Numerical Simulation of Mantle Convection Using a 2 Temperature Dependent Nonlinear Viscoelastic Model 3 4 by M
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Chapter 6 Natural Convection in a Large Channel with Asymmetric
Chapter 6 Natural Convection in a Large Channel with Asymmetric Radiative Coupled Isothermal Plates Main contents of this chapter have been submitted for publication as: J. Cadafalch, A. Oliva, G. van der Graaf and X. Albets. Natural Convection in a Large Channel with Asymmetric Radiative Coupled Isothermal Plates. Journal of Heat Transfer, July 2002. Abstract. Finite volume numerical computations have been carried out in order to obtain a correlation for the heat transfer in large air channels made up by an isothermal plate and an adiabatic plate, considering radiative heat transfer between the plates and different inclination angles. Numerical results presented are verified by means of a post-processing tool to estimate their uncertainty due to discretization. A final validation process has been done by comparing the numerical data to experimental fluid flow and heat transfer data obtained from an ad-hoc experimental set-up. 111 112 Chapter 6. Natural Convection in a Large Channel... 6.1 Introduction An important effort has already been done by many authors towards to study the nat- ural convection between parallel plates for electronic equipment ventilation purposes. In such situations, since channels are short and the driving temperatures are not high, the flow is usually laminar, and the physical phenomena involved can be studied in detail both by means of experimental and numerical techniques. Therefore, a large experience and much information is available [1][2][3]. In fact, in vertical channels with isothermal or isoflux walls and for laminar flow, the fluid flow and heat trans- fer can be described by simple equations arisen from the analytical solutions of the natural convection boundary layer in isolated vertical plates and the fully developed flow between two vertical plates. -
Soret and Dufour Effects on MHD Boundary Layer Flow of Non
Pramana – J. Phys. (2020) 94:108 © Indian Academy of Sciences https://doi.org/10.1007/s12043-020-01984-z Soret and Dufour effects on MHD boundary layer flow of non-Newtonian Carreau fluid with mixed convective heat and mass transfer over a moving vertical plate ANIL KUMAR GAUTAM1, AJEET KUMAR VERMA1, KRISHNENDU BHATTACHARYYA1 ,∗ and ASTICK BANERJEE2 1Department of Mathematics, Institute of Science, Banaras Hindu University, Varanasi 221 005, India 2Department of Mathematics, Sidho-Kanho-Birsha University, Purulia 723 104, India ∗Corresponding author. E-mail: [email protected], [email protected] MS received 1 August 2019; revised 24 April 2020; accepted 3 May 2020 Abstract. In this analysis, the mixed convection boundary layer MHD flow of non-Newtonian Carreau fluid subjected to Soret and Dufour effects over a moving vertical plate is studied. The governing flow equations are converted into a set of non-linear ordinary differential equations using suitable transformations. For numerical computations, bvp4c in MATLAB package is used to solve the resulting equations. Impacts of various involved parameters, such as Weissenberg number, power-law index, magnetic parameter, thermal buoyancy parameter, solutal buoyancy parameter, thermal radiation, Dufour number, Soret number and reaction rate parameter, on velocity, temperature and concentration are shown through figures. Also, the local skin-friction coefficient, local Nusselt number and local Sherwood number are calculated and shown graphically and in tabular form for different parameters. Some important facts are revealed during the investigation. The temperature and concentration show decreasing trends with increasing values of power-law index, whereas velocity shows reverse trend and these trends are more prominent for larger values of Weissenberg number. -
Thermal Radiations and Mass Transfer Analysis of the Three-Dimensional Magnetite Carreau Fluid Flow Past a Horizontal Surface of Paraboloid of Revolution
processes Article Thermal Radiations and Mass Transfer Analysis of the Three-Dimensional Magnetite Carreau Fluid Flow Past a Horizontal Surface of Paraboloid of Revolution T. Abdeljawad 1,2,3 , Asad Ullah 4 , Hussam Alrabaiah 5,6, Ikramullah 7, Muhammad Ayaz 8, Waris Khan 9 , Ilyas Khan 10,∗ and Hidayat Ullah Khan 11 1 Department of Mathematics and General Sciences, Prince Sultan University, Riyadh 11 586, Saudi Arabia; [email protected] 2 Department of Medical Research, China Medical University, Taichung 40402, Taiwan 3 Department of Computer Science and Information Engineering, Asia University, Taichung, Taiwan 4 Institute of Numerical Sciences, Kohat University of Science & Technology, Kohat 26000, Khyber Pakhtunkhwa, Pakistan; [email protected] 5 College of Engineering, Al Ain University, Al Ain 64141, UAE; [email protected] 6 Department of Mathematics, Tafila Technical University, Tafila 66110, Jordan 7 Department of Physics, Kohat University of Science & Technology, Kohat 26000, Khyber Pakhtunkhwa, Pakistan; [email protected] 8 Department of Mathematics, Abdul Wali Khan University, Mardan 23200, Khyber Pakhtunkhwa, Pakistan; [email protected] 9 Department of Mathematics, Islamia College University Peshawar, Peshawar 25000, Khyber Pakhtunkhwa, Pakistan; [email protected] 10 Faculty of Mathematics and Statistics, Ton Duc Thang University, Ho Chi Minh City 72915, Vietnam 11 Department of Economics, Abbottabad University of Science and Technology (AUST), Abbottabad Havelian 22500, Khyber Pakhtunkhwa, Pakistan; [email protected] * Correspondence: [email protected] Received: 18 April 2020; Accepted: 22 May 2020; Published: 1 June 2020 Abstract: The dynamics of the 3-dimensional flow of magnetized Carreau fluid past a paraboloid surface of revolution is studied through thermal radiation and mass transfer analysis. -
Forced and Natural Convection
FORCED AND NATURAL CONVECTION Forced and natural convection ...................................................................................................................... 1 Curved boundary layers, and flow detachment ......................................................................................... 1 Forced flow around bodies .................................................................................................................... 3 Forced flow around a cylinder .............................................................................................................. 3 Forced flow around tube banks ............................................................................................................. 5 Forced flow around a sphere ................................................................................................................. 6 Pipe flow ................................................................................................................................................... 7 Entrance region ..................................................................................................................................... 7 Fully developed laminar flow ............................................................................................................... 8 Fully developed turbulent flow ........................................................................................................... 10 Reynolds analogy and Colburn-Chilton's analogy between friction and heat -
Convectional Heat Transfer from Heated Wires Sigurds Arajs Iowa State College
Iowa State University Capstones, Theses and Retrospective Theses and Dissertations Dissertations 1957 Convectional heat transfer from heated wires Sigurds Arajs Iowa State College Follow this and additional works at: https://lib.dr.iastate.edu/rtd Part of the Physics Commons Recommended Citation Arajs, Sigurds, "Convectional heat transfer from heated wires " (1957). Retrospective Theses and Dissertations. 1934. https://lib.dr.iastate.edu/rtd/1934 This Dissertation is brought to you for free and open access by the Iowa State University Capstones, Theses and Dissertations at Iowa State University Digital Repository. It has been accepted for inclusion in Retrospective Theses and Dissertations by an authorized administrator of Iowa State University Digital Repository. For more information, please contact [email protected]. CONVECTIONAL BEAT TRANSFER FROM HEATED WIRES by Sigurds Arajs A Dissertation Submitted to the Graduate Faculty in Partial Fulfillment of The Requirements for the Degree of DOCTOR 01'' PHILOSOPHY Major Subject: Physics Signature was redacted for privacy. In Chapge of K or Work Signature was redacted for privacy. Head of Major Department Signature was redacted for privacy. Dean of Graduate College Iowa State College 1957 ii TABLE OF CONTENTS Page I. INTRODUCTION 1 II. THEORETICAL CONSIDERATIONS 3 A. Basic Principles of Heat Transfer in Fluids 3 B. Heat Transfer by Convection from Horizontal Cylinders 10 C. Influence of Electric Field on Heat Transfer from Horizontal Cylinders 17 D. Senftleben's Method for Determination of X , cp and ^ 22 III. APPARATUS 28 IV. PROCEDURE 36 V. RESULTS 4.0 A. Heat Transfer by Free Convection I4.0 B. Heat Transfer by Electrostrictive Convection 50 C. -
Forced Convection Heat Transfer Convection Is the Mechanism of Heat Transfer Through a Fluid in the Presence of Bulk Fluid Motion
Forced Convection Heat Transfer Convection is the mechanism of heat transfer through a fluid in the presence of bulk fluid motion. Convection is classified as natural (or free) and forced convection depending on how the fluid motion is initiated. In natural convection, any fluid motion is caused by natural means such as the buoyancy effect, i.e. the rise of warmer fluid and fall the cooler fluid. Whereas in forced convection, the fluid is forced to flow over a surface or in a tube by external means such as a pump or fan. Mechanism of Forced Convection Convection heat transfer is complicated since it involves fluid motion as well as heat conduction. The fluid motion enhances heat transfer (the higher the velocity the higher the heat transfer rate). The rate of convection heat transfer is expressed by Newton’s law of cooling: q hT T W / m 2 conv s Qconv hATs T W The convective heat transfer coefficient h strongly depends on the fluid properties and roughness of the solid surface, and the type of the fluid flow (laminar or turbulent). V∞ V∞ T∞ Zero velocity Qconv at the surface. Qcond Solid hot surface, Ts Fig. 1: Forced convection. It is assumed that the velocity of the fluid is zero at the wall, this assumption is called no‐ slip condition. As a result, the heat transfer from the solid surface to the fluid layer adjacent to the surface is by pure conduction, since the fluid is motionless. Thus, M. Bahrami ENSC 388 (F09) Forced Convection Heat Transfer 1 T T k fluid y qconv qcond k fluid y0 2 y h W / m .K y0 T T s qconv hTs T The convection heat transfer coefficient, in general, varies along the flow direction. -
Chaotic Flow in a 2D Natural Convection Loop
International Journal of Heat and Mass Transfer 61 (2013) 565–576 Contents lists available at SciVerse ScienceDirect International Journal of Heat and Mass Transfer journal homepage: www.elsevier.com/locate/ijhmt Chaotic flow in a 2D natural convection loop with heat flux boundaries ⇑ William F. Louisos a,b, , Darren L. Hitt a,b, Christopher M. Danforth a,c a College of Engineering & Mathematical Sciences, The University of Vermont, Votey Building, 33 Colchester Avenue, Burlington, VT 05405, United States b Mechanical Engineering Program, School of Engineering, The University of Vermont, Votey Building, 33 Colchester Avenue, Burlington, VT 05405, United States c Department of Mathematics & Statistics, Vermont Complex Systems Center, Vermont Advanced Computing Core, The University of Vermont, Farrell Hall, 210 Colchester Avenue, Burlington, VT 05405, United States article info abstract Article history: This computational study investigates the nonlinear dynamics of unstable convection in a 2D thermal Received 13 August 2012 convection loop (i.e., thermosyphon) with heat flux boundary conditions. The lower half of the thermosy- Received in revised form 1 February 2013 phon is subjected to a positive heat flux into the system while the upper half is cooled by an equal-but- Accepted 3 February 2013 opposite heat flux out of the system. Water is employed as the working fluid with fully temperature dependent thermophysical properties and the system of governing equations is solved using a finite vol- ume method. Numerical simulations are performed for varying levels of heat flux and varying strengths Keywords: of gravity to yield Rayleigh numbers ranging from 1.5 Â 102 to 2.8 Â 107. -
Research Article a Combined Convection Carreau–Yasuda Nanofluid Model Over a Convective Heated Surface Near a Stagnation Point: a Numerical Study
Hindawi Mathematical Problems in Engineering Volume 2021, Article ID 6665743, 14 pages https://doi.org/10.1155/2021/6665743 Research Article A Combined Convection Carreau–Yasuda Nanofluid Model over a Convective Heated Surface near a Stagnation Point: A Numerical Study Azad Hussain,1 Aysha Rehman ,1 Sohail Nadeem,2 M. Y. Malik ,3 Alibek Issakhov,4,5 Lubna Sarwar,1 and Shafiq Hussain6 1Department of Mathematics, University of Gujrat, Gujrat 50700, Pakistan 2Department of Mathematics, Quaid-I-Azam University, Islamabad 44000, Pakistan 3Department of Mathematics, College of Sciences, King Khalid University, Abha 61413, Saudi Arabia 4Department of Mathematical and Computer Modeling, Al-Farabi Kazakh National University, Almaty, Kazakhstan 5Department of Mathematical and Computer Modeling, Kazakh British-Technical University, Almaty, Kazakhstan 6Department of Computer Science, University of Sahiwal, Sahiwal, Pakistan Correspondence should be addressed to Aysha Rehman; [email protected] Received 18 November 2020; Revised 1 March 2021; Accepted 22 March 2021; Published 5 April 2021 Academic Editor: Adrian Neagu Copyright © 2021 Azad Hussain et al. 'is is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited. 'e focus of this manuscript is on two-dimensional mixed convection non-Newtonian nanofluid flow near stagnation point over a stretched surface with convectively heated boundary conditions. -
Enhancement of Natural Convection Heat Transfer Coefficient by Using V-Fin Array
International Journal of Engineering Research and General Science Volume 3, Issue 2, March-April, 2015 ISSN 2091-2730 Enhancement of Natural convection heat transfer coefficient by using V-fin array Rameshwar B. Hagote, Sachin K. Dahake Student of mechanical Engg. Department, MET’s IOE, Adgaon, Nashik (Maharashtra,India). Email. Id: [email protected], Contact No. +919730342211 Abstract— Extended surfaces known as fins are, used to enhance convective heat transfer in a wide range of engineering applications, and offer an economical and trouble free solution in many situations demanding natural convection heat transfer. Fin arrays on horizontal, inclined and vertical surfaces are used in variety of engineering applications to dissipate heat to the surroundings. Studies of heat transfer and fluid flow associated with such arrays are therefore of considerable engineering significance. The main controlling variables generally available to the designer are the orientation and the geometry of the fin arrays. An experimental work on natural convection adjacent to a vertical heated plate with a multiple V- type partition plates (fins) in ambient air surrounding is already done. Boundary layer development makes vertical fins inefficient in the heat transfer enhancement. As compared to conventional vertical fins, this V-type partition plate works not only as extended surface but also as flow turbulator. This V-type partition plate is compact and hence highly economical. The numerical analysis of this technique is done using Computational Fluid Dynamics (CFD) software, Ansys CFX , for natural convection adjacent to a vertical heated plate in ambient air surrounding. In numerical analysis angle of V-fin is further optimized for maximum average heat transfer coefficient. -
On Dimensionless Numbers
chemical engineering research and design 8 6 (2008) 835–868 Contents lists available at ScienceDirect Chemical Engineering Research and Design journal homepage: www.elsevier.com/locate/cherd Review On dimensionless numbers M.C. Ruzicka ∗ Department of Multiphase Reactors, Institute of Chemical Process Fundamentals, Czech Academy of Sciences, Rozvojova 135, 16502 Prague, Czech Republic This contribution is dedicated to Kamil Admiral´ Wichterle, a professor of chemical engineering, who admitted to feel a bit lost in the jungle of the dimensionless numbers, in our seminar at “Za Plıhalovic´ ohradou” abstract The goal is to provide a little review on dimensionless numbers, commonly encountered in chemical engineering. Both their sources are considered: dimensional analysis and scaling of governing equations with boundary con- ditions. The numbers produced by scaling of equation are presented for transport of momentum, heat and mass. Momentum transport is considered in both single-phase and multi-phase flows. The numbers obtained are assigned the physical meaning, and their mutual relations are highlighted. Certain drawbacks of building correlations based on dimensionless numbers are pointed out. © 2008 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved. Keywords: Dimensionless numbers; Dimensional analysis; Scaling of equations; Scaling of boundary conditions; Single-phase flow; Multi-phase flow; Correlations Contents 1. Introduction ................................................................................................................. -
Chapter 7. Convection and Complexity
Chapter 7 Convection and complexity ... if your theory is found to be convection has been taken as the classic exam against the second law of ple of thermal convection, and the hexagonal planform has been considered to be typical of thermodynamics, I can give you no convective patterns at the onset of thermal con hope; there is nothing for it but to vection. Fifty years went by before it was real collapse in deepest humiliation. ized that Benard's patterns were actually driven from above, by surface tension. not from below by Eddington an unstable thermal boundary layer. Experiments Contrary to current textbooks ... the showed the san1.e style of convection when the fluid was heated from above, cooled from below observed world does not proceed or when performed in the absence of gravity. This from lower to higher "degrees of confirmed the top-down surface-driven nature of disorder", since when all the convection which is now called Marangoni or B€mard-Marangoni convection. gravitationally-induced phenomena Although it is not generally recognized as are taken into account the emerging such, mantle convection is a branch of the newly result indicates a net decrease in the renamed science of complexity. Plate tectonics may be a self-drivenfarjrom-equilibrium system that orga "degrees of disorder", a greater nizes itself by dissipation in and between the "degree of structuring" ... classical plates, the mantle being a passive provider of equilibrium thermodynamics ... has energy and material. Far-from-equilibrium sys to be completed by a theory of tems, particularly those in a gravity field, can locally evolve toward a high degree of order. -
Convective Mass Transfer Correlations 5.9 Fluid Flow Through Pipes 5.10 Hot Wire Anemometer
SCH1309 TRANSPORT PHENOMENA UNIT-V UNIT 5: Analogies for Transport processes Contents 5.1 Analogy for mass transfer 5.2 Application of dimensional analysis 5.3 Analogy among Mass, Heat and Momentum Transfer 5.4 Reynolds Analogy 5.5 Chilton Colburn analogy 5.6 Prandtl analogy 5.7 VanKarman analogy 5.8 Convective mass transfer correlations 5.9 Fluid flow through pipes 5.10 Hot wire anemometer 1 SCH1309 TRANSPORT PHENOMENA UNIT-V 5.1 Analogy of Mass Transfer Mass transfer by convection involves the transport of material between a boundary surface (such as solid or liquid surface) and a moving fluid or between two relatively immiscible, moving fluids. There are two different cases of convective mass transfer: 1. Mass transfer takes place only in a single phase either to or from a phase boundary, as in sublimation of naphthalene (solid form) into the moving air. 2. Mass transfer takes place in the two contacting phases as in extraction and absorption. Convective Mass Transfer Coefficient In the study of convective heat transfer, the heat flux is connected to heat transfer coefficient as Q A q h t s t m -------------------- (1.1) The analogous situation in mass transfer is handled by an equation of the form N A k c C As C A -------------------- (1.2) The molar flux N A is measured relative to a set of axes fixed in space. The driving force is the difference between the concentration at the phase boundary, CAS (a solid surface or a fluid interface) and the concentration at some arbitrarily defined point in the fluid medium, C A .