摘要
在直径100m m ×3m 的实验台上,利用热粒子为示踪剂,研究快速床提升管内的颗粒的扩散行为。在不同的径向位置测得反映扩散行为的温度响应曲线,提出二维扩散模型来描述颗粒的轴、径向扩散。通过最小二乘拟和估计轴向扩散系统Da 和径向扩散系数Dr。实验发现,Da 随气体表面风速的增加而增加,Dr 则基本保持不变。静止床高的增加使Da、Dr 略有增加。
Lateral and axial solids mixing are studied experimentally in 100mm×3m fast fluidized bed riser.Using hot particles as tracer,the temperature response curve at different radial position in fast fluidized bed are measured.A proposed two-dimensional dispersion model describes the experimental data very well.The axial dispersion coefficient,D a increases with increasing of superficial gas velocity v g and increases little with increasing bed height(H),while the lateral dispersion coefficient,D r changes little with the increasing of v g and H.
出处
《中国粉体技术》
CAS
1999年第6期5-8, ,共4页
China Powder Science and Technology