Revision on Important Concepts

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    Revision on Important Concepts

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    111 RT V P =

    2211 V PV P

    =

    Check the right unit to use for P and T when R = 8.314 J/mol.K is used.

    Given

    Find P 2 using the following equation (revise polytropic process)

    Calculate W using the equation given but ensure the right unit is used so that W is in J.Then find internal energy using first law.

    12 2V V =

    W QU +=0

    Ans. 1499.8 J

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    4

    1

    2

    1

    2 lnlnPP

    RT T

    C S P =

    1

    2

    1

    2 lnlnV V

    RT T

    C S V +=

    Or, derive the following equation from dS = dQ/T and dU = dQ + dW

    Important: Do not assume 1 mol. Check if amount or volume is informed.

    In this case, calculate the no. of mole since volume is given.nRT PV t =

    ( )12 T T nC U V = Ans. 20.79 J/K for both (a) and (b)

    Note that the work from stirrer is not the same as the work of gas. Do

    not assume W = 0 for part (b) stirrer gas W W QW QU ++=+=

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    5

    There are many ways to prove this equation.You may start with either of the following together with use of Maxwells equations.

    ( )

    dV

    V

    U dT

    T

    U dU

    V T U U

    T V

    +

    =

    = ,

    PdV TdS dU =

    ( )

    dV V

    S dT

    T

    S dS

    V T S S

    T V

    +

    =

    = ,

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    Ans. 331.2 K, y 1 = 0.67, y 2 = 0.33

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    BUBL P / DEW P Calculation

    7

    sat sat P xP xP 222111 +=

    sat iiii P xP y: Laws Raoult' Modified =

    sat sat P y

    P y

    P

    22

    2

    11

    1

    1

    +

    =

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    BUBL T Calculation

    (1. by iteration to convergence)

    Pconstant given ,T xT xT byT initial Estimate1. sat 22sat

    11 +=

    T initial from /PPand , , A,Find 2. sat 2sat

    121

    ii

    isat i C P A

    BT

    =

    ln

    / 2211 x xP

    P

    fromP newFind 3.

    sat 1

    sat 1

    +=

    equation Antoineinto3Step fromPinsertingbyT newFind 4. sat 1

    T new fromvaluesthose find but 2Stepto Return5.

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    BUBL T Calculation

    (2. by trial)

    Pconstant given ,T xT xT byT initial Estimate1. sat 22sat

    11 +=

    T initial fromPand P , , A,Find 2. sat 2sat

    121

    ii

    isat i C P A

    BT

    =

    ln

    Pgiventoequalisit if seetoequationP BUBLintoubstituteS 3.

    3)Step fromPcalculated on(dependingT newareguessnot, If 4.

    sat sat P xP xP 222111 +=

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    Solution ThermodynamicsChemical potential (by definition)

    the change in energy when an infinitesimal number of particles ofspecies i is added at const T & P

    At equilibrium,Partial property (by definition)

    Measure of response of total property nM to the addition at const T & Pof a differential amount of species i to a finite amount of solution

    ii =

    ( ) jnPT i

    i nnG

    ,,

    ( ) jnPT i

    i nnM

    M ,,

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    Solution Thermodynamics

    Total property from summability relation

    Gibbs/Duhem equation

    Must be satisfied for all changes in P, T, and partial property in ahomogeneous phase

    =i

    ii M x M

    dT T

    M dP

    P M

    M d x

    xP xT i

    ii

    ,,

    +

    =

    P)&T const (at 0 M d xi ii =

    ( ) ,... ,...,n ,nT,P,n nM i21= From

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    Solution ThermodynamicsPartial property for binary system at const T & P

    121 dx

    dM x M M +=

    112 dx

    dM x M M =

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    Solution ThermodynamicsParallelism

    Ideal gas mixture model: Gibbs theorem

    Apply to get partial properties from pure-species properties

    Combined with summability relation to get solution properties

    ( ) iii V PU H vs. nV PnU nH +=+=

    ( ) ( ) igiigiiigiigi V M that provided pT M PT M = ,,

    igi

    igi

    igi

    igi

    igi

    igi GS H fromGS H Calculate ,,,,

    igi

    igi

    igi

    igigig GS H fromGS H Calculate ,,,,

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    Solution ThermodynamicsFugacity, f vs. fugacity coefficient, = f /P

    For an ideal gas, f = P and = f /P = 1For a real gas, f = P (for simplicity, i is omitted)

    Knowing

    At any P, use cubic equations of state

    or generalized correlation for Z

    At low to moderate P, use generalized correlation for B( )( ) 10=

    ( )+= 10

    exp B BT P

    r

    r

    ( )P

    dP Z

    RT

    G P R

    ==

    01ln

    ( ) qI Z Z = ln1ln

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    Solution ThermodynamicsFugacity, f vs. fugacity coefficient, = f /P

    For an ideal gas, f = P and = f /P = 1For a real gas, f = P (for simplicity, i is omitted)For a pure liquid,

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    vnvn

    nn

    yo

    iioii +

    +==

    +

    +==

    j j j

    j j jiiii vn

    vn

    nn

    y

    0

    ,0 (multireaction)i = species

    j = reaction index

    (single reaction)

    K PP

    y iiii

    = o)( K x iiii

    = )(Ans. 70%