Hydrogenation of Dicyclopentadiene in the Presence of a Nickel Catalyst Supported onto a Cation Exchanger in a Flow-Type Reactor


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Abstract

The process of dicyclopentadiene hydrogenation in the gas–liquid–solid catalyst system with a catalyst of nickel nanoparticles supported onto a Purolite CT-175 cation exchange resin was studied. The surface structure of the catalyst and the kinetics of the dicyclopentadiene hydrogenation process were examined. Optimum conditions were found for the production of endo-tetrahydrodicyclopentadiene and the simultaneous production of endo-tetrahydrodicyclopentadiene and 5,6-dihydrodicyclopentadiene at atmospheric pressure.

About the authors

Yu. V. Popov

Volgograd State Technical University

Author for correspondence.
Email: tons@vstu.ru
Russian Federation, Volgograd, 400131

V. M. Mokhov

Volgograd State Technical University

Email: tons@vstu.ru
Russian Federation, Volgograd, 400131

D. N. Nebykov

Volgograd State Technical University

Email: tons@vstu.ru
Russian Federation, Volgograd, 400131

S. E. Latyshova

Volgograd State Technical University

Email: tons@vstu.ru
Russian Federation, Volgograd, 400131

K. V. Shcherbakova

Volgograd State Technical University

Email: tons@vstu.ru
Russian Federation, Volgograd, 400131

A. O. Panov

Volgograd State Technical University

Email: tons@vstu.ru
Russian Federation, Volgograd, 400131

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