Direct numerical simulation study of end effects and D/d ratio on mass transfer in packed beds. (December 2018)

• Record Type: Journal Article
• Authors: Bale, Shivkumar; Tiwari, Shashank; Sathe, Mayur; Berrouk, Abdallah S.; Nandakumar, Krishnaswamy; Joshi, Jyeshtharaj
• Is Part Of: International journal of heat and mass transfer. Volume 127(2018)Part B
• Page Start: 234
• Page End: 244
• Publication Date: 2018-12
• Subjects: Mass transfer -- End effects -- Packed bed -- Direct numerical simulation (DNS); Heat -- Transmission -- Periodicals; Mass transfer -- Periodicals; Chaleur -- Transmission -- Périodiques; Transfert de masse -- Périodiques; Electronic journals; 621.4022
• DOI: 10.1016/j.ijheatmasstransfer.2018.07.100
• Languages: English
• ISSNs: 0017-9310

Abstract

Highlights: DNS was carried out to study the end effects on mass transfer in a packed bed. DEM-CFD simulation was performed to create packed bed geometries. Effect of confining wall on end effects in a packed bed was investigated. Probability and spatial distribution of the computed 'local' Sh were developed. Abstract: Direct Numerical Simulation (DNS) was performed to investigate the end effects on mass transfer in a packed bed for Reynolds number ( Re ) ≤ 100. The system considered in this study was naphthalene-air with a Schmidt number ( Sc ) ∼ 2.52. The location of the spheres' centers in a randomly packed bed were obtained from Discrete Element Method – Computational Fluid Dynamics (DEM-CFD) simulations. The influence of the confining wall on how packed bed ends affect mass transfer was studied by examining the axial void fraction profile with varying ratio of the column diameter to the particle sphere diameter ( D / d ). Overall, it was found that the confining wall has a significant impact. The 'local' mass transfer coefficient was calculated based on the obtained DNS results and the probability distribution curve and the spatial distribution of the computed 'local' Sherwood numbers as function of the ratio X/L (ratio of the height of the active part of the bed to the total height of the bed) were developed to quantify the end effects on mass transfer within packed beds. For a packed bed with no wall effects ( D / d = 11), it was found that the end effects can be eliminated by replacing the active particles located at ∼2 sphere diameters from the entrance and ∼1 sphere diameter from the exit by inert particles.