Hydrogenation of Dicyclopentadiene in the Presence of a Nickel Catalyst Supported onto a Cation Exchanger in a Flow-Type Reactor
- Authors: Popov Y.V.1, Mokhov V.M.1, Nebykov D.N.1, Latyshova S.E.1, Shcherbakova K.V.1, Panov A.O.1
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Affiliations:
- Volgograd State Technical University
- Issue: Vol 59, No 4 (2018)
- Pages: 444-449
- Section: Article
- URL: https://journal-vniispk.ru/0023-1584/article/view/163910
- DOI: https://doi.org/10.1134/S0023158418040109
- ID: 163910
Cite item
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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