Macrokinetic model of pyrolysis of carbonaceous feedstock in a tubular reactor

被引：4
|
作者：
Bykov, V. I. [1 ]
Lomakin, S. M. [1 ]
Tsybenova, S. B. [1 ]
Varfolomeev, S. D. [1 ]
机构：
[1] Russian Acad Sci, Emanuel Inst Biochem Phys, Ul Kosygina 4, Moscow 119334, Russia
来源：
DOKLADY CHEMISTRY | 2016年 / 467卷
基金：
俄罗斯基础研究基金会;
关键词：
RENEWABLE FUELS; TEMPERATURE;
D O I：
10.1134/S0012500816030083
中图分类号：
O6 [化学];
学科分类号：
0703 ;
摘要：
A macrokinetic model of pyrolysis of carbonaceous feedstock in a tubular reactor was proposed. It was shown that, under unsteady-state conditions (at oscillating temperature of feedstock heating), higher conversions can be reached in comparison with steady-state conditions, which agrees with experimental data on flash pyrolysis of biomass in a tubular reactor during heating-cooling cycles.
引用
收藏
页码：76 / 78
页数：3
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