摘要
Fluidization characteristics of silicon particle system are studied by the pressure fluctuation method.The existence of fine particles in the system can improve fluidization. Silicon particles with a wide size distribution,preferably with some fines, behave as Group A particles according to Geldart classification, although the system belongs to Group B actually. The system is also approved to be suitable for organochlorosilane monomer production using a fluidized bed reactor. Experimental data obtained in this work are important for the design and operation of commercial fluidized bed reactors for the production of organochlorosilane monomers.
Fluidization characteristics of silicon particle system are studied by thepressure fluctuation method. The existence of fine particles in the system can improve fluidization.Silicon particles with a wide size distribution, preferably with some fines, behave as Group Aparticles according to Geldart classification, although the system belongs to Group B actually. Thesystem is also approved to be suitable for organochlorosilane monomer production using a fluidizedbed reactor. Experimental data obtained in this work are important for the design and operation ofcommercial fluidized bed reactors for the production of organochlorosilane monomers.
