Photocatalytic hydrogen production using Me/Cd0.3Zn0.7S (Me = Au, Pt, Pd) catalysts: Transformation of the metallic catalyst under the action of the reaction medium
- 作者: Kozlova E.A.1,2, Kurenkova A.Y.1,2, Kolinko P.A.1,2, Saraev A.A.1,2, Gerasimov E.Y.1,2, Kozlov D.V.1,2
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隶属关系:
- Boreskov Institute of Catalysis, Siberian Branch
- Novosibirsk State University
- 期: 卷 58, 编号 4 (2017)
- 页面: 431-440
- 栏目: Article
- URL: https://journals.rcsi.science/0023-1584/article/view/163145
- DOI: https://doi.org/10.1134/S0023158417040097
- ID: 163145
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详细
The activity and stability of Me/Cd0.3Zn0.7S (Me = Au, Pt, Pd) photocatalysts in the course of hydrogen production from water under the action of visible radiation have been investigated. The mechanism of activation and deactivation of the catalysts have been elucidated for the first time using X-ray diffraction, transmission electron microscopy, and X-ray photoelectron spectroscopy. An increase in the hydrogen evolution rate is observed for all of the catalysts at the early stages of testing. The highest hydrogen evolution rate, 5.4 μmol/min, is afforded by the 1%Pt/Cd0.3Zn0.7S catalyst. The activity of the Au/Cd0.3Zn0.7S and Pt/Cd0.3Zn0.7S catalysts becomes constant 7.5–9 h after the beginning of the photocatalytic test, while in the case of Pd/Cd0.3Zn0.7S the hydrogen evolution rate increases over the initial 6 h and then decreases. These specific features of the catalysts likely correlate with the initial state of the metals on the support surface. In particular, supported palladium is in the form of PdO, while gold and platinum are in the metallic state. The Au/Cd0.3Zn0.7S and Pt/Cd0.3Zn0.7S photocatalysts are activated due to metal encapsulation; the 1%Pd/Cd0.3Zn0.7S catalyst, due to the partial reduction of PdO to PdOx. The 1%Pd/Cd0.3Zn0.7S catalyst is deactivated because of the aggregation of nanoparticles of the cadmium sulfide–zinc sulfide solid solution.
作者简介
E. Kozlova
Boreskov Institute of Catalysis, Siberian Branch; Novosibirsk State University
编辑信件的主要联系方式.
Email: kozlova@catalysis.ru
俄罗斯联邦, Novosibirsk, 630090; Novosibirsk, 630090
A. Kurenkova
Boreskov Institute of Catalysis, Siberian Branch; Novosibirsk State University
Email: kozlova@catalysis.ru
俄罗斯联邦, Novosibirsk, 630090; Novosibirsk, 630090
P. Kolinko
Boreskov Institute of Catalysis, Siberian Branch; Novosibirsk State University
Email: kozlova@catalysis.ru
俄罗斯联邦, Novosibirsk, 630090; Novosibirsk, 630090
A. Saraev
Boreskov Institute of Catalysis, Siberian Branch; Novosibirsk State University
Email: kozlova@catalysis.ru
俄罗斯联邦, Novosibirsk, 630090; Novosibirsk, 630090
E. Gerasimov
Boreskov Institute of Catalysis, Siberian Branch; Novosibirsk State University
Email: kozlova@catalysis.ru
俄罗斯联邦, Novosibirsk, 630090; Novosibirsk, 630090
D. Kozlov
Boreskov Institute of Catalysis, Siberian Branch; Novosibirsk State University
Email: kozlova@catalysis.ru
俄罗斯联邦, Novosibirsk, 630090; Novosibirsk, 630090
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