Prediction of Catalyst Bed Density and Simulation of Glycerol Steam Reformer for Hydrogen Production

Authors

  • Vorathorn Charoensuk Chulalongkorn University
  • Palang Bumroongsakulsawat Chulalongkorn University
  • Pattaraporn Kim-Lohsoontorn Chulalongkorn University
  • Piyasan Praserthdam Chulalongkorn University
  • Suttichai Assabumrungrat Chulalongkorn University

DOI:

https://doi.org/10.4186/ej.2022.26.7.1

Keywords:

computational fluid dynamics, catalyst packing density, void fraction, catalyst pellet, glycerol steam reforming, hydrogen production

Abstract

The work focuses on mimicking the loading of the catalyst pellets into a reactor in a realistic manner and proposing a simple method to predict catalyst bed density using Blender 3D Software, a free and open-source 3D creation suite. The catalyst freely falling into a container was animated. The void fraction of loose and close-packing catalyst bed was compared. The effects of different catalyst shapes (sphere and cylinder) and sizes (2–5 mm) on the catalyst bed density in different reactor sizes (18-50 mm) were investigated. It could well predict the values with the error ranging from 0.36 to 6.59%. The obtained information from Blender was employed in a computational fluid dynamics (CFD) model for simulating hydrogen production in a glycerol steam reformer packed with Co-Ni/Al2O3 catalyst.

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Author Biographies

Vorathorn Charoensuk

Center of Excellence on Catalysis and Catalytic Reaction Engineering, Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Bangkok, 10330, Thailand

Palang Bumroongsakulsawat

Center of Excellence on Catalysis and Catalytic Reaction Engineering, Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Bangkok, 10330, Thailand

Bio-Circular-Green economy Technology & Engineering Center, BCGeTEC, Faculty of Engineering, Chulalongkorn University, Bangkok, 10330, Thailand

Pattaraporn Kim-Lohsoontorn

Center of Excellence on Catalysis and Catalytic Reaction Engineering, Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Bangkok, 10330, Thailand

Bio-Circular-Green economy Technology & Engineering Center, BCGeTEC, Faculty of Engineering, Chulalongkorn University, Bangkok, 10330, Thailand

Piyasan Praserthdam

Center of Excellence on Catalysis and Catalytic Reaction Engineering, Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Bangkok, 10330, Thailand

Suttichai Assabumrungrat

Center of Excellence on Catalysis and Catalytic Reaction Engineering, Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Bangkok, 10330, Thailand

Bio-Circular-Green economy Technology & Engineering Center, BCGeTEC, Faculty of Engineering, Chulalongkorn University, Bangkok, 10330, Thailand

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Published In
Vol 26 No 7, Jul 31, 2022
How to Cite
[1]
V. Charoensuk, P. Bumroongsakulsawat, P. Kim-Lohsoontorn, P. Praserthdam, and S. Assabumrungrat, “Prediction of Catalyst Bed Density and Simulation of Glycerol Steam Reformer for Hydrogen Production”, Eng. J., vol. 26, no. 7, pp. 1-11, Jul. 2022.

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