Modeling of carbonaceous feedstock pyrolysis in a multichannel reactor
- Авторы: Bykov V.I.1, Lomakin S.M.1, Tsybenova S.B.1, Varfolomeev S.D.1
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Учреждения:
- Emanuel Institute of Biochemical Physics
- Выпуск: Том 470, № 2 (2016)
- Страницы: 293-296
- Раздел: Chemistry
- URL: https://journals.rcsi.science/0012-5008/article/view/153789
- DOI: https://doi.org/10.1134/S0012500816100049
- ID: 153789
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Аннотация
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.
Об авторах
V. Bykov
Emanuel Institute of Biochemical Physics
Автор, ответственный за переписку.
Email: bykov@deom.chph.ras.ru
Россия, ul. Kosygina 4, Moscow, 119991
S. Lomakin
Emanuel Institute of Biochemical Physics
Email: bykov@deom.chph.ras.ru
Россия, ul. Kosygina 4, Moscow, 119991
S. Tsybenova
Emanuel Institute of Biochemical Physics
Email: bykov@deom.chph.ras.ru
Россия, ul. Kosygina 4, Moscow, 119991
S. Varfolomeev
Emanuel Institute of Biochemical Physics
Email: bykov@deom.chph.ras.ru
Россия, ul. Kosygina 4, Moscow, 119991
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