Modeling and control of solar-grade silicon production in a fluidized bed reactor

被引:15
作者
Du, Juan [1 ]
Dutta, Soham [1 ]
Ydstie, Birger Erik [1 ]
机构
[1] Carnegie Mellon Univ, Dept Chem Engn, Pittsburgh, PA 15213 USA
关键词
solar-grade silicon production; fluidized bed reactor; inventory control; multiscale modeling; sensitivity analysis; CHEMICAL-VAPOR-DEPOSITION; DECOMPOSITION; POWDERS; SILANE;
D O I
10.1002/aic.14378
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A multiscale model predicts silicon production yield and powder loss in a fluidized bed reactor for solar silicon production. The reaction module calculates the silicon vapor deposition and powder scavenging rates. A computational fluid dynamics model predicts temperature and bed density. A population balance model calculates the particle-mass distribution functions on silicon yield. The model results are validated against industrial data. Furthermore, we conduct a sensitivity analysis to investigate the effect of gas flow rate and inlet silane concentration. Finally, a control strategy is proposed to maintain the process at the desired operating point. (c) 2014 American Institute of Chemical Engineers AIChE J, 60: 1740-1751, 2014
引用
收藏
页码:1740 / 1751
页数:12
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