超高镍层状材料LiNi_(0.92)Co_(0.04)Mn_(0.04)O_(2)(简称NCM92)因其具有较高的能量密度和价格优势,已成为锂离子电池重要的正极材料来源之一。然而,由于该材料的界面不稳定和不可逆相变,商业应用面临特别是在高截止电压下快速的容量衰...超高镍层状材料LiNi_(0.92)Co_(0.04)Mn_(0.04)O_(2)(简称NCM92)因其具有较高的能量密度和价格优势,已成为锂离子电池重要的正极材料来源之一。然而,由于该材料的界面不稳定和不可逆相变,商业应用面临特别是在高截止电压下快速的容量衰落和严重的结构退化的问题。本研究设计了一种ZrO_(2)/Li_(2)ZrO_(3)双包覆层改性超高镍单晶正极材料,同时材料表面均匀掺杂有Zr元素,通过双包覆层协同策略显著增强了正极的高压性能和结构稳定性。研究结果表明,ZrO_(2)/Li_(2)ZrO_(3)双包覆层可以有效缓解超高镍正极材料H2-H3相变的不可逆性,提高力学稳定性和界面稳定性,同时表面Zr掺杂进入晶体结构中的TM层与Li位抑制Li/Ni混排并扩宽了晶格间距,ZrO_(2)/Li_(2)ZrO_(3)双包覆层与Zr掺杂改性的材料(NCM92-Zr)展现出优异的电化学性能,在0.5 C(200 mA·g^(-1))电流密度下,2.75~4.4 V电压范围内循环150圈后仍有155.2 mA h g^(-1)的放电比容量,容量保持率高达75.5%。此研究为在高截止电压下超高镍正极的复杂机制和改进的结构稳定性提供了新的思路。展开更多
Solid acid MoO_(3)/ZrO_(2)-TiO_(2)catalysts were prepared by impregnation method,and catalytic hydrolysis of difluorodichloromethane(CFC-12)over the catalyst was studied.The presence of MoO_(3)/ZrO_(2)-TiO_(2)catalyst...Solid acid MoO_(3)/ZrO_(2)-TiO_(2)catalysts were prepared by impregnation method,and catalytic hydrolysis of difluorodichloromethane(CFC-12)over the catalyst was studied.The presence of MoO_(3)/ZrO_(2)-TiO_(2)catalyst in polycrystalline state could be clearly observed by transmission electron microscopy(TEM).Mesopores were detected by N2 adsorption-desorption isotherms which further confirmed the MoO_(3)/ZrO_(2)-TiO_(2)structural characteristics of catalyst.The results of NH_(3)-TPD showed that the calcination temperatures had a great influence on the acidity of the catalyst,and the weak acidic site had a strong catalytic activity for the catalytic hydrolysis of CFC-12.Moreover,ZrO_(2)-TiO_(2)was highly dispersed in the MoO_(3)framework,suggested by powder X-ray diffraction(XRD)and N_(2)adsorption-desorption results.The effects of the catalyst calcination temperatures on the conversion rate of CFC-12 were studied.The effects of catalytic hydrolysis temperatures and water vapor concentration on the catalytic hydrolysis rate of CFC-12 were also studied.The solid acid MoO_(3)/ZrO_(2)-TiO_(2)was calcined at 500℃for 3 h at a catalytic hydrolysis temperature of 400℃and water vapor concentration of 83.18%,and catalytic hydrolysis rate of CFC-12 reached 98.65%.The hydrolysis rate of CFC-12 remained above 65.34%after 30 hours continuous reaction.展开更多
文摘超高镍层状材料LiNi_(0.92)Co_(0.04)Mn_(0.04)O_(2)(简称NCM92)因其具有较高的能量密度和价格优势,已成为锂离子电池重要的正极材料来源之一。然而,由于该材料的界面不稳定和不可逆相变,商业应用面临特别是在高截止电压下快速的容量衰落和严重的结构退化的问题。本研究设计了一种ZrO_(2)/Li_(2)ZrO_(3)双包覆层改性超高镍单晶正极材料,同时材料表面均匀掺杂有Zr元素,通过双包覆层协同策略显著增强了正极的高压性能和结构稳定性。研究结果表明,ZrO_(2)/Li_(2)ZrO_(3)双包覆层可以有效缓解超高镍正极材料H2-H3相变的不可逆性,提高力学稳定性和界面稳定性,同时表面Zr掺杂进入晶体结构中的TM层与Li位抑制Li/Ni混排并扩宽了晶格间距,ZrO_(2)/Li_(2)ZrO_(3)双包覆层与Zr掺杂改性的材料(NCM92-Zr)展现出优异的电化学性能,在0.5 C(200 mA·g^(-1))电流密度下,2.75~4.4 V电压范围内循环150圈后仍有155.2 mA h g^(-1)的放电比容量,容量保持率高达75.5%。此研究为在高截止电压下超高镍正极的复杂机制和改进的结构稳定性提供了新的思路。
基金Funded by the National Natural Science Foundation of China(No.51568068)the Young and Middle-aged Academic and Technical Leaders Reserve Talent Program(No.202105AC160054)。
文摘Solid acid MoO_(3)/ZrO_(2)-TiO_(2)catalysts were prepared by impregnation method,and catalytic hydrolysis of difluorodichloromethane(CFC-12)over the catalyst was studied.The presence of MoO_(3)/ZrO_(2)-TiO_(2)catalyst in polycrystalline state could be clearly observed by transmission electron microscopy(TEM).Mesopores were detected by N2 adsorption-desorption isotherms which further confirmed the MoO_(3)/ZrO_(2)-TiO_(2)structural characteristics of catalyst.The results of NH_(3)-TPD showed that the calcination temperatures had a great influence on the acidity of the catalyst,and the weak acidic site had a strong catalytic activity for the catalytic hydrolysis of CFC-12.Moreover,ZrO_(2)-TiO_(2)was highly dispersed in the MoO_(3)framework,suggested by powder X-ray diffraction(XRD)and N_(2)adsorption-desorption results.The effects of the catalyst calcination temperatures on the conversion rate of CFC-12 were studied.The effects of catalytic hydrolysis temperatures and water vapor concentration on the catalytic hydrolysis rate of CFC-12 were also studied.The solid acid MoO_(3)/ZrO_(2)-TiO_(2)was calcined at 500℃for 3 h at a catalytic hydrolysis temperature of 400℃and water vapor concentration of 83.18%,and catalytic hydrolysis rate of CFC-12 reached 98.65%.The hydrolysis rate of CFC-12 remained above 65.34%after 30 hours continuous reaction.
