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首页> 外文期刊>Journal of Materials Science >Kinetics of direct nitridation of pelletized silicon grains in a fluidized bed: experiment, mechanism and modelling
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Kinetics of direct nitridation of pelletized silicon grains in a fluidized bed: experiment, mechanism and modelling

机译:流化床中颗粒硅颗粒直接氮化的动力学:实验,机理和模型

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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-Si3N4 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. [References: 63]
机译:在没有外部传热和传质影响的条件下,在1200〜1300℃的温度范围内进行了粒径分布宽的粒状硅粒的流化床氮化。在大气压下,将N-2(30%-90%)-H-2(5%-50%)-Ar(余量)混合物用作氮化气体。在氮化气氛中,温度和氮气浓度都会影响α-Si3N4的产率和最终的硅总转化率,但氢气对这两种气体的影响均较小。考虑到氮化过程中发生的一些结构变化后,得出了一个简单的模型。该模型表明,第二氮化阶段的拟渐近指数转化趋势可以通过各种反应机理加以解释,并根据硅晶粒尺寸分布的特性以及实验观察到的硅表面产物鳞片的剥落进行了调整。在研究的实验条件范围内,氮化可被视为具有约340 kJ mol(-1)的E-app表观活化能。 (C)1998查普曼和霍尔。 [参考:63]

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