Modeling of carbonaceous feedstock pyrolysis in a multichannel reactor

V. I. Bykov; S. M. Lomakin; S. B. Tsybenova; S. D. Varfolomeev

doi:10.1134/S0012500816100049

Modeling of carbonaceous feedstock pyrolysis in a multichannel reactor

作者: Bykov V.I.¹, Lomakin S.M.¹, Tsybenova S.B.¹, Varfolomeev S.D.¹
隶属关系:
1. Emanuel Institute of Biochemical Physics
期: 卷 470, 编号 2 (2016)
页面: 293-296
栏目: Chemistry
URL: https://journals.rcsi.science/0012-5008/article/view/153789
DOI: https://doi.org/10.1134/S0012500816100049
ID: 153789

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详细

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.