Email this article Modeling of carbonaceous feedstock pyrolysis in a multichannel reactor
- Authors: Bykov V.I.1, Lomakin S.M.1, Tsybenova S.B.1, Varfolomeev S.D.1
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Affiliations:
- Emanuel Institute of Biochemical Physics
- Issue: Vol 470, No 2 (2016)
- Pages: 293-296
- Section: Chemistry
- URL: https://journals.rcsi.science/0012-5008/article/view/153789
- DOI: https://doi.org/10.1134/S0012500816100049
- ID: 153789
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Abstract
A mathematical model of unsteady-state carbonaceous feedstock pyrolysis in a multichannel tubular reactor was proposed. It was shown that the conversion of feedstock being heated at periodically varying temperature can exceed the conversion on heating at constant temperature. The main design parameters of the multichannel reactor were determined.
About the authors
V. I. Bykov
Emanuel Institute of Biochemical Physics
Author for correspondence.
Email: bykov@deom.chph.ras.ru
Russian Federation, ul. Kosygina 4, Moscow, 119991
S. M. Lomakin
Emanuel Institute of Biochemical Physics
Email: bykov@deom.chph.ras.ru
Russian Federation, ul. Kosygina 4, Moscow, 119991
S. B. Tsybenova
Emanuel Institute of Biochemical Physics
Email: bykov@deom.chph.ras.ru
Russian Federation, ul. Kosygina 4, Moscow, 119991
S. D. Varfolomeev
Emanuel Institute of Biochemical Physics
Email: bykov@deom.chph.ras.ru
Russian Federation, ul. Kosygina 4, Moscow, 119991
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