{"title":"金属氧化物基阳极电催化剂抑制反向电流降解的放电行为研究","authors":"Kazuaki Oda, Yoshiyuki Kuroda, Shigenori Mitsushima","doi":"10.1007/s12678-023-00815-0","DOIUrl":null,"url":null,"abstract":"<div><p>In the bipolar-type alkaline water electrolysis powered by renewable energy, electrocatalysts are degraded by repeated potential change associated with the generation of reverse current. If an electrode has large discharge capacity, the opposite electrode on the same bipolar plate is degraded by the reverse current. In this study, discharge capacity of various transition metal-based electrocatalysts was investigated to clarify the determining factors of electrocatalysts on the reverse current and durability. The discharge capacities from 1.5 to 0.5 V vs. RHE (<i>Q</i><sub>dc,0.5</sub>) of electrocatalysts are proportional to the surface area in most cases. The proportionality coefficient, corresponding to the specific capacity, is 1.0 C·m<sup>–2</sup> for Co<sub>3</sub>O<sub>4</sub> and 2.3 C·m<sup>–2</sup> for manganese-based electrocatalysts. The substitution of Co<sup>3+</sup> in Co<sub>3</sub>O<sub>4</sub> with Ni<sup>3+</sup> increased<i> Q</i><sub>dc,0.5</sub>. The upper limit of theoretical specific capacity for Co<sub>3</sub>O<sub>4</sub> is estimated to be 1.699 C·m<sup>–2</sup>, meaning the former and latter cases correspond to 2- and 1-electron reactions, respectively, per a cation at the surface. The discharge capacities of the elctrocatalysts increased because of the dissolution and recrystallization of nickel and/or cobalt into metal hydroxides. The increase in the capacities of Co<sub>3</sub>O<sub>4</sub> and NiCo<sub>2</sub>O<sub>4</sub> during ten charge–discharge cycles was below 2–9% and 0.5–38%, respectively. Therefore, if a cathode electrocatalyst with relatively low redox durability is used on the one side of a bipolar plate, it is necessary to control optimum discharge capacity of the anode by changing surface area and constituent metal cations to minimize the generation of reverse current.</p><h3>Graphical Abstract</h3>\n <figure><div><div><div><picture><source><img></source></picture></div></div></div></figure>\n </div>","PeriodicalId":535,"journal":{"name":"Electrocatalysis","volume":"14 3","pages":"499 - 510"},"PeriodicalIF":2.7000,"publicationDate":"2023-02-10","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://link.springer.com/content/pdf/10.1007/s12678-023-00815-0.pdf","citationCount":"1","resultStr":"{\"title\":\"Investigation of Charge–Discharging Behavior of Metal Oxide–Based Anode Electrocatalysts for Alkaline Water Electrolysis to Suppress Degradation due to Reverse Current\",\"authors\":\"Kazuaki Oda, Yoshiyuki Kuroda, Shigenori Mitsushima\",\"doi\":\"10.1007/s12678-023-00815-0\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>In the bipolar-type alkaline water electrolysis powered by renewable energy, electrocatalysts are degraded by repeated potential change associated with the generation of reverse current. If an electrode has large discharge capacity, the opposite electrode on the same bipolar plate is degraded by the reverse current. In this study, discharge capacity of various transition metal-based electrocatalysts was investigated to clarify the determining factors of electrocatalysts on the reverse current and durability. The discharge capacities from 1.5 to 0.5 V vs. RHE (<i>Q</i><sub>dc,0.5</sub>) of electrocatalysts are proportional to the surface area in most cases. The proportionality coefficient, corresponding to the specific capacity, is 1.0 C·m<sup>–2</sup> for Co<sub>3</sub>O<sub>4</sub> and 2.3 C·m<sup>–2</sup> for manganese-based electrocatalysts. The substitution of Co<sup>3+</sup> in Co<sub>3</sub>O<sub>4</sub> with Ni<sup>3+</sup> increased<i> Q</i><sub>dc,0.5</sub>. The upper limit of theoretical specific capacity for Co<sub>3</sub>O<sub>4</sub> is estimated to be 1.699 C·m<sup>–2</sup>, meaning the former and latter cases correspond to 2- and 1-electron reactions, respectively, per a cation at the surface. The discharge capacities of the elctrocatalysts increased because of the dissolution and recrystallization of nickel and/or cobalt into metal hydroxides. The increase in the capacities of Co<sub>3</sub>O<sub>4</sub> and NiCo<sub>2</sub>O<sub>4</sub> during ten charge–discharge cycles was below 2–9% and 0.5–38%, respectively. Therefore, if a cathode electrocatalyst with relatively low redox durability is used on the one side of a bipolar plate, it is necessary to control optimum discharge capacity of the anode by changing surface area and constituent metal cations to minimize the generation of reverse current.</p><h3>Graphical Abstract</h3>\\n <figure><div><div><div><picture><source><img></source></picture></div></div></div></figure>\\n </div>\",\"PeriodicalId\":535,\"journal\":{\"name\":\"Electrocatalysis\",\"volume\":\"14 3\",\"pages\":\"499 - 510\"},\"PeriodicalIF\":2.7000,\"publicationDate\":\"2023-02-10\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"https://link.springer.com/content/pdf/10.1007/s12678-023-00815-0.pdf\",\"citationCount\":\"1\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Electrocatalysis\",\"FirstCategoryId\":\"92\",\"ListUrlMain\":\"https://link.springer.com/article/10.1007/s12678-023-00815-0\",\"RegionNum\":4,\"RegionCategory\":\"化学\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q3\",\"JCRName\":\"CHEMISTRY, PHYSICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Electrocatalysis","FirstCategoryId":"92","ListUrlMain":"https://link.springer.com/article/10.1007/s12678-023-00815-0","RegionNum":4,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"CHEMISTRY, PHYSICAL","Score":null,"Total":0}
引用次数: 1
摘要
在以可再生能源为动力的双极性碱性电解中,电催化剂的降解是通过与产生逆流相关的反复电位变化来实现的。如果一个电极具有较大的放电容量,则同一双极板上的另一个电极受到反向电流的影响而退化。本研究考察了各种过渡金属基电催化剂的放电容量,以阐明电催化剂对电流和耐久性的决定因素。在大多数情况下,电催化剂的放电容量从1.5 V到0.5 V vs. RHE (Qdc,0.5)与比表面积成正比。Co3O4电催化剂的比例系数为1.0 C·m-2,锰基电催化剂的比例系数为2.3 C·m-2。用Ni3+取代Co3O4中的Co3+使Qdc增大0.5。Co3O4的理论比容量上限估计为1.699 C·m-2,这意味着前一种和后一种情况分别对应于表面每个阳离子的2电子和1电子反应。由于镍和/或钴在金属氢氧化物中的溶解和再结晶,电催化剂的放电容量增加。在10次充放电循环中,Co3O4和NiCo2O4的容量增幅分别小于2-9%和0.5-38%。因此,如果在双极板的一侧使用氧化还原耐久性相对较低的阴极电催化剂,则需要通过改变阳极的表面积和组成金属阳离子来控制阳极的最佳放电容量,以尽量减少反向电流的产生。图形抽象
Investigation of Charge–Discharging Behavior of Metal Oxide–Based Anode Electrocatalysts for Alkaline Water Electrolysis to Suppress Degradation due to Reverse Current
In the bipolar-type alkaline water electrolysis powered by renewable energy, electrocatalysts are degraded by repeated potential change associated with the generation of reverse current. If an electrode has large discharge capacity, the opposite electrode on the same bipolar plate is degraded by the reverse current. In this study, discharge capacity of various transition metal-based electrocatalysts was investigated to clarify the determining factors of electrocatalysts on the reverse current and durability. The discharge capacities from 1.5 to 0.5 V vs. RHE (Qdc,0.5) of electrocatalysts are proportional to the surface area in most cases. The proportionality coefficient, corresponding to the specific capacity, is 1.0 C·m–2 for Co3O4 and 2.3 C·m–2 for manganese-based electrocatalysts. The substitution of Co3+ in Co3O4 with Ni3+ increased Qdc,0.5. The upper limit of theoretical specific capacity for Co3O4 is estimated to be 1.699 C·m–2, meaning the former and latter cases correspond to 2- and 1-electron reactions, respectively, per a cation at the surface. The discharge capacities of the elctrocatalysts increased because of the dissolution and recrystallization of nickel and/or cobalt into metal hydroxides. The increase in the capacities of Co3O4 and NiCo2O4 during ten charge–discharge cycles was below 2–9% and 0.5–38%, respectively. Therefore, if a cathode electrocatalyst with relatively low redox durability is used on the one side of a bipolar plate, it is necessary to control optimum discharge capacity of the anode by changing surface area and constituent metal cations to minimize the generation of reverse current.
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