Chinese Journal of Catalysis ›› 2022, Vol. 43 ›› Issue (8): 2034-2044.DOI: 10.1016/S1872-2067(21)64021-4
• Special column on surface & interface chemistry connecting thermo-,photo- and electro-catalysis • Previous Articles Next Articles
Guang Gao,†, Zelun Zhao,†, Jia Wang, Yongjie Xi, Peng Sun(), Fuwei Li(
)
Received:
2021-10-21
Accepted:
2021-11-10
Online:
2022-08-18
Published:
2022-06-20
Contact:
Peng Sun, Fuwei Li
About author:
Prof. Fuwei Li (Lanzhou Institute of Chemical Physics, Chinese Academy of Science) received his B.A. degree from Henan University (P. R. China) in 2000, and Ph.D. degree from Lanzhou Institute of Chemical Physics (LICP), Chinese Academy of Sciences (CAS) in 2005. Then he became a research assistant at the Institute of Process Engineering of CAS, and moved to the Department of Chemistry of the National University of Singapore in 2006 as a postdoctoral fellow. Since 2010, he has been working in State Key Laboratory for Oxo Synthesis and Selective Oxidation in LICP. He is an Excellent Young Scholar Recipient of National Natural Science Foundation of China (2015). His research interests mainly focus on the catalytic conversion of bulk oxygenates, bio-based platform molecules and waste oxygen-containing polymer into value-added oxygenates. He has published more than 100 peer-reviewed papers. He was invited as an associated editor of the 6th Editorial Board of Chin. J. Catal. in 2020.†Contributed equally to this work.
Supported by:
Guang Gao, Zelun Zhao, Jia Wang, Yongjie Xi, Peng Sun, Fuwei Li. Boosting chiral carboxylic acid hydrogenation by tuning metal-MOx-support interaction in Pt-ReOx/TiO2 catalysts[J]. Chinese Journal of Catalysis, 2022, 43(8): 2034-2044.
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URL: https://www.cjcatal.com/EN/10.1016/S1872-2067(21)64021-4
Fig. 1. (a) Reaction pathway for the hydrogenation of CDA to CDM. (b) Catalytic performance of the PtReOx/TiO2 catalysts in a fixed-bed reactor. Reaction conditions: feedstock (5 wt% CDA + 15 wt% EtOH + 80 wt% H2O) flow rate: 0.02 mL min-1, catalyst: 1 g, temperature: 130 °C, H2 pressure: 6 MPa. (c) Initial reaction rate of PtReOx/TiO2 under less than 10% conversion with a feedstock flow rate of 0.25 mL min-1. (d) Arrhenius plots for HB hydrogenation over the PtReOx/TiO2 catalysts obtained at 100, 110, 120, 130, 140, and 150 °C, respectively, with a feedstock rate of 0.25 mL min-1 (other conditions were same as those mentioned for Fig. 1(b)). (e) Stability of the PtReOx/TiO2(R)-catalyzed hydrogenation of CDA.
Fig. 2. STEM images with histogram of size distribution, EDS mapping images, and high-resolution STEM images of PtReOx/TiO2(R) (a-c), PtReOx/TiO2(B) (d-f), and PtReOx/TiO2(A) (g-i).
Sample | Re0/(Reδ++Re0)a (%) | Ti3+/(Ti3++Ti4+) (%) | Ti3+-Vö/ [(Ti3+-Vö) + (Ti4+-O)] (%) | Density of Pt0 b (nm-2) | Density of Re0 c (nm-2) | Density of Vö d (nm-2) |
---|---|---|---|---|---|---|
PtReOx/TiO2(R) | 19 | 22 | 24 | 5.48 | 1.46 | 220 |
PtReOx/TiO2(B) | 13 | 17 | 16 | 2.40 | 0.49 | 64 |
PtReOx/TiO2(A) | 0 | 14 | 14 | 1.13 | 0 | 29 |
Table 1 Deconvolution of the XPS spectra of the PtReOx/TiO2 samples.
Sample | Re0/(Reδ++Re0)a (%) | Ti3+/(Ti3++Ti4+) (%) | Ti3+-Vö/ [(Ti3+-Vö) + (Ti4+-O)] (%) | Density of Pt0 b (nm-2) | Density of Re0 c (nm-2) | Density of Vö d (nm-2) |
---|---|---|---|---|---|---|
PtReOx/TiO2(R) | 19 | 22 | 24 | 5.48 | 1.46 | 220 |
PtReOx/TiO2(B) | 13 | 17 | 16 | 2.40 | 0.49 | 64 |
PtReOx/TiO2(A) | 0 | 14 | 14 | 1.13 | 0 | 29 |
Fig. 4. (a) Spin density map of PtReOx/TiO2 (the calculated magnetic moment of Ti3+ is indicated by arrow). (b) Quasi in situ EPR spectra of bare TiO2 and PtReOx/TiO2 at -150 °C.
Fig. 5. (a) In situ FTIR spectra obtained after CO adsorption and evacuation over the PtReOx/TiO2 catalysts. (b) H2-TPD of the PtReOx/TiO2 catalysts. (c) In situ FTIR spectra of HB adsorption on PtReOx/TiO2. (d) In situ FTIR spectra of HB hydrogenation on PtReOx/TiO2(R) catalyst at 130 °C.
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