• DOI:10.1007/s00231-022-03249-4
• Corpus ID: 249797482

Drying performance of limonite pellets in the hot air-assisted microwave

@article{Li2022DryingPO,
  title={Drying performance of limonite pellets in the hot air-assisted microwave},
  author={Jilu Li and Meiqian Chen and B. A. Fu and Junli Guan},
  journal={Heat and Mass Transfer},
  year={2022},
  volume={59},
  pages={185-202},
  url={https://api.semanticscholar.org/CorpusID:249797482}
}

• Jilu Li, Meiqian Chen, +1 author Junli Guan
• Published in Heat and Mass Transfer 16 June 2022
• Materials Science, Environmental Science

The limonite acted as the raw material for iron smelting should be pre-dried due to its high initial moisture content. Based on a lab-scale setup, the drying performance of limonite pellets (diameter: 15 mm) was evaluated in terms of the influence of the hot air (100–200 °C), microwave power (100–600 W) and microwave combined with hot air drying. As the temperature of hot air rose from 100 to 200 °C, the drying time of limonite during the hot air drying alone saved by 54%. The effective… 

The limonite acted as the raw material for iron smelting should be pre-dried due to its high initial moisture content. Based on a lab-scale setup, the drying performance of limonite pellets (diameter: 15 mm) was evaluated in terms of the influence of the hot air (100–200 °C), microwave power (100–600 W) and microwave combined with hot air drying. As the temperature of hot air rose from 100 to 200 °C, the drying time of limonite during the hot air drying alone saved by 54%. The effective moisture diffusivities ( D eff ) of limonite in the hot air were between 2.07 × 10 –9 and 4.78 × 10 –8 m 2 /s. With lifting the microwave power from 100 to 600 W, the time in the microwave heating alone saved by 80%. The values for D eff of the limonite in the microwave drying were between 1.71 × 10 –8 and 1.23 × 10 –7 m 2 /s. The apparent activation energy ( E a ) of the limonite in the hot air drying was 12.3 kJ/mol. E a for the microwave drying was 37.4 W/g, while that after adding 0.6% Na 2 CO 3 was about 56% lower than that of the pellet without Na 2 CO 3 . In the combined drying, the hot air temperature of 145 °C, the air velocity of 0.5 m/s and microwave power of 500 W were determined as optimized parameters regarding the minimum drying time integrated with energy consumption according to the response surface methodology. Increasing the feed sources and hot air assisted drying could all improve the microwave heating uniformity.