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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

Postal Subscription Code 80-969

2018 Impact Factor: 2.809

Front. Chem. Sci. Eng.    2022, Vol. 16 Issue (8) : 1211-1223    https://doi.org/10.1007/s11705-022-2145-3
RESEARCH ARTICLE
Ultrasound-assisted co-precipitation synthesis of mesoporous Co3O4–CeO2 composite oxides for highly selective catalytic oxidation of cyclohexane
Shangjun Fu1, Kuiyi You1,2(), Zhenpan Chen1(), Taobo Liu1, Qiong Wang1, Fangfang Zhao1, Qiuhong Ai1,2, Pingle Liu1,2, He’an Luo1,2
1. School of Chemical Engineering, Xiangtan University, Xiangtan 411105, China
2. National & Local United Engineering Research Center for Chemical Process Simulation and Intensification, Xiangtan University, Xiangtan 411105, China
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Abstract

The one-step highly selective oxidation of cyclohexane into cyclohexanone and cyclohexanol as the essential intermediates of nylon-6 and nylon-66 is considerably challenging. Therefore, an efficient and low-cost catalyst must be urgently developed to improve the efficiency of this process. In this study, a Co3O4–CeO2 composite oxide catalyst was successfully prepared through ultrasound-assisted co-precipitation. This catalyst exhibited a higher selectivity to KA-oil, which was benefited from the synergistic effects between Co3+/Co2+ and Ce4+/Ce3+ redox pairs, than bulk CeO2 and/or Co3O4. Under the optimum reaction conditions, 89.6% selectivity to KA-oil with a cyclohexane conversion of 5.8% was achieved over Co3O4–CeO2. Its catalytic performance remained unchanged after five runs. Using the synergistic effects between the redox pairs of different transition metals, this study provides a feasible strategy to design high-performance catalysts for the selective oxidation of alkanes.

Keywords Co3O4–CeO2 composite oxides      cyclohexanone      cyclohexanol      ultrasonic-assisted co-precipitation      selective oxidation      solvent-free     
Corresponding Author(s): Kuiyi You,Zhenpan Chen   
Online First Date: 24 April 2022    Issue Date: 02 August 2022
 Cite this article:   
Shangjun Fu,Kuiyi You,Zhenpan Chen, et al. Ultrasound-assisted co-precipitation synthesis of mesoporous Co3O4–CeO2 composite oxides for highly selective catalytic oxidation of cyclohexane[J]. Front. Chem. Sci. Eng., 2022, 16(8): 1211-1223.
 URL:  
https://academic.hep.com.cn/fcse/EN/10.1007/s11705-022-2145-3
https://academic.hep.com.cn/fcse/EN/Y2022/V16/I8/1211
Entry Catalyst Conversion/% Selectivity/%b)
A K KA-oil CHHP Acid Ester
1 None 2.3 15.2 27.7 42.9 55.8 1.0 0.3
2 CeO2 c) 5.3 47.9 25.9 73.8 13.9 7.9 4.3
3 Co3O4 d) 7.5 39.8 28.9 68.7 2.3 9.6 19.4
4 Co3O4 e) 5.8 53.6 24.5 78.1 4.9 7.3 9.7
5 NiO–CeO2 6.6 44.3 29.8 74.1 10.7 7.0 8.3
6 Fe2O3–CeO2 6.4 38.4 24.0 62.9 22.6 6.2 8.2
7 MnO2–CeO2 6.5 48.2 27.4 75.6 9.5 6.9 7.9
8 Al2O3–Co3O4 6.6 39.6 23.0 62.6 23.0 6.8 7.5
9 MoO3–Co3O4 5.6 31.4 38.9 70.3 5.2 14.7 9.8
10 Co3O4–CeO2 5.8 60.2 29.4 89.6 0 5.7 4.7
11 Co3O4–CeO2 f) 5.9 54.5 28.4 82.9 0.1 7.2 9.9
12 Co3O4+CeO2 g) 6.4 46.6 24.1 70.7 14.3 6.7 8.3
13 Co3O4+CeO2 h) 4.5 44.2 17.5 61.7 23.9 7.9 6.5
14 Co3O4–CeO2 i) 1.7 38.3 23.8 62.1 0 10.3 27.5
15 Co3O4–CeO2 j) 5.9 53.1 35.1 88.2 0 6.4 5.4
Tab.1  Catalytic properties of different catalysts a)
Entry Ce/Co (molar ratio) Conversion/% Selectivity/%
A K KA-oil CHHP Acid Ester
1 1∶5 6.0 57.6 27.7 85.3 1.8 6.8 6.2
2 1∶2 5.7 54.6 30.3 84.9 1.5 8.7 4.9
3 1∶1 5.5 59.3 25.7 85.0 2.7 7.0 5.3
4 2∶1 5.8 60.2 29.4 89.6 0 5.7 4.7
5 4∶1 6.0 54.1 32.6 86.7 0.5 6.7 6.1
6 b) 1∶5 7.2 49.4 33.4 82.8 0.8 7.3 9.1
7 b) 1∶2 7.5 52.2 29.1 81.3 0.7 7.5 10.5
8 b) 1∶1 7.8 54.4 29.0 83.4 1.6 8.1 7.0
9 b) 2∶1 7.2 54.0 31.1 85.1 0 6.4 8.0
10 b) 4∶1 7.6 50.2 33.3 83.5 0 6.0 10.4
Tab.2  Effects of Ce/Co molar ratio on the oxidation reaction a)
Fig.1  Results of selective aerobic oxidation of cyclohexane under different reaction conditions: (a) 60 g cyclohexane, 0.1 g Co3O4–CeO2 catalyst (Ce/Co = 2∶1), 150 °C, 1.5 h; (b) 60 g cyclohexane, 0.1 g Co3O4–CeO2 catalyst (Ce/Co = 2∶1), 150 °C, 0.6 MPa; (c) 60 g cyclohexane, 0.1 g Co3O4–CeO2 catalyst (Ce/Co = 2∶1), 0.6 MPa, 1.5 h; (d) 60 g cyclohexane, 0.6 MPa, 150 °C, 0.6 MPa, 1.5 h.
Fig.2  Cyclic performance of Co3O4–CeO2 catalyst used in selective oxidation of cyclohexane. Reaction conditions: 60 g cyclohexane, 0.1 g Co3O4–CeO2 catalyst (Ce/Co = 2∶1), 150 °C, 0.6 MPa and 1.5 h.
Fig.3  XRD profiles of (a) Co3O4, (b) CeO2, (c) fresh, and (d) used Co3O4–CeO2 catalysts. Crystalline phases detected: (♦) Co3O4, (●) CeO2.
Fig.4  The 532 nm Raman spectra of (a) Co3O4, (b) CeO2, (c) fresh and (d) used Co3O4–CeO2 catalysts. The enlarged image in the inset shows the appearance of oxygen vacancy (defect oxygen) for the Co3O4–CeO2 catalyst.
Fig.5  XPS spectra of (a, d) Co 2p, (b, e) Ce 3d, and (c, f) O 1s of fresh and used Co3O4–CeO2 samples (OC: chemisorbed oxygen; OV: oxygen vacancy; OL: lattice oxygen).
Sample Ce 3d binding energy/eV Contents of Ce species a)
V U V' U' V'' U'' V''' U''' Ce3+ Ce4+
Fresh sample 882.4 900.8 885.7 904.1 888.8 907.1 898.4 916.5 26.0 74.0
Used sample 882.2 900.6 885.5 903.9 888.8 907.1 898.1 916.5 25.7 74.3
Tab.3  The Ce 3d binding energies and contents of Ce3+ or Ce4+ species for fresh and used Co3O4–CeO2 samples
Sample O 1s binding energy/eV Percentages of different oxygen species a)
OL OV OC OL OV OC
Fresh sample 529.2 531.2 532.3 65.4 19.5 15.1
Used sample 529.2 531.2 532.3 46.8 27.0 26.2
Tab.4  The O 1s binding energies and contents of OL, OV or OC species for fresh and used Co3O4–CeO2 samples.
Fig.6  EPR characterization of fresh and used Co3O4–CeO2 samples.
Fig.7  H2-TPR characterization of (a) CeO2, (b) Co3O4, (c) fresh Co3O4–CeO2, and (d) used Co3O4–CeO2 catalysts.
Catalysts Ce:Co (mole ratio) Surface area/(cm2?g−1) Pore volume/(cm3?g−1) Pore diameter/nm
Theory ICP-AES
Co3O4 31 0.11 3.77
CeO2 104 0.27 9.72
Fresh Co3O4–CeO2 2:1 2.10:1 145 0.24 6.19
Used Co3O4–CeO2 2:1 2.15:1 131 0.22 6.16
Tab.5  ICP-AES and N2 adsorption-desorption results of different samples
Fig.8  N2 adsorption-desorption isotherm and pore diameter distribution diagram of fresh and used Co3O4–CeO2 samples.
Fig.9  (a) TEM, (b) HRTEM images, and (c) histogram of particle diameter distribution of fresh Co3O4–CeO2 catalyst.
Fig.10  Elemental mapping images and EDS results of fresh Co3O4–CeO2.
Fig.11  Possible mechanism for the synergistic catalytic oxidation of cyclohexane to KA-oil with molecular oxygen over Co3O4–CeO2 composite oxides: (a) oxygen activation, (b) formation of CHHP, and (c) decomposition/reduction of CHHP.
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