1 mol ideal gas, PV=RT, show the entropy can be written as! S = C v. lnt + RlnV + cons tant
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1 1 mol ideal gas, PV=RT, show the entropy can be written as! S = C v lnt + RlnV + cons tant
2 (1) p, V, T change Reversible isothermal process (const. T) TdS=du-!W"!S = # "Q r = Q r T T Q r = $W = # pdv = # nrt dv V!S = nr 1 V dv # = nrln V 2 V 1 = nrln P 1 P 2
3 Reversible isochoric process (const. V) HEATING TdS=du-!W" TdS = du = C v dt T 2!S = " C vdt = C v ln( T 2 ) T T 1 T 1 C v = T (!S!T ) v
4 Reversible isobaric process (const. P) TdS=du-!W" HEATING TdS = d(u + pv ) = dh = C p dt T 2!S = " C p dt = C p ln( T 2 ) T T 1 T 1 C p = T (!S!T ) p
5 A( 1mol, g, V1, T1)!B(1 mol, g,v2,t2)" P (P1,V1,T1) const. V (Px,V1,T2) const. T (P2,V2,T2) T 2!S 1 = " C vdt = C v ln( T 2 ) T T 1 T 1!S 2 = Rln V 2 V 1 = Rln P 1 P 2 V!S = C V,m ln T 2 T 1 + Rln V 2 V 1
6 A( 1mol, g, V1, T1)!B(1 mol, g,v2,t2)" TdS = du + pdv du = C v dt P = RT V TdS = C v dt + RT V dv ds = C v T dt + R V dv!s = C v ln T 2 T 1 + Rln V 2 V 1
7 P A( 1mol, g, P1, T1)!B(1 mol, g,p2,t2)" const. P (P1,V1,T1) (P1,Vx,T2) const. T T 2!S 1 = " C p dt = C p ln( T 2 ) T T 1 T 1 (P2,V2,T2) V!S 2 = Rln V 2 V 1 = Rln P 1 P 2!S = C p,m ln T 2 T 1 or!s = C p,m ln T 2 T 1 + Rln V 2 V 1 " Rln P 2 P 1
8 A( 1mol, g, V1, T1)!B(1 mol, g,v2,t2)" TdS = du + pdv du = dh! pdv! Vdp TdS = dh! VdP dh = C p dt V = RT P TdS = C p dt! RT P dp ds = C p T dt! R p dp "S = C p ln T 2 T 1! Rln P 2 P 1
9 A( 1mol, g, P1,V1)!B(1 mol, g,p2, V2)" Proof "!S = C p ln V 2 V 1 + C V ln p 2 p 1 We already have!!s = C p ln T 2 T 1 " Rln P 2 P 1 Ideal gas! T 2 T 1 = P 2 V 2 P 1 V 1!S = C p ln P 2 V 2 P 1 V 1 " Rln P 2 P 1 = C p ln V 2 V 1 + (C p " R)ln P 2 P 1 = C p ln V 2 V 1 + C V ln P 2 P 1
10 !S = C p ln V 2 V 1 + C V ln p 2 p 1 can be used to determine isentropic relationships between properties in states 1 and 2!!S = C p ln V 2 V 1 + C V ln p 2 p 1 = 0 C p C v ln V 2 V 1 + ln p 2 p 1 = 0 define C p C v =! ln[ p 2 p 1 ( V 2 V 1 )! ] = 0 Isentropic compression process on a T-S diagram! P 2 V 2! = P 1 V 1! What we have for adiabatic process (isentropic process)!
11 (2) mixing of different perfect gas at constant temperature and constant pressure mixing at constant T, p n 1 n 2 n 1 +n 2 T, p, V 1 T, p,v 2 T, p, V 1 +V 2 Two steps (1) n 1 T, p, V 1 n 1 T, p 1, V 1 +V 2 (2) n 2 T, p,v 2 n 2 T, p 2, V 1 +V 2 V 2!S = nrt " 1 dv = nrtln V 2 V V 1 V 1
12 (2) mixing of different perfect gas at constant temperature and constant pressure mixing at constant T, p n 1 n 2 n 1 +n 2 T, p, V 1 T, p,v 2 T, p, V 1 +V 2 at constant T, p! mix S = (n 1 Rlny 1 n 2 Rlny 2 ) y 1 1 y 2 1 so! mix S
13 ! mix S = (n 1 Rlny 1 n 2 Rlny 2 ) y 1 1 y 2 1 so! mix S
14
15 2. The phase transition (1) The phase transition at transition temperature At constant T, p, the two phase in the system are in equilibrium, the process is reversible, and W" so Q p!h! fus H m! vap H m S m (s) S m (l) S m (g)
16
17 (2) irreversible phase transition eg.!s!s!s!s
18 Supercooled Water " Supercooling was discovered already in 1724 by Fahrenheit, but even today the phenomenon remains a subject for intense discussions.! Supercooled water freezes at different temperatures in the presence of a surface with a positive or negative charge Science 2010, 327, 672. Supercool: Water Doesn't Have to Freeze Until -48 C (-55 F) Nature, 2011, 479, 506
19
20
21 For example H 2 O l, 90,100kPa)!S =? Irreversible H 2 O g, 90, 100kPa)!S 1!S 3!S 2 H 2 O l, 100, 100kPa) H 2 O g, 100, 100kPa) Reversible!S!S!S!S
22 Absolute Entropies "
23 "S m =S m (298.15K) S m (0K)= J/K mol.!
24
25 2.2 The third law The third law Nernst heat theorem (1905): The entropy change accompanying any physical or chemical transformation approaches zero as the temperature approaches zero:!s!0,!t!0 More general and useful formulation! Planck (1911): The entropy of all perfect crystalline substance is zero at 0 K. S * (perfect crystalline 0 K) -
26 Lowest Achieved Temperature! Achieved by MIT researchers in 2003! 0.45 nk =4.5 x K! You can approach 0K, but can not reach the limit.!
27 2.2.3 The entropy change of chemical reaction For reaction aa b B #yy zz! r S! m( T) $! S! m B,%,T )! r S! m (298.15K) $! S! m B, %,298.15K )! r S! m (T) = ys! m (Y, %,T ) z S! m (Z, %,T ) a S! m (A, %,T ) b S! m (B, %,T )
28 Standard entropy S o (at K and 1 bar)!
29
30 2.3 Helmholtz and Gibbs energies- Criteria for Spontaneous Change The 2 nd Law gave the Clausius inequality TdS &Q du = &Q +&W &W=-pdV 1 st Law TdS du+pdv Combined statement of 1 st and 2 nd Law "
31 Use the general criterion to under specific conditions " TdS du+pdv
32 TdS du+pdv
33 TdS du+pdv
34 TdS du+pdv
35
36 TdS du+pdv For constant V and constant T=T surr, equilibrium is achieved! when the Helmholtz free energy is minimized!
37 TdS du+pdv For constant P=P ext and constant T=T surr, equilibrium is achieved when the Gibbs free energy is minimized!
38
39 2.3.3 Calculation of!a and!g (1) change p,v at constant temperature du = TdS - pdv A =U-TS da = - SdT - pdv at constant T, reversible da T pdv V 2!A T = "# pdv V 1 closed system, change p,v at constant T, W! 0 reversible process For perfect gas
40 du = TdS - pdv H =U+PV G=H-TS dg = - SdT + Vdp at constant T, reversible dg T Vdp closed system, change p,v at constant T, reversible process For an perfect gas
41 (2) phase transition (i) reversible phase transition G =H - (TS)!G =!H-!(TS) =!H- T!S reversible phase transition at constant T and p!h =T!S!G=!H- T!S = 0
42 (i) reversible phase transition A = U - (TS)!A =!U -!(TS) =!U - T!S reversible vaporization or sublimation at constant T and p, and vapor is an perfect gas!u =!H-!(pV) =!H- p!v =!H- nrt!a =!U -!(TS) =!H - nrt - T!S = - nrt (ii) irreversible phase transition
43 2.3.4 Fundamental relations of thermodynamic functions U, H, S, A, G, p, V and T H = U + pv
44 1. Fundamental equations of thermodynamic For a reversible change If &W r " 0 then &W r pdv &Q r TdS du=&q r +&W r H =U+pV A =U-TS G =H-TS du = TdS - pdv dh = TdS + Vdp da = - SdT - pdv dg = - SdT + Vdp closed system of constant composition reversible process volume work only. Fundamental equation of thermodynamic
45 dz = M dx + N dy du = TdS pdv dh = TdS + Vdp da = SdT pdv dg = SdT + Vdp
46 2. Maxwell s relation dz = M dx + N dy du = TdS pdv dh = TdS + Vdp da = SdT pdv dg = SdT + Vdp
47 Quotient Rule for Derivatives! Product Rule! [ f (x) g(x) ]' = [ f (x) 1 g(x) ]' = f (x)[ 1 g(x) ]'+ f (x)' 1 g(x) =! f (x)g'(x) g 2 (x) = + f (x)' 1 g(x) f (x)'g(x)! f (x)g'(x) g 2 (x)
48 3. Gibbs - helmholtz equation dg = SdT + Vdp " # $!(G / T )!T % & ' = ( H V T 2
49 3. Gibbs - helmholtz equation " # $!(A / T )!T % & ' = V T " # $! A!T % & ' " ( A!T # $!T V T 2 =!TS! A T 2 % & ' V da = SdT pdv =! U T 2 " # $!(A / T )!T % & ' = ( U V T 2
50 2.4 Chemical potential Chemical potential Consider a system that consists of a single homogeneous phase whose composition can be varied G f (T p n A n B ) Total differential
51
52 Chemical potential is an intensive state function. µ B of pure substance G * (T p n B ) = n B G * m,b (T p )
53 Heterogeneous system du = " T! ds! #" p! dv! + " µ! dn! B B!! "! B
54 2.4.2 Equilibrium criterion of substance (1) Condition of phase equilibrium dn B B(') B(% ) T p µ B! = µ B " Condition of phase equilibrium µ B! > µ B " '!% spontaneous
55 (2) Condition of chemical reaction equilibrium Chemical reaction Homogeneous system d" $v B µ B 0 d" 0 spontaneous $v B µ B 0 equilibrium For example aa bb yy zz aµ A +bµ B yµ Y +zµ Z
56 A potential of chemical reaction aa bb yy zz A= (aµ A +bµ B ) -( yµ Y +zµ Z ) A 0 at equilibrium A 0 right spontaneous A 0 left spontaneous
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