Abstract
The optimum conditions for the hydrogenation of 2,3-dihydropyran to tetrahydropyran on an industrial nickel-chromium catalyst under flow and periodic conditions were found. A regression model for the process was found. The results of hydrogenation of 2,3-dihydropyran by means of a flow reactor and an autoclave of the Vishnevskii type are compared.
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Translated from Khimiya Geterotsiklicheskikh Soedinenii, No. 4, pp. 469–472, April, 1982.
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Kuplenieks, V.A., Kreile, D.R., Slavinskaya, V.A. et al. Hydrogenation of 2,3-dihydropyran to tetrahydropyran. Chem Heterocycl Compd 18, 351–354 (1982). https://doi.org/10.1007/BF00503549
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DOI: https://doi.org/10.1007/BF00503549