Numerical Investigation of a Desiccant Packed Bed Performance
A. M. Said, A., A. Ibrahim, M., Mostafa, A. (2021). Numerical Investigation of a Desiccant Packed Bed Performance. EKB Journal Management System, 169(0), 266-279. doi: 10.21608/erj.2021.238706
Ahmed A. M. Said; M. A. Ibrahim; A. Mostafa. "Numerical Investigation of a Desiccant Packed Bed Performance". EKB Journal Management System, 169, 0, 2021, 266-279. doi: 10.21608/erj.2021.238706
A. M. Said, A., A. Ibrahim, M., Mostafa, A. (2021). 'Numerical Investigation of a Desiccant Packed Bed Performance', EKB Journal Management System, 169(0), pp. 266-279. doi: 10.21608/erj.2021.238706
A. M. Said, A., A. Ibrahim, M., Mostafa, A. Numerical Investigation of a Desiccant Packed Bed Performance. EKB Journal Management System, 2021; 169(0): 266-279. doi: 10.21608/erj.2021.238706

Numerical Investigation of a Desiccant Packed Bed Performance

Engineering Research Journal
Article 15, Volume 169, Issue 0, March 2021, Page 266-279  XML PDF (472.22 K)
Document Type: Original Article
DOI: 10.21608/erj.2021.238706
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Authors
Ahmed A. M. Said* 1; M. A. Ibrahim1; A. Mostafa2
1Engineering Physics and Mathematics Department, Faculty of Engineering at El-Mattaria, Helwan university, Cairo, Egypt. Egyptian Academy of Engineering and Advanced Technology Affiliated to Ministry of Military Production, Cairo, Egypt.
2Mechanical Power Engineering Department, Faculty of Engineering at El-Mattaria, Helwan university, Cairo, Egypt Egyptian Academy of Engineering and Advanced Technology Affiliated to Ministry of Military Production, Cairo, Egypt.
Abstract
The main objective of the present work is to give the results of theoretical investigations of a desiccant packed bed. For this purpose, the finite difference scheme is proposed and investigated numerically by solving the equation describing mass diffusion in the desiccant bed. This results in a tridiagonal system, which is solved by using Thomas Algorithm. Also, the mass transfer of water vapor and the energy balance equations in both air stream and solid desiccant are solved using the fourth order Runge – Kutta method. The analysis is carried out for typical inlet conditions of 28oC dry bulb temperature and 66% humidity ratio for desiccant masses (5, 10 and 15 kg) and air mass flow rates (7.4 and 10.2 kg/min) during dehumidification operation mode. The reactivation of the desiccant at different regeneration temperatures and air flow rates as well as desiccant masses is also investigated. For the same layer thickness the water content in the desiccant increases by 65% when the desiccant mass increased from 5 to 10 kg while it’s increased by 170% when the desiccant mass increased from 5 to 15 kg.
Keywords
Desiccant packed bed; finite difference; Thomas Algorithm; Runge – Kutta
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