Modeling of filtration combustion of carbon

被引：5

作者：

Becker, AV ^{[1
]}

Polianczyk, EV ^{[1
]}

Volkova, N ^{[1
]}

Manelis, GB ^{[1
]}

机构：

[1] Russian Acad Sci, Inst Problems Chem Phys, Chernogolovka 142432, Moscow Oblast, Russia

来源：

THEORETICAL FOUNDATIONS OF CHEMICAL ENGINEERING | 2004年 / 38卷 / 05期

关键词：

D O I：

10.1023/B:TFCE.0000043804.82560.fb

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

The kinetics of the overall reactions of carbon gasification at temperatures up to 1600 K is studied. The kinetic characteristics of the reactions are taken into account in a distributed mathematical model of filtration combustion of carbon. By computational experiment at different values of process control parameters (the gas flow rate, the fraction of the oxidant in the gas, and the mass ratio of carbon to the inert material in the combustible mixture), it is found that, in the wave of filtration combustion of carbon under superadiabatic conditions, carbon gasification can predominately yield either CO2 or CO.

引用

页码：510 / 515

页数：6

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