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Energy & Fuels | 自重构 Fe / 活性炭催化剂助力甲酸脱氢反应:高效能与可持续性的结合

Carbon Research  · 公众号  ·  · 2024-10-30 07:55

主要观点总结

本文介绍了一种新型自重构和可循环使用的Fe/活性炭催化剂(ACox@ImFe)在甲酸脱氢反应中的应用。该催化剂具有高效的催化性能,能够在多次循环中保持高转化次数(TON)和高催化速率(TOFs),并展现出良好的耐用性和可重复使用性。通过光谱和显微技术对催化剂的结构变化进行了详细分析,发现其与催化剂的疏水性和结构特性的改善密切相关。

关键观点总结

关键观点1: 新型Fe/活性炭催化剂的开发

研究人员基于碳材料开发了一种新型催化剂ACox@ImFe,该催化剂结合了铁(Fe2+)金属中心和通过硅氧键合链接的咪唑,具有创新的混合结构。

关键观点2: 催化剂的卓越性能

ACox@ImFe催化剂在甲酸脱氢反应中展现出显著的催化效率,累计气体生产量达44.2升,并且在每次使用中活动均有所增强,显示出其保持高催化效率的能力。

关键观点3: 催化剂的结构变化和耐久性

尽管观察到了催化位点的聚集和基质重构等结构变化,ACox@ImFe催化剂的性能仍未减弱。这些变化与催化剂的疏水性和结构特性的改善密切相关,显著增强了催化剂在水中的耐久性。

关键观点4: 催化剂的应用前景

ACox@ImFe催化剂在可持续氢气生产中展现出巨大潜力,其自重构能力和结构变化对于可再生能源技术的长效稳定性和成本效益至关重要。


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自重构 Fe / 活性炭催化剂助力甲酸脱氢反应:高效能与可持续性的结合

Formic Acid Dehydrogenation over a Recyclable and Self-Reconstructing Fe/Activated Carbon Catalyst



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索引

Formic Acid Dehydrogenation over a Recyclable and Self-Reconstructing Fe/Activated Carbon Catalyst. Christos Gkatziouras, Maria Solakidou, and Maria Louloudi. Energy & Fuels 2024 38 (18), 17914-17926, DOI: 10.1021/acs.energyfuels.4c03191



下载PDF文件(仅供学术交流)

Formic Acid Dehydrogenation over a Recyclable and Self-Reconstructing Fe-Activated Carbon Catalyst.pdf



文章摘要

近日, 希腊伊奥尼纳大学化学系仿生催化与混合材料实验室研究 人员通过在碳表面以硅氧键合的方式合成了一种新型催化剂,命名为ACox@ImFe。该催化剂采用基质活化氧化碳(ACox)作为载体,结合了以[Fe2+-咪唑]为基础的复合物,这一创新型混合结构在碳基质中成功实现了高效的化学反应。该催化系统在多齿膦的存在下,展现出显著的催化效率,循环转化次数(TON)达到428,880,并有效分解了53毫升的甲酸(FA)进行8个循环。这一持久的性能凸显了催化剂的有效性、稳定性和耐久性,累计产生氢气22.1升,进一步证实了其在可持续氢气生产中的潜力。

该研究由参与者进行的结构分析使用了拉曼光谱、傅里叶变换红外光谱(FT-IR)、扫描电子显微镜(SEM)和电子顺磁共振(EPR)光谱等多个手段,揭示了使用后催化剂与原始材料相比的结构变化。尽管观察到了铁位点聚集和基质重构等结构变化,催化剂在每次重复使用中均保持高效率,表现出活性增强的趋势。研究人员确认,基于碳的自由基的稳定性是催化剂持续性能的关键。

值得注意的是,在多次使用后,催化剂经历了一种自重构过程,这与催化剂的疏水性和整体结构的变化有关,从而增强了其耐水性和性能表现。总的来说,研究结果表明,ACox@ImFe是一种强大而有效的催化系统,具有可持续氢气生产的广阔前景。这项研究由XXX研究机构进行,为碳材料的催化应用提供了新的思路及方向。



要点图例

Abstract


Scheme 1. Schematic Illustration of the Synthesis and Functionalization of AC ox @ImFe a


a The carbon matrix (AC), oxidation of AC to form AC ox , ligand functionalization, and metal grafting to form AC ox @ImFe are Shown. Insets include Raman spectra (D and G bands) after the 8th use, Fourier transform infrared spectroscopy (FT-IR) spectra showing characteristic peaks, SEM image showing the morphology, and the EPR spectrum of the catalyst.


Figure 1. (a) Gas production ( V H 2 +CO 2 ) following successive additions of FA, catalyzed by the AC ox @ImFe/PP 3 system vs the control system [AC ox /Fe 2+ /PP 3 ]. (b) Mapping of the redox potential ( E h vs standard hydrogen electrode, SHE) across various stages of the reaction for the catalytic system AC ox @ImFe/PP 3 and the control system [AC ox /Fe 2+ /PP 3 ].


Figure 2. (a) Recyclability of the AC ox @ImFe/PP 3 system for the dehydrogenation of FA (data for all of the reuses are shown in Figure S3a ). (b) Reaction time evolution of E h vs SHE for the [AC ox @ImFe/PP 3 /FA] solution. (c) Arrhenius plot demonstrating E a reduction for the catalytic reaction in the 1st, 2nd, and 3rd uses.



Figure 3. (a) Average rates of all uses of the AC ox @ImFe/PP 3 catalytic system for the dehydrogenation of FA. (b) TONs and TOFs through consecutive uses. Conditions: [AC ox @ImFe] = 15 μmol, [PP 3 ] = 7.5 μmol, 7 mL mixture of PC+FA (5/2, ν/ν), T = 80 °C (±1), along with continuous addition of FA.


Figure 4. Raman spectra of [AC ox @ImFe] (a) before 1st use and (b) after 8th use.


Figure 5. FT-IR spectra of [AC ox @ImFe/PP 3 ] (a) before 1st use and (b) after the 8th use.


Figure 6. SEM images of (a) AC ox , (b) pristine AC ox @ImFe, and (c) [AC ox @ImFe] after the 8th use.


Figure 7. EPR spectra for [AC ox @ImFe] before 1st use and after the 8th use. Experimental conditions: T = 77 K, microwave frequency, 9.49 GHz, modulation amplitude, 10 Gpp, and microwave power, 32 mW.


Figure 8. (a) Catalyst resistance in water accumulation vs TONs normalized upon consecutive uses of catalyst. (b) Anticorrelation between accumulated water and the mass of catalyst. (c) Schematic illustration showing the evolution of the material’s hydrophilicity and water sensitivity over repeated uses. On the left, during the first use, the material is more sensitive to water (H 2 O) due to its higher hydrophilicity. Over time and with continued use (by the eighth use), the material becomes less hydrophilic and more resilient to water exposure, indicating an improvement in its water resistance properties. The molecular structural modifications associated with this transition are also depicted, highlighting the chemical changes that occur within the material.



文章结论

研究人员开发了一种新型催化剂ACox@ImFe,该催化剂基于基质活化氧化碳(ACox),结合了铁(Fe2+)金属中心和通过硅氧键合链接的咪唑。 此催化剂具有创新的混合结构,能够在氧化碳基质中实现高转化次数(TONs)和高催化速率(TOFs),并在多个循环中展现出卓越的耐用性和可重复使用性。 研究表明,该催化剂在8个循环内实现了累计气体生产量达44.2升,并且在每次使用中活动均有所增强,显示出其保持高催化效率的能力。

尽管观察到了催化位点的聚集和基质重构等结构变化,催化剂的性能仍未减弱。这些变化通过先进的光谱和显微技术进行了详细分析,发现其与催化剂的疏水性和结构特性的改善密切相关,显著增强了催化剂在水中的耐久性。这种持久性赋予催化剂更高的性能输出,显示出ACox@ImFe在可持续氢气生产中的巨大潜力。

另外,通过多次循环的适应性和提升的性能,对于可再生能源技术中的长效稳定性及成本效益至关重要。此次研究不仅推动了氢气生产催化材料的知识发展,也强调了基于碳材料的非贵金属催化剂的潜力,为寻求环保且经济高效的传统贵金属催化剂替代品提供了新思路。这些发现对提高FADH催化的效率和耐久性具有重要意义,为未来的催化剂开发指明了方向。


复制浏览以下链接, 进入投审稿系统

https://www.springer.com/journal/44246

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