氰化钠(Na4[Fe(CN)6])溶于2.5 L去离子水形成透明澄清溶液B,将溶液A和溶液B在室温下均匀混合得到灰白色浑浊液体,在室温(25℃)下反应24小时,得到深蓝色普鲁士蓝配位晶体溶液,将得到的普鲁士蓝配位晶体溶液用10000 rpm的速度离心分离得到普鲁士蓝配位晶体固体;a、将得到的普鲁士蓝配位晶体固体放入20 ml工业酒精中超声10 min分散,再用8000 rpm的速度离心分离得到普鲁士蓝配位晶体固体;b、将a得到的普鲁士蓝配位晶体固体放入20ml去离子水超声10min分散,再用10000rpm的速度离心分离得到普鲁士蓝配位晶体固体;重复a、b两步骤3次。把最后得到的固体置于室温下,真空干燥20 h,真空度小于0.1 Pa;Dissolve 16.7 g of ferrous chloride hydrate (FeCl 2 ·6H 2 O) and 20 g of sodium citrate dihydrate (HOC(COOH)(CH 2 COONa) 2 ·1.5H 2 O) in 2.5 L of deionized water A transparent and clear solution A was formed; 14.5 g of sodium ferrocyanide (Na 4 [Fe(CN) 6 ]) was dissolved in 2.5 L of deionized water to form a transparent and clear solution B, and the solution A and solution B were uniformly mixed at room temperature to obtain The gray-white turbid liquid was reacted at room temperature (25°C) for 24 hours to obtain a dark blue Prussian blue coordination crystal solution. The obtained Prussian blue coordination crystal solution was centrifuged at 10,000 rpm to obtain a Prussian blue coordination crystal solid; a , put the obtained Prussian blue coordination crystalline solid into 20 ml of industrial alcohol and disperse by ultrasonic for 10 min, and then centrifuge at a speed of 8000 rpm to obtain the Prussian blue coordination crystalline solid; b, the Prussian blue coordination crystalline solid obtained by a Put 20ml of deionized water into 20ml of deionized water for ultrasonic dispersion for 10min, and then centrifuge at 10000rpm to obtain a Prussian blue coordination crystal solid; repeat steps a and b three times. The final obtained solid was placed at room temperature, dried in vacuum for 20 h, and the degree of vacuum was less than 0.1 Pa;
步骤2:海水电池阴极流体的制备Step 2: Preparation of Cathode Fluid for Seawater Batteries
取50 g步骤1中的普鲁士蓝配位晶体固体500 ml 天然海水置于容积为1 L的烧杯中,放入功率为50 kHz的超声清洗仪中,连续超声30分钟,成为均匀连续的浆料。得到的产品可作为海水电池的阴极流体;Take 50 g of the Prussian blue coordination crystal solid in
步骤3:海水电池阴极集流体的制备Step 3: Preparation of Seawater Battery Cathode Current Collector
把碳毡剪裁成1.5 cm×1.5 cm×1 cm 的块状,即可作为海水电池的阴极集流体。The carbon felt is cut into a block of 1.5 cm×1.5 cm×1 cm, which can be used as the cathode current collector of the seawater battery.
步骤4:海水电池阳极的制备Step 4: Preparation of Seawater Battery Anode
选择牌照为1A99的工业纯铝,将其分割成尺寸为3 cm×3 cm×0.5 cm的铝片,即可作为海水电池的阳极。Select industrial pure aluminum with a license plate of 1A99, and divide it into aluminum sheets with a size of 3 cm × 3 cm × 0.5 cm, which can be used as the anode of the seawater battery.
步骤5:海水电池的组装和恒定电流的产生Step 5: Assembly of Seawater Battery and Generation of Constant Current
将步骤3得到的碳毡和步骤4得到的金属铝片分别放于用型号为CMI 7000的阳离子交换膜分隔开的两个电解槽内。海水电解液和阴极流体分别放于两个1 L的烧杯中,用蠕动泵和硅胶管分别将海水电解液和阴极流体引入阳极电解槽和阴极电解槽。阴阳极分别用铜导线引出来,连接在用电器两极,即可输出稳定的直电流。The carbon felt obtained in
图5是本实施例的流体海水电池的恒电流放电图,测试条件为,将步骤3得到的碳毡和步骤4得到的金属铝片分别放于用型号为CMI 7000的阳离子交换膜分隔开的两个电解槽内。海水电解液和阴极流体分别放于两个1 L的烧杯中,用蠕动泵和硅胶管分别将海水电解液和阴极流体引入阳极电解槽和阴极电解槽。阴阳极分别用铜导线引出来,连接到蓝电电池测试系统的恒电流模式下以5 mA的电流进行放电,可得到图5所示的电压-时间关系图。Fig. 5 is the galvanostatic discharge diagram of the fluid seawater battery of the present embodiment, and the test conditions are that the carbon felt obtained in
本实施例中,将海水电解液和阴极流体分别通入用型号为CMI 7000的阳离子交换膜分隔开的两个电解槽内中并浸没铝片和碳毡集流体时,由于1A99铝合金较低的氧化还原势,会驱动电子向碳毡端移动,并最终传递给阴极流体,普鲁士蓝配位晶体接受电子,同时吸收一个海水中的阳离子,形成普鲁士白配位晶体,金属铝会变成离子形式溶解于海水中,由于有电子的流动所以产生了电流。当阴极流体与被引出电解槽之后,与海水中的溶解氧或空气的氧气接触,会氧化普鲁士白配位晶体,同时放出一个阳离子,恢复成为普鲁士蓝配位晶体,此过程为配位晶体的循环再生。如此往复,可提供稳定的电流。整个工艺简便易行,对海水环境友好无污染。In this embodiment, when the seawater electrolyte and the cathode fluid are respectively passed into two electrolytic cells separated by a cation exchange membrane with a model of CMI 7000, and the aluminum sheet and the carbon felt current collector are immersed, the 1A99 aluminum alloy is relatively The low redox potential will drive the electrons to move to the carbon felt end, and finally transfer them to the cathode fluid. The Prussian blue coordination crystal accepts electrons and absorbs a cation in seawater at the same time to form a Prussian white coordination crystal. The metal aluminum will become The ionic form dissolves in seawater, and an electric current is generated due to the flow of electrons. When the cathode fluid comes into contact with the dissolved oxygen in seawater or oxygen in the air after being drawn out of the electrolytic cell, it will oxidize the Prussian white coordination crystal and release a cation at the same time, which will restore to the Prussian blue coordination crystal. Cycle regeneration. This reciprocation can provide a stable current. The whole process is simple and easy to implement, and is friendly to the seawater environment without pollution.
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