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离子交换-电沉积法制备高Pt利用率多孔电极
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作者 陈四国 丁炜 +3 位作者 齐学强 李莉 邓子华 魏子栋 《电化学》 CAS CSCD 北大核心 2013年第1期53-58,共6页
采用离子交换-电沉积的方法(Ion-Exchange/Electrodeposition,IEE)制备了一种高Pt利用率催化电极,对所制备电极的表面形貌、催化活性及单电池性能用线性扫描伏安(LSV)、扫描电镜(SEM)、透射电镜(TEM)和单电池测试进行了表征.结果表明,... 采用离子交换-电沉积的方法(Ion-Exchange/Electrodeposition,IEE)制备了一种高Pt利用率催化电极,对所制备电极的表面形貌、催化活性及单电池性能用线性扫描伏安(LSV)、扫描电镜(SEM)、透射电镜(TEM)和单电池测试进行了表征.结果表明,通过电极制备工艺和离子交换-电沉积参数的调控,能够消除碳载体表面官能团的影响,使铂阳离子只与全氟磺酸树脂(Nafion)上的H+进行交换.在无铂离子的电解质中,将被交换的铂阳离子还原到与Nafion接触的碳载体上,使每一个铂纳米粒子都处于气体多孔电极的三相界面上,有效地调控铂纳米粒子的尺寸和分散度.单电池测试表明,以铂载量为0.014 mgP.tcm-2的IEE电极组装的电池的输出功率与铂载量为0.3 mgP.tcm-2的Nafion粘接Pt/C电极相当. 展开更多
关键词 燃料电池 离子交换.电沉积 铂利用率
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硫化亚锡敏化纳晶TiO_2膜的制备及光电性能研究 被引量:2
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作者 张晓萍 兰章 +4 位作者 陈琳 高素雯 吴晚霞 阙兰芳 张晓佩 《无机材料学报》 SCIE EI CAS CSCD 北大核心 2013年第10期1093-1097,共5页
采用简单的离子交换沉积法制备了SnS敏化的纳晶TiO2光阳极。通过SEM、XRD、UV-Vis等手段对光阳极的表面形貌,晶态结构,紫外-可见吸收和散射性能进行表征。并分别以聚苯胺和铂为催化剂制备对电极,以含碘氧化还原电对和硫氧化还原电对溶... 采用简单的离子交换沉积法制备了SnS敏化的纳晶TiO2光阳极。通过SEM、XRD、UV-Vis等手段对光阳极的表面形貌,晶态结构,紫外-可见吸收和散射性能进行表征。并分别以聚苯胺和铂为催化剂制备对电极,以含碘氧化还原电对和硫氧化还原电对溶液为电解质,组装SnS敏化太阳能电池,对其光电性能进行研究。通过比较不同光阳极、电解质和对电极的组合,发现用光阳极为离子交换沉积9次SnS的纳晶TiO2膜,对电极为聚苯胺不锈钢网压片膜,电解质为含硫氧化还原电对溶液组装的太阳能电池光电性能最佳,其短路电流、开路电压、填充因子和光电转换效率分别达到4.59 mA/cm2、0.547 V、0.505和1.27%。 展开更多
关键词 硫化亚锡敏化太阳能电池 离子交换沉积 聚苯胺 光电性能
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Electrodeposition of cobalt in double-membrane three-compartment electrolytic reactor 被引量:8
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作者 周键 王三反 宋小三 《Transactions of Nonferrous Metals Society of China》 SCIE EI CAS CSCD 2016年第6期1706-1713,共8页
The process parameters were optimized for the electrodeposition of cobalt from cobalt chloride solution in the membrane electrolytic reactor. Effects of parameters such as catholyte composition, current density and t... The process parameters were optimized for the electrodeposition of cobalt from cobalt chloride solution in the membrane electrolytic reactor. Effects of parameters such as catholyte composition, current density and temperature on the current efficiency, specific power consumption and quality of deposition were studied. The catholyte was a mixed solution of cobalt chloride, the initial middle electrolyte consisted of diluted hydrochloric acid, and the anolyte was sulfuric acid. An anion exchange membrane separated the catholyte from the middle electrolyte, and a cation exchange membrane separated the anolyte from the middle electrolyte. The results showed that a maximum current efficiency of 97.5% was attained under the optimum experimental condition of an catholyte composition of 80 g/L Co^2+, 20 g/L H3BO3, 3 g/L NaF and pH of 4, at a cathode current density of 250 A/m2 and a temperature of 50 ℃ HCl could be produced in the middle compartment electrochemically up to 0.45 mol/L. 展开更多
关键词 COBALT ELECTRODEPOSITION anion exchange membrane cation exchange membrane membrane electrolytic reactor
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Electrodeposition conditions of metallic nickel in electrolytic membrane reactor 被引量:10
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作者 任秀莲 魏琦峰 +1 位作者 刘喆 刘军 《Transactions of Nonferrous Metals Society of China》 SCIE EI CAS CSCD 2012年第2期467-475,共9页
The process parameters were optimized for the eleetrodeposition of nickel in an electrolytic membrane reactor. Nickel(Ⅱ) and boric acid concentrations, pH and temperature were varied to evaluate the changes in curr... The process parameters were optimized for the eleetrodeposition of nickel in an electrolytic membrane reactor. Nickel(Ⅱ) and boric acid concentrations, pH and temperature were varied to evaluate the changes in current efficiency and specific energy consumption of nickel electrodeposition. The catholyte was aqueous nickel(Ⅱ) sulfate and boric acid, and the anolyte was sulfuric acid solution. An anionic membrane separated the anolyte from the catholyte while maintained a conductive path between the two compartments. The results indicated that the cathode current efficiency increased with the increase of nickel concentration, pH and boric acid concentration, and decreased with the increase of current density and stirring rate. A maximum current efficiency of 97.15% was obtained under the optimized conditions of electrolyte composition of 40 g/L Ni and 40 g/L boric acid at temperature of 42 ℃ and pH of 6 with a cathode current density of 300 A/m2. 展开更多
关键词 NICKEL eleetrodeposition anion-exchange membrane electrolytic membrane reactor
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