Modeling and control of solar‐grade silicon production in a fluidized bed reactor |
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Authors: | Juan Du Soham Dutta Birger Erik Ydstie |
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Affiliation: | Dept. of Chemical Engineering, Carnegie Mellon University, Pittsburgh, PA |
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Abstract: | 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. © 2014 American Institute of Chemical Engineers AIChE J, 60: 1740–1751, 2014 |
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Keywords: | solar‐grade silicon production multiscale modeling sensitivity analysis inventory control fluidized bed reactor |
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