摘要
This article presents a mathematical model of heat and mass transfer for the process of fluidized-bed spray granulation, which can be applied in the analysis of bed temperature profile, temperature and humidity of outlet gas and moisture content of particles. Effects of operation parameters on the batch granulation are investigated. The theoretical calculation agrees reasonably well with the experimental data.
This article presents a mathematical model of heat and mass transfer for theprocess of fluidized-bed spray granulation, which can be applied in the analysis of bed temperatureprofile, temperature and humidity of outlet gas and moisture content of particles. Effects ofoperation parameters on the batch granulation are investigated. The theoretical calculation agreesreasonably well with the experimental data.
