MCE 855: CONDUCTIVE HEAT TRANSFER MCE 855 COURSE SYNOPSIS CONDUCTIVE HEAT TRANSFER PROFESSOR M. A. WAHEED VISITING PROFESSOR COVENANT UNIVERSITY, OTA akindoye@gmail.com 1 2 Course Outling Course Outling Contd • Derivation of Heat Conduction Equation for Heterogeneous, Isotropic Materials in Cartesian Coordinates. Heat conduction equation for homogeneous, isotropic materials in Cartesian, Cylindrical and Spherical Coordinates. Summary of basic steady 1D heat conduction solutions including concept of resistances. • Illustration #2: 2D Steady State Heat Conduction with Constant Heat Generation in a Long Rod of Rectangular Cross-section with Boundaries at the ambient temperature (large heat transfer coefficient) • • Heat transfer from a fin of uniform cross-section. Fin efficiency and fin effectiveness. Fin with variable cross-section. • Two-dimensional Steady State Heat Conduction: Illustration # 1: A rod with rectangular cross-section with three sides having temperature, To and other side at T = f(x). Solution by Method of Separation of Variables. Isotherms and Heat Flux Lines. Steady 2D Conduction in Cylindrical Coordinates: Examples of various 2D conduction problems in cylindrical coordinates. Illustration #1: T (r, z), Circular Cylinder of Finite Length (Axi-symmetric Problem with top surface at T = f (r) and other surfaces at T = Tc). Fourier-Bessel Series Solution. • Illustration #2: Long Cylinder having Circumferential Surface Temperature Variation: T (r, φ) Problem: Periodic boundary conditions in φ-direction. Justification of orthogonality in φdirection. Solution by Separation of Variables method. 1 Course Outling Contd • • Treatment of variable conductivity by Kirchhoff transformation. Unsteady State Conduction: Applications. Definition of Lumped and Distributed Systems. Biot Number and its Physical Significance. Characteristic lengths for plane wall, long cylinder and sphere. Lumped System Analysis: Derivation of the governing equation. Solution. T vs. t as a function of hA/ρcV for the cases of heating and cooling. Time Constant and its Physical Significance. Distributed Systems Analysis: Plane Wall: CaseI: Large Heat Transfer Coefficient. Case II: Moderate Heat Transfer Coefficient. Long Cylinder: Case I: Large Heat Transfer Coefficient. Case II: Moderate Heat Transfer Coefficient. Introduction to Heisler Charts. Multi-dimensional transient heat conduction: Nondimensional temperature expressed as a product of 1D transient solution in each direction. Course Outling Contd. • Semi-Infinite Solid: Definition. 1D Transient Solution by Laplace Transform and Similarity technique (Error function solution) when temperature of the surface at x = 0 is suddenly changed to T∞ (< Ti). Expression of heat flux at x = 0. Other surface boundary conditions: (i) Surface Convection (ii) Constant surface heat flux. Penetration depth. • Time-dependent Boundary Conditions-Duhamel’s Superposition Integral: Principle. Derivation of the integral. Solidification and Melting: Introduction. 1D Solidification Analysis: Stefan (1891) Problem. Melting of a Solid: 1D Analysis. • Inverse heat conduction: Determination of unknown boundary conditions; Experimental determination of thermal conductivity and heat capacity. • Microscale heat transfer: hyperbolic heat conduction, speed of propagation of thermal waves, time lag, solution for a thin slab. • Gra Grading Policy: ding Policy Resources for our learning • Textbook: Fundamental of Heat and Mass Transfer: F. P. Incropera and D. P. Dewitt Homework 10% • Heat Transfer: Yunus A. Cengel Mid-Semester Exam 15% • Heat Transfer: J.P. Holman Class Attendance/Quiz • Read assigned sections before coming to class. Final Semester Exam • Class participation welcome and essential. • Other Instructors, i. e., Classmates, Organized Learning Groups • Homework: Submission, grading, and return policies will be announced in the class. Total (Date?) 5% 70% (Date?) 100% Please turn in homework on time! May discuss, but do not copy solutions from any source! 10% penalty for late homework. No credit after solutions have been posted, except in serious situations. 2 IMPORTANT INFORMATION • • • • • • • • • • Homework: You are encouraged to work along with your colleagues, but each of you must provide your own individual solution set. Plagiarism will result in a zero for that set. Exam: There will be a midterm and comprehensive final exams Student responsibilities: You have certain responsibilities and rights as an adult and a student. Please refer to the student manual for a description of what these entail. Use of Laptop/Cell Phone in Classroom: No Laptop or Cell Phone (please turn off your cell phones) is allowed during the class periods. You may use a PC Tablet strictly for note-taking. Academic Integrity: Academic integrity is the cornerstone of the university and will be strongly enforced in this course. Any student found in violation of the academic integrity policy will be given an “F” for the course and will be referred to the Student Disciplinary Committee. For additional information about FUNAAB’s Academic Integrity policy/procedures please contact the office of the College officer. Your Performance in the Course • You will find that this is a very interesting course about how many useful devices work: cars, air planes, heaters, power plants, air conditioners, refrigerators etc. • If you don’t do well on early homework, quizzes and exams? • Ensure you understand the material (Ask questions in class, Form a Study Group- use Blackboard and/or Mixable to stay in touch with your study group, See one of the Teaching Assistants or one of the Instructors in their Office Hours) • Ensure you are doing homework on your own (A little help that allows you to complete homework well may not be available in quizzes and exams). • See me early and discuss your situation (in confidence). Heat Transfer as a Course CONDUCTIVE HEAT TRANSFER • • INTRODUCTORY CHAPTER – HEAT TRANSFER • Has a “reputation” for being one of the most challenging, fundamental, conceptual courses in ME. It is the “heart” of thermal engineering Why?? – Physically diverse: thermodynamics, material science, diffusion theory, fluid mechanics, radiation theory – Higher-level math: vector calculus, ODEs, PDEs, numerical methods – Physically elusive: heat is invisible; developing intuition takes time – Appropriate assumptions: required to simplify and solve most problems However, Heat Transfer is interesting, fun, and readily applicable to the real world 12 3 THERMODYNAMICS AND HEAT TRANSFER • Heat: The form of energy that can be transferred from one system to another as a result of temperature difference. • Thermodynamics is concerned with system in equilibrium; may be used to predict the amount of heat transfer as a system undergoes a process from one equilibrium state to another. • Heat Transfer deals with the determination of the rates of such energy transfers as well as variation of temperature. • The transfer of energy as heat is always from the highertemperature medium to the lower-temperature one. • Heat transfer stops when the two mediums reach the same temperature. • Heat can be transferred in three different modes: All modes of heat transfer require the existence of a temperature difference. • Net radiation heat transfer occurs when there exists a temperature difference between two or more surfaces emitting radiation energy 13 Application Areas of Heat Transfer • • • • Conduction heat transfer is due to a temperature gradient in a stationary medium or media • Radiation heat transfer occurs due to emission of energy in the form of electromagnetic waves by all bodies above absolute zero temperature 14 Application Areas of Heat Transfer indeed a relevant subject in many industrial and environmental problem • • Different types of heat transfer processes are called different modes of heat transfer • Convection heat transfer occurs between a surface and a moving fluid at different temperatures conduction, convection, radiation • Definition • Heat transfer is energy transfer due to a temperature difference in a medium or between two or more media Power generation and distribution: In energy production and conversion, i.e. in the generation of electrical power whether through nuclear fission or fusion, the combustion of fossil fuels, magnetohydrodynamic processes, or the use of geothermal energy sources, there are numerous heat transfer problem that must be solved, i.e. in boilers, condensers, cooling towers, feed heaters, transformer cooling, transmission cable cooling, etc. Renewable energy system: Development of solar energy conversion systems for space heating as well as for electric power production, flat plate collectors, thermal energy storage, photovoltaic cell (PVC) module cooling, etc. Transportation: In propulsion systems such as internal combustion, gas turbine, and rocket engines, engine cooling, automobile radiators, etc. Comfort heating, ventilation, and air conditioning: Design of convectional space and water heating systems in the design of incinerator and cryogenic storage equipment, in the design of refrigeration and air conditioning systems, and in many manufacturing processes, mobile food storage, 15 • Aviation and space exploration: Gas turbine blade cooling, vehicle heat shields, rocket engine/nozzles cooling, space suits, space power generation, etc. • Chemical, petrochemical and process industry: heat exchangers, reactors, reboilers, etc. • Electrical machines and electronic equipment: Cooling of motors, generators, computers and microelectronic devices, etc. • Manufacturing and material processing: Metal processing, heat treatment, composite material processing, crystal growth, micromachining, laser machining, etc. • Fire and combustion: combustion plant • Domestic applications: ovens, stoves, toaster, etc. • Health care and biomedical applications: blood warmers, organ and tissue storage, hypothermia, etc. • Weather and environmental changes: Also relevant to air and water pollution and strongly influences local and global climate, climate control, etc 16 4 Application Areas of Heat Transfer 17 18 17 Heat Transfer Applications Human body • • Heat transfer is commonly encountered in engineering systems and other aspects of life, and one does not need to go very far to see some application areas of heat transfer. 5 Historical Background Kinetic theory: Treats molecules as tiny balls that are in motion and thus possess kinetic energy. Heat: The energy associated with the random motion of atoms and molecules. Caloric theory: Heat is a fluidlike substance called the caloric that is a massless, colorless, odorless, and tasteless substance that can be poured from one body into another It was only in the middle of the nineteenth century that we had a true physical understanding of the nature of heat. Careful experiments of the Englishman James P. Joule published in 1843 convinced the skeptics that heat was not a substance after all, and thus put the caloric theory to rest. 21 HEAT AND OTHER FORMS OF ENERGY • Energy can exist in numerous forms such as: thermal, mechanical, kinetic, ENGINEERING HEAT TRANSFER Heat transfer equipment such as heat exchangers, boilers, condensers, radiators, heaters, furnaces, refrigerators, and solar collectors are designed primarily on the basis of heat transfer analysis. The heat transfer problems encountered in practice can be considered in two groups: (1) rating and (2) sizing problems. The rating problems deal with the determination of the heat transfer rate for an existing system at a specified temperature difference. The sizing problems deal with the determination of the size of a system in order to transfer heat at a specified rate for a specified temperature difference. An engineering device or process can be studied either experimentally (testing and taking measurements) or analytically (by analysis or calculations). The experimental approach has the advantage that we deal with the actual physical system, and the desired quantity is determined by measurement, within the limits of experimental error. However, this approach is expensive, timeconsuming, and often impractical. The analytical approach (including the numerical approach) has the advantage that it is fast and inexpensive, but the results obtained are subject to the accuracy of the assumptions, approximations, and idealizations made in the analysis. 22 • Internal energy: May be viewed as the sum of the kinetic and potential energies of the molecules. • Sensible heat: The kinetic energy of the molecules. • Latent heat: The internal energy associated with the phase of a system. • Chemical (bond) energy: The internal energy associated with the atomic bonds in a molecule. • Nuclear energy: The internal energy associated with the bonds within the nucleus of the atom itself. potential, electrical, magnetic, chemical, nuclear. • Their sum constitutes the total energy E (or e on a unit mass basis) of a system. • The sum of all microscopic forms of energy is called the internal energy of a system. What is thermal energy? What is the difference between thermal energy and heat? 23 24 6 Internal Energy and Enthalpy • • • Specific Heats of Gases, Liquids, and Solids In the analysis of systems that involve fluid flow, we frequently encounter the combination of properties u and Pv. • Specific heat: The energy required to raise the temperature of a unit mass of a substance by one degree. • Two kinds of specific heats: specific heat at constant volume cv The combination is defined as enthalpy (h = u + Pv). specific heat at constant pressure cp • The specific heats of a substance, in general, depend on two independent properties such as temperature and pressure. • At low pressures all real gases approach ideal gas behavior, and therefore their specific heats depend on temperature only. The term Pv represents the flow energy of the fluid (also called the flow work). 25 26 Energy Transfer Energy can be transferred to or from a given mass by two mechanisms: when is constant: heat transfer and work. Heat transfer rate: The amount of heat transferred per unit time. • Heat flux: The rate of heat transfer per unit area normal to the direction of heat transfer. Incompressible substance: A substance whose specific volume (or density) does not change with temperature or pressure. • The constant-volume and constantpressure specific heats are identical for incompressible substances. • The specific heats of incompressible substances depend on temperature only. Power: The work done per unit time. 27 28 7 Energy Balance for Steady-Flow Systems Surface Energy Balance A surface contains no volume or mass, and thus no energy. Thereore, a surface can be viewed as a fictitious system whose energy content remains constant during a process. A large number of engineering devices such as water heaters and car radiators involve mass flow in and out of a system, and are modeled as control volumes. Most control volumes are analyzed under steady operating conditions. The term steady means no change with time at a specified location. Mass flow rate: The amount of mass flowing through a cross section of a flow device per unit time. Volume flow rate: The volume of a fluid flowing through a pipe or duct per unit time. This relation is valid for both steady and transient conditions, and the surface energy balance does not involve heat generation since a surface does not have a volume. 29 MECHANISMS OF HEAT TRANSFER MECHANISMS • Heat as the form of energy that can be transferred from one system to another as a result of temperature difference. • A thermodynamic analysis is concerned with the amount of heat transfer as a system undergoes a process from one equilibrium state to another. • The science that deals with the determination of the rates of such energy transfers is the heat transfer. • The transfer of energy as heat is always from the highertemperature medium to the lower-temperature one, and heat transfer stops when the two mediums reach the same temperature. • MECHANISMS OF HEAT TRANSFER BY CONDUCTION Conduction: The transfer of energy from the more energetic particles of a substance to the adjacent less energetic ones as a result of interactions between the particles. In gases and liquids, conduction is due to the collisions and diffusion of the molecules during their random motion. In solids, it is due to the combination of vibrations of the molecules in a lattice and the energy transport by free electrons. The rate of heat conduction through a plane layer is proportional to the temperature difference across the layer and the heat transfer area, but is inversely proportional to the thickness of the layer. Heat can be transferred in three basic modes: conduction convection radiation • All modes of heat transfer require the existence of a temperature difference. 30 31 Heat conduction through a large plane wall of thickness x and area A. 32 8 When x → 0 Thermal Conductivity Fourier’s law of heat conduction Thermal conductivity, k: A measure of the ability of a material to conduct heat. Thermal conductivity: The rate of heat transfer through a unit thickness of the material per unit area per unit temperature difference. Temperature gradient dT/dx: The slope of the temperature curve on a T-x diagram. Heat is conducted in the direction of decreasing temperature, and the temperature gradient becomes negative when temperature decreases with increasing x. The negative sign in the equation ensures that heat transfer in the positive x direction is a positive quantity. In heat conduction analysis, A represents the area normal to the direction of heat transfer. The thermal conductivity of a material is a measure of the ability of the material to conduct heat. The rate of heat conduction through a solid is directly proportional to its thermal 33 conductivity. A high value for thermal conductivity indicates A simple experimental setup that the material is a to determine the thermal good heat conductor, conductivity of a material. and a low value indicates that the material is a poor heat conductor or insulator. 34 The thermal conductivities of gases such as air vary by a factor of 104 from those of pure metals such as copper. Pure crystals and metals have the highest thermal conductivities, and gases and insulating materials the lowest. The range of thermal conductivity of various materials at room temperature. 35 The mechanisms of heat conduction in different phases of a substance. 36 9 Thermal Diffusivity cp Specific heat, J/kg · °C: Heat capacity per unit mass cp Heat capacity, J/m3·°C: Heat capacity per unit volume Thermal diffusivity, m2/s: Represents how fast heat diffuses through a material A material that has a high thermal conductivity or a low heat capacity will obviously have a large thermal diffusivity. The variation of the thermal conductivity of various solids, liquids, and gases with temperature. The larger the thermal diffusivity, the faster the propagation of heat into the medium. A small value of thermal diffusivity means that heat is mostly absorbed by the material and a small amount of heat is conducted further. 37 CONVECTION Forced convection: If the fluid is forced to flow over the surface by external means such as a fan, pump, or the wind. Convection: The mode of energy transfer between a solid surface and the adjacent liquid or gas that is in motion, and it involves the combined effects of conduction and fluid motion. Natural (or free) convection: If the fluid motion is caused by buoyancy forces that are induced by density differences due to the variation of temperature in the fluid. The faster the fluid motion, the greater the convection heat transfer. In the absence of any bulk fluid motion, heat transfer between a solid surface and the adjacent fluid is by pure conduction. 38 The cooling of a boiled egg by forced and natural convection. Heat transfer processes that involve change of phase of a fluid are also considered to be convection because of the fluid motion induced during the process, such as the rise of the vapor bubbles during boiling or the fall of the liquid droplets during condensation. Heat transfer from a hot surface to air by convection. 39 40 10 Newton’s law of cooling h As Ts T RADIATION convection heat transfer coefficient, W/m2 · °C the surface area through which convection heat transfer takes place the surface temperature the temperature of the fluid sufficiently far from the surface. The convection heat transfer coefficient h is not a property of the fluid. It is an experimentally determined parameter whose value depends on all the variables influencing convection such as - the surface geometry - the nature of fluid motion - the properties of the fluid - the bulk fluid velocity • Radiation: The energy emitted by matter in the form of electromagnetic waves (or photons) as a result of the changes in the electronic configurations of the atoms or molecules. • Unlike conduction and convection, the transfer of heat by radiation does not require the presence of an intervening medium. • In fact, heat transfer by radiation is fastest (at the speed of light) and it suffers no attenuation in a vacuum. This is how the energy of the sun reaches the earth. • In heat transfer studies we are interested in thermal radiation, which is the form of radiation emitted by bodies because of their temperature. • All bodies at a temperature above absolute zero emit thermal radiation. • Radiation is a volumetric phenomenon, and all solids, liquids, and gases emit, absorb, or transmit radiation to varying degrees. • However, radiation is usually considered to be a surface phenomenon for solids. 41 Stefan–Boltzmann law = 5.670 108 W/m2 · K4 42 Absorptivity : The fraction of the radiation energy incident on a surface that is absorbed by the surface. 0 1 Stefan–Boltzmann constant A blackbody absorbs the entire radiation incident on it ( = 1). Blackbody: The idealized surface that emits radiation at the maximum rate. Kirchhoff’s law: The emissivity and the absorptivity of a surface at a given temperature and wavelength are equal. Radiation emitted by real surfaces Emissivity : A measure of how closely a surface approximates a blackbody for which = 1 of the surface. 0 1. Blackbody radiation represents the maximum amount of radiation that can be emitted from a surface at a specified temperature. 43 The absorption of radiation incident on an opaque surface of absorptivity . 44 11 Net radiation heat transfer: The difference between the rates of radiation emitted by the surface and the radiation absorbed. The determination of the net rate of heat transfer by radiation between two surfaces is a complicated matter since it depends on • the properties of the surfaces • their orientation relative to each other • the interaction of the medium between the surfaces with radiation Radiation is usually significant relative to conduction or natural convection, but negligible relative to forced convection. When a surface is completely enclosed by a much larger (or black) surface at temperature Tsurr separated by a gas (such as air) that does not intervene with radiation, the net rate of radiation heat transfer between these two surfaces is given by When radiation and convection occur simultaneously between a surface and a gas: Combined heat transfer coefficient hcombined Includes the effects of both convection and radiation Radiation heat transfer between a surface and the surfaces surrounding it. 45 46 SIMULTANEOUS HEAT TRANSFER MECHANISMS Heat transfer is only by conduction in opaque solids, but by conduction and radiation in semitransparent solids. A solid may involve conduction and radiation but not convection. A solid may involve convection and/or radiation on its surfaces exposed to a fluid or other surfaces. Heat transfer is by conduction and possibly by radiation in a still fluid (no bulk fluid motion) and by convection and radiation in a flowing fluid. In the absence of radiation, heat transfer through a fluid is either by conduction or convection, depending on the presence of any bulk fluid motion. Convection = Conduction + Fluid motion Although there are three mechanisms of Heat transfer through a vacuum is by radiation. heat transfer, a medium may involve only two of them simultaneously. Most gases between two solid surfaces do not interfere with radiation. Liquids are usually strong absorbers of 47 radiation. 12