Hydrogen generation from hydrous hydrazine over Rh/g-C3N4 nanocatalysts
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摘要: 本研究将三聚氰胺在静态空气中焙烧合成的g-C3N4作为载体,通过简单的浸渍还原法将Rh纳米粒子负载在g-C3N4载体上制备出Rh/g-C3N4催化剂。采用多种表征方法对催化剂的微观结构、组成成分进行研究。此外,还研究了反应温度和NaOH浓度对催化剂催化水合肼分解的影响。研究结果表明,催化剂优异的催化活性源于g-C3N4载体为金属Rh提供了锚定位点,并且载体和金属之间存在强相互作用。催化剂的催化活性随着反应温度的升高而不断提升,当NaOH浓度为0.75 mol/L时Rh/g-C3N4催化剂具有最高的催化活性。Rh/g-C3N4催化剂催化水合肼分解制氢的活化能为30.7 kJ/mol,TOF值为1466.4 h−1,在经过五次循环后,催化剂依旧保持着较好的催化活性,表明催化剂具有良好的循环稳定性。Abstract: In this paper, g-C3N4 obtained by calcining melamine at high temperature in static air was used as the carrier, and the precious metal Rh was used as the active component. The Rh nanoparticles were supported on the g-C3N4 support by a simple impregnation reduction method to prepare high activity and high selectivity. Various characterization methods were used to study the microstructure and composition of the catalyst. In addition, the effect of reaction temperature and NaOH concentration on the catalytic decomposition of hydrous hydrazine was also investigated. The results show that the excellent catalytic activity of the catalyst stems from the fact that the g-C3N4 support provides anchor sites for the metal Rh and the support and the strong metal-support interactions. The catalytic activity of the catalyst increases with the increase of the reaction temperature, and the Rh/g-C3N4 catalyst has the highest catalytic activity when the NaOH concentration is 0.75 mol/L. The Rh/g-C3N4 catalyst has an activation energy of 30.7 kJ/mol and TOF value of 1466.4 h−1 for catalyzing the decomposition of hydrous hydrazine for hydrogen production. After 5 cycles, the catalyst still maintains a good catalytic activity, indicating that the catalyst has a good cyclic stability.
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Key words:
- hydrous hydrazine /
- g-C3N4 /
- rhodium /
- dehydrogenation
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图 5 (a) 343 K下Rh/g-C3N4在不同浓度的碱溶液中催化水合肼分解产生的气体;(b) 343 K下不同NaOH浓度反应对应的TOF值;(c) 不同温度下Rh/g-C3N4上水合肼分解生成气体与时间的关系;(d) Rh/g-C3N4催化剂催化水合肼分解阿伦尼乌斯曲线
Figure 5 (a) Plots equivalent produced by dehydrogenation of hydrous hydrazine catalyzed by Rh/g-C3N4 in alkaline solutions with different concentrations at 343 K; (b) TOF values corresponding to different NaOH concentration reactions at 343 K; (c) Relationship between volume and time of gas generated by hydrous hydrazine dehydrogenation at Rh/g-C3N4 at different temperatures; (d) Arrhenius diagram of dehydrogenation of hydrous hydrazine catalyzed by Rh/g-C3N4 catalyst
表 1 Rh/g-C3N4催化剂的ICP-AES测试
Table 1 ICP-AES results of Rh/g-C3N4 catalyst
Catalyst Rh w/% Final metals/catalyst
(mmol·(100 mg)−1)Rh/g-C3N4 12.37 0.137 表 2 不同催化剂在水合肼产氢中的性能
Table 2 Comparison performance of different catalysts for dehydrogenation of hydrous hydrazine
Catalyst T/K TOF/ h−1 Ea/ (kJ·mol−1) Ref. Rh/g-C3N4 323 1466.4 30.7 This work Rh55Ni45/Ce(OH)CO3 323 395 38.8 [19] Rh4Ni1@RGO 298 20.1 − [24] Rh4Ni 298 6 − [33] Ni0.90Pt0.05Rh0.05/La2O3 298 66.7 − [34] Ni66Rh34@ZIF-8 323 140 58.1 [35] Rh47Ni18P35@MOF-74 323 715.4 49.39 [21] Ni37Pt63/g-C3N4 323 570 36.6 [29] Ni0.4Pt0.6/CNTs 323 1725.3 36.3 [36] Pt0.6Ni0.4/(MnOx)2-C3N4 323 2749 48.7 [37] -
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