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The drying kinetics of celery in a microwave assisted fluidized bed dryer was studied at different drying air temperatures (45°C, 55°C and 65°C) and at different initial microwave power densities (0W/g, 1W/g and 2W/g). Dried product quality, product mass, air temperature, air relative humidity, and electric power consumption were used to monitor the performance of the drying process. The results showed that the Midilli-Kucuk model was best in predicting the moisture ratio as a function of drying time. At any given temperature, the utilization of the microwave energy reduced by more than 50% the drying time. Keywords: drying; celery; MWFBD
Intensification, Energy, Dehydration, Evaporation, Sublimation, Celery, MWFBD, Dewatering, Environmental, Diffusion, Emerging technologies, Process control, Products quality, Drying
Intensification, Energy, Dehydration, Evaporation, Sublimation, Celery, MWFBD, Dewatering, Environmental, Diffusion, Emerging technologies, Process control, Products quality, Drying
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