FORCED CONVECTION HEAT TRANSFER INPARALLEL PLATE CHANNELS PARTIALLY FI

J. SHARATH KUMAR REDDY

ISBN 10: 6208442974 / ISBN 13: 9786208442972

Published by Omniscriptum, LAP Lambert Academic Publishing, 2025

About this Item

This item is printed on demand - it takes 3-4 days longer - Neuware -This book explains the hydrodynamic and thermal behavior of laminar Newtonian fluid flow in channels partially filled with porous material, symmetrically distributed at the walls. Using the Successive Accelerated Replacement (SAR) numerical scheme, the analysis explores the influence of porous fraction (Gamma ), Darcy number (Da), Peclet number (Pe), and Brinkman number (Br) on flow and heat transfer. Results show that axial conduction significantly affects temperature profiles at low Pe (<100), while viscous dissipation (Br) alters thermal gradients, elevating bulk temperatures under constant heat flux. A minimum local Nusselt number occurs at intermediate Gamma , independent of axial location, suggesting optimal porous thickness for heat transfer. The interplay of parameters highlights design considerations for systems balancing flow resistance and thermal efficiency, particularly in applications requiring precise thermal management. 272 pp. Englisch.

Seller Inventory # 9786208442972

Bibliographic Details

• Title: FORCED CONVECTION HEAT TRANSFER INPARALLEL PLATE CHANNELS PARTIALLY FI
• Publisher: Omniscriptum, LAP Lambert Academic Publishing
• Publication Date: 2025
• Language: English
• ISBN 10: 6208442974
• ISBN 13: 9786208442972
• Binding: Taschenbuch
• Condition: Neu
• Dimensions: 220W x 150H x 33D millimeters 220 millimeters width by 150 millimeters height by 33 millimeters depth

About this title

Synopsis

This book explains the hydrodynamic and thermal behavior of laminar Newtonian fluid flow in channels partially filled with porous material, symmetrically distributed at the walls. Using the Successive Accelerated Replacement (SAR) numerical scheme, the analysis explores the influence of porous fraction (γₚ), Darcy number (Da), Peclet number (Pe), and Brinkman number (Br) on flow and heat transfer. Results show that axial conduction significantly affects temperature profiles at low Pe (<100), while viscous dissipation (Br) alters thermal gradients, elevating bulk temperatures under constant heat flux. A minimum local Nusselt number occurs at intermediate γₚ, independent of axial location, suggesting optimal porous thickness for heat transfer. The interplay of parameters highlights design considerations for systems balancing flow resistance and thermal efficiency, particularly in applications requiring precise thermal management.