4.7 Article

Influence of Cocatalysts (Ni, Co, and Cu) and Synthesis Method on the Photocatalytic Activity of Exfoliated Graphitic Carbon Nitride for Hydrogen Production

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NANOMATERIALS
卷 12, 期 22, 页码 -

出版社

MDPI
DOI: 10.3390/nano12224006

关键词

graphitic carbon nitride; water splitting; hydrogen production; nickel; cocatalyst deposition

资金

  1. Deutsche Forschungsgemeinschaft (DFG, German Research Foundation) under Germany's Excellence Strategy [EXC 2008/1, 390540038]

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In this study, exfoliated graphitic carbon nitride loaded with non-noble metals was synthesized and tested for hydrogen production. Among the different synthesis methods, the colloidal deposition method showed the best performance for Ni-loaded ex-g-CN with a hydrogen production rate of 43.6 μmol h(-1) g(-1).
Exfoliated graphitic carbon nitride (ex-g-CN) was synthesized and loaded with non-noble metals (Ni, Cu, and Co). The synthesized catalysts were tested for hydrogen production using a 300-W Xe lamp equipped with a 395 nm cutoff filter. A noncommercial double-walled quartz-glass reactor irradiated from the side was used with a 1 g/L catalyst in 20 mL of a 10 vol% triethanolamine aqueous solution. For preliminary screening, the metal-loaded ex-g-CN was synthesized using the incipient wetness impregnation method. The highest hydrogen production was observed on the Ni-loaded ex-g-CN, which was selected to assess the impact of the synthesis method on hydrogen production. Ni-loaded ex-g-CN was synthesized using different synthesis methods: incipient wetness impregnation, colloidal deposition, and precipitation deposition. The catalysts were characterized by X-ray powder diffraction, X-ray photoelectron spectroscopy, nitrogen adsorption using the Brunauer-Emmett-Teller method, and transmission electron microscopy. The Ni-loaded ex-g-CN synthesized using the colloidal method performed best with a hydrogen production rate of 43.6 mu mol h(-1) g(-1). By contrast, the catalysts synthesized using the impregnation and precipitation methods were less active, with 28.2 and 10.1 mu mol h(-1) g(-1), respectively. The hydrogen production performance of the suspended catalyst (440 mu mol m(-2) g(-1)) showed to be superior to that of the corresponding immobilized catalyst (236 mu mol m(-2) g(-1)).

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