One-Pot Synthesis of Secondary Amines from Nitroarenes and Aldehydes on Supported Copper Catalysts in a Flow Reactor: The Effect of the Support
- Authors: Artyukha E.A.1, Nuzhdin A.L.1, Bukhtiyarova G.A.1, Derevyannikova E.A.1, Gerasimov E.Y.1, Gladkii A.Y.1, Bukhtiyarov V.I.1,2
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Affiliations:
- Boreskov Institute of Catalysis, Siberian Branch
- Novosibirsk State University
- Issue: Vol 59, No 5 (2018)
- Pages: 593-600
- Section: Article
- URL: https://journal-vniispk.ru/0023-1584/article/view/164016
- DOI: https://doi.org/10.1134/S0023158418050014
- ID: 164016
Cite item
Abstract
The effect of the support on the properties of copper catalysts supported on γ-Al2O3, SiO2, and TiO2–SiO2 with a ~5 wt % Cu content was studied in the one-pot synthesis of N-heptyl-p-toluidine from p-nitrotoluene and n-heptanal. The catalysts were characterized by elemental analysis, X-ray diffraction analysis, transmission electron microscopy, temperature-programmed reduction, and low-temperature nitrogen adsorption. The reaction was carried out in a flow reactor with the use of molecular hydrogen as a reducing agent. It was established that the nature of the support exerts a profound effect on the yield of the target secondary amine; in this case, 5%Cu/Al2O3 was found the most active catalyst. A combination of high catalyst activity in the hydrogenation of a nitro group to an amino group with the presence of acid sites, which facilitate imine formation as a result of the interaction of n-heptanal with p-toluidine, on the catalyst surface is necessary for reaching the greatest yield of N-heptyl-p-toluidine. The study of reaction mechanism on the 5%Cu/Al2O3 catalyst showed that p-nitrotoluene inhibits the hydrogenation of n-heptanal, and aldehyde hydrogenation into alcohol begins only after the conversion of the major portion of p-nitrotoluene as a result of the selective adsorption of the nitroarene under the conditions of the simultaneous presence of p-nitrotoluene and n-heptanal in the reaction mixture.
About the authors
E. A. Artyukha
Boreskov Institute of Catalysis, Siberian Branch
Email: anuzhdin@catalysis.ru
Russian Federation, Novosibirsk, 630090
A. L. Nuzhdin
Boreskov Institute of Catalysis, Siberian Branch
Author for correspondence.
Email: anuzhdin@catalysis.ru
Russian Federation, Novosibirsk, 630090
G. A. Bukhtiyarova
Boreskov Institute of Catalysis, Siberian Branch
Email: anuzhdin@catalysis.ru
Russian Federation, Novosibirsk, 630090
E. A. Derevyannikova
Boreskov Institute of Catalysis, Siberian Branch
Email: anuzhdin@catalysis.ru
Russian Federation, Novosibirsk, 630090
E. Yu. Gerasimov
Boreskov Institute of Catalysis, Siberian Branch
Email: anuzhdin@catalysis.ru
Russian Federation, Novosibirsk, 630090
A. Yu. Gladkii
Boreskov Institute of Catalysis, Siberian Branch
Email: anuzhdin@catalysis.ru
Russian Federation, Novosibirsk, 630090
V. I. Bukhtiyarov
Boreskov Institute of Catalysis, Siberian Branch; Novosibirsk State University
Email: anuzhdin@catalysis.ru
Russian Federation, Novosibirsk, 630090; Novosibirsk, 630090
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