Preparation and characterization of Ni/Al2O3 catalyst for catalytic reduction of CO2 to formic acid in the presence of hydrazine hydrate as a hydrogen source

Rajeev Ranjan, Prakash Biswas
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Abstract

In this study, the catalytic reduction of CO2 into formic acid was investigated over a Ni/Al2O3 catalyst synthesized by wet-impregnation technique. The CO2 hydrogenation reaction was performed in a slurry reactor in the temperature range of 100–300 °C and at an autogenerated pressure. The Na2CO3 was used as a CO2 source, and hydrazine hydrate was used as a hydrogen source. The effect of reaction temperature, catalyst metal loading (5–15 wt%), and catalyst amount were optimized for the higher yield of formic acid. The catalyst was very selective to formic acid, and a very high formic acid selectivity of ∼99 % was achieved in the presence of 10 wt% Ni/Al2O3 catalyst at a much lower reaction temperature of 250 °C. The obtained formic acid yield was ∼53.5 %. The result demonstrated that the Ni/Al2O3 catalyst developed was very promising for the selective hydrogenation of CO2 molecules to formic acid via the in situ hydrogenation from hydrazine hydrate.
以水合肼为氢源催化 CO2 还原成甲酸的 Ni/Al2O3 催化剂的制备与表征
本研究考察了通过湿法浸渍技术合成的 Ni/Al2O3 催化剂催化二氧化碳还原成甲酸的过程。二氧化碳加氢反应在浆料反应器中进行,温度范围为 100-300 °C,压力为自生压力。Na2CO3 用作二氧化碳源,水合肼用作氢源。为了获得更高的甲酸产量,对反应温度、催化剂金属负载量(5-15 wt%)和催化剂用量的影响进行了优化。催化剂对甲酸的选择性非常高,在 10 wt% Ni/Al2O3 催化剂存在下,反应温度更低,为 250 ℃,甲酸选择性高达 ∼ 99 %。甲酸产量为 53.5%。结果表明,所开发的 Ni/Al2O3 催化剂在通过水合肼原位氢化将 CO2 分子选择性氢化为甲酸方面具有很好的前景。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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