Upload
others
View
5
Download
0
Embed Size (px)
Citation preview
1
Physical Chemistry I for BiochemistsChem340Chem340
Lecture 23 (3/07/11)
Yoshitaka IshiiCh 6.10-6.12 HW7
Ch 7.1-7.4
• P6.5) The pressure dependence of G is quite different for gases and condensed phases. Calculate Gm(C, solid, graphite, 100 bar, 298.15 K) and Gm(He, g, 100 bar, 298.15 K) relative to their standard state values. By what factor is the change in G greater for HeBy what factor is the change in Gm greater for He than for graphite?
'),(),(0
000 P
P mmmm dPVTPGTPGG
)()( PPVgraphiteG [Q1] )()( 0PPVgraphiteG mm
)/ln(')/(')( 000PPRTdPPRTdPVHeG
P
P
P
P mm
[Q1]
[Q2]
2
• P6.8) Calculate and for the reaction CH4(g) + 2O2(g) CO2(g) + 2H2O(l) at 298 K from the combustion enthalpy of methane and the entropies of the reactants and productsentropies of the reactants and products.
• Greaction0 is easy to obtain.
• Greaction0 = Hreaction
0 -TSreaction0
The question is how to get Areaction0
A 0 G 0 (PV)• Areaction0 = Greaction
0 - (PV)
= Greaction0 - (ngas)RT Q. How do you get this (PV)?
We had a similar question between U and H.
6.7 Expressing Chemical Equilibrium in Terms of the i
• mAA + mBB + mCC .. mMM + mNN + mOO• We write the reaction in an abbreviated form as
- mAA - mBB - mCC .. + mMM + mNN + mOO =0 A B C M N O
• iXi = 0 (i = -mi if Xi is a reactant; i = mi if Xi is a product).
• dG associated with change in ni is given bydG = idni (*)
Now, we introduce extent of the reaction (0≤ ≤ 1)n = n initial + dn = dni = ni + i dni = i d
ni = niinitial + i = mi(1- ) for reactant
= mi for product
when 100 % of reactants reacted.
3
HW Q2 (text P126-127)• 2NO2(g) ↔ N2O4(g)(2 - 2) mole mole
G = (2 - 2)G NO20 + G N2O4
0
Q3. Where is the equilibrium point?
Gpure (2 2)Gm,NO2 + Gm,N2O4
Gmixture = Gpure + Gmix
Gmix = nNO2RTln(xNO2)
+ nN2O4RTln(xN2O4)
2Gm,NO20
G 0Gm,N2O40
Q1. How much is Greaction0 ?
Greaction0 = - 2Gm,NO2
0 + Gm,N2O40
Q2. How much is Greaction ?
[Q1]
Greaction = Greaction0 - 2RTln(XNO2)+RTln(XN2O4)[Q2]
HW Q3 (text P126-127)• 2NO2(g) ↔ N2O4(g)(2 - 2) mole mole
G = (2 - 2)G NO2(T) + G N2O4(T)
Q1 How do you read Gm,N2O4
from the graph below?
Q2. How about Gm,NO2 ?Gpure (2 2)Gm,NO2(T) + Gm,N2O4(T)Gmixture = Gpure + Gmix
Gmix = nNO2RTln(xNO2)
+ nN2O4RTln(xN2O4)
T =350 K
-120
-115
-110
Plot @ 400K(don’t use itfor HW)
Jmol
-1)
xNO2 = nNO2/{nNO2+nN2O4}= (2-2)/(2-)
Q3. Where is the equilibrium point?
xN2O4 = nN2O4/{nNO2+nN2O4}= /(2-)
-130
-125
120
0 0.5 1
Gpure
Gmixture
G(k
J
4
6.7 Expressing Chemical Equilibrium in Terms of the i
• mAA + mBB + mCC .. mMM + mNN + mOO• We write the reaction in an abbreviated form as
- mAA - mBB - mCC .. + mMM + mNN + mOO =0 A B C M N O
• iXi = 0 (i = -mi if Xi is a reactant; i = mi if Xi is a product).
• dG associated with change in ni is given bydG = idni (*)
Now, we introduce extent of the reaction (0≤ ≤ 1)n = n initial + dn = dni = ni + i dni = i d
From (*)dG = iid = Greactiond
. .
(G/)T,P =0 System reaches equilibrium.
(G/)T,P = ii =Greaction..
• For a compound, consider a formation reaction from elements (A, B): A + 2B C
G 0 G 0 G 0 2G 0
Reaction Gibbs Energy (p127)
Gf0 = Gm,C
0 - Gm,A0 - 2Gm,B
0
• For a reaction (PA=PB=PC=PD=1bar): A +2B C + 2D• Greaction = Gm,C
0 +2Gm,D0 - Gm,A
0 - 2Gm,B0
= Gf,C0 +2 Gf,D
0 - Gf,A0 - 2Gf,B
0
In general,
• Gf0 = Gm,product
0 + i Gm,reactant i0
Greaction0 = iGf.i
0
For a pure element, Gf0 = 0. [Q1]
Greaction0 = iGm.i
0
= iμi0
5
6.8 Calculating Greaction and Introducing the Equilibrium Constant for a Mixture of Ideal Gas• 2A + B ↔3C + D Greaction = iGf.i = 3Gf.C(PC) + Gf.D(PD)
@ Partial Pressure PA, PB, ..
• mAA + mBB ↔ mCC + mDD
reaction i f.i f.C( C) f.D( D)– 2Gf.A (PA) – Gf.B (PB)
= 30C + 3RTln(PC/P0) + 0
D + RTln(PD/P0) - 20
A - 2RTln(PA/P0) - 0B - RTln(PB/P0)
= 30C + 0
D - 20A - 0
B
mBeq
mAeq
mDeq
mceq
p
PP
PP
PP
PP
K
00
00
BA
DC
mAA + mBB ↔ mCC + mDD
Greaction = iGf.i = Greaction0 + iRTln(Pi/P0)
=Greaction0 + RTlnKp
+ [Q1]
Q. What isGreaction0 ? Greaction
0 = iμ0i
6.8 Continued
Greaction = iGf.i = Greaction0 + iRTln(Pi/P0)
=G 0 + RTlnK=Greaction0 + RTlnKp
• At equilibrium, Greaction =0
RTlnKp = -Greaction0 mB
eqmA
eq
mDeq
mceq
p
PP
PP
PP
PP
K
00
00
BA
DC
Thermodynamic Equilibrium Const
Kp = exp(- Greaction0/RT) (at 298K)
When A ↔ B Kp = PA/PB = exp(-G0/RT)
6
6.9 Calculating the Equilibrium Partial Pressure in a Mixture of Ideal Gases
• Cl2(g) ↔ 2Cl(g) For the reaction above, derive an expression for Kp in terms of n0,
, and P assuming the reaction starts from n0 mole of Cl2.
Total n0 + ξeq
Kp = exp(-Greaction0/RT)
Greaction0
= 2Gf, Cl0 - Gf, Cl2
0
6.10 Variation of Kp with T
2
000 1
RT
H
dT
TGd
RdT
RTGd
dT
Kdreactionreactionreactionp
)/()/()ln(
HTG / dT >0 & H > 0 dln(K ) >0 2T
H
T
TG
P
/
Gibbs-Helmholtz
dT
RT
HTKTKK
Tfin
Tini
reactioninipfinpp 2
0
)}(ln{)}(ln{)ln(
dT >0 & H > 0 dln(Kp) >0More product
dT >0 & H < 0 dln(Kp) < 0Less product
KTR
H
RT
H
fin
reaction
Tfin
Tini
reaction
298
1100
KTR
HKKTK
fin
reactionpfinp 298
11)}298(ln{)}(ln{
0- Greaction
0/RT0-Greaction(Tf)/RTf
7
7.10 Conformational Transitions of Biological Polymers
N ↔ DCini(1- fD) CinifD
D
D
iniN
iniD
N
D
f
f
Cf
Cf
C
CK
1
At Tm K =1 & fD = 0.5D
• HW 7 P6.18) Many biological macromolecules undergo a transition called denaturation. Denaturation is a process whereby a structured, biological active molecule, called the native form, unfolds or becomes unstructured and biologically inactive. The equilibrium is N (Native) ↔ D (Denatured)
• For a protein at pH = 2, the enthalpy change associated withFor a protein at pH 2, the enthalpy change associated with denaturation is H° = 418.0 kJ mol–1 and the entropy change is S° = 1.3 kJ K–1 mol–1.
a. Calculate the Gibbs energy change for the denaturation of the protein at pH = 2 and T = 303 K. Assume the enthalpy and entropy are temperature independent between 298.15 and 303 K.
G °(298K) = H °- TS °[Q1 ] GD (298K) = HD - TSD
b. Calculate the equilibrium constant for the denaturation of protein at pH = 2 and T = 303 K.
c. Based on your answers for parts (a) and (b), is protein structurally stable at pH = 2 and T = 303 K?
[Q1 ]
121
122
11
TTH
T
TGTTG D
D [Q2 ]
KD(T2) = exp(- GD/(RT2))
8
6.11 Equilibria Involving Ideal Gases and Solid or Liquid Phase
• We consider equilibrium in a thermal decomposition of CaCO3:
CaCO (s) CaO(s) + CO (g)• CaCO3(s) CaO(s) + CO2(g)
In this case, gas (CO2) is in equilibrium with two solid phase (CaCO3 &CaO)
Greaction = ii = 0
0 = eq(CaO,s,P) + eq(CO2,g,P) - eq(CaCO3,s,P)
(C O P) 0(C O ) (C CO P) 0(C CO )eq(CaO,s,P)~ eq0(CaO,s) ; eq(CaCO3,s,P)~eq
0(CaCO3,s)
0 = 0(CaO,s) + 0(CO2,g) - 0(CaCO3,s) + RTln(PCO2/P0)
Greaction0 = - RTln(PCO2/P0)
6.12 Expressing the Equilibrium Constant in Terms of Mole Fraction
0000 PPx
PPx
PP
PP
mDeq
mceq
mDeq
mceq
DCDC
0
0000
P
P
xx
xx
PPx
PPx
PP
PP
PP
PPK
mBmAmDmc
mBeqmAeq
mDeqmceq
mBeq
mAeq
mBeq
mAeq
p
BA
DC
BABA
0
0
P
PKK
P
PK
PX
X
BA
9
• HW7 P6.14 Consider the equilibrium
NO2(g) NO(g) +1/2O2(g)
One mole of NO2(g) is placed in a vessel and allowed to come to ilib i l f 1 b A l i f h
(1- y) y (1/2) y
equilibrium at a total pressure of 1 bar. An analysis of the contents of the vessel gives the following results:
T 700 K 800 K
PNO/PNO2 0.872 2.50
a. Calculate KP at 700 and 800 K. 2
1
OpNOp 2
1
y
y
1n
n
x
x
p
p872.0
222 NO
NO
NO
NO
NO
NO
@700K
b. Calculate G0reaction for this reaction at 298.15 K,
assuming that H0reaction is independent of temperature.
2
1
21
2
2
21
px
xx
p
Op
NOp
NOp
pNOp
pOp
pNOp
KNO
ONO2
21
2
2
p
p
HW8 P6.15• Consider the equilibrium CO(g) + H2O(g) ↔ CO2(g) + H2(g)
At 1000 K, the composition of the reaction mixture is
CO2 H2(g) CO(g) H2O(g) Substance (g)
27 1 27 1 22 9 22 9 M l %• 27.1 27.1 22.9 22.9 Mole %
a. Calculate KP and at 1000 K.
b. Given the answer to part (a), use the of the reaction species to calculate at 298.15 K. Assume that is independent of temperature.
922922
1.271.270
22
mBmAmDmc
HCOp P
PxxK [Q1] [Q2]
H f
Greaction
9.229.220
2
OHCO
p Pxx
)1000K
1-ΔH G
1000K
298.15K
ΔHΔHΔHΔHΔH
oreactionf,
oreaction
oCf,
oHf,
oCf,
oHf,
oreactionf, 22
KKKG
TKRTTG
oreaction
OOO
preaction
298
11000298
2
()()(
)(ln)(
KTR
HKKTK
fin
reactionpfinp 298
11)}298(ln{)}(ln{
0
10
6.7 Expressing Chemical Equilibrium in Terms of the i
• mAA + mBB + mCC .. mMM + mNN + mOO• We write the reaction in an abbreviated form asWe write the reaction in an abbreviated form as
- mAA - mBB - mCC .. + mMM + mNN + mOO =0
• iXi = 0 (i = -mi if Xi is a reactant; i = mi if Xi is a product).
Q11 From the following data at 298.15 K and 1 bar, choose the closest value to the standard formation enthalpy for CO(g). Reactions Reaction enthalpy (kJmol-1) Fe2O3(s) + 3C(graphite) 2Fe(s) + 3CO(g) 493 FeO(s) + C(graphite) Fe(s) + CO(g) 156 CO2(g) CO(g) + 1/2O2(g) 283
266
A
B
C
Fe(s)+ 1/2O2(g) FeO(s) -266 D
2A Fe(s) + 3A CO(g) – A Fe2O3(s) -3A C(gra) =0B Fe(s) + B CO(g) – B FeO(s) -B C(gra) =0
C CO(g) + C/2 O2(g) – C CO2(g) =0D FeO(s) – D Fe(s) – D/2 O2(g) =0
(2A+ B-D)Fe(s) + (3A+B +C) CO(g) –AFe2O3 -(3A+B)C(gra)(-B+D) FeO(s) –C CO2(g) +(C/2 – D/2)O2(g) =0
Hf(CO(g)) is calculated for the following reaction:C(grap) + 1/2O2(g)CO(g)CO(g) – C(grap) –1/2O2(g) = 0
2A+ B-D =0; -A =0;-B + D =0; -C = 0 A = 0, C = 0, B =DFor CO, (3A + B +C) =1 B =1 & D = B = 1 .
11
7.1 What Determines the Relative Stability of the Solid, Liquid, and Gas Phase
• Phase: Solid Liquid Gas
Phase refers to “a form of matter that isPhase refers to a form of matter that is uniform with respect to chemical composition and the state of aggregation”
Q. What determines most stable phase?
solid(T, P), liquid(T, P), gas(T, P)[Answer here?]solid( , ), liquid( , ), gas( , )[ ]
How does in three phases depends on T?
d(T, P) = -SmdT + VmdP = -SmdT
0 < S (T) < S (T) < S (T)
(T, P) = (0, P) - SmT
0 < Sm, solid(T) < Sm, liquid(T) < Sm, gas(T)
(T) for 3 phases
entia
l ()
Q1. Where is the melting i t?
Assuming Sm is constant,
Che
mic
al p
otepoint?
Q2. Which line represents solid(T)?
Q3. How do you explain the phase transition from solid to liquid using the figure?
12
(T) plot when P is increased- How are Tm and Tb affected by P?
VmGas > Vm
Liquid > VmSolid Vm
Gas > VmSolid > Vm
Liquid
(T, P + P) ~ {(0, P) + Vm P} – SmT
Sublimation and Triple Point
Sublimation TempSolid Gas
Triple Point
Solid, Gas, and Liquid Coexist
Triple Point Temp
13
7.2 The Pressure-Temperature Phase Diagram
P-T Phase Diagram (VmSolid < Vm
Liquid)Isobar T Increases • S L G
L-G coexists above critical point(T ≥Tc, P ≥ Pc) Supercritical Fluid
Water• S L G(P higher than triple point Pressure)b) S G (P lower than triple point P)
Isotherm; P Increasesc) G L S (T higher than triple point T)
• P7.3) Within what range can you restrict the values of P and T if the following information is known about CO2? Use Figure 7.8 to answer this problem.
a. As the temperature is increased, the solid is first converted to the liquid and subsequently to the gaseous state.
b. As the pressure on a cylinder containing pure CO2 is increased from 65 to 80 atm, no interface delineating liquid and gaseous phases is observed.
c. Solid, liquid, and gas
phases coexist at equilibrium.
b80
aa. 5.11 atm < P < 73.75 atm
14
7.4 Providing a Theoretical Basis for the P-T Phase Diagram
• When two phase and are in equilibrium at a constant P and T,
(P, T) = (P, T) When (P,T) is changed by (dP,dT) while keeping the
equilibrium,(P, T) +d = (P, T)+ d
Thus, d = dd d
-SmdT +VmdP = -SmdT +VmdP 0 = (Sm -Sm)dT - (Vm - Vm)dP = SmdT - VmdP
Clapeyron equation
m
m
V
S
dT
dP
dP/dT for fusion and vaporization
1122
KJmolSdP
fusion
m
Average of Sm and Vm for Ag, AgCl, Ca, CaCl2, KCl, Na, NaCl
For Fusion
116
136
551055
104
KbarPaK
molmVdT fusionfusion m
m
.
~
F V i ti Average of S and V in Table 7.3
Negative sign only for H2O(dT/dP)fusion ~ 0.05K bar-1
For Vaporization
1213
132
11
1051005
102
95
KbarPaK
molm
KJmol
V
S
dT
dPvap
m
vapm
vap
.
~
Average of Sm and Vm in Table 7.3
(dT/dP)vap ~ 20K bar-1
15
7.5 Using the Clapeyron Equation to Calculate Vapor Pressure as a Function of T
2RT
HP
TV
H
TV
H
V
S
dT
dP vapm
vapm
vap
vapm
vap
vapm
For Vaporization
2RTTVTVVdT gasmvap
mvap
mvap ,
dTTnR
HdP
P
vapm
2
11
dTH
dPvapm
TfinPfin 11
Clausius-Clapeyron equation
dTTR
dPP
m
TiniPini2
inifin
vapm
ini
fin
TTR
H
P
P 11ln
• P6.17) If the reaction Fe2N(s) +3/2H2(g) 2Fe(s)+NH3(g)comes to equilibrium at a total pressure of 1 bar, analysis of the gas shows that at 700 and 800 K, PNH3/PH2 = 2.165 and 1.083, respectively, if only H2(g) was initially present in the gas phase and Fe2N(s) was in excess. a. Calculate KPat 700 and 800 K. b. Calculate Sreaction
0 at 700 and 800 K reactionand Hreaction
0 assuming that it is independent of temperature. c. Calculate Greaction
0 for this reaction at 298.15 K.
• Fe2N(s) + 3/2H2(g) 2Fe(s) + NH3(g)Nini nini
Nini - ξ nini – 3/2ξ 2ξ ξ
a K = exp(-G0/RT) = (P /P )/(P /P )3/2 (*)a. Kp = exp(-G /RT) = (PNH3/P0)/(PH2/P0) ( )PNH3 = xNH3 P0; PH2 = (1-xNH3) P0
PNH3/PH2 = 2.165 = xNH3 /(1-xNH3) xNH3 @700Kb. Ln{Kp(800K)} - Kn{Kp(700K)} = -(H/R)(1/800K – 1/700K) G = H - TS. From (*) G = -RTln(Kp)
16
• P6.24) At T = 298 K and pH=3 chymotrypsinogen denatures with
G° = 30 5 kJ mol–1 H° = 163 kJ mol–1 and C = 8 36 kJG = 30.5 kJ mol 1, H = 163 kJ mol 1, and CP,m = 8.36 kJ
K–1 mol–1. Determine G° for the denaturation of
chymotrypsinogen at T = 320. K and pH=3. Assume CP,m is
constant between T = 298 K and T = 320. K.
• First, we calculate S0 at T = 298 K:
0 0 0Use S0 = (G0 - H0)/T
H(320K) = CP,m T + H0
S(320K) = + S0 = S0 + Cp,mln(Tfin/Tini)Tfin
Tini
dTT
Cp
• P6.30) You have containers of pure H2 and He at 298 K and 1 atm pressure. Calculate Gmixing relative to the unmixed gases of
a. a mixture of 10 mol of H2 and 10 mol of He.
b. a mixture of 10 mol of H2 and 20 mol of He.
Gmixing = nARTln(xA) + nBRTln(xB)
c. Calculate Gmixing if 10 mol of pure He are added to the mixture of 10 mol of H2 and 10 mol of He.
Gmixing = Gb - Ga
17
• P6.38) Consider the equilibrium in the reaction
3O2 ↔ 2O3 with at 298 K. Assume that is independent of temperature.
• a. Without doing a calculation, predict whether the equilibrium position will shift toward reactants or products as
Hreaction 285.4 103 J mol1
Hreaction
q p pthe pressure is increased.
• b. Without doing a calculation, predict whether the equilibrium position will shift toward reactants or products as the temperature is increased.
• c. Calculate KP at 550 K.
d C l l t K t 550 K d 0 500 b• d. Calculate Kx at 550 K and 0.500 bar.
• Kp(298K) = exp(-G/RT)
• Use ln(Kp(550K)) = ln(K(298K)) –H{1/T2-1/T1}/R
Kp = Kx(P/P0)v Kx = (P/P0) -vKp