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Chapter 1:
      Introduction and Basic
            Concepts
                                      Yoav Peles
Department of Mechanical, Aerospace and Nuclear Engineering
              Rensselaer Polytechnic Institute




          Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.
Objectives
When you finish studying this chapter, you should be able
  to:
• Understand how thermodynamics and heat transfer are
  related to each other,
• Distinguish thermal energy from other forms of energy,
  and heat transfer from other forms of energy transfer,
• Perform general energy balances as well as surface
  energy balances,
• Understand the basic mechanisms of heat transfer
   Fourier's law of heat conduction, Newton's law of
  cooling, and the Stefan–Boltzmann law of radiation,
• Identify the mechanisms of heat transfer that occur
  simultaneously in practice,
1.1 Thermodynamics (熱力學) and
          Heat Transfer (熱傳)
• The science of thermodynamics deals with the
  amount of heat transfer as a system undergoes a
  process from one equilibrium state to another,
  and makes no reference to how long the process
  will take.


• The science of heat transfer deals with the
  determination of the rates of energy that can be
  transferred from one system to another as a
  result of temperature difference.
需要多久瓶中之coffee
會冷卻至 常溫?


Thermodynamics無法解
決此冷卻速率之問題
• Thermodynamics deals with equilibrium states
  and changes from one equilibrium state to
  another. Heat transfer, on the other hand, deals
  with systems that lack thermal equilibrium, and
  thus it is a non-equilibrium phenomenon.


• Therefore, the study of heat transfer cannot be
  based on the principles of thermodynamics alone.


• However, the laws of thermodynamics lay the
  framework for the science of heat transfer.
Heat Transfer
• The basic requirement for heat transfer is the presence
  of a temperature difference.
• The second law requires that heat be transferred in the
  direction of decreasing temperature.
• The temperature difference is the driving force for heat
  transfer.
• The rate of heat transfer in a certain direction depends
  on the magnitude of the temperature gradient in that
  direction.
• The larger the temperature gradient, the higher the rate
  of heat transfer.
Application Areas of Heat Transfer
歷史發展

• Caloric theory (1789 Antoine Lavoisier, French):
  Heat is a fluid-like substance (錯誤!)

• James P. Joule (1843, Engilishman):
  實驗證明 Heat is not a substance
1.3 Heat (熱) and Other Forms of Energy
• Energy can exist in numerous forms such as:
   –   thermal,
   –   mechanical,
   –   kinetic,
   –   potential,
   –   electrical,
   –   magnetic,
   –   chemical, and
   –   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.
• Internal energy may be viewed as the sum of the
  kinetic and potential energies of the molecules.
• The kinetic energy of the molecules is called
  sensible heat.
• The internal energy associated with the phase of a
  system is called latent heat.
• The internal energy associated with the atomic
  bonds in a molecule is called chemical (or bond)
  energy.
• The internal energy associated with the bonds
  within the nucleus of the atom itself is called
  nuclear energy.
Internal Energy (u, 內能) and Enthalpy (h, 焓)
 • In the analysis of systems
   that involve fluid flow,
   we frequently encounter
   the combination of
   properties u and Pv.
 • The combination is
   defined as enthalpy
    (h = u + Pv).
 • The term Pv represents
   the flow energy of the
   fluid (also called the flow
   work).
Specific Heats of Gases, Liquids, and Solids
• Specific heat (比熱) is defined as the energy required
  to raise the temperature of a unit mass of a substance
  by one degree (kJ/kg-K).
• Two kinds of specific heats:
   – specific heat at constant volume cv, and
   – specific heat at constant pressure cp.
• The specific heats of a substance, in general, depend on
  two independent properties such as temperature and
  pressure.
• For an ideal gas, however, they depend on temperature
  only.
Specific Heats
• At low pressures all real gases approach ideal gas
  behavior, and therefore their specific heats depend on
  temperature only.
• A substance whose specific volume (or density) does
  not change with temperature or pressure is called an
  incompressible substance.
• The constant-volume and constant-pressure specific
  heats are identical for incompressible
  substances.
• The specific heats of incompressible
  substances depend on temperature
  only.
Energy Transfer
• Energy can be transferred to or from a given mass by
  two mechanisms:
   – heat transfer, and
   – work.

• The amount of heat transferred during a process is
  denoted by Q.

• The amount of heat transferred per unit time is called
  heat transfer rate, and is denoted by Q .
• The total amount of heat transfer Q during a time
  interval ∆t can be determined from
                         ∆t
                                            (1-6)
                     Q = ∫ Qdt    (J)
                          0

• The rate of heat transfer per unit area normal to the
  direction of heat transfer is called heat flux (熱通量),
  and the average heat flux is expressed as

                          Q
                       q=        (W/m 2 )     (1-8)
                          A
1.4 The First Law of Thermodynamics

• The first law of thermodynamics states that energy
  can neither be created nor destroyed during a process;
  it can only change forms.

   For the control volume (CV):
            [入] - [出] + [生成量] = [增加量]
                                  =0
   Total energy       Total energy   Change in the
   entering the   -    leaving the = total energy of   (1-9)
     system              system        the system
The energy balance for any system undergoing any
  process can be expressed as (in the rate form)

          Ein − Eout      =      dEsystem dt     (W)

 Rate of net energy transfer      Rate of change in internal
  by heat, work, and mass      kinetic, potential, etc., energies
                                                            (1-11)
• In heat transfer problems it is convenient to write
  a heat balance and to treat the conversion of
  nuclear, chemical, mechanical, and electrical
  energies into thermal energy as heat generation.
• The energy balance in that case can be expressed
  as
       Qin − Qout + Egen =         ∆Ethermal , system   (J)   (1-13)
  Net heat transfer     Heat        Change in thermal
                      generation   energy of the system
Energy Balance

              (i) Closed systems

• Stationary closed system, no work:

          Q = mcv ∆T       (J)         (1-15)
(ii) Steady-Flow Systems
• For system with one inlet and one exit:
             min = mout = m    (kg/s)

• When kinetic and potential energies are negligible,
  and there is no work interaction
             Q = m∆h = mc p ∆T          (kJ/s)
                                                   (1-18)
Surface Energy Balance
1.5 Heat Transfer Mechanisms
• Heat can be transferred in three basic modes:
  – conduction,
  – convection,
  – radiation.

• All modes of heat
  transfer require the
  existence of a temperature difference.
• All modes are from the high-temperature
  medium to a lower-temperature one.
1.6 Conduction
• Conduction is 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.
• Conduction can take place in solids,
  liquids, or gases
   – In gases and liquids conduction is due to
     the collisions and diffusion of the
     molecules during their random motion.
   – In solids conduction is due to the
     combination of vibrations of the
     molecules in a lattice and the energy
     transport by free electrons.
Rate of heat conduction ∝
                                 ( Area )( Temperature difference )
                                            Thickness
             T1 − T2        ∆T
Qcond = kA           = − kA      (W)   (1-21)
               ∆x           ∆x



where the constant of proportionality k is the
thermal conductivity of the material.


 In differential form
                dT
   Qcond = −kA        (W)              (1-22)
                dx

which is called Fourier’s law of heat conduction.
Thermal Conductivity

• The thermal conductivity of a material is a
  measure of the ability of the material to conduct
  heat.
• High value for thermal conductivity
                      good heat conductor
• Low value
                 poor heat conductor or insulator.
Thermal Conductivities of Materials

• 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.
Thermal Conductivities and Temperature

• The thermal conductivities of materials vary
  with temperature.


• The temperature dependence of thermal
  conductivity causes considerable complexity in
  conduction analysis.


• A material is normally assumed to be isotropic.
k 值之量測儀器與方法
Thermal diffusivity
         Heat conducted    k
      α=                =            ( m2 s )    (1-23)
          Heat stored     ρcp

• The thermal diffusivity represents how fast heat
  diffuses through a material.
• Appears in the transient heat conduction analysis.
• A material that has a high thermal conductivity or a
  low heat capacity will have a large thermal diffusivity.
• The larger the thermal diffusivity, the faster the
  propagation of heat into the medium.
1.7 Convection
   Convection = Conduction + Advection
                            (fluid motion)
• Convection is the mode of energy transfer between a
  solid surface and the adjacent liquid or gas that is in
  motion.
• Convection is commonly
  classified into three sub-modes:
   – Forced convection,
   – Natural (or free) convection,
   – Change of phase
     (liquid/vapor, solid/liquid, etc.)
• The rate of convection heat transfer is expressed by
  Newton’s law of cooling as

           Qconv = hAs (Ts − T∞ )   (W)      (1-24)


• h is the convection heat transfer coefficient in
  W/m2°C.

• h depends on variables such as the surface
  geometry, the nature of fluid motion,
  the properties of the fluid, and the
  bulk fluid velocity.
1.8 Radiation
• Radiation is 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.
• Heat transfer by radiation does not require the presence of
  an intervening medium.
• In heat transfer studies we are interested in thermal
  radiation (radiation emitted by bodies because of their
  temperature).
• Radiation is a volumetric phenomenon. However, radiation
  is usually considered to be a surface phenomenon for
  solids that are opaque to thermal radiation.
Radiation - Emission
• The maximum rate of radiation that can be
  emitted from a surface at a thermodynamic
  temperature Ts (in K or R) is given by the
   Stefan–Boltzmann law as

          Qemit ,max = σ AsTs4   (W)        (1-25)

  σ = 5.670 x 108 (W/m2·K4) is the Stefan–Boltzmann
  constant.

• The idealized surface that emits radiation at this
  maximum rate is called a blackbody.
• The radiation emitted by all real surfaces is
  less than the radiation emitted by a blackbody
  at the same temperature, and is expressed as

          Qemit , real = εσ AsTs4   (W)   (1-26)
          0 ≤ ε ≤1

  ε is the emissivity of the surface.
Radiation - Absorption
• The fraction of the
  radiation energy
   incident on a surface
   that is absorbed by
   the surface is termed
   the absorptivity α.

       0 ≤α ≤1

• Both ε and α of a surface depend on the temperature
  and the wavelength of the radiation.
1.9 Simultaneous Heat Transfer Mechanisms
RPI Chapter 1 Introduction to Heat Transfer Concepts
RPI Chapter 1 Introduction to Heat Transfer Concepts
RPI Chapter 1 Introduction to Heat Transfer Concepts
RPI Chapter 1 Introduction to Heat Transfer Concepts
RPI Chapter 1 Introduction to Heat Transfer Concepts
RPI Chapter 1 Introduction to Heat Transfer Concepts
RPI Chapter 1 Introduction to Heat Transfer Concepts
RPI Chapter 1 Introduction to Heat Transfer Concepts
RPI Chapter 1 Introduction to Heat Transfer Concepts

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RPI Chapter 1 Introduction to Heat Transfer Concepts

  • 1. Chapter 1: Introduction and Basic Concepts Yoav Peles Department of Mechanical, Aerospace and Nuclear Engineering Rensselaer Polytechnic Institute Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.
  • 2. Objectives When you finish studying this chapter, you should be able to: • Understand how thermodynamics and heat transfer are related to each other, • Distinguish thermal energy from other forms of energy, and heat transfer from other forms of energy transfer, • Perform general energy balances as well as surface energy balances, • Understand the basic mechanisms of heat transfer Fourier's law of heat conduction, Newton's law of cooling, and the Stefan–Boltzmann law of radiation, • Identify the mechanisms of heat transfer that occur simultaneously in practice,
  • 3. 1.1 Thermodynamics (熱力學) and Heat Transfer (熱傳) • The science of thermodynamics deals with the amount of heat transfer as a system undergoes a process from one equilibrium state to another, and makes no reference to how long the process will take. • The science of heat transfer deals with the determination of the rates of energy that can be transferred from one system to another as a result of temperature difference.
  • 5. • Thermodynamics deals with equilibrium states and changes from one equilibrium state to another. Heat transfer, on the other hand, deals with systems that lack thermal equilibrium, and thus it is a non-equilibrium phenomenon. • Therefore, the study of heat transfer cannot be based on the principles of thermodynamics alone. • However, the laws of thermodynamics lay the framework for the science of heat transfer.
  • 6. Heat Transfer • The basic requirement for heat transfer is the presence of a temperature difference. • The second law requires that heat be transferred in the direction of decreasing temperature.
  • 7. • The temperature difference is the driving force for heat transfer. • The rate of heat transfer in a certain direction depends on the magnitude of the temperature gradient in that direction. • The larger the temperature gradient, the higher the rate of heat transfer.
  • 8. Application Areas of Heat Transfer
  • 9. 歷史發展 • Caloric theory (1789 Antoine Lavoisier, French): Heat is a fluid-like substance (錯誤!) • James P. Joule (1843, Engilishman): 實驗證明 Heat is not a substance
  • 10. 1.3 Heat (熱) and Other Forms of Energy • Energy can exist in numerous forms such as: – thermal, – mechanical, – kinetic, – potential, – electrical, – magnetic, – chemical, and – 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.
  • 11. • Internal energy may be viewed as the sum of the kinetic and potential energies of the molecules. • The kinetic energy of the molecules is called sensible heat. • The internal energy associated with the phase of a system is called latent heat.
  • 12. • The internal energy associated with the atomic bonds in a molecule is called chemical (or bond) energy. • The internal energy associated with the bonds within the nucleus of the atom itself is called nuclear energy.
  • 13. Internal Energy (u, 內能) and Enthalpy (h, 焓) • In the analysis of systems that involve fluid flow, we frequently encounter the combination of properties u and Pv. • The combination is defined as enthalpy (h = u + Pv). • The term Pv represents the flow energy of the fluid (also called the flow work).
  • 14. Specific Heats of Gases, Liquids, and Solids • Specific heat (比熱) is defined as the energy required to raise the temperature of a unit mass of a substance by one degree (kJ/kg-K). • Two kinds of specific heats: – specific heat at constant volume cv, and – specific heat at constant pressure cp. • The specific heats of a substance, in general, depend on two independent properties such as temperature and pressure. • For an ideal gas, however, they depend on temperature only.
  • 15.
  • 16. Specific Heats • At low pressures all real gases approach ideal gas behavior, and therefore their specific heats depend on temperature only. • A substance whose specific volume (or density) does not change with temperature or pressure is called an incompressible substance. • The constant-volume and constant-pressure specific heats are identical for incompressible substances. • The specific heats of incompressible substances depend on temperature only.
  • 17. Energy Transfer • Energy can be transferred to or from a given mass by two mechanisms: – heat transfer, and – work. • The amount of heat transferred during a process is denoted by Q. • The amount of heat transferred per unit time is called heat transfer rate, and is denoted by Q .
  • 18. • The total amount of heat transfer Q during a time interval ∆t can be determined from ∆t (1-6) Q = ∫ Qdt (J) 0 • The rate of heat transfer per unit area normal to the direction of heat transfer is called heat flux (熱通量), and the average heat flux is expressed as Q q= (W/m 2 ) (1-8) A
  • 19.
  • 20.
  • 21. 1.4 The First Law of Thermodynamics • The first law of thermodynamics states that energy can neither be created nor destroyed during a process; it can only change forms. For the control volume (CV): [入] - [出] + [生成量] = [增加量] =0 Total energy Total energy Change in the entering the - leaving the = total energy of (1-9) system system the system
  • 22. The energy balance for any system undergoing any process can be expressed as (in the rate form) Ein − Eout = dEsystem dt (W) Rate of net energy transfer Rate of change in internal by heat, work, and mass kinetic, potential, etc., energies (1-11)
  • 23. • In heat transfer problems it is convenient to write a heat balance and to treat the conversion of nuclear, chemical, mechanical, and electrical energies into thermal energy as heat generation. • The energy balance in that case can be expressed as Qin − Qout + Egen = ∆Ethermal , system (J) (1-13) Net heat transfer Heat Change in thermal generation energy of the system
  • 24.
  • 25. Energy Balance (i) Closed systems • Stationary closed system, no work: Q = mcv ∆T (J) (1-15)
  • 26. (ii) Steady-Flow Systems • For system with one inlet and one exit: min = mout = m (kg/s) • When kinetic and potential energies are negligible, and there is no work interaction Q = m∆h = mc p ∆T (kJ/s) (1-18)
  • 28.
  • 29.
  • 30.
  • 31.
  • 32. 1.5 Heat Transfer Mechanisms • Heat can be transferred in three basic modes: – conduction, – convection, – radiation. • All modes of heat transfer require the existence of a temperature difference. • All modes are from the high-temperature medium to a lower-temperature one.
  • 33. 1.6 Conduction • Conduction is 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. • Conduction can take place in solids, liquids, or gases – In gases and liquids conduction is due to the collisions and diffusion of the molecules during their random motion. – In solids conduction is due to the combination of vibrations of the molecules in a lattice and the energy transport by free electrons.
  • 34. Rate of heat conduction ∝ ( Area )( Temperature difference ) Thickness T1 − T2 ∆T Qcond = kA = − kA (W) (1-21) ∆x ∆x where the constant of proportionality k is the thermal conductivity of the material. In differential form dT Qcond = −kA (W) (1-22) dx which is called Fourier’s law of heat conduction.
  • 35. Thermal Conductivity • The thermal conductivity of a material is a measure of the ability of the material to conduct heat. • High value for thermal conductivity good heat conductor • Low value poor heat conductor or insulator.
  • 36.
  • 37.
  • 38. Thermal Conductivities of Materials • 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.
  • 39.
  • 40.
  • 41.
  • 42. Thermal Conductivities and Temperature • The thermal conductivities of materials vary with temperature. • The temperature dependence of thermal conductivity causes considerable complexity in conduction analysis. • A material is normally assumed to be isotropic.
  • 43.
  • 45. Thermal diffusivity Heat conducted k α= = ( m2 s ) (1-23) Heat stored ρcp • The thermal diffusivity represents how fast heat diffuses through a material. • Appears in the transient heat conduction analysis. • A material that has a high thermal conductivity or a low heat capacity will have a large thermal diffusivity. • The larger the thermal diffusivity, the faster the propagation of heat into the medium.
  • 46.
  • 47.
  • 48.
  • 49.
  • 50. 1.7 Convection Convection = Conduction + Advection (fluid motion) • Convection is the mode of energy transfer between a solid surface and the adjacent liquid or gas that is in motion. • Convection is commonly classified into three sub-modes: – Forced convection, – Natural (or free) convection, – Change of phase (liquid/vapor, solid/liquid, etc.)
  • 51.
  • 52. • The rate of convection heat transfer is expressed by Newton’s law of cooling as Qconv = hAs (Ts − T∞ ) (W) (1-24) • h is the convection heat transfer coefficient in W/m2°C. • h depends on variables such as the surface geometry, the nature of fluid motion, the properties of the fluid, and the bulk fluid velocity.
  • 53.
  • 54.
  • 55.
  • 56. 1.8 Radiation • Radiation is 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. • Heat transfer by radiation does not require the presence of an intervening medium. • In heat transfer studies we are interested in thermal radiation (radiation emitted by bodies because of their temperature). • Radiation is a volumetric phenomenon. However, radiation is usually considered to be a surface phenomenon for solids that are opaque to thermal radiation.
  • 57. Radiation - Emission • The maximum rate of radiation that can be emitted from a surface at a thermodynamic temperature Ts (in K or R) is given by the Stefan–Boltzmann law as Qemit ,max = σ AsTs4 (W) (1-25) σ = 5.670 x 108 (W/m2·K4) is the Stefan–Boltzmann constant. • The idealized surface that emits radiation at this maximum rate is called a blackbody.
  • 58.
  • 59. • The radiation emitted by all real surfaces is less than the radiation emitted by a blackbody at the same temperature, and is expressed as Qemit , real = εσ AsTs4 (W) (1-26) 0 ≤ ε ≤1 ε is the emissivity of the surface.
  • 60.
  • 61. Radiation - Absorption • The fraction of the radiation energy incident on a surface that is absorbed by the surface is termed the absorptivity α. 0 ≤α ≤1 • Both ε and α of a surface depend on the temperature and the wavelength of the radiation.
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  • 63.
  • 64.
  • 65. 1.9 Simultaneous Heat Transfer Mechanisms