Effect of Operational Parameters on Drying Rate and Energy Consumption of Epoxy-Based Coating Powder in a Fluidized Bed Dryer System

Document Type : Original Article

Authors

1 Department of Chemical Engineering, Hamedan University of Technology, Hamedan, Iran

2 Department of Chemical Engineering, University of the Basque Country UPV/EHU, P.O. Box 644-E48080, Bilbao, Spain

Abstract
In this work, the effect of inlet air temperature and volume flow rate is studied on the moisture content of epoxy-based coating powder and energy consumption of a fluidized bed dryer system. The inlet air temperature range was determined to be 45-60 oC based on the glass transition temperature of epoxy-based coating powder. The results showed that by increasing the inlet air temperature in the fluidized bed dryer, the drying rate of the samples increased, where the highest drying rate was obtained at 60 oC. In the temperature range of 55 to 60 oC, an increase in inlet air volume flow rate led to an increase in the drying rate. An increase in the inlet air temperature significantly led to an increase in the energy consumption for drying the samples. The drying rate of the samples did not have a constant trend because of an increase in the inlet air volume flow rate. The results showed the drying rate of samples increased by an increase in volume flow rate from 1.0 to 1.4 m3/s, and its value decreased from 1.4 to 1.6 m3/s. However, the amount of energy consumed by the dried samples increases with the increase in the inlet air volume flow rate. The results of this study can be effective in achieving the optimal amount for drying the powder and reaching the optimum value of less than 2% by spending the minimum amount of necessary energy and the maximum drying rate of the powder.

Highlights

  • The effect of inlet temperature and volumetric air flow rate on the moisture content of epoxy-based coating powder.
  • A direct relationship between the inlet air temperature, drying rate and energy consumption of dryer system.
  • The relationship between the energy consumption and the volumetric flowrate of the inlet air.
  • Study on an optimum moisture content, minimum energy consumption, and the maximum drying rate of powder.

Keywords

Subjects

1. Xiang, Q., & Xiao, F. (2020). Applications of epoxy materials in pavement engineering. Construction and Building Materials, 235, 117529.
2. Pearce, P. J., Davidson, R. G., & Morris, C. E. M. (1981). Hydrolytic stability of some uncured epoxy resins. Journal of Applied Polymer Science, 26(7), 2363-2372.
3. Tanaka, K., & Yamaguchi, M. (1995). Dynamic mechanical properties of multi-functional epoxy resin cured with diamine and filled with pitch-based carbon short fibers treated with coupling agents. Advanced Composite Materials, 5(1), 45-62.
4. Fache, M., Montérémal, C., Boutevin, B., & Caillol, S. (2015). Amine hardeners and epoxy cross-linker from aromatic renewable resources. European Polymer Journal, 73, 344-362.
5. Mora, A. S., Tayouo, R., Boutevin, B., David, G., & Caillol, S. (2020). A perspective approach on the amine reactivity and the hydrogen bonds effect on epoxy-amine systems. European Polymer Journal, 123, 109460.
6. Mora, A. S., Tayouo, R., Boutevin, B., David, G., & Caillol, S. (2020). A perspective approach on the amine reactivity and the hydrogen bonds effect on epoxy-amine systems. European Polymer Journal, 123, 109460.
7. Maguire, J. M., Nayak, K., & Brádaigh, C. M. Ó. (2018). Characterisation of epoxy powders for processing thick-section composite structures. Materials & Design, 139, 112-121.
8. Akpinar, E. K., Midilli, A. D. N. A. N., & Bicer, Y. (2005). Energy and exergy of potato drying process via cyclone type dryer. Energy Conversion and Management, 46(15-16), 2530-2552.
9. Kalbasi, M., Khanlarkhani, M.R., & Ahmad Pour, A. (2010). Modeling and simulation of Alumin drying in a spray dryer with co-current flow, Iranian Journal of Chemistry and Chemical Engineering. 9(49), 94-104. https://www.magiran.com/p775997.
10. Barriga, R., Romero, M., Hassan, H., & Nettleton, D. F. (2023). Energy Consumption Optimization of a Fluid Bed Dryer in Pharmaceutical Manufacturing Using EDA (Exploratory Data Analysis). Sensors, 23(8), 3994.
11. Taghavivand, M., Choi, K., & Zhang, L. (2017). Investigation on drying kinetics and tribocharging behaviour of pharmaceutical granules in a fluidized bed dryer. Powder Technology, 316, 171-180.
12. Firouzi, S., Alizadeh, M. R., & Haghtalab, D. (2017). Energy consumption and rice milling quality upon drying paddy with a newly-designed horizontal rotary dryer. Energy, 119, 629-636.
13. Abbasfard, H., Rafsanjani, H. H., Ghader, S., & Ghanbari, M. (2013). Mathematical modeling and simulation of an industrial rotary dryer: A case study of ammonium nitrate plant. Powder technology, 239, 499-505.
14. Rousselet, Y., & Dhir, V. K. (2016). Numerical modeling of a co-current cascading rotary dryer. Food and bioproducts processing, 99, 166-178.
15. Khanali, M., Giglou, A. K., & Rafiee, S. (2018). Model development for shelled corn drying in a plug flow fluidized bed dryer. Engineering in agriculture, environment and food, 11(1), 1-8.
16. Bahramian, A., & Olazar, M. (2012). Fluidization of micronic particles in a conical fluidized bed: experimental and numerical study of static bed height effect. AIChE journal, 58(3), 730-744.
17. Filippin, A. P., Molina Filho, L., Fadel, V., & Mauro, M. A. (2018). Thermal intermittent drying of apples and its effects on energy consumption. Drying technology, 36(14), 1662-1677.
18. Kumar, A., Kandasamy, P., Chakraborty, I., & Hangshing, L. (2022). Analysis of energy consumption, heat and mass transfer, drying kinetics and effective moisture diffusivity during foam-mat drying of mango in a convective hot-air dryer. Biosystems Engineering, 219, 85-102.
Volume 1, Issue 3 - Serial Number 6
Summer 2025
Pages 193-202

  • Receive Date 27 August 2024
  • Revise Date 10 October 2024
  • Accept Date 30 October 2024
  • First Publish Date 06 November 2024