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Copper Hydrotalcite(Cu-HT)as an Efficient Catalyst for the Hydrogena-tion of CO2 to Formic Acid

机译:铜水滑石(Cu-HT)作为氢化二氧化碳的氢化的有效催化剂

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Hydrogenation of CO2 to energy-rich products over heterogeneous metal catalysts has gained much attention due to their commercial applications.Specifically,the first-row transition metal catalysts are very rarely reported and discussed for the production of formic acid from the hydrogenation of CO2.Herein,hydrotalcite supported copper metal has shown activity and efficiency to produce formic acid from the hydrogenation of CO2,without adding any additional base or promoter and was effectively recycled 4 times after separating by simple filtration without compromising the formic acid yield.Hydrotalcite supported copper-based catalyst(Cu-HT)was synthesized through the co-precipitation method and used as a heterogeneous catalyst for the hydrogenation of CO2.The precise copper metal content determined by ICP in Cu-HT is 0.00944 mmol.The catalyst afforded maximum TOF,124 h~(-1)under the employed reaction conditions:100 mg catalyst,60 °C,60 bar total pressure of CO2/H2(1:1,p/p)with 60 mL of mixed methanol:water(5:1,v/v)solvent.Cu-HT catalyst was synthe-sised and thoroughly characterized by FT-IR,PXRD,SEM,TEM,XPS and BET surface area.The first-order kinetic dependence with respect to the catalyst amount,partial pressures of CO2j and of H2 was observed and a plausible reaction mechanism is suggested.Background:CO2 hydrogenation to energy-rich products over heterogeneous metal catalysts has gained much attention due to their commercial applications.Specifically,the first-row transition metal catalysts are very rarely reported and discussed for the production of formic acid from the hydrogenation of CO2.Objective:The aim is to investigate the heterogeneous catalyst systems,using solid soft base hydrotalcite supported Cu metal-based catalyst for effective and selective hydrogenation of CO2 to formic acid.Methods:The Cu-HT catalyst was synthesized and characterized by FT-IR,PXRD,SEM,TEM,XPS and BET surface area in which the precise copper content was 0.00944 mmol.The Cu-HT catalysed hydrogenation of CO2 was carried out in the autoclave.Results:The Cu-HT catalyst afforded maximum TOF of 124 h~(-1)under the employed reaction conditions:100 mg catalyst,60 °C,60 bar total pressure of CO2/H2(1:1,p/p)with 60 mL of mixed methanol:water(5:1,v/v)solvent,without adding any additional base or promoter and was recycled 4 times by simple filtration without compromising the formic acid yield.Formation of formic acid was observed to depend on the amount of the catalyst,partial pressures of CO2 and H2,total pressure,temperature and time.Conclusion:Cu-HT based heterogeneous catalyst was found to be efficient for selective hydrogenation of CO2 to formic acid and was effectively recycled four times after elegantly separating by simple filtration.
机译:由于其商业应用,二氧化碳与富含能量富含能量的产物的氢化。特殊地,非常罕见地报告了第一行过渡金属催化剂并讨论了来自CO2的氢化的甲酸的生产,水滑石支撑的铜金属表明了从CO 2的氢化产生甲酸的活性和效率,而不加入任何另外的基础或启动子,并且在通过简单过滤分离后有效地再循环4次,而不损害甲酸产率。支持铜基通过共沉淀法合成催化剂(Cu-HT)并用作二氧化碳氢化的异质催化剂。通过ICP在Cu-HT中测定的精确铜金属含量为0.00944mmol。催化剂得到最大TOF,124小时〜(-1)在所用的反应条件下:100mg催化剂,60℃,60巴的CO 2 / H 2(1:1,P / P)的总压力为60ml m Ixed甲醇:水(5:1,v / v)溶剂。Cu-Ht催化剂被用于FT-IR,PXRD,SEM,TEM,XPS和BET表面积的彻底表征。一阶动力学依赖关于催化剂量,观察到CO2J和H 2的部分压力,并提出了合理的反应机理。背景:由于其商业应用,非均相金属催化剂的富含能量富含能量的产物的CO 2氢化。特殊,首先 - 从CO 2的氢化产生过渡金属催化剂并讨论甲酸的生产。目的是研究异质催化剂体系,采用固体软基水滑型催化剂,支持Cu金属基催化剂的有效和选择性CO 2的氢化至甲酸。方法:Cu-HT催化剂合成,其特征在于FT-IR,PXRD,SEM,TEM,XPS和BET表面积,其中精确的铜含量为0.00944mmol。CU-HT Catal CO 2的YSED氢化在高压釜中进行。结果:Cu-HT催化剂在所用反应条件下提供124小时〜(-1)的最大TOF:100mg催化剂,60℃,60巴的CO 2 / H 2(1:1,p / p),具有60ml混合甲醇:水(5:1,v / v)溶剂,无需添加任何另外的碱或促进剂,并且通过简单的过滤再循环4次,而不会损害甲酸产率。观察到甲酸的形成,取决于催化剂的量,CO 2和H 2的部分压力,总压力,温度和时间。结论:Cu-HT基的非均相催化剂是有效的CO 2对甲酸的选择性氢化通过简单过滤优雅分离,酸性和有效地再循环四次。

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