TY - JOUR
T1 - Morphological regulation of Pt/CeO2 and its catalytic dehydrogenation of methylcyclohexane in fixed bed reactor
AU - Zhang, Qianlin
AU - Zhang, Zhao
AU - Ma, Yueer
AU - Ren, Wenchen
AU - Dai, Xiaomin
AU - Chang, Hui
AU - Zhu, Xunjin
N1 - This work was financially supported by National Natural Science Foundation of China (22171170, 21703131), Shaanxi Provincial Key R & D Plan (2022GY-279). X. Zhu thanks the financial support from the General Research Fund (HKBU 12304320), NSFC/RGC Joint Research Scheme (N_HKBU213/22) from the Hong Kong Research Grants Council.
Publisher Copyright:
© 2024 Hydrogen Energy Publications LLC.
PY - 2024/9/19
Y1 - 2024/9/19
N2 - A series of Pt/CeO2 compounds with hollow spheres (Pt/CeO2–S), wires (Pt/CeO2–W), and particle (Pt/CeO2–P) morphologies were prepared and further used for catalytic liquid organic hydrogen carrier (LOHC) dehydrogenation. The exposure and distribution of different crystal faces affected the nucleation process of crystals and then formed different microscopic morphologies. Compared with Pt/CeO2–W and Pt/CeO2–P, Pt/CeO2–S showed hollow spherical structures with significantly higher oxygen vacancy concentrations and specific surface areas. These structural differences not only affected platinum (Pt) dispersion, but also affected the activity and stability of the catalyst, thus promoting methylcyclohexane (MCH) conversion. The fixed bed reaction showed that Pt/CeO2–S had excellent catalytic activity, with the MCH conversion rate at 97.7 % and hydrogen release rate of 350.50 mmol/g(Pt)/min, and it still maintained stable activity after 72 h. Under the same conditions, the MCH conversion rates for Pt/CeO2–W and Pt/CeO2–P were only 77.23 % and 32.02 %, respectively. Therefore, through the growth pattern and morphology controls of catalyst supports, this was an effective means for improving the dehydrogenation performance of LOHC.
AB - A series of Pt/CeO2 compounds with hollow spheres (Pt/CeO2–S), wires (Pt/CeO2–W), and particle (Pt/CeO2–P) morphologies were prepared and further used for catalytic liquid organic hydrogen carrier (LOHC) dehydrogenation. The exposure and distribution of different crystal faces affected the nucleation process of crystals and then formed different microscopic morphologies. Compared with Pt/CeO2–W and Pt/CeO2–P, Pt/CeO2–S showed hollow spherical structures with significantly higher oxygen vacancy concentrations and specific surface areas. These structural differences not only affected platinum (Pt) dispersion, but also affected the activity and stability of the catalyst, thus promoting methylcyclohexane (MCH) conversion. The fixed bed reaction showed that Pt/CeO2–S had excellent catalytic activity, with the MCH conversion rate at 97.7 % and hydrogen release rate of 350.50 mmol/g(Pt)/min, and it still maintained stable activity after 72 h. Under the same conditions, the MCH conversion rates for Pt/CeO2–W and Pt/CeO2–P were only 77.23 % and 32.02 %, respectively. Therefore, through the growth pattern and morphology controls of catalyst supports, this was an effective means for improving the dehydrogenation performance of LOHC.
KW - Dehydrogenation
KW - Fixed bed reactor
KW - Growth mechanism
KW - Liquid organic hydrogen carrier
KW - Morphological control of CeO2
UR - http://www.scopus.com/inward/record.url?scp=85201207094&partnerID=8YFLogxK
U2 - 10.1016/j.ijhydene.2024.08.178
DO - 10.1016/j.ijhydene.2024.08.178
M3 - Journal article
AN - SCOPUS:85201207094
SN - 0360-3199
VL - 83
SP - 1338
EP - 1348
JO - International Journal of Hydrogen Energy
JF - International Journal of Hydrogen Energy
ER -