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Introduction to Thermodynamics II

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    Thermo

    Thermodynamics

    dynamics

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    3CHAPTERCHAPTER

    The First Law ofThermodynamics:

    Closed Systems

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    Chapter SummaryChapter Summary

    The first law of thermodynamics is essentially

    an expression of the conservation of energy

    principle. Energy can cross the boundaries of

    a closed system in the form of heat or work.

    If the energy transfer across the boundaries of

    a closed system is due

    to a temperature difference, it is heat;

    otherwise, it is work.

    3-22

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    Chapter SummaryChapter Summary

    Heat is transferred in three ways: conduction,convection, and radiation.

    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 theparticles.

    Convection is 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. 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.

    3-23

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    Chapter SummaryChapter Summary

    The three modes of heat transfer are expressed

    as:

    3-24

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    Various forms of work are expressed as follows:

    Electricalwork: (kJ)

    Boundarywork: (kJ)

    Gravitationalwork(=DPE): (kJ)

    Accelerationwork(=DKE): (kJ)

    Shaftwork: (kJ)

    Spring work: (kJ)

    Chapter SummaryChapter Summary3-25

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    Chapter SummaryChapter Summary

    For the ploytropicprocess (Pvn = constant) of real

    gases, the boundary work can be expressed as:

    3-26

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    Chapter SummaryChapter Summary

    The energy balance foranysystemundergoing

    anyprocesscan be expressed as:

    3-27

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    Chapter SummaryChapter Summary

    The energy balances foranysystemundergoing

    anyprocesscan be expressed in the rateformas:

    3-28

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    Chapter SummaryChapter Summary

    For a constant-pressureprocess, .

    Thus

    3-30

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    Chapter SummaryChapter Summary

    The amount of energy needed to raise the

    temperature of a unit of mass of a substance by

    one degree is called the specificheatatconstant

    volume Cv for a constant-volume process and thespecificheatatconstantpressure Cp for a

    constant pressure process. They are defined as:

    3-31

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    Chapter SummaryChapter Summary

    For ideal gases u, h, Cv, and Cp are functions of

    temperature alone. The #uand #h of ideal gases

    can be expressed as:

    3-32

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    Chapter SummaryChapter Summary

    For ideal gases Cv, and Cp are related by:

    3-33

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    Chapter SummaryChapter Summary

    The specificheatratiok is defined as:

    3-34

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    Chapter SummaryChapter Summary

    Forincompressiblesubstances(liquids and

    solids), both the constant-pressure and constant-

    volume specific heats are identical and denoted by

    C:

    3-35

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    Chapter SummaryChapter Summary

    The uand h of incompressible substances are

    given by

    3-36

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    Chapter SummaryChapter Summary

    The refrigeration and freezing of foods is a major

    application area of thermodynamics.

    3-37

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    Heat TransferHeat Transfer3-1

    (Fig. 3-3)

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    Adiabatic ProcessAdiabatic Process

    (Fig. 3-4)

    3-2

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    Convection: Heat TransferConvection: Heat Transfer

    (Fig. 3-8)

    3-3

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    Convection: CoolingConvection: Cooling

    (Fig. 3-9)

    3-4

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    RadiationRadiation

    (Fig. 3-10)

    3-5

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    Heat and WorkHeat and Work

    (Fig. 3-15)

    3-6

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    Path FunctionsPath Functions

    (Fig. 3-16)

    3-7

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    Boundary WorkBoundary Work

    (Fig. 3-27)

    3-8

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    Net Work per CycleNet Work per Cycle

    (Fig. 3-29)

    3-9

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    Schematic/Diagram for Ex. 3-8Schematic/Diagram for Ex. 3-8

    (Fig. 3-31)

    3-10

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    Schematic/Diagram for Ex. 3-9Schematic/Diagram for Ex. 3-9

    (Fig. 3-32)

    3-11

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    Schematic/Diagram for thePolytropic ProcessSchematic/Diagram for thePolytropic Process

    (Fig. 3-33)

    3-12

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    Schematic/Diagram for Ex. 3-13Schematic/Diagram for Ex. 3-13

    (Fig. 3-43)

    3-13

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    Stretching a Liquid FilmStretching a Liquid Film

    (Fig. 3-45)

    3-14

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    System Energy ChangeSystem Energy Change

    (Fig. 3-52)

    3-15

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    Energy Change for a CycleEnergy Change for a Cycle

    (Fig. 3-54)

    3-16

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    Closed-Systems, First-LawClosed-Systems, First-Law

    (Fig. 3-55)

    3-17

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    Formal Definitions ofCv and CpFormal Definitions ofCv and Cp

    (Fig. 3-72)

    3-18

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    Specific Heats for Some GasesSpecific Heats for Some Gases

    (Fig. 3-76)

    3-19

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    Three Ways to Calculate uThree Ways to Calculate u3-20

    (Fig. 3-80)

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    Typical Freezing Curve (food)Typical Freezing Curve (food)

    (Fig. 3-91)

    3-21


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