Kinetics of direct nitridation of pelletized silicon grains in a fluidized bed: experiment, mechanism and modelling

被引:17
作者
Jovanovic, ZR [1 ]
机构
[1] Oregon State Univ, Dept Chem Engn, Corvallis, OR 97331 USA
基金
美国国家科学基金会;
关键词
D O I
10.1023/A:1004395506202
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
A fluidized-bed nitridation of pelletized silicon grains having a wide size distribution was carried out in the temperature range 1200-1300 degrees C under conditions free of external heat and mass transfer effects. N(2)(30%-90%)-H(2) (5%-50%)-Ar (balance) mixtures were used as the nitriding gas at atmospheric pressure. Both the yield of alpha-Si(3)N(4) and the final overall conversion of silicon are affected by temperature and nitrogen gas concentration in a nitriding atmosphere, but hydrogen gas has a minor effect on either of these. After accounting for some of the structural changes that occur during nitridation, a simple model was derived. The model has shown that the pseudo-asymptotic exponential conversion trend in the second nitridation stage could be explained by various reaction mechanisms, adjusted for properties of the size distribution of silicon grains and the experimentally observed spalling of the product scale from the silicon surface. In the investigated range of experimental conditions, nitridation could be considered as having an apparent activation energy of E(app) approximate to 340 kJ mol(-1). (C) 1998 Chapman & Hall.
引用
收藏
页码:2339 / 2355
页数:17
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