CN114759294A - Electrolyte for efficiently regulating and controlling dissolution behavior of magnesium anode and preparation method thereof - Google Patents
Electrolyte for efficiently regulating and controlling dissolution behavior of magnesium anode and preparation method thereof Download PDFInfo
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- 239000011777 magnesium Substances 0.000 title claims abstract description 84
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 title claims abstract description 83
- 229910052749 magnesium Inorganic materials 0.000 title claims abstract description 83
- 239000003792 electrolyte Substances 0.000 title claims abstract description 64
- 230000001105 regulatory effect Effects 0.000 title claims abstract description 26
- 238000004090 dissolution Methods 0.000 title claims abstract description 25
- 238000002360 preparation method Methods 0.000 title claims abstract description 17
- 230000001276 controlling effect Effects 0.000 title claims description 7
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims abstract description 44
- 238000000034 method Methods 0.000 claims abstract description 34
- 239000011780 sodium chloride Substances 0.000 claims abstract description 22
- YCPXWRQRBFJBPZ-UHFFFAOYSA-N 5-sulfosalicylic acid Chemical compound OC(=O)C1=CC(S(O)(=O)=O)=CC=C1O YCPXWRQRBFJBPZ-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000000203 mixture Substances 0.000 claims abstract description 15
- 239000000463 material Substances 0.000 claims abstract description 13
- 239000000243 solution Substances 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000007864 aqueous solution Substances 0.000 claims abstract description 5
- YGSDEFSMJLZEOE-UHFFFAOYSA-N salicylic acid Chemical compound OC(=O)C1=CC=CC=C1O YGSDEFSMJLZEOE-UHFFFAOYSA-N 0.000 claims abstract description 5
- FJKROLUGYXJWQN-UHFFFAOYSA-N papa-hydroxy-benzoic acid Natural products OC(=O)C1=CC=C(O)C=C1 FJKROLUGYXJWQN-UHFFFAOYSA-N 0.000 claims abstract 2
- 229960004889 salicylic acid Drugs 0.000 claims abstract 2
- 239000008367 deionised water Substances 0.000 claims description 10
- 229910021641 deionized water Inorganic materials 0.000 claims description 10
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 6
- 239000008151 electrolyte solution Substances 0.000 claims description 5
- 229910000861 Mg alloy Inorganic materials 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 238000012545 processing Methods 0.000 abstract description 3
- 239000013535 sea water Substances 0.000 abstract description 3
- 230000000052 comparative effect Effects 0.000 description 18
- 238000005260 corrosion Methods 0.000 description 16
- 230000007797 corrosion Effects 0.000 description 16
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 11
- 239000001257 hydrogen Substances 0.000 description 11
- 229910052739 hydrogen Inorganic materials 0.000 description 11
- 230000000694 effects Effects 0.000 description 7
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 4
- 238000002791 soaking Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000003112 inhibitor Substances 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 235000010333 potassium nitrate Nutrition 0.000 description 2
- 239000004323 potassium nitrate Substances 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 238000010998 test method Methods 0.000 description 2
- 230000004580 weight loss Effects 0.000 description 2
- 229910019440 Mg(OH) Inorganic materials 0.000 description 1
- ABBQHOQBGMUPJH-UHFFFAOYSA-M Sodium salicylate Chemical compound [Na+].OC1=CC=CC=C1C([O-])=O ABBQHOQBGMUPJH-UHFFFAOYSA-M 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 239000003929 acidic solution Substances 0.000 description 1
- 238000005275 alloying Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000000536 complexating effect Effects 0.000 description 1
- 239000008139 complexing agent Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000011245 gel electrolyte Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 229960004025 sodium salicylate Drugs 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
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- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M12/00—Hybrid cells; Manufacture thereof
- H01M12/04—Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type
- H01M12/06—Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type with one metallic and one gaseous electrode
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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
- H01M2300/00—Electrolytes
- H01M2300/0002—Aqueous electrolytes
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Abstract
一种高效调控镁阳极溶解行为的电解液及其制备方法,电解液为氯化钠和5‑磺基水杨酸的混合水溶液,其中氯化钠的浓度为0.5~0.7M,5‑磺基水杨酸的浓度为0.01~0.1M,pH值=7.0±0.2;制备方法为:(1)将氯化钠和5‑磺基水杨酸混合,制成混合物料;(2)将去离子水加入到混合物料中,搅拌形成透明溶液;(3)调节pH值=7.0±0.2,制成高效调控镁阳极溶解行为的电解液。本发明可调控溶质比例来改善镁合金电化学行为、电解质成分易于取得、加工制备电解液工艺简单、可作用于海水环境、适应于三种不同放电电流密度及环保等特点;可很好地提高镁空气电池性能。
An electrolyte for efficiently regulating the dissolution behavior of magnesium anodes and a preparation method thereof. The electrolyte is a mixed aqueous solution of sodium chloride and 5-sulfosalicylic acid, wherein the concentration of sodium chloride is 0.5-0.7M, and the concentration of 5-sulfosalicylic acid is 0.5-0.7M. The concentration of salicylic acid is 0.01~0.1M, and pH value=7.0±0.2; the preparation method is: (1) mixing sodium chloride and 5-sulfosalicylic acid to prepare a mixed material; (2) deionizing Water is added to the mixture and stirred to form a transparent solution; (3) the pH value is adjusted to 7.0±0.2 to prepare an electrolyte for efficiently regulating the dissolution behavior of the magnesium anode. The invention can adjust the solute ratio to improve the electrochemical behavior of the magnesium alloy, the electrolyte components are easy to obtain, the process for processing and preparing the electrolyte is simple, it can act on the seawater environment, and it is suitable for three different discharge current densities and environmental protection. Magnesium-air battery performance.
Description
技术领域technical field
本发明涉及一种高效调控镁阳极溶解行为的电解液及其制备方法,属于镁空气电池电解液技术领域。The invention relates to an electrolyte for efficiently regulating the dissolution behavior of magnesium anodes and a preparation method thereof, and belongs to the technical field of electrolytes for magnesium-air batteries.
背景技术Background technique
能源问题永远是21世纪的热点问题,随着科技进展,人们对于能源需求量和使用量明显加大。煤炭,石油等化石能源目前消耗严重且不可再生,燃烧后会产生SO2、CO2等有害气体。SO2气体进入大气层中会出现酸雨现象,CO2气体造成―温室效应现象,致使海平面上升等极端恶劣气候变化情况出现,进而很大程度的影响了人们的生产生活;因此对于新型能源(电池)的探究尤为重要。Energy issues will always be a hot issue in the 21st century. With the development of science and technology, people's demand for and use of energy has increased significantly. Fossil energy such as coal and petroleum is currently consumed seriously and is not renewable. After combustion, harmful gases such as SO 2 and CO 2 will be produced. When SO 2 gas enters the atmosphere, acid rain will occur, and CO 2 gas will cause the greenhouse effect phenomenon, resulting in extreme climate change such as sea level rise, which will greatly affect people's production and life; therefore, for new energy (battery) ) is particularly important.
镁空气电池因其具有高的理论电压及电容量,有望随着研究进程的不断深入,替代化石能源。但同时镁空气电池也因自身的特点也存在着应用上的限制,如阳极在水溶液中耐蚀性较差,展示出较低的阳极利用率。阳极放电后放电产物易于沉积至阳极表面,空气阴极利用氧气反应来进行电荷传导存在阻碍,最终导致实际镁空气电池放电电压较低。因此,改善镁空气电池的放电性能具有极大的研究价值。Because of its high theoretical voltage and electric capacity, magnesium-air batteries are expected to replace fossil energy with the deepening of the research process. However, magnesium-air batteries also have application limitations due to their own characteristics. For example, the anode has poor corrosion resistance in aqueous solution and shows a low anode utilization rate. After the anode is discharged, the discharge products are easily deposited on the surface of the anode, and the use of oxygen reaction in the air cathode to conduct charge conduction is hindered, which eventually leads to a lower discharge voltage of the actual magnesium-air battery. Therefore, it is of great research value to improve the discharge performance of magnesium-air batteries.
针对镁空气电池的性能的改善,主要是提升镁空气电池中阳极部分的性能。通常提升阳极性能的手段有两种,分别是通过挤压和合金化等手段改善阳极成分、调节电解液成分方式提升阳极性能。调控电解液成分,提高镁阳极耐蚀性或加快阳极表面放电产物的脱落,从而更大程度的维持放电过程中镁表面电荷的转移过程,保证长周期下放电电位的稳定以及高的阳极利用率和比容量。利用电解液改善阳极放电性能和阳极耐蚀性能的方法成本较低且加工工艺简便,相较于传统的改善阳极成分的方式,具有更大的实际生产应用的意义。For the improvement of the performance of the magnesium-air battery, the main purpose is to improve the performance of the anode part of the magnesium-air battery. There are usually two ways to improve anode performance, namely, improving anode composition by means of extrusion and alloying, and adjusting electrolyte composition to improve anode performance. Adjust the composition of the electrolyte, improve the corrosion resistance of the magnesium anode or accelerate the shedding of the discharge products on the anode surface, so as to maintain the transfer process of the surface charge on the magnesium surface during the discharge process to a greater extent, and ensure the stability of the discharge potential under long-term cycles and high anode utilization. and specific capacity. The method of using electrolyte to improve anode discharge performance and anode corrosion resistance is low in cost and simple in processing technology. Compared with the traditional method of improving anode composition, it has greater significance in practical production and application.
尽管通过改善或调控电解液成分具有诸多优势,但是目前对于镁空气电池电解液的发明非常少,并没有受到人们的广泛关注。申请号为201911073752.X的专利提出一种用增塑剂,第一聚合物单体,第二聚合物单体,引发剂,无机盐填料、复合缓蚀剂提升阳极性能的方法;该方法能够提高镁合金在溶液中的耐蚀性。但是缓蚀剂的过度添加减少了阳极与电解液之间的接触面积,不利于维持放电电位的低且稳定。并且该发明提供的电解质成分复杂,需要搅拌、马弗炉加热处理、研磨粉末及制备凝胶电解液等复杂工艺,为工业生产、大规模应用带来了不便。Although there are many advantages by improving or regulating the composition of the electrolyte, the invention of the electrolyte for magnesium-air batteries is very few at present, and it has not received widespread attention. The patent with the application number of 201911073752.X proposes a method for improving anode performance with a plasticizer, a first polymer monomer, a second polymer monomer, an initiator, an inorganic salt filler, and a composite corrosion inhibitor; this method can Improve the corrosion resistance of magnesium alloys in solution. However, excessive addition of corrosion inhibitor reduces the contact area between the anode and the electrolyte, which is not conducive to maintaining a low and stable discharge potential. In addition, the electrolyte provided by the invention has complex components, and requires complicated processes such as stirring, heating treatment in a muffle furnace, grinding powder, and preparing a gel electrolyte, which brings inconvenience to industrial production and large-scale application.
申请号为202110301670.7的专利提出一种用硝酸钾和水杨酸类化合物的电解液改善电池性能的方法,提升了2.5mA cm-2下AZ31阳极的放电性能,该专利表明AZ31阳极在0.05mol/L硝酸钾和0.1mol/L水杨酸钠混合电解液中放电性能最好,放电电位最低,但仍然仅在-1.0V左右,远低于理论值。该发明仅仅提供了电解液在2.5mA cm-2的电流密度下对阳极的作用,没有提供高电流密度下电解液对于阳极性能的影响。镁空气电池主要应用于海水环境,但是该发明并没有考虑到氯化钠溶液对于阳极的影响,存在较大缺陷。The patent with the application number of 202110301670.7 proposes a method for improving the battery performance with the electrolyte of potassium nitrate and salicylic acid compounds, which improves the discharge performance of the AZ31 anode at 2.5mA cm -2 . The patent shows that the AZ31 anode is at 0.05mol/mol/ The mixed electrolyte of L potassium nitrate and 0.1mol/L sodium salicylate has the best discharge performance and the lowest discharge potential, but it is still only around -1.0V, which is far lower than the theoretical value. The invention only provides the effect of the electrolyte on the anode at a current density of 2.5 mA cm -2 , but does not provide the effect of the electrolyte on the performance of the anode at a high current density. Magnesium-air batteries are mainly used in seawater environment, but the invention does not take into account the influence of sodium chloride solution on the anode, and there are major defects.
发明内容SUMMARY OF THE INVENTION
本发明针对镁空气电池中阳极耐蚀性差,放电过程中阳极表面放电产物累积而造成电压迟滞等问题,提供一种高效调控镁阳极溶解行为的电解液及其制备方法,有效改善镁阳极的耐蚀行为并提升放电性能。Aiming at the problems of poor corrosion resistance of the anode in the magnesium-air battery, voltage hysteresis caused by the accumulation of discharge products on the anode surface during the discharge process, and the like, the invention provides an electrolyte for efficiently regulating the dissolution behavior of the magnesium anode and a preparation method thereof, and effectively improves the resistance of the magnesium anode. corrosion behavior and improved discharge performance.
本发明的高效调控镁阳极溶解行为的电解液为氯化钠和5-磺基水杨酸的混合水溶液,其中氯化钠的浓度为0.5~0.7M,5-磺基水杨酸的浓度为0.01~0.1M,pH值=7.0±0.2。The electrolyte for efficiently regulating the dissolution behavior of magnesium anode in the present invention is a mixed aqueous solution of sodium chloride and 5-sulfosalicylic acid, wherein the concentration of sodium chloride is 0.5-0.7M, and the concentration of 5-sulfosalicylic acid is 0.01~0.1M, pH=7.0±0.2.
本发明的高效调控镁阳极溶解行为的电解液的制备方法按以下步骤进行:The preparation method of the electrolytic solution for efficiently regulating and controlling the dissolution behavior of magnesium anode of the present invention is carried out according to the following steps:
(1)将氯化钠和5-磺基水杨酸混合,制成混合物料;(1) sodium chloride and 5-sulfosalicylic acid are mixed to make mixed material;
(2)将去离子水加入到混合物料中,然后对全部物料进行搅拌,直至形成透明溶液;(2) deionized water is added to the mixture, and then all the materials are stirred until a transparent solution is formed;
(3)用氢氧化钠或盐酸调节透明溶液的pH值,至pH值=7.0±0.2,制成高效调控镁阳极溶解行为的电解液。(3) The pH value of the transparent solution is adjusted with sodium hydroxide or hydrochloric acid to pH value=7.0±0.2, so as to prepare an electrolyte for efficiently regulating the dissolution behavior of magnesium anode.
上述的步骤(2)中,加入去离子水时,是将混合物料置于容器中,将去离子水沿容器内壁倒入。In the above-mentioned step (2), when adding deionized water, the mixture material is placed in a container, and the deionized water is poured along the inner wall of the container.
上述的步骤(2)中,搅拌速度为100~150rpm。In the above-mentioned step (2), the stirring speed is 100-150 rpm.
上述的步骤(3)中,调节pH值时用pH-电导率仪进行监测。In the above-mentioned step (3), the pH-conductivity meter is used to monitor the pH value.
本发明的高效调控镁阳极溶解行为的电解液的使用方法为:The using method of the electrolyte of the present invention for efficiently regulating and controlling the dissolving behavior of magnesium anode is:
将镁阳极置于高效调控镁阳极溶解行为的电解液中,构成一个镁空气电池;通过电源向镁阳极通电。The magnesium anode is placed in an electrolyte that can efficiently regulate the dissolution behavior of the magnesium anode to form a magnesium-air battery; the magnesium anode is energized through a power source.
上述的使用方法中,镁阳极的材质为纯度≥99.5%的纯镁。In the above method of use, the material of the magnesium anode is pure magnesium with a purity of ≥99.5%.
上述的使用方法中,通电的电流密度为2.5~10mA·cm-2。In the above-mentioned usage method, the current density of the energization is 2.5 to 10 mA·cm −2 .
上述的使用方法中,阴极为空气阴极。In the above method of use, the cathode is an air cathode.
本发明提供的高效调节镁阳极的电解液首次引入氯化钠和强络合剂5-磺基水杨酸,可通过调控二者比例从而改善纯镁的耐蚀性和放电性能;具有电解质易于取得、加工工艺简单、成本低、绿色环保及适用于海洋环境等特点。The electrolyte for high-efficiency adjustment of magnesium anode provided by the present invention introduces sodium chloride and strong complexing agent 5-sulfosalicylic acid for the first time, and the corrosion resistance and discharge performance of pure magnesium can be improved by adjusting the ratio of the two; It has the characteristics of simple acquisition, simple processing technology, low cost, green environmental protection and suitable for marine environment.
镁阳极在本发明提供的电解液中展示出优良的耐蚀性;未加电流状态下,缓蚀效率达到66.7%;平均放电电位达到-1.83V;电位下降明显,相较于氯化钠溶液降低了约200mV。The magnesium anode shows excellent corrosion resistance in the electrolyte provided by the present invention; in the state of no current application, the corrosion inhibition efficiency reaches 66.7%; the average discharge potential reaches -1.83V; the potential drops significantly, compared with the sodium chloride solution reduced by about 200mV.
本发明提供的电解液显著提升了镁阳极的利用效率;镁阳极在本发明提供的电解液中放电比容量得到很大提升。The electrolyte provided by the present invention significantly improves the utilization efficiency of the magnesium anode; the discharge specific capacity of the magnesium anode is greatly improved in the electrolyte provided by the present invention.
本发明成功制备一种高效调控镁阳极溶解行为的电解液,与原有发明相比,具有如下优势:可调控溶质比例来改善镁合金电化学行为、电解质成分易于取得、加工制备电解液工艺简单、可作用于海水环境、适应于三种不同放电电流密度及环保等特点;可很好地提高镁空气电池性能。Compared with the original invention, the present invention successfully prepares an electrolyte for efficiently regulating the dissolution behavior of magnesium anode, and has the following advantages: the ratio of solute can be regulated to improve the electrochemical behavior of magnesium alloy, the electrolyte composition is easy to obtain, and the process for preparing the electrolyte is simple. , Can act in seawater environment, adapt to three different discharge current densities and environmental protection characteristics; can well improve the performance of magnesium-air batteries.
附图说明Description of drawings
图1为镁阳极在对比例和本发明实施例中浸泡两天后的析氢量曲线图;Fig. 1 is the hydrogen evolution curve diagram of magnesium anode after soaking for two days in the comparative example and the embodiment of the present invention;
图2为镁阳极在对比例和本发明实施例中在2.5mA·cm-2时平均放电电位曲线图;2 is a graph of the average discharge potential of the magnesium anode at 2.5 mA cm −2 in the comparative example and the embodiment of the present invention;
图3为镁阳极在对比例和本发明实施例中在5mA·cm-2时平均放电电位曲线图;3 is a graph of the average discharge potential of the magnesium anode at 5 mA·cm −2 in the comparative example and the embodiment of the present invention;
图4为镁阳极在对比例和本发明实施例中在10mA·cm-2时平均放电电位曲线图;4 is a graph of the average discharge potential of the magnesium anode at 10 mA·cm −2 in the comparative example and the embodiment of the present invention;
图5为镁阳极在对比例和本发明实施例中在不同电流密度下利用效率曲线图;5 is a graph showing the utilization efficiency of magnesium anodes under different current densities in the comparative example and the embodiment of the present invention;
图6为镁阳极在对比例和本发明实施例中在不同电流密度下放电比容量曲线图。FIG. 6 is a graph showing the discharge specific capacity of the magnesium anode at different current densities in the comparative example and the embodiment of the present invention.
具体实施方式Detailed ways
下面对本发明提供的实施例进行进一步说明,特此提出以下的实施例仅说明本发明的实施方法。熟练操作人员可对该实施方法进行适度改善,该实施方法并不局限于本发明提供的实施例。The embodiments provided by the present invention will be further described below, and the following embodiments are hereby proposed only to illustrate the implementation method of the present invention. A skilled operator can make appropriate improvements to the implementation method, and the implementation method is not limited to the examples provided in the present invention.
对比例Comparative ratio
将去离子水加入氯化钠中,然后对全部物料进行搅拌,搅拌速度为120rpm,直至形成透明溶液;用pH-电导率仪进行监测pH值为7.0±0.2;制成对比电解液;Add deionized water to sodium chloride, and then stir all the materials at a stirring speed of 120 rpm until a transparent solution is formed; use a pH-conductivity meter to monitor the pH value of 7.0 ± 0.2; make a comparative electrolyte;
将镁阳极置于对比电解液中,构成一个镁空气电池;通过电源向镁阳极通电’镁阳极的材质为纯度≥99.5%的纯镁;通电的电流密度为2.5~10mA·cm-2;阴极为空气阴极;The magnesium anode is placed in a comparative electrolyte to form a magnesium-air battery; the magnesium anode is energized through a power source; the material of the magnesium anode is pure magnesium with a purity of ≥99.5%; the current density of the electrification is 2.5-10 mA·cm -2 ; the cathode is is the air cathode;
镁阳极在对比电解液中浸泡两天,测试的镁阳极面积为900cm-2,最终得到总的析氢量;放电电流密度分别为2.5、5和10mA·cm-2,放电时长为10h;测试镁阳极在对比例1中放电完毕后的失重,得到阳极利用效率和放电比容量;The magnesium anode was soaked in the comparative electrolyte for two days, and the area of the tested magnesium anode was 900cm -2 , and the total amount of hydrogen evolution was finally obtained; the discharge current densities were 2.5, 5 and 10mA·cm -2 respectively, and the discharge time was 10h; The weight loss of the anode after the discharge in Comparative Example 1 was completed, and the anode utilization efficiency and discharge specific capacity were obtained;
浸泡两天后的析氢量如图1所示;从图1可知,镁阳极在对比例1中的耐蚀性较差,阳极在三个放电电流密度下放电电位如图2~4所示,放电电位较高,这表明阳极在放电后,阳极表面有大量的放电产物堆积,阳极与电解液接触面积剧烈减小;利用效率和放电比容量分别如图5、6所示,证明了阳极在放电完毕后的利用效率及放电比容量较低,这意味着阳极在放电过程存在大块的镁基体脱落现象,不利于提升镁阳极的放电性能。The amount of hydrogen evolution after soaking for two days is shown in Figure 1; it can be seen from Figure 1 that the corrosion resistance of the magnesium anode in Comparative Example 1 is poor, and the discharge potential of the anode under three discharge current densities is shown in Figures 2 to 4. The potential is higher, which indicates that after the anode is discharged, a large number of discharge products are deposited on the surface of the anode, and the contact area between the anode and the electrolyte is drastically reduced; The utilization efficiency and discharge specific capacity after completion are low, which means that the anode has a large magnesium matrix shedding phenomenon during the discharge process, which is not conducive to improving the discharge performance of the magnesium anode.
实施例1Example 1
高效调控镁阳极溶解行为的电解液中,氯化钠的浓度为0.62M,5-磺基水杨酸的浓度为0.01M;In the electrolyte for efficiently regulating the dissolution behavior of magnesium anode, the concentration of sodium chloride is 0.62M, and the concentration of 5-sulfosalicylic acid is 0.01M;
将氯化钠和5-磺基水杨酸混合,制成混合物料;Mix sodium chloride and 5-sulfosalicylic acid to prepare a mixture;
将去离子水加入到混合物料中,然后对全部物料进行搅拌,直至形成透明溶液;加入去离子水时,是将混合物料置于容器中,将去离子水沿容器内壁倒入;搅拌速度为100~150rpm;Add deionized water to the mixture, and then stir all the materials until a transparent solution is formed; when adding deionized water, place the mixture in a container, and pour the deionized water along the inner wall of the container; the stirring speed is 100~150rpm;
用氢氧化钠或盐酸调节透明溶液的pH值,用pH-电导率仪进行监测,至pH值=7.0±0.2,制成高效调控镁阳极溶解行为的电解液。The pH value of the transparent solution is adjusted with sodium hydroxide or hydrochloric acid, and the pH value is monitored with a pH-conductivity meter until the pH value is 7.0±0.2, and an electrolyte solution for efficiently regulating the dissolution behavior of magnesium anode is prepared.
使用方法为:The method of use is:
将镁阳极置于高效调控镁阳极溶解行为的电解液中,构成一个镁空气电池;通过电源向镁阳极通电;镁阳极的材质为纯度≥99.5%的纯镁;通电的电流密度分别为2.5、5和10mA·cm-2;阴极为空气阴极;The magnesium anode is placed in an electrolyte that efficiently regulates the dissolution behavior of the magnesium anode to form a magnesium air battery; the magnesium anode is energized through a power source; the material of the magnesium anode is pure magnesium with a purity of ≥99.5%; 5 and 10 mA·cm -2 ; the cathode is an air cathode;
镁阳极在高效调控镁阳极溶解行为的电解液中浸泡两天,测试的镁阳极面积约为900cm2,最终得到总的析氢量,判断阳极的耐蚀性;镁阳极在实施例1中的放电时长为10个小时;测试了镁阳极放电完毕后的失重,得到阳极利用效率和放电比容量;The magnesium anode was soaked for two days in an electrolyte that efficiently regulates the dissolution behavior of the magnesium anode, and the area of the magnesium anode tested was about 900 cm 2 , and the total amount of hydrogen evolution was finally obtained to judge the corrosion resistance of the anode; the discharge of the magnesium anode in Example 1 The duration is 10 hours; the weight loss after the discharge of the magnesium anode is tested, and the anode utilization efficiency and discharge specific capacity are obtained;
析氢量如图1所示;镁阳极化学性质活泼,在水溶液中易于失去最外层轨道电子而变为Mg2+,失去的两个电子易于与中性溶液中的H2O或酸性溶液中的H+结合而产生氢气;因此,浸泡2天的析氢量情况可很好的反应阳极的耐蚀性;从图1可知,镁阳极的耐蚀性很好,48小时后,阳极的析氢量约为5mL cm-2,明显低于阳极在对比例1中的析氢量,表明具有很好地调控阳极溶解行为的能力,增强了阳极耐蚀性。The amount of hydrogen evolution is shown in Figure 1; the magnesium anode is chemically active, and it is easy to lose the outermost orbital electrons in aqueous solution to become Mg 2+ , and the two lost electrons are easy to be combined with H 2 O in neutral solution or in acidic solution. Therefore, the amount of hydrogen evolution of the immersion for 2 days can reflect the corrosion resistance of the anode very well; it can be seen from Figure 1 that the corrosion resistance of the magnesium anode is very good, after 48 hours, the amount of hydrogen evolution of the anode It is about 5 mL cm -2 , which is significantly lower than the hydrogen evolution amount of the anode in Comparative Example 1, indicating that it has the ability to well control the dissolution behavior of the anode and enhance the corrosion resistance of the anode.
实施例2Example 2
高效调控镁阳极溶解行为的电解液中,氯化钠的浓度为0.62M,5-磺基水杨酸的浓度为0.05M;In the electrolyte for efficiently regulating the dissolution behavior of magnesium anode, the concentration of sodium chloride is 0.62M, and the concentration of 5-sulfosalicylic acid is 0.05M;
制备方法同实施例1;The preparation method is the same as in Example 1;
使用方法和测试方法同实施例1,浸泡两天后的析氢量如图1所示;镁阳极化学性质活泼,析氢总量高于对比例1,这表明有助于增加镁阳极的电化学活性,加大阳极与电解液的接触,有利于促进阳极溶解,以便提供更低的放电电位;由图2~4可见,当电流密度为2.5,5mA cm-2时,阳极的平均放电电位明显低于对比例1;镁阳极在实施例2中展示出了-1.82V的平均放电电位(2.5mA cm-2);由图5、6可见,观察发现有效提升了阳极利用效率及比容,其原因电解液络合能力较强,抑制了大块的未溶解镁基体在放电过程中脱落于电解液中的现象发生,从而提升了阳极利用效率及比容;当电流密度为2.5mA cm-2时,相较于对比例1,阳极利用效率提升了11.5%,比容量提升了255mAgh-1。The use method and test method are the same as in Example 1, and the amount of hydrogen evolution after soaking for two days is shown in Figure 1; the chemical properties of the magnesium anode are active, and the total amount of hydrogen evolution is higher than that of Comparative Example 1, which shows that it is helpful to increase the electrochemical activity of the magnesium anode, Increasing the contact between the anode and the electrolyte is conducive to promoting the dissolution of the anode, so as to provide a lower discharge potential; it can be seen from Figures 2 to 4 that when the current density is 2.5 and 5 mA cm -2 , the average discharge potential of the anode is significantly lower than Comparative Example 1; the magnesium anode showed an average discharge potential of -1.82V (2.5mA cm -2 ) in Example 2; as can be seen from Figures 5 and 6, it was observed that the anode utilization efficiency and specific volume were effectively improved. The reason The strong complexing ability of the electrolyte inhibits the phenomenon that large pieces of undissolved magnesium matrix fall off into the electrolyte during the discharge process, thereby improving the anode utilization efficiency and specific volume; when the current density is 2.5mA cm -2 , compared with Comparative Example 1, the anode utilization efficiency is increased by 11.5%, and the specific capacity is increased by 255mAgh -1 .
实施例3Example 3
高效调控镁阳极溶解行为的电解液中,氯化钠的浓度为0.62M,5-磺基水杨酸的浓度为0.1M;In the electrolyte for efficiently regulating the dissolution behavior of magnesium anode, the concentration of sodium chloride is 0.62M, and the concentration of 5-sulfosalicylic acid is 0.1M;
制备方法同实施例1;The preparation method is the same as in Example 1;
使用方法和测试方法同实施例1,浸泡两天后的析氢量达到最高,为27mL/cm2;这表明镁阳极在电解液中溶解速度最快,电化学活性最强,放电潜力最大;快速的阳极溶解能力决定放电产物在阳极表面沉积异常困难;阳极在放电过程中Mg(OH)2出现的概率最小,便于阳极与电解液的接触,提供低且平稳的放电电位;镁阳极在电解液中的放电电位如图2~4所示;三个放电电流密度下,阳极在电解液中的平均放电电位明显低于对比例1;强的络合镁阳极能力极大减轻了放电产物对于阳极放电电位的迟滞影响;当电流密度为2.5mA cm-2时,镁阳极在电解液中平均放电电位约为-1.84V,比对比例1中平均放电电位低200mV;图5、6证明电解液改善了阳极利用效率及比容,电解液成功抑制了大块的未溶脱落现象的发生,最大程度提升了阳极利用效率及比容;当电流密度为10mA cm-2时,阳极在电解液中利用效率达到了57.6%,比容量达到了1286.5mAg h-1。The use method and test method are the same as in Example 1, and the hydrogen evolution amount after soaking for two days reaches the highest, which is 27mL/cm 2 ; this shows that the magnesium anode dissolves the fastest in the electrolyte, has the strongest electrochemical activity, and has the greatest discharge potential; fast The ability to dissolve the anode determines that the deposition of discharge products on the surface of the anode is extremely difficult; the probability of the appearance of Mg(OH) 2 in the anode is the smallest during the discharge process, which facilitates the contact between the anode and the electrolyte and provides a low and stable discharge potential; the magnesium anode is in the electrolyte. The discharge potentials are shown in Figures 2-4; under three discharge current densities, the average discharge potential of the anode in the electrolyte is significantly lower than that of Comparative Example 1; the strong ability to complex magnesium anode greatly reduces the effect of discharge products on anode discharge. The hysteresis effect of the potential; when the current density is 2.5mA cm -2 , the average discharge potential of the magnesium anode in the electrolyte is about -1.84V, which is 200mV lower than the average discharge potential in Comparative Example 1; Figures 5 and 6 demonstrate that the electrolyte improves The anode utilization efficiency and specific volume were improved, and the electrolyte successfully suppressed the occurrence of large undissolved shedding, which maximized the anode utilization efficiency and specific volume; when the current density was 10mA cm -2 , the anode was utilized in the electrolyte. The efficiency reaches 57.6% and the specific capacity reaches 1286.5mAg h -1 .
实施例4Example 4
高效调控镁阳极溶解行为的电解液中,氯化钠的浓度为0.5M,5-磺基水杨酸的浓度为0.01M;In the electrolyte for efficiently regulating the dissolution behavior of magnesium anode, the concentration of sodium chloride is 0.5M, and the concentration of 5-sulfosalicylic acid is 0.01M;
制备方法同实施例1;The preparation method is the same as in Example 1;
使用方法同实施例1。The use method is the same as that of Example 1.
实施例5Example 5
高效调控镁阳极溶解行为的电解液中,氯化钠的浓度为0.7M,5-磺基水杨酸的浓度为0.01M;In the electrolyte for efficiently regulating the dissolution behavior of magnesium anode, the concentration of sodium chloride is 0.7M, and the concentration of 5-sulfosalicylic acid is 0.01M;
制备方法同实施例1;The preparation method is the same as in Example 1;
使用方法同实施例1。The use method is the same as that of Example 1.
实施例6Example 6
高效调控镁阳极溶解行为的电解液中,氯化钠的浓度为0.5M,5-磺基水杨酸的浓度为0.1M;In the electrolyte for efficiently regulating the dissolution behavior of magnesium anode, the concentration of sodium chloride is 0.5M, and the concentration of 5-sulfosalicylic acid is 0.1M;
制备方法同实施例1;The preparation method is the same as in Example 1;
使用方法同实施例1。The use method is the same as that of Example 1.
实施例7Example 7
高效调控镁阳极溶解行为的电解液中,氯化钠的浓度为0.7M,5-磺基水杨酸的浓度为0.01M;In the electrolyte for efficiently regulating the dissolution behavior of magnesium anode, the concentration of sodium chloride is 0.7M, and the concentration of 5-sulfosalicylic acid is 0.01M;
制备方法同实施例1;The preparation method is the same as in Example 1;
使用方法同实施例1。The use method is the same as that of Example 1.
实施例8Example 8
高效调控镁阳极溶解行为的电解液中,氯化钠的浓度为0.7M,5-磺基水杨酸的浓度为0.1M;In the electrolyte for efficiently regulating the dissolution behavior of magnesium anode, the concentration of sodium chloride is 0.7M, and the concentration of 5-sulfosalicylic acid is 0.1M;
制备方法同实施例1;The preparation method is the same as in Example 1;
使用方法同实施例1。The use method is the same as that of Example 1.
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