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Summary of Dimensionless Numbers of Fluid Mechanics and Heat Transfer 1. Nusselt Number Average Nusselt Number: Nul = Convective
Jingwei Zhu http://jingweizhu.weebly.com/course-note.html Summary of Dimensionless Numbers of Fluid Mechanics and Heat Transfer 1. Nusselt number Average Nusselt number: convective heat transfer ℎ퐿 Nu = = L conductive heat transfer 푘 where L is the characteristic length, k is the thermal conductivity of the fluid, h is the convective heat transfer coefficient of the fluid. Selection of the characteristic length should be in the direction of growth (or thickness) of the boundary layer; some examples of characteristic length are: the outer diameter of a cylinder in (external) cross flow (perpendicular to the cylinder axis), the length of a vertical plate undergoing natural convection, or the diameter of a sphere. For complex shapes, the length may be defined as the volume of the fluid body divided by the surface area. The thermal conductivity of the fluid is typically (but not always) evaluated at the film temperature, which for engineering purposes may be calculated as the mean-average of the bulk fluid temperature T∞ and wall surface temperature Tw. Local Nusselt number: hxx Nu = x k The length x is defined to be the distance from the surface boundary to the local point of interest. 2. Prandtl number The Prandtl number Pr is a dimensionless number, named after the German physicist Ludwig Prandtl, defined as the ratio of momentum diffusivity (kinematic viscosity) to thermal diffusivity. That is, the Prandtl number is given as: viscous diffusion rate ν Cpμ Pr = = = thermal diffusion rate α k where: ν: kinematic viscosity, ν = μ/ρ, (SI units : m²/s) k α: thermal diffusivity, α = , (SI units : m²/s) ρCp μ: dynamic viscosity, (SI units : Pa ∗ s = N ∗ s/m²) W k: thermal conductivity, (SI units : ) m∗K J C : specific heat, (SI units : ) p kg∗K ρ: density, (SI units : kg/m³). -
Me6502 Heat & Mass Transfer
M.I.E.T. ENGINEERING COLLEGE/ DEPT. of Mechanical Engineering M.I.E.T. ENGINEERING COLLEGE (Approved by AICTE and Affiliated to Anna University Chennai) TRICHY – PUDUKKOTTAI ROAD, TIRUCHIRAPPALLI – 620 007 DEPARTMENT OF MECHANICAL ENGINEERING COURSE MATERIAL ME6502 - HEAT & MASS TRANSFER III YEAR - V SEMESTER M.I.E.T. /Mech. / III /HMT M.I.E.T. ENGINEERING COLLEGE/ DEPT. of Mechanical Engineering M.I.E.T. ENGINEERING COLLEGE (Approved by AICTE and Affiliated to Anna University Chennai) TRICHY – PUDUKKOTTAI ROAD, TIRUCHIRAPPALLI – 620 007 DEPARTMENT OF MECHANICAL ENGINEERING SYLLABUS (THEORY) Sub. Code : ME6502 Branch / Year / Sem : MECH/III/V Sub.Name : HEAT & MASS TRANSFER Staff Name : E MANIKANDAN L T P C 3 0 0 3 UNIT I CONDUCTION 9 General Differential equation of Heat Conduction– Cartesian and Polar Coordinates – One Dimensional Steady State Heat Conduction –– plane and Composite Systems – Conduction with Internal Heat Generation – Extended Surfaces – Unsteady Heat Conduction – Lumped Analysis – Semi Infinite and Infinite Solids –Use of Heisler’s charts. UNIT II CONVECTION 9 Free and Forced Convection - Hydrodynamic and Thermal Boundary Layer. Free and Forced Convection during external flow over Plates and Cylinders and Internal flow through tubes . UNIT III PHASE CHANGE HEAT TRANSFER AND HEAT EXCHANGERS 9 σusselt’s theory of condensation - Regimes of Pool boiling and Flow boiling. Correlations in boiling and condensation. Heat Exchanger Types - Overall Heat Transfer Coefficient – Fouling Factors - Analysis – LMTD method - NTU method. UNIT IV RADIATION 9 Black Body Radiation – Grey body radiation - Shape Factor – Electrical Analogy – Radiation Shields. Radiation through gases. UNIT V MASS TRANSFER 9 Basic Concepts – Diffusion Mass Transfer – Fick’s Law of Diffusion – Steady state Molecular Diffusion – Convective Mass Transfer – Momentum, Heat and Mass Transfer Analogy –Convective Mass Transfer Correlations. -
A Heat Transfer Textbook
A Heat Transfer Textbook Third Edition by John H. Lienhard IV and John H. Lienhard V Professor John H. Lienhard IV Department of Mechanical Engineering University of Houston Houston TX 77204-4792 U.S.A. Professor John H. Lienhard V Department of Mechanical Engineering Massachusetts Institute of Technology 77 Massachusetts Avenue Cambridge MA 02139-4307 U.S.A. Copyright ©2000 by John H.Lienhard IV and John H.Lienhard V All rights reserved Please note that this material is copyrighted under U.S. Copyright Law. The authors grant you the right to download and print it for your personal use or for non-profit instructional use.Any other use, including copying, distributing or modifying the work for commercial purposes, is subject to the restrictions of U.S. Copyright Law. International copyright is subject to the Berne International Copyright Convention. The authors have used their best efforts to ensure the accuracy of the methods, equations, and data described in this book, but they do not guarantee them for any particular purpose.The authors and publisher offer no warranties or representations, nor do they accept any liabilities with respect to the use of this information.Please report any errata to authors. Lienhard, John H., 1930– A heat transfer textbook / John H.Lienhard IV and John H.Lienhar d V — 3rd ed.— Cambridge, MA : J.H. Lienhard V, c2000 Includes bibliographic references 1.Heat—Transmission 2.Mass Transfer I.Lienhard, John H.,V, 1961– II.Title TJ260.L445 2000 Published by J.H. Lienhard V Cambridge, Massachusetts, U.S.A. This book was typeset in Lucida Bright and Lucida New Math fonts (designed by Bigelow & Holmes) using LATEX under the Y&Y TEX System. -
Fourier and Biot Numbers and the Accuracy of Conduction Modelling
FOURIER AND BIOT NUMBERS AND THE ACCURACY OF CONDUCTION MODELLING Jan L M Hensen, Abdullatif E Nakhi University of Strathclyde Energy Systems Research Unit 75 Montrose Street, James Weir Bldng GLASGOW G1 1XJ Abstract Recent validation work has shown the importance of accurate modelling in order to bring together experimental results and predictions. A number of important areas were identified: heat transfer coefficient, edge effects, etc. This paper dwells on the latter. After a short review of the associated theory the paper concentrates on the effects of Fourier and Biot numbers on the accuracy of the numerical approximation of the diffusion equation for heat flow through solid elements of buildings. Since this is the most widely used method, the paper focusses on finite-difference modelling. However, the main conclusions are applicable to other numerical approaches as well. By practical examples, representing typical building applications, it is demonstrated that it is easy to introduce - but also relatively easy to minimalize - errors due to space and time discretisation of building structures. Symbols λ −1 α λρ−1 −1 2 −1 Bi Biot number (h 1/2d ), - thermal diffusivity( c ), m s c specific heat, Jkg−1 K−1 ρ density, kg m−3 d wall thickness, m γ implicit/ explicit weighting factor, - * α π −1 1/2 θ ° d effective thickness (( t0 ) , m temperature, C α ∆ ∆ −2 λ −1 −1 Fo Fourier number ( t x ), - thermal conductivity, Wm K h convective heat transfer coefficient, Wm−2K−2 Λ growth factor, - n space step level s time step level t time, s t0 cycle time, s x space co-ordinate, m 1. -
Stability, Convergence and Optimization of Interface Treatments in Weak and Strong Thermal Fluid-Structure Interaction R
Stability, Convergence and Optimization of Interface Treatments in Weak and Strong Thermal Fluid-Structure Interaction R. Moretti, Marc-Paul Errera, Vincent Couaillier, Frédéric Feyel To cite this version: R. Moretti, Marc-Paul Errera, Vincent Couaillier, Frédéric Feyel. Stability, Convergence and Optimization of Interface Treatments in Weak and Strong Thermal Fluid-Structure In- teraction. International Journal of Thermal Sciences, Elsevier, 2017, 126, pp.23 - 37. 10.1016/j.ijthermalsci.2017.12.014. hal-01789013 HAL Id: hal-01789013 https://hal.archives-ouvertes.fr/hal-01789013 Submitted on 9 May 2018 HAL is a multi-disciplinary open access L’archive ouverte pluridisciplinaire HAL, est archive for the deposit and dissemination of sci- destinée au dépôt et à la diffusion de documents entific research documents, whether they are pub- scientifiques de niveau recherche, publiés ou non, lished or not. The documents may come from émanant des établissements d’enseignement et de teaching and research institutions in France or recherche français ou étrangers, des laboratoires abroad, or from public or private research centers. publics ou privés. 1 Stability, Convergence and Optimization of Interface Treatments in Weak and Strong Thermal Fluid-Structure Interaction Rocco Moretti (1) , Marc-Paul Errera (*) (2), Vincent Couaillier (3) , Frédéric Feyel (4) (1) ONERA, The French Aerospace Lab, France, Email: [email protected] (2) ONERA, The French Aerospace Lab, France, Email: [email protected] (3) ONERA, The French Aerospace Lab, France, Email: [email protected] (4) SafranTech, Safran Group, France, Email: [email protected] Abstract - This paper presents the stability, convergence and optimization characteristics of interface treatments for steady conjugate heat transfer problems.