7 the first law of thermodynamics (adv)

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  • 7/30/2019 7 the First Law of Thermodynamics (Adv)

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    Lecture 2 The First Law of Thermodynamics (Ch.1)

    Lecture 1 - we introduced macroscopic parameters that describethe state of a thermodynamic system (including temperature), the

    equation of state f(P,V,T) = 0, and linked the internal energy ofthe ideal gas to its temperature.

    Outline:

    1. Internal Energy, Work, Heating

    2. Energy Conservation the First Law

    3. Enthalpy

    4. Heat Capacity

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    Internal Energy

    systemU = kinetic + potential

    system

    boundary

    environment

    The internal energy of a system of particles, U, is the sum of the kineticenergy in the reference frame in which the center of mass is at rest and the

    potential energy arising from the forces of the particles on each other.

    Difference between the total energy and the internal energy?

    The internal energy is a state function it depends only on

    the values of macroparameters (the state of a system), not

    on the method of preparation of this state (the path in the

    macroparameter space is irrelevant).

    U = U (V, T)In equilibrium [ f(P,V,T)=0 ] :

    U depends on the kinetic energy of particles in a system and an averageinter-particle distance (~ V-1/3) interactions.

    P

    VT A

    B

    For an ideal gas (no interactions) :

    U = U (T) - pure kinetic

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    Work and Heating (Heat)

    We are often interested in U , not U. U isdue to:Q - energy flow between a system and itsenvironment due to T across a boundary and a finite

    thermal conductivity of the boundary

    heating (Q > 0) /cooling (Q < 0)(there is no such physical quantity as heat; to

    emphasize this fact, it is better to use the term

    heating rather than heat)

    W - any other kind of energy transfer acrossboundary - work

    Heating/cooling processes:

    conduction: the energy transfer by molecular contact fast-movingmolecules transfer energy to slow-moving molecules by collisions;

    convection: by macroscopic motion of gas or liquid

    radiation: by emission/absorption of electromagnetic radiation.

    HEATING

    WORK

    Work and Heating are both defined to describe energy transfer

    across a system boundary.

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    The First Law

    For a cyclic process (Ui = Uf) Q= - W.If, in addition, Q = 0 then W =0

    Perpetual motion machines come in two types: type 1 violates

    the 1st Law (energy would be created from nothing), type 2 violates

    the 2nd Law (the energy is extracted from a reservoir in a way that

    causes the net entropy of the machine+reservoir to decrease).

    The first law of thermodynamics: the internal energy of a system can be

    changed by doing work on it or by heating/cooling it.

    U = Q + WFrom the microscopic point of view, this statement is equivalent to

    a statement ofconservation of energy.

    P

    VT

    An equivalent formulation:

    Perpetual motion machines of the first type do not exist.

    Sign convention: we considerQ and W to be positive if energy flows

    into the system.

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    Quasi-Static Processes

    Quasi-static (quasi-equilibrium) processes sufficiently

    slow processes, any intermediate state can be consideredas an equilibrium state (the macroparamers are well-

    defined for all intermediate states).

    Examples ofquasi-

    equilibrium processes:

    isochoric: V = const

    isobaric: P = const

    isothermal: T = const

    adiabatic: Q = 0

    For quasi-equilibrium processes, P, V, T are

    well-defined the path between two statesis a continuouslines in the P, V,T space.

    P

    V

    T

    1

    2

    Advantage: the state of a system that participates in a quasi-equilibriumprocess can be described with the same (small) number of macro

    parameters as for a system in equilibrium (e.g., for an ideal gas in quasi-equilibrium processes, this could be T and P). By contrast, for non-equilibrium processes (e.g. turbulent flow of gas), we need a huge numberof macro parameters.

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    Work

    The sign: if the volume is decreased, W is positive(bycompressing gas, we increase its internal energy); if the

    volume is increased, W is negative (the gas decreasesits internal energy by doing some work on the

    environment).

    2

    1

    ),(21V

    V

    dVVTPW

    The workdone by an external forceon a gasenclosed within a cylinder fitted with a piston:

    W =(PA) dx = P (Adx) = - PdV

    x

    P

    W = - PdV - applies to anyshape of system boundary

    The work is not necessarily associated with the volume changes e.g.,

    in the Joules experiments on determining the mechanical equivalent of

    heat, the system (water) was heated by stirring.

    dU = Q PdV

    A the

    pistonarea

    force

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    W and Qare not State Functions

    P

    V

    P2

    P1

    V1 V2

    A B

    CD

    - the work is negative for the clockwise cycle; if

    the cyclic process were carried out in the reverse

    order (counterclockwise), the net work done on

    the gas would be positive.

    01212

    211122

    VVPP

    VVPVVPWWW CDABnet

    2

    1

    ),(21V

    VdVVTPW

    - we can bring the system from state 1 to

    state 2 along infinite # of paths, and for each

    path P(T,V) will be different.

    U is a state function, W - is not thus, Qisnot a state function either.

    U = Q + W

    Since the work done on a system depends not

    only on the initial and final states, but also on theintermediate states, it is not a state function.

    PV diagram

    P

    V

    T1

    2

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    Comment on State Functions

    U, P, T, and V are the state functions, Q and W are not. Specifying an initial and finalstates of a system does not fix the values of Q and W, we need to know the wholeprocess (the intermediate states). Analogy: in classical mechanics, if a force is not

    conservative (e.g., friction), the initial and final positions do not determine the work, the

    entire path must be specified.

    x

    y z(x1,y1)

    z(x2,y2)

    dyy

    zdx

    x

    zzd

    xy

    dyyxAdxyxAad yx ,, - it is an exact differential if it is

    x

    yxA

    y

    yxA yx

    ,,

    yxzdyydxxzad ,, the difference between the values of some (state) function

    z(x,y) at these points:

    A necessary and sufficient condition for this:

    If this condition

    holds:

    y

    yxzyxA

    x

    yxzyxA yx

    ,,

    ,,

    e.g., for an ideal gas:

    dV

    V

    TdT

    fNkPdVdUQ

    B 2 - cross derivatives

    are not equal

    dVPSdTUd

    U

    VS- an exact differential

    In math terms, Q and W are not exact differentials of some functionsof macroparameters. To emphasize that W and Q are NOT the statefunctions, we will use sometimes the curled symbols (instead ofd)for their increments (Q and W).

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    Problem

    Imagine that an ideal monatomic gas is taken from its initial state A to stateB by an isothermalprocess, from B to C by an isobaricprocess, and fromC back to its initial state A by an isochoricprocess. Fill in the signs ofQ,W, and U for each step.

    V, m3

    P,105Pa

    A

    BC

    Step Q W UA B

    B C

    C A

    2

    1

    1 2

    + -- 0

    -- + --

    + 0 +

    T=const

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    Another Problem

    During the ascent of a meteorological helium-gas filled balloon,

    its volume increases from Vi = 1 m3 to Vf = 1.8 m

    3, and the

    pressure inside the balloon decreases from 1 bar (=105 N/m2) to

    0.5 bar. Assume that the pressure changes linearly with volume

    between Vi and Vf.(a) If the initialT is 300K, what is the finalT?(b) How much work is done by the gas in the balloon?(c) How much heat does the gas absorb, if any?

    P

    V

    Pf

    P i

    Vi Vf

    K2701mbar1

    1.8mbar5.0K300

    3

    3

    ii

    ff

    if

    B

    BVP

    VPTT

    Nk

    PVTTNkPV

    (a)

    (b) f

    i

    V

    V

    ON dVVPW )(

    bar625.1bar/m625.0 3 VVP

    (c) ONWQU

    Jmbarmbarmbar 333 41066.04.05.08.05.0)( f

    i

    V

    V

    BY dVVPW

    - work done on a system f

    i

    V

    V

    BY dVVPW )( - work done by a system

    BYON WW

    JJJ 445 105.41061.0105.112

    3

    2

    3

    BY

    i

    f

    iiONifBON WT

    TVPWTTNkWUQ

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    Quasistatic Processes in an Ideal Gas

    isochoric ( V = const )

    isobaric ( P = const )

    021 W

    TCTTNkQ VB 02

    31221

    0),( 122

    1

    21 VVPdVTVPW

    TCTTNkQ PB 02

    51221

    21QdU

    2121 QWdU

    V

    P

    V1,2

    PV= NkBT1

    PV= NkBT21

    2

    V

    P

    V1

    PV= NkBT1

    PV= NkBT21

    2

    V2

    (see the last slide)

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    Isothermal Process in an Ideal Gas

    1

    221 ln),(

    2

    1

    2

    1V

    VTNk

    V

    dVTNkdVTVPW B

    V

    V

    B

    V

    V

    f

    iBfi

    V

    VTNkW ln

    Wi-f> 0 ifVi>Vf (compression)

    Wi-f< 0 ifVi

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    Adiabatic Process in an Ideal Gas

    adiabatic(thermallyisolatedsystem)

    PdVdTNkf

    dUTNkf

    U BB 22

    ( f the # of unfrozen degrees of freedom )

    dTNkVdPPdVTNkPV BB PVPdVfVdPPdV 2

    fP

    dP

    fV

    dV 21,0

    21

    constVPPVP

    P

    V

    V

    111

    1lnln

    The amount of work needed to change the state of a thermally isolated systemdepends only on the initialand finalstates and not on the intermediate states.

    021 Q 21WdU

    to calculate W1-2 , we need to know P(V,T)

    for an adiabatic process

    2

    1

    ),(21

    V

    V

    dVTVPW

    0

    11

    P

    P

    V

    VP

    dP

    V

    dV

    V

    P

    V1

    PV= NkBT1

    PV= NkBT21

    2

    V2

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    Adiabatic Process in an Ideal Gas (cont.)

    V

    P

    V1

    PV= NkBT1

    PV= NkBT21

    2

    1

    1

    1

    2

    11

    1121

    11

    1

    1

    ),(2

    1

    2

    1

    VVVP

    dVV

    VPdVTVPW

    V

    V

    V

    V

    1+2/31.67 (monatomic), 1+2/5 =1.4 (diatomic), 1+2/6 1.33 (polyatomic)(again, neglecting the vibrational degrees of freedom)

    constVPPV

    11

    An adiabata is steeper than an isotherma:

    in an adiabatic process, the work flowing

    out of the gas comes at the expense of its

    thermal energy its temperature will

    decrease.V2

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    Problem

    Imagine that we rapidly compress a sample of air whose initial pressure is

    105 Pa and temperature is 220C (= 295 K) to a volume that is a quarter of

    its original volume (e.g., pumping bikes tire). What is its final temperature?

    2211

    222

    111

    VPVP

    TNkVP

    TNkVP

    B

    B

    1

    2

    1

    2

    12

    1

    1121

    2

    11

    2

    112T

    T

    V

    VTT

    VPTNkV

    VP

    V

    VPP B

    constVTVT 1

    22

    1

    11

    KKKV

    VTT 51474.12954295 4.0

    1

    2

    112

    For adiabatic processes:

    Rapid compression approx. adiabatic, no time for the energyexchange with the environment due to thermal conductivity

    constTP

    /1

    also

    - poor approx. for a bike pump, works better for diesel engines

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    Non-equilibrium Adiabatic Processes

    - applies only to quasi-equilibrium processes !!!constTV 1

    2. On the other hand, U = Q + W = 0U ~ T T unchanged

    (agrees with experimental finding)

    Contradiction because approach

    #1 cannot be justified violent

    expansion of gas is not a quasi-

    static process. T must remain the

    same.

    (Joules Free-Expansion Experiment)

    constTV 11. V increases T decreases (cooling)

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    The Enthalpy

    Isobaric processes (P = const):

    dU = Q - PV = Q -(PV) Q = U +(PV)

    The enthalpy is a state function, because U, P,

    and V are state functions. In isobaric processes,the energy received by a system by heating equalsto the change in enthalpy.

    Q = Hisochoric:

    isobaric:

    in both cases, Qdoes not

    depend on the

    path from 1 to 2.

    Consequence: the energy released (absorbed) in chemical reactions at constantvolume (pressure) depends only on the initial and final states of a system.

    H U + PV - the enthalpy

    The enthalpy of an ideal gas:

    (depends on T only)

    TNkf

    TNkTNkf

    PVUH BBB

    1

    22

    Q = U

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    Heat Capacity

    T

    QC

    The heat capacity of a system - the amount of energytransfer due to heating required to produce a unit

    temperature rise in that system

    Cis NOT a state function (since Q is not astate function) it depends on the path

    between two states of a system

    T

    V

    T1

    T1+dT

    i

    f1 f2 f3

    The specific heat capacitym

    Cc

    ( isothermic C =, adiabatic C = 0 )

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    CV and CP

    dT

    PdVdU

    dT

    QC

    VV

    T

    U

    C

    the heat capacity atconstant volume

    the heat capacity atconstant pressure

    P

    PT

    HC

    To find CP and CV, we need f(P,V,T) = 0 and U = U (V,T)

    dT

    dVP

    V

    U

    T

    U

    dVV

    UdT

    T

    UdU

    dT

    PdVdUC

    TV

    TV

    PT

    VPdT

    dVP

    V

    UCC

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    CV and CPforan Ideal Gas

    nRf

    Nkf

    C BV22

    CV = dU/dT

    3/2NkB

    5/2NkB

    7/2NkB

    10 100 1000 T, K

    Translation

    Rotation

    Vibration

    CV

    of one mole of H2

    R

    NkP

    Nk

    PdT

    dV

    PV

    U

    CC BB

    PTVP

    ( for one mole )0 nR

    f

    Nkf

    NkCC BBVP

    12

    1

    2

    For an ideal gas

    TNkf

    U B2

    # of moles

    For one mole of a monatomic ideal gas: RCRCPV 2

    5

    2

    3