CN115911596B - Zinc metal battery electrolyte and preparation method and application thereof - Google Patents
Zinc metal battery electrolyte and preparation method and application thereof Download PDFInfo
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- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 title claims abstract description 72
- 239000011701 zinc Substances 0.000 title claims abstract description 58
- 229910052725 zinc Inorganic materials 0.000 title claims abstract description 55
- 239000003792 electrolyte Substances 0.000 title claims abstract description 44
- 229910052751 metal Inorganic materials 0.000 title claims abstract description 19
- 239000002184 metal Substances 0.000 title claims abstract description 19
- 238000002360 preparation method Methods 0.000 title abstract description 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims abstract description 147
- 239000002904 solvent Substances 0.000 claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 27
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 claims description 26
- 229960001763 zinc sulfate Drugs 0.000 claims description 26
- 229910000368 zinc sulfate Inorganic materials 0.000 claims description 26
- 239000003365 glass fiber Substances 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 8
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 claims description 4
- ZOIORXHNWRGPMV-UHFFFAOYSA-N acetic acid;zinc Chemical compound [Zn].CC(O)=O.CC(O)=O ZOIORXHNWRGPMV-UHFFFAOYSA-N 0.000 claims description 2
- NGTSQWJVGHUNSS-UHFFFAOYSA-N bis(sulfanylidene)vanadium Chemical compound S=[V]=S NGTSQWJVGHUNSS-UHFFFAOYSA-N 0.000 claims description 2
- 239000004246 zinc acetate Substances 0.000 claims description 2
- 239000011592 zinc chloride Substances 0.000 claims description 2
- 235000005074 zinc chloride Nutrition 0.000 claims description 2
- ZMLPZCGHASSGEA-UHFFFAOYSA-M zinc trifluoromethanesulfonate Chemical compound [Zn+2].[O-]S(=O)(=O)C(F)(F)F ZMLPZCGHASSGEA-UHFFFAOYSA-M 0.000 claims description 2
- CITILBVTAYEWKR-UHFFFAOYSA-L zinc trifluoromethanesulfonate Substances [Zn+2].[O-]S(=O)(=O)C(F)(F)F.[O-]S(=O)(=O)C(F)(F)F CITILBVTAYEWKR-UHFFFAOYSA-L 0.000 claims description 2
- RXBXBWBHKPGHIB-UHFFFAOYSA-L zinc;diperchlorate Chemical compound [Zn+2].[O-]Cl(=O)(=O)=O.[O-]Cl(=O)(=O)=O RXBXBWBHKPGHIB-UHFFFAOYSA-L 0.000 claims description 2
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 abstract 3
- 230000000052 comparative effect Effects 0.000 description 23
- 239000008151 electrolyte solution Substances 0.000 description 20
- 239000000243 solution Substances 0.000 description 18
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 11
- 239000011889 copper foil Substances 0.000 description 11
- 238000012360 testing method Methods 0.000 description 11
- 238000004519 manufacturing process Methods 0.000 description 8
- 239000008367 deionised water Substances 0.000 description 6
- 229910021641 deionized water Inorganic materials 0.000 description 6
- 229910052739 hydrogen Inorganic materials 0.000 description 6
- 239000001257 hydrogen Substances 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 5
- 238000009825 accumulation Methods 0.000 description 4
- 210000001787 dendrite Anatomy 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000004146 energy storage Methods 0.000 description 4
- -1 hydroxide ions Chemical class 0.000 description 4
- 238000011056 performance test Methods 0.000 description 4
- PTFCDOFLOPIGGS-UHFFFAOYSA-N Zinc dication Chemical compound [Zn+2] PTFCDOFLOPIGGS-UHFFFAOYSA-N 0.000 description 3
- 239000006227 byproduct Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000007086 side reaction Methods 0.000 description 3
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 210000004027 cell Anatomy 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 229910001416 lithium ion Inorganic materials 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 238000002161 passivation Methods 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- AFCARXCZXQIEQB-UHFFFAOYSA-N N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CCNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 AFCARXCZXQIEQB-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000002484 cyclic voltammetry Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000012983 electrochemical energy storage Methods 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000005486 organic electrolyte Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000004451 qualitative analysis Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000000844 transformation Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Classifications
-
- 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
- Y02E60/10—Energy storage using batteries
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- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
技术领域technical field
本发明涉及锌金属电池技术领域,尤其是涉及一种锌金属电池电解液及其制备方法与应用。The invention relates to the technical field of zinc metal batteries, in particular to an electrolyte solution for zinc metal batteries and a preparation method and application thereof.
背景技术Background technique
随着对能源日益增长的需求和对气候变化的认识,人们迫切的需要推动和加速从化石燃料向清洁的可再生能源过渡。在众多的电化学储能装置中。电池既能作为电子设备稳定动力的基本单元,又能作为电网能量储存的储能装置,因而受到了广泛的关注。With the growing demand for energy and awareness of climate change, there is an urgent need to facilitate and accelerate the transition from fossil fuels to clean, renewable energy. Among the numerous electrochemical energy storage devices. Batteries have attracted extensive attention because they can be used not only as the basic unit for stable power of electronic equipment, but also as an energy storage device for grid energy storage.
在众多的电池系统中,锂离子电池由于高能量密度,长循环寿命在各个领域中受到了广泛的运用。但锂资源的稀缺和可燃性有机电解液的使用,严重阻碍了锂离子电池在大规模存储领域的进一步发展。为了降低储能电池的成本,人们开始探索和开发其它的储能电池。Among many battery systems, lithium-ion batteries are widely used in various fields due to their high energy density and long cycle life. However, the scarcity of lithium resources and the use of flammable organic electrolytes seriously hinder the further development of lithium-ion batteries in the field of large-scale storage. In order to reduce the cost of energy storage batteries, people began to explore and develop other energy storage batteries.
其中,水系锌金属电池因高体积比容量、锌资源储量高、以及电解液的阻燃性等优点而受到了广泛关注。但是锌片负极在循环过程中存在的枝晶,腐蚀,产氢等问题大大阻碍了它的实际生产运用。Among them, aqueous zinc metal batteries have attracted extensive attention due to their advantages such as high volume specific capacity, high reserves of zinc resources, and the flame retardancy of the electrolyte. However, problems such as dendrites, corrosion, and hydrogen production in the zinc sheet anode during the cycle have greatly hindered its actual production and application.
因此,提高锌电池的整体性能还需要进一步的研究。Therefore, further research is needed to improve the overall performance of Zn batteries.
发明内容Contents of the invention
本发明所要解决的第一个技术问题是:The first technical problem to be solved by the present invention is:
提供一种电解液。An electrolyte is provided.
本发明所要解决的第二个技术问题是:The second technical problem to be solved by the present invention is:
提供一种所述电解液的制备方法。A method for preparing the electrolyte is provided.
本发明所要解决的第三个技术问题是:The third technical problem to be solved by the present invention is:
所述电解液的应用。Application of the electrolyte.
为了解决所述第一个技术问题,本发明采用的技术方案为:In order to solve the first technical problem, the technical solution adopted in the present invention is:
一种电解液,包括以下组分:An electrolyte comprising the following components:
锌源;Zinc source;
溶剂;solvent;
乙二醇;ethylene glycol;
所述溶剂与所述乙二醇的体积比为52-99.75:0.25-48。The volume ratio of the solvent to the ethylene glycol is 52-99.75:0.25-48.
根据本发明的实施方式,所述技术方案中的一个技术方案至少具有如下优点或有益效果之一:According to the embodiments of the present invention, one of the technical solutions has at least one of the following advantages or beneficial effects:
相比于没有添加乙二醇的电解液,本发明的电解液在高浓度和低浓度乙二醇含量下均可以有效提高锌金属电池的循环稳定性能。其中,当乙二醇的体积较小时,其能够通过特异性的尖端吸附达到抑制枝晶的效果,避免尖端处的电子的聚集,从而避免电子的聚集导致产氢的问题和产氢后留下大量的氢氧根离子,这些氢氧根离子和锌离子发生沉淀,又会导致锌片负极表面发生钝化的问题。其中,当乙二醇的体积较大时,高浓度下则会抑制溶剂参与的一系列副反应的问题,从而达到了提高电池寿命的效果。Compared with the electrolytic solution without ethylene glycol, the electrolytic solution of the present invention can effectively improve the cycle stability performance of the zinc metal battery at both high and low concentrations of ethylene glycol. Among them, when the volume of ethylene glycol is small, it can achieve the effect of suppressing dendrites through specific tip adsorption, avoiding the accumulation of electrons at the tip, thereby avoiding the problem of hydrogen production caused by the accumulation of electrons and leaving behind after hydrogen production. A large number of hydroxide ions, these hydroxide ions and zinc ions will precipitate, which will lead to the passivation of the surface of the zinc sheet negative electrode. Among them, when the volume of ethylene glycol is large, a series of side reactions involving the solvent will be suppressed at a high concentration, thereby achieving the effect of improving battery life.
根据本发明的一种实施方式,所述锌源包括硫酸锌、醋酸锌、三氟甲磺酸锌、氯化锌和高氯酸锌中的至少一种。According to one embodiment of the present invention, the zinc source includes at least one of zinc sulfate, zinc acetate, zinc trifluoromethanesulfonate, zinc chloride and zinc perchlorate.
根据本发明的一种实施方式,所述锌源在所述电解液中的摩尔浓度为1-2mol/L。According to one embodiment of the present invention, the molar concentration of the zinc source in the electrolyte is 1-2 mol/L.
根据本发明的一种实施方式,所述锌源在所述电解液中的摩尔浓度为1-1.5mol/L。According to one embodiment of the present invention, the molar concentration of the zinc source in the electrolyte is 1-1.5 mol/L.
根据本发明的一种实施方式,所述锌源在所述电解液中的摩尔浓度为0.5-1.5mol/L。According to one embodiment of the present invention, the molar concentration of the zinc source in the electrolyte is 0.5-1.5 mol/L.
根据本发明的一种实施方式,所述溶剂与所述乙二醇的体积比为52-60:0.25-1。According to one embodiment of the present invention, the volume ratio of the solvent to the ethylene glycol is 52-60:0.25-1.
根据本发明的一种实施方式,所述溶剂与所述乙二醇的体积比为52-60:1-48。According to one embodiment of the present invention, the volume ratio of the solvent to the ethylene glycol is 52-60:1-48.
本发明的电解液,包括锌源、溶剂和乙二醇,当锌源的用量确定后,通过调整所述溶剂与所述乙二醇的体积比,可以调整锌源和乙二醇在电解液中的浓度。而本发明的电解液,在低浓度下能够有效抑制负极枝晶生长,在高浓度下能够有效抑制活性水参与一系列副反应,从而显著提高锌金属电池循环性能,延长使用寿命。Electrolyte of the present invention comprises zinc source, solvent and ethylene glycol, after the consumption of zinc source is determined, by adjusting the volume ratio of described solvent and described ethylene glycol, can adjust zinc source and ethylene glycol in electrolytic solution concentration in . However, the electrolyte solution of the present invention can effectively inhibit the dendrite growth of the negative electrode at a low concentration, and can effectively inhibit active water from participating in a series of side reactions at a high concentration, thereby significantly improving the cycle performance of the zinc metal battery and prolonging the service life.
为了解决所述第二个技术问题,本发明采用的技术方案为:In order to solve the second technical problem, the technical solution adopted in the present invention is:
一种制备所述电解液的方法,包括以下步骤:A method for preparing the electrolyte, comprising the steps of:
混合锌源和乙二醇于溶剂中,得到所述电解液。The zinc source and ethylene glycol are mixed in a solvent to obtain the electrolyte.
本发明制备所述电解液的方法,工艺简单,容易操作,适用于工业化大规模生产应用。The method for preparing the electrolyte of the present invention has simple process and easy operation, and is suitable for industrial large-scale production and application.
根据本发明的一种实施方式,还提供一种锌金属电池,包括正极、负极、电极液和隔膜,其中,所述电极液包括所述的一种电解液。According to an embodiment of the present invention, there is also provided a zinc metal battery, including a positive electrode, a negative electrode, an electrode solution and a separator, wherein the electrode solution includes the above-mentioned electrolyte solution.
根据本发明的一种实施方式,所述电池中,电解液的用量为150-220μL。According to one embodiment of the present invention, in the battery, the electrolyte solution is used in an amount of 150-220 μL.
根据本发明的一种实施方式,所述电池中,电解液的用量为180-200μL。According to one embodiment of the present invention, in the battery, the electrolyte solution is used in an amount of 180-200 μL.
根据本发明的一种实施方式,所述正极包括二硫化钒极片。According to one embodiment of the present invention, the positive electrode includes a vanadium disulfide pole piece.
根据本发明的一种实施方式,所述负极包括锌箔。According to one embodiment of the present invention, the negative electrode includes zinc foil.
根据本发明的一种实施方式,所述隔膜包括玻璃纤维隔膜。According to one embodiment of the present invention, the membrane comprises a glass fiber membrane.
根据本发明的一种实施方式,所述电池中,以锌箔为工作电极,以锌箔作为对/参比电极。According to one embodiment of the present invention, in the battery, the zinc foil is used as the working electrode, and the zinc foil is used as the counter/reference electrode.
本发明的其它特征和优点将在随后的说明书中阐述,并且,部分地从说明书中变得显而易见,或者通过实施本发明而了解。Additional features and advantages of the invention will be set forth in the description which follows, and in part will be apparent from the description, or may be learned by practice of the invention.
附图说明Description of drawings
本发明的上述和/或附加的方面和优点从结合下面附图对实施例的描述中将变得明显和容易理解,其中:The above and/or additional aspects and advantages of the present invention will become apparent and understandable from the description of the embodiments in conjunction with the following drawings, wherein:
图1为实施例1-2和对比例1制备半电池的循环性能图;Fig. 1 is the cycle performance figure of embodiment 1-2 and comparative example 1 preparation half cell;
图2为实施例1-2和对比例1制备全电池的循环性能图;Fig. 2 is the cycle performance diagram of the full battery prepared in Example 1-2 and Comparative Example 1;
图3为实施例1和对比例1制备半电池的电极双电层电容统计图;Fig. 3 is the statistical diagram of the electric double layer capacitance of the electrode prepared in embodiment 1 and comparative example 1 half cell;
图4为实施例2和对比例1循环50圈后锌电极表面生成物X射线衍射图。Fig. 4 is the X-ray diffraction pattern of the product on the surface of the zinc electrode after 50 cycles of Example 2 and Comparative Example 1.
具体实施方式Detailed ways
下面将结合本发明实施例,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the embodiments of the present invention. Obviously, the described embodiments are only some of the embodiments of the present invention, not all of them. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the scope of the present invention.
本发明所采用的试剂、方法和设备,如无特殊说明,均为本技术领域常规试剂、方法和设备。The reagents, methods and equipment used in the present invention are conventional reagents, methods and equipment in the technical field unless otherwise specified.
实施例1Example 1
一种电解液,包括以下组分:An electrolyte comprising the following components:
硫酸锌;zinc sulfate;
水;water;
乙二醇;ethylene glycol;
上述水与上述乙二醇的体积比为99.75:0.25;The volume ratio of the above water to the above ethylene glycol is 99.75:0.25;
硫酸锌的浓度为2mol/L ZnSO4。The concentration of zinc sulfate is 2mol/L ZnSO 4 .
制备上述电解液,包括以下步骤:Prepare above-mentioned electrolytic solution, comprise the following steps:
以体积比为99.75:0.25,混合去离子水和乙二醇,随后添加硫酸锌,至电解液中硫酸锌的浓度达到2mol/L,使用磁力搅拌器搅拌溶液,直到溶液变成透明,得到上述电解液。Mix deionized water and ethylene glycol at a volume ratio of 99.75:0.25, then add zinc sulfate until the concentration of zinc sulfate in the electrolyte reaches 2mol/L, stir the solution with a magnetic stirrer until the solution becomes transparent, and obtain the above electrolyte.
以直径为12mm的锌箔为工作电极,采用12mm的锌箔作为对/参比电极,采用玻璃纤维隔膜和标准的CR2032型电池壳组装成电池,每个电池使用180μL上述电解液,得到锌电池。A zinc foil with a diameter of 12mm is used as the working electrode, a 12mm zinc foil is used as the counter/reference electrode, and a battery is assembled with a glass fiber separator and a standard CR2032 battery case. Each battery uses 180 μL of the above electrolyte to obtain a zinc battery .
实施例1的电解液,乙二醇的体积较小时,其能够通过特异性的尖端吸附达到抑制枝晶的效果,避免尖端处的电子的聚集,从而避免电子的聚集导致产氢的问题和产氢后留下大量的氢氧根离子,这些氢氧根离子和锌离子发生沉淀,又会导致锌片负极表面发生钝化的问题。In the electrolyte solution of Example 1, when the volume of ethylene glycol is small, it can achieve the effect of suppressing dendrites through specific tip adsorption, avoiding the accumulation of electrons at the tip, thereby avoiding the problem of hydrogen production and the production of hydrogen caused by the accumulation of electrons. A large number of hydroxide ions are left after the hydrogen, and these hydroxide ions and zinc ions precipitate, which will lead to the passivation of the surface of the negative electrode of the zinc sheet.
实施例2Example 2
实施例2与实施例1区别在于:水与乙二醇的体积比不同。其中,实施例2的水与上述乙二醇的体积比为60:40。其中,实施例1的水与上述乙二醇的体积比为99.75:0.25。The difference between embodiment 2 and embodiment 1 is that the volume ratio of water to ethylene glycol is different. Wherein, the volume ratio of water in Example 2 to the above-mentioned ethylene glycol is 60:40. Wherein, the volume ratio of water in Example 1 to the above-mentioned ethylene glycol is 99.75:0.25.
一种电解液,包括以下组分:An electrolyte comprising the following components:
硫酸锌;zinc sulfate;
水;water;
乙二醇;ethylene glycol;
上述水与上述乙二醇的体积比为60:40;The volume ratio of the above water to the above ethylene glycol is 60:40;
硫酸锌的浓度为2mol/L ZnSO4。The concentration of zinc sulfate is 2mol/L ZnSO 4 .
制备上述电解液,包括以下步骤:Prepare above-mentioned electrolytic solution, comprise the following steps:
以体积比为60:40。The volume ratio is 60:40.
制备上述电解液,包括以下步骤:Prepare above-mentioned electrolytic solution, comprise the following steps:
以体积比为60:40,混合去离子水和乙二醇,随后添加硫酸锌,至电解液中硫酸锌的浓度达到2mol/L,使用磁力搅拌器搅拌溶液,直到溶液变成透明,得到上述电解液。Mix deionized water and ethylene glycol at a volume ratio of 60:40, then add zinc sulfate until the concentration of zinc sulfate in the electrolyte reaches 2mol/L, stir the solution with a magnetic stirrer until the solution becomes transparent, and obtain the above electrolyte.
以直径为12mm的锌箔为工作电极,采用12mm的锌箔作为对/参比电极,采用玻璃纤维隔膜和标准的CR2032型电池壳组装成电池,每个电池使用180μL上述电解液,得到锌电池。A zinc foil with a diameter of 12mm is used as the working electrode, a 12mm zinc foil is used as the counter/reference electrode, and a battery is assembled with a glass fiber separator and a standard CR2032 battery case. Each battery uses 180 μL of the above electrolyte to obtain a zinc battery .
实施例2中,乙二醇的体积较大,高浓度的乙二醇会抑制溶剂参与的一系列副反应的问题,避免产生副产物,如Zn4(OH)6SO4·5H2O,从而达到了提高电池寿命的效果。In Example 2, the volume of ethylene glycol is relatively large, and high-concentration ethylene glycol will suppress the problem of a series of side reactions in which the solvent participates, avoiding the production of by-products, such as Zn 4 (OH) 6 SO 4 ·5H 2 O, Thereby, the effect of improving battery life is achieved.
实施例3Example 3
实施例3与实施例1区别在于:电池结构不同。其中,实施例3的电池包括直径为12mm的,沉积了一定量锌的铜箔为负极(正负极容量比为1:5),采用12mm VS2极片为正极。其中,实施例1的电池包括以直径为12mm的锌箔为工作电极,采用12mm的锌箔作为对/参比电极,采用玻璃纤维隔膜和标准的CR2032型电池壳组装成电池。其中,铜箔上沉积锌的负载量约为2.85mg/cm2。The difference between Embodiment 3 and Embodiment 1 lies in that the battery structure is different. Among them, the battery of Example 3 includes a copper foil with a diameter of 12mm and deposited a certain amount of zinc as the negative electrode (the positive and negative electrode capacity ratio is 1:5), and a 12mm VS 2 pole piece is used as the positive electrode. Wherein, the battery of Example 1 includes a zinc foil with a diameter of 12 mm as the working electrode, a 12 mm zinc foil as the counter/reference electrode, a glass fiber separator and a standard CR2032 battery case to assemble the battery. Wherein, the loading amount of zinc deposited on the copper foil is about 2.85 mg/cm 2 .
一种电解液,包括以下组分:An electrolyte comprising the following components:
硫酸锌;zinc sulfate;
水;water;
乙二醇;ethylene glycol;
上述水与上述乙二醇的体积比为99.75:0.25;The volume ratio of the above water to the above ethylene glycol is 99.75:0.25;
硫酸锌的浓度为2mol/L ZnSO4。The concentration of zinc sulfate is 2mol/L ZnSO 4 .
制备上述电解液,包括以下步骤:Prepare above-mentioned electrolytic solution, comprise the following steps:
以体积比为99.75:0.25,混合去离子水和乙二醇,随后添加硫酸锌,至电解液中硫酸锌的浓度达到2mol/L,使用磁力搅拌器搅拌溶液,直到溶液变成透明,得到上述电解液。Mix deionized water and ethylene glycol at a volume ratio of 99.75:0.25, then add zinc sulfate until the concentration of zinc sulfate in the electrolyte reaches 2mol/L, stir the solution with a magnetic stirrer until the solution becomes transparent, and obtain the above electrolyte.
直径为12mm的,沉积了一定量锌的铜箔为负极(正负极容量比为1:5),采用12mmVS2极片为正极,采用玻璃纤维隔膜和标准的CR2032型电池壳组装成电池,每个电池使用180μL上述电解液,得到锌电池。The copper foil with a diameter of 12mm and deposited a certain amount of zinc is used as the negative electrode (the capacity ratio of positive and negative electrodes is 1:5), and the 12mm VS 2 pole piece is used as the positive electrode, and the battery is assembled with a glass fiber separator and a standard CR2032 battery case. 180 μL of the above electrolyte solution was used for each battery to obtain a zinc battery.
实施例4Example 4
实施例4与实施例2区别在于:电池结构不同。其中,实施例4的电池包括直径为12mm的,沉积了一定量锌的铜箔为负极(正负极容量比为1:5),采用12mm VS2极片为正极。其中,实施例4的电池包括直径为12mm的,沉积了一定量锌的铜箔为负极(正负极容量比为1:5),采用12mm VS2极片为正极。其中,实施例1的电池包括以直径为12mm的锌箔为工作电极,采用12mm的锌箔作为对/参比电极,采用玻璃纤维隔膜和标准的CR2032型电池壳组装成电池。其中,铜箔上沉积锌的负载量约为2.85mg/cm2。The difference between Embodiment 4 and Embodiment 2 lies in that the battery structure is different. Among them, the battery of Example 4 includes a copper foil with a diameter of 12mm and deposited a certain amount of zinc as the negative electrode (the positive and negative electrode capacity ratio is 1:5), and a 12mm VS 2 pole piece is used as the positive electrode. Among them, the battery of Example 4 includes a copper foil with a diameter of 12mm and deposited a certain amount of zinc as the negative electrode (the positive and negative electrode capacity ratio is 1:5), and a 12mm VS 2 pole piece is used as the positive electrode. Wherein, the battery of Example 1 includes a zinc foil with a diameter of 12 mm as the working electrode, a 12 mm zinc foil as the counter/reference electrode, a glass fiber separator and a standard CR2032 battery case to assemble the battery. Wherein, the loading amount of zinc deposited on the copper foil is about 2.85 mg/cm 2 .
一种电解液,包括以下组分:An electrolyte comprising the following components:
硫酸锌;zinc sulfate;
水;water;
乙二醇;ethylene glycol;
上述水与上述乙二醇的体积比为60:40;The volume ratio of the above water to the above ethylene glycol is 60:40;
硫酸锌的浓度为2mol/L ZnSO4。The concentration of zinc sulfate is 2mol/L ZnSO 4 .
制备上述电解液,包括以下步骤:Prepare above-mentioned electrolytic solution, comprise the following steps:
以体积比为60:40。The volume ratio is 60:40.
制备上述电解液,包括以下步骤:Prepare above-mentioned electrolytic solution, comprise the following steps:
以体积比为60:40,混合去离子水和乙二醇,随后添加硫酸锌,至电解液中硫酸锌的浓度达到2mol/L,使用磁力搅拌器搅拌溶液,直到溶液变成透明,得到上述电解液。Mix deionized water and ethylene glycol at a volume ratio of 60:40, then add zinc sulfate until the concentration of zinc sulfate in the electrolyte reaches 2mol/L, stir the solution with a magnetic stirrer until the solution becomes transparent, and obtain the above electrolyte.
直径为12mm的,沉积了一定量锌的铜箔为负极(正负极容量比为1:5),采用12mmVS2极片为正极,采用玻璃纤维隔膜和标准的CR2032型电池壳组装成电池,每个电池使用180μL上述电解液,得到锌电池。其中,铜箔上沉积锌的负载量约为2.85mg/cm2。The copper foil with a diameter of 12mm and deposited a certain amount of zinc is used as the negative electrode (the capacity ratio of positive and negative electrodes is 1:5), and the 12mm VS 2 pole piece is used as the positive electrode, and the battery is assembled with a glass fiber separator and a standard CR2032 battery case. 180 μL of the above electrolyte solution was used for each battery to obtain a zinc battery. Wherein, the loading amount of zinc deposited on the copper foil is about 2.85 mg/cm 2 .
对比例1Comparative example 1
对比例1与实施例1区别在于:水与乙二醇的体积比不同。其中,对比例1的水与乙二醇的体积比为100:0。其中,实施例1的水与上述乙二醇的体积比为99.75:0.25。The difference between Comparative Example 1 and Example 1 is that the volume ratio of water to ethylene glycol is different. Wherein, the volume ratio of water to ethylene glycol in Comparative Example 1 is 100:0. Wherein, the volume ratio of water in Example 1 to the above-mentioned ethylene glycol is 99.75:0.25.
一种电解液,包括以下组分:An electrolyte comprising the following components:
硫酸锌;zinc sulfate;
水;water;
乙二醇;ethylene glycol;
上述水与上述乙二醇的体积比为99.75:0.25;The volume ratio of the above water to the above ethylene glycol is 99.75:0.25;
硫酸锌的浓度为2mol/L ZnSO4。The concentration of zinc sulfate is 2mol/L ZnSO 4 .
制备上述电解液,包括以下步骤:Prepare above-mentioned electrolytic solution, comprise the following steps:
以体积比为99.75:0.25,混合去离子水和乙二醇,随后添加硫酸锌,至电解液中硫酸锌的浓度达到2mol/L,使用磁力搅拌器搅拌溶液,直到溶液变成透明,得到上述电解液。Mix deionized water and ethylene glycol at a volume ratio of 99.75:0.25, then add zinc sulfate until the concentration of zinc sulfate in the electrolyte reaches 2mol/L, stir the solution with a magnetic stirrer until the solution becomes transparent, and obtain the above electrolyte.
以直径为12mm的锌箔为工作电极,采用12mm的锌箔作为对/参比电极,采用玻璃纤维隔膜和标准的CR2032型电池壳组装成电池,每个电池使用180μL上述电解液,得到锌电池。A zinc foil with a diameter of 12mm is used as the working electrode, a 12mm zinc foil is used as the counter/reference electrode, and a battery is assembled with a glass fiber separator and a standard CR2032 battery case. Each battery uses 180 μL of the above electrolyte to obtain a zinc battery .
对比例2Comparative example 2
对比例2与对比例1区别在于:电池结构不同。其中,对比例2的电池包括直径为12mm的,沉积了一定量锌的铜箔为负极(正负极容量比为1:5),采用12mm VS2极片为正极。对比例1的电池包括直径为12mm的锌箔为工作电极,12mm的锌箔作为对/参比电极。其中,铜箔上沉积锌的负载量约为2.85mg/cm2。The difference between Comparative Example 2 and Comparative Example 1 lies in that the battery structure is different. Among them, the battery of Comparative Example 2 includes a copper foil with a diameter of 12mm and deposited a certain amount of zinc as the negative electrode (the positive and negative electrode capacity ratio is 1:5), and a 12mm VS 2 pole piece is used as the positive electrode. The battery of Comparative Example 1 included a 12 mm diameter zinc foil as a working electrode and a 12 mm zinc foil as a counter/reference electrode. Wherein, the loading amount of zinc deposited on the copper foil is about 2.85 mg/cm 2 .
一种电解液,包括以下组分:An electrolyte comprising the following components:
硫酸锌;zinc sulfate;
水;water;
乙二醇;ethylene glycol;
上述水与上述乙二醇的体积比为99.75:0.25;The volume ratio of the above water to the above ethylene glycol is 99.75:0.25;
硫酸锌的浓度为2mol/L ZnSO4。The concentration of zinc sulfate is 2mol/L ZnSO 4 .
制备上述电解液,包括以下步骤:Prepare above-mentioned electrolytic solution, comprise the following steps:
以体积比为99.75:0.25,混合去离子水和乙二醇,随后添加硫酸锌,至电解液中硫酸锌的浓度达到2mol/L,使用磁力搅拌器搅拌溶液,直到溶液变成透明,得到上述电解液。Mix deionized water and ethylene glycol at a volume ratio of 99.75:0.25, then add zinc sulfate until the concentration of zinc sulfate in the electrolyte reaches 2mol/L, stir the solution with a magnetic stirrer until the solution becomes transparent, and obtain the above electrolyte.
直径为12mm的,沉积了一定量锌的铜箔为负极(正负极容量比为1:5),采用12mmVS2极片为正极,采用玻璃纤维隔膜和标准的CR2032型电池壳组装成电池,每个电池使用180μL上述电解液,得到锌电池。The copper foil with a diameter of 12mm and deposited a certain amount of zinc is used as the negative electrode (the capacity ratio of positive and negative electrodes is 1:5), and the 12mm VS 2 pole piece is used as the positive electrode, and the battery is assembled with a glass fiber separator and a standard CR2032 battery case. 180 μL of the above electrolyte solution was used for each battery to obtain a zinc battery.
测试例1test case 1
将本发明实施例1-2和对比例1制成半电池样品,测试半电池的循环稳定性(测试系统使用新威电池充放电测试仪)。图1为实施例1-2和对比例1的半电池样品的循环性能测试图,测试条件为为电流密度2mA/cm2,恒电流沉积-电解容量2mAh/cm2,进行循环性能测试。Examples 1-2 of the present invention and Comparative Example 1 were made into half-cell samples, and the cycle stability of the half-cell was tested (the test system used Xinwei battery charge and discharge tester). Fig. 1 is the cycle performance test graph of the half-cell samples of Examples 1-2 and Comparative Example 1, the test conditions are current density 2mA/cm 2 , galvanostatic deposition-electrolytic capacity 2mAh/cm 2 , and the cycle performance test is carried out.
如图1所示,由实施例1-2制成半电池分别可稳定运行循环2400h和1730h。而由对比例1制成半电池在90h后发生短路,随即电池失效。这说明了乙二醇在高浓度和低浓度下均能够有效的提高电池寿命,展现出了优异的效果。As shown in Fig. 1, the half-cells made by Examples 1-2 can run stably for 2400h and 1730h respectively. However, the half-cell made of Comparative Example 1 short-circuited after 90 hours, and then the battery failed. This shows that ethylene glycol can effectively improve battery life at both high and low concentrations, showing excellent results.
测试例2test case 2
将本发明实施例3-4和对比例2制备制成全电池样品,测试全电池的循环寿命(测试系统使用新威电池充放电测试仪)。图2为实施例3-4和对比例2的全电池样品的循环性能测试图,测试条件为电流密度1A/g,进行循环性能测试。Examples 3-4 of the present invention and Comparative Example 2 were prepared as full battery samples, and the cycle life of the full battery was tested (the test system used Xinwei battery charge and discharge tester). FIG. 2 is a cycle performance test chart of the full battery samples of Examples 3-4 and Comparative Example 2. The test condition is a current density of 1A/g, and the cycle performance test is performed.
如图2所示,由实施例3,和4制成的全电池在稳定运行循环650次后分别能够保持82.7%和98.4%的容量保持率。而由对比例2制成全电池在165次循环后出现容量大幅下降,说明电池发生短路,这也展现出了实施例3-4对锌金属电池性能的有效提高。As shown in FIG. 2 , the full batteries made in Examples 3 and 4 can maintain a capacity retention rate of 82.7% and 98.4%, respectively, after 650 cycles of stable operation. However, the capacity of the full battery made in Comparative Example 2 dropped significantly after 165 cycles, indicating that a short circuit occurred in the battery, which also showed that Examples 3-4 effectively improved the performance of the zinc metal battery.
测试例3Test case 3
将本发明实施例1和对比例1制成半电池样品,测试电极表面的双电层电容(测试系统为辰华电化学工作站)。图3为实施例1和对比例1的半电池样品的电极表面的双电层电容统计图,采用循环伏安法,测试范围为-0.015-0.015V,扫描速率为12-20mV。Example 1 of the present invention and Comparative Example 1 were made into half-cell samples, and the electric double layer capacitance on the electrode surface was tested (the test system was Chenhua Electrochemical Workstation). Fig. 3 is a statistical diagram of the electric double layer capacitance on the electrode surface of the half-cell samples of Example 1 and Comparative Example 1, using cyclic voltammetry, the test range is -0.015-0.015V, and the scan rate is 12-20mV.
如图3所示,实施例1电极表面的双电层电容相比对比例1有明显下降,说明乙二醇在电极表面发生了吸附行为,从而引导锌离子的均匀沉积。As shown in Figure 3, the electric double layer capacitance on the electrode surface of Example 1 is significantly lower than that of Comparative Example 1, indicating that ethylene glycol is adsorbed on the electrode surface, thereby guiding the uniform deposition of zinc ions.
测试例4Test case 4
将本发明实施例2和对比例1制成半电池样品,在电流密度5mA/cm2,恒电流沉积-电解容量2mAh/cm2条件下循环50圈后,通过X射线衍射对锌箔表面生成物进行了定性分析。Example 2 of the present invention and comparative example 1 were made into half-cell samples, and after 50 cycles at a current density of 5 mA/cm 2 and a constant current deposition-electrolytic capacity of 2 mAh/cm 2 , the surface of the zinc foil was formed by X-ray diffraction. Qualitative analysis was carried out.
如图4所示,通过XRD测试图,实施例2表面副产物Zn4(OH)6SO4·5H2O的信号(对应8度峰)明显低于对比例1,这表明实施例2对于副产物的产生有很明显的抑制作用,从而可以改善电池性能。As shown in Figure 4, through the XRD test pattern, the signal (corresponding to the peak of 8 degrees) of the surface by-product Zn 4 (OH) 6 SO 4 5H 2 O in Example 2 is significantly lower than that of Comparative Example 1, which shows that Example 2 is for The production of by-products can be significantly inhibited, which can improve battery performance.
以上仅为本发明的实施例,并非因此限制本发明的专利范围,凡是利用本发明说明书内容所作的等同变换,或直接或间接运用在相关的技术领域,均同理包括在本发明的专利保护范围内。The above are only examples of the present invention, and are not intended to limit the patent scope of the present invention. All equivalent transformations made by using the content of the description of the present invention, or directly or indirectly used in related technical fields, are equally included in the patent protection of the present invention. within range.
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