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Chapter 11 - Section B - Non-Numerical Solutions
11.6 Apply Eq. (11.7):
Ti ≡
[
∂(nT )
∂ni
]
P,T,n j
= T(
∂n∂ni
)
T,P,n j
= T Pi ≡
[
∂(n P)
∂ni
]
P,T,n j
= P(
∂n∂ni
)
T,P,n j
= P
11.7 (a) Let m be the mass of the solution, and define the partial molar mass by: mi ≡
(
∂m∂ni
)
T,P,n j
Let Mk be the molar mass of species k. Then
m = �k
nkMk = niMi + �j
n jM j ( j �= i)
and(
∂m∂ni
)
T,P,n j
=
[
∂(niMi )
∂ni
]
T,P,n j
= Mi Whence, mi = Mi
(b) Define a partial specific property as: Mi ≡
(
∂ M t
∂mi
)
T,P,m j
=
(
∂ M t
∂ni
)
T,P,m j
(
∂ni
∂mi
)
T,P,m j
If Mi is the molar mass of species i , ni =mi
Miand
(
∂ni
∂mi
)
T,P,m j
=1
Mi
Because constant m j implies constant n j , the initial equation may be written: Mi =Mi
Mi
11.8 By Eqs. (10.15) and (10.16), V1 = V + x2dVdx1
and V2 = V − x1dVdx1
Because V = ρ−1 thendVdx1
=−1ρ2
dρ
dx1whence
V1 =1ρ
−x2
ρ2
dρ
dx1=
1ρ
(
1 −x2
ρ
dρ
dx1
)
=1ρ2
(
ρ − x2dρ
dx1
)
V2 =1ρ
+x1
ρ2
dρ
dx1=
1ρ
(
1 +x1
ρ
dρ
dx1
)
=1ρ2
(
ρ + x1dρ
dx1
)
With ρ = a0 + a1x1 + a2x21 and
dρ
dx1= a1 + 2a2x1 these become:
V1 =1ρ2
[a0 − a1 + 2(a1 − a2)x1 + 3a2x21 ] and V2 =
1ρ2
(a0 + 2a1x1 + 3a2x21)
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11.9 For application of Eq. (11.7) all mole fractions must be eliminated from the given equation by therelation xi = ni/n:
nM = n1 M1 + n2 M2 + n3 M3 +n1n2n3
n2C
For M1,[
∂(nM)
∂n1
]
T,P,n2,n3
= M1 + n2n3C
[
1n2
−2n1
n3
(
∂n∂n1
)
T,P,n2,n3
]
Because n = n1 + n2 + n3,(
∂n∂n1
)
T,P,n2,n3
= 1
Whence, M1 = M1 +n2n3
n2
[
1 − 2n1
n
]
C and M1 = M1 + x2x3[1 − 2x1]C
Similarly, M2 = M2 + x1x3[1 − 2x2]C and M3 = M3 + x1x2[1 − 2x3]C
One can readily show that application of Eq. (11.11) regenerates the original equation for M . Theinfinite dilution values are given by:
M∞i = Mi + x j xkC ( j, k �= i)
Here x j and xk are mole fractions on an i-free basis.
11.10 With the given equation and the Dalton’s-law requirement that P =∑
i pi , then:
P =RTV �
iyi Z i
For the mixture, P = Z RT/V . These two equations combine to give Z =∑
i yi Z i .
11.11 The general principle is simple enough:
Given equations that represent partial properties Mi , M Ri , or M E
i as functions of com-position, one may combine them by the summability relation to yield a mixture property.Application of the defining (or equivalent) equations for partial properties then regeneratesthe given equations if and only if the given equations obey the Gibbs/Duhen equation.
11.12 (a) Multiply Eq. (A) of Ex. 11.4 by n (= n1 + n2) and eliminate x1 by x1 = n1/(n1 + n2):
nH = 600(n1 + n2) − 180 n1 − 20n3
1
(n1 + n2)2
Form the partial derivative of nH with respect to n1 at constant n2:
H1 = 600 − 180 − 20[
3n21
(n1 + n2)2−
2n31
(n1 + n2)3
]
= 420 − 60n2
1
(n1 + n2)2+ 40
n31
(n1 + n2)3
Whence, H1 = 420 − 60 x21 + 40 x3
1
Form the partial derivative of nH with respect to n2 at constant n1:
H2 = 600 + 202 n3
1
(n1 + n2)3or H2 = 600 + 40 x3
1
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(b) In accord with Eq. (11.11),
H = x1(420 − 60 x21 + 40 x3
1) + (1 − x2)(600 + 40 x31)
Whence, H = 600 − 180 x1 − 20 x31
(c) Write Eq. (11.14) for a binary system and divide by dx1: x1d H1
dx1+ x2
d H2
dx1= 0
Differentiate the the boxed equations of part (a):
d H1
dx1= −120 x1 + 120 x2
1 = −120 x1x2 andd H2
dx1= 120 x2
1
Multiply each derivative by the appropriate mole fraction and add:
−120 x21 x2 + 120x2
1 x2 = 0
(d) Substitute x1 = 1 and x2 = 0 in the first derivative expression of part (c) and substitute x1 = 0in the second derivative expression of part (c). The results are:
(
d H1
dx1
)
x1=1=
(
d H2
dx1
)
x1=0= 0
(e)
11.13 (a) Substitute x2 = 1 − x1 in the given equation for V and reduce:
V = 70 + 58 x1 − x21 − 7 x3
1
Apply Eqs. (11.15) and (11.16) to find expressions for V1 and V2. First,
dVdx1
= 58 − 2 x1 − 21 x21
Then, V1 = 128 − 2 x1 − 20 x21 + 14 x3
1 and V2 = 70 + x21 + 14 x3
1
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(b) In accord with Eq. (11.11),
V = x1(128 − 2 x1 − 20 x21 + 14 x3
1) + (1 − x1)(70 + x21 + 14 x3
1)
Whence, V = 70 + 58 x1 − x21 − 7 x3
1
which is the first equation developed in part (a).
(c) Write Eq. (11.14) for a binary system and divide by dx1: x1dV1
dx1+ x2
dV2
dx1= 0
Differentiate the the boxed equations of part (a):
dV1
dx1= −2 − 40 x1 + 42 x2
1 anddV2
dx1= 2 x1 + 42 x2
1
Multiply each derivative by the appropriate mole fraction and add:
x1(−2 − 40 x1 + 42 x21) + (1 − x1)(2 x1 + 42 x2
1) = 0
The validity of this equation is readily confirmed.
(d) Substitute x1 = 1 in the first derivative expression of part (c) and substitute x1 = 0 in the secondderivative expression of part (c). The results are:
(
dV1
dx1
)
x1=1=
(
dV2
dx1
)
x1=0= 0
(e)
11.14 By Eqs. (11.15) and (11.16):
H1 = H + x2d Hdx1
and H2 = H − x1d Hdx1
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Given that: H = x1(a1 + b1x1) + x2(a2 + b2x2)
Then, after simplification,d Hdx1
= a1 + 2b1x1 − (a2 + 2b2x2)
Combining these equations gives after reduction:
H1 = a1 + b1x1 + x2(x1b1 − x2b2) and H2 = a2 + b2x2 − x1(x1b1 − x2b2)
These clearly are not the same as the suggested expressions, which are therefore not correct. Notethat application of the summability equation to the derived partial-property expressions reproducesthe original equation for H . Note further that differentiation of these same expressions yields resultsthat satisfy the Gibbs/Duhem equation, Eq. (11.14), written:
x1d H1
dx1+ x2
d H2
dx1= 0
The suggested expresions do not obey this equation, further evidence that they cannot be valid.
11.15 Apply the following general equation of differential calculus:(
∂x∂y
)
z=
(
∂x∂y
)
w
+
(
∂x∂w
)
y
(
∂w
∂y
)
z
[
∂(nM)
∂ni
]
T,P,n j
=
[
∂(nM)
∂ni
]
T,V,n j
+
[
∂(nM)
∂V
]
T,n
(
∂V∂ni
)
T,P,n j
Whence,
Mi = Mi + n(
∂ M∂V
)
T,n
(
∂V∂ni
)
T,P,n j
or Mi = Mi − n(
∂ M∂V
)
T,n
(
∂V∂ni
)
T,P,n j
By definition,
Vi ≡
[
∂(nV )
∂ni
]
T,P,n j
= n(
∂V∂ni
)
T,P,n j
+ V or n(
∂V∂ni
)
T,P,n j
= Vi − V
Therefore, Mi = Mi + (V − Vi )
(
∂ M∂V
)
T,x
11.20 Equation (11.59) demonstrates that ln φi is a partial property with respect to G R/RT . Thus ln φi =
G i/RT . The partial-property analogs of Eqs. (11.57) and (11.58) are:
(
∂ ln φi
∂ P
)
T,x
=V R
i
RTand
(
∂ ln φi
∂T
)
P,x
= −H R
i
RT 2
The summability and Gibbs/Duhem equations take on the following forms:
G R
RT= �
ixi ln φi and �
ixi d ln φi = 0 (const T, P)
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11.26 For a pressure low enough that Z and ln φ are given approximately by Eqs. (3.38) and (11.36):
Z = 1 +B PRT
and ln φ =B PRT
then: ln φ ≈ Z − 1
11.28 (a) Because Eq. (11.96) shows that ln γi is a partial property with respect to G E/RT , Eqs. (11.15)and (11.16) may be written for M ≡ G E/RT :
ln γ1 =G E
RT+ x2
d(G E/RT )
dx1ln γ2 =
G E
RT− x1
d(G E/RT )
dx1
Substitute x2 = 1 − x1 in the given equaiton for G E/RT and reduce:
G E
RT= −1.8 x1 + x2
1 + 0.8 x31 whence
d(G E/RT )
dx1= −1.8 + 2 x1 + 2.4 x2
1
Then, ln γ1 = −1.8 + 2 x1 + 1.4 x21 − 1.6 x3
1 and ln γ2 = −x21 − 1.6 x3
1
(b) In accord with Eq. (11.11),
G E
RT= x1 ln γ1 + x2 ln γ2 = x1(−1.8 + 2 x1 + 1.4 x2
1 − 1.6 x31) + (1 − x1)(−x2
1 − 1.6 x31)
Whence,G E
RT= −1.8 x1 + x2
1 + 0.8 x31
which is the first equation developed in part (a).
(c) Write Eq. (11.14) for a binary system with Mi = ln γi and divide by dx1:
x1d ln γ1
dx1+ x2
d ln γ2
dx1= 0
Differentiate the the boxed equations of part (a):
d ln γ1
dx1= 2 + 2.8 x1 − 4.8 x2
1 andd ln γ2
dx1= −2 x1 − 4.8 x2
1
Multiply each derivative by the appropriate mole fraction and add:
x1(2 + 2.8 x1 − 4.8 x21) + (1 − x1)(−2 x1 − 4.8 x2
1) = 0
The validity of this equation is readily confirmed.
(d) Substitute x1 = 1 in the first derivative expression of part (c) and substitute x1 = 0 in the secondderivative expression of part (c). The results are:
(
d ln γ1
dx1
)
x1=1=
(
d ln γ2
dx1
)
x1=0= 0
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(e)
11.29 Combine definitions of the activity coefficient and the fugacity coefficients:
γi ≡fi/xi Pfi/P
or γi =φi
φi
Note: See Eq. (14.54).
11.30 For C EP = const., the following equations are readily developed from those given in the last column
of Table 11.1 (page 415):
�H E = C EP �T and �SE = −�
(
∂G E
∂T
)
P,x= C E
P�T〈T 〉
Working equations are then:
SE1 =
H E1 − G E
1
T1and SE
2 = SE1 + C E
P�T〈T 〉
H E2 = H E
1 + C EP �T and G E
2 = H E2 − T2SE
2
For T1 = 298.15, T2 = 328.15, 〈T 〉 = 313.15 and �T = 30, results for all parts of the problem aregiven in the following table:
I. II. For C EP = 0
G E1 H E
1 SE1 C E
P SE2 H E
2 G E2 SE
2 H E2 G E
2
(a) −622 −1920 −4.354 4.2 −3.951 −1794 −497.4 −4.354 −1920 −491.4(b) 1095 1595 1.677 3.3 1.993 1694 1039.9 1.677 1595 1044.7(c) 407 984 1.935 −2.7 1.677 903 352.8 1.935 984 348.9(d) 632 −208 −2.817 23.0 −0.614 482 683.5 −2.817 −208 716.5(e) 1445 605 −2.817 11.0 −1.764 935 1513.7 −2.817 605 1529.5(f) 734 −416 −3.857 11.0 −2.803 −86 833.9 −3.857 −416 849.7(g) 759 1465 2.368 −8.0 1.602 1225 699.5 2.368 1465 688.0
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11.31 (a) Multiply the given equation by n (= n1 + n2), and convert remaining mole fractions to ratios ofmole numbers:
nG E
RT= A12
n1n2
n+ A13
n1n3
n+ A23
n2n3
nDifferentiation with respect to n1 in accord with Eq. (11.96) yields [(∂n/∂n1)n2,n3 = 1]:
ln γ1 = A12n2
(
1n
−n1
n2
)
+ A13n3
(
1n
−n1
n2
)
− A23n2n3
n2
= A12x2(1 − x1) + A13x3(1 − x1) − A23x2x3
Similarly, ln γ2 = A12x1(1 − x2) − A13x1x3 + A23x3(1 − x2)
ln γ3 = −A12x1x2 + A13x1(1 − x3) + A23x2(1 − x3)
(b) Each ln γi is multiplied by xi , and the terms are summed. Consider the first terms on the right ofeach expression for ln γi . Multiplying each of these terms by the appropriate xi and adding gives:
A12(x1x2 − x21 x2 + x2x1 − x2
2 x1 − x1x2x3) = A12x1x2(1 − x1 + 1 − x2 − x3)
= A12x1x2[2 − (x1 + x2 + x3)] = A12x1x2
An analogous result is obtained for the second and third terms on the right, and adding themyields the given equation for G E/RT .
(c) For infinite dilution of species 1, x1 = 0: ln γ1(x1 = 0) = A12x2 + A13x3 − A23x2x3
For pure species 1, x1 = 1: ln γ1(x1 = 1) = 0
For infinite dilution of species 2, x2 = 0: ln γ1(x2 = 0) = A13x23
For infinite dilution of species 3, x3 = 0: ln γ1(x3 = 0) = A12x22
11.35 By Eq. (11.87), written with M ≡ G and with x replaced by y: G E = G R − �i
yi G Ri
Equations (11.33) and (11.36) together give G Ri = Bi i P . Then for a binary mixture:
G E = B P − y1 B11 P − y2 B22 P or G E = P(B − y1 B11 − y2 B22)
Combine this equation with the last equation on Pg. 402: G E = δ12 Py1 y2
From the last column of Table 11.1 (page 415): SE = −
(
∂G E
∂T
)
P,x
Because δ12 is a function of T only: SE = −dδ12
dTPy1 y2
By the definition of G E , H E = G E + T SE ; whence, H E =
(
δ12 − Tdδ12
dT
)
Py1 y2
Again from the last column of Table 11.1: C EP =
(
∂ H E
∂T
)
P,x
This equation and the preceding one lead directly to: C EP = −T
d2δ12
dT 2Py1 y2
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11.41 From Eq. (11.95):(
∂(G E/RT )
∂T
)
P=
−H E
RT 2or
(
∂(G E/T )
∂T
)
P=
−H E
T 2
To an excellent approximation, write:(
∂(G E/T )
∂T
)
P≈
�(G E/T )
�T≈
−H E
T 2mean
From the given data:�(G E/T )
�T=
785/323 − 805/298323 − 298
=−0.271
25= −0.01084
and−H E
T 2mean
=−10603132
= −0.01082
The data are evidently thermodynamically consistent.
11.42 By Eq. (11.14), the Gibbs/Duhem equation, x1d M1
dx1+ x2
d M2
dx1= 0
Given that M1 = M1 + Ax2 and M2 = M2 + Ax1 thend M1
dx1= −A and
d M2
dx1= A
Then x1d M1
dx1+ x2
d M2
dx1= −x1 A + x2 A = A(x2 − x1) �= 0
The given expressions cannot be correct.
11.45 (a) For M E = Ax21 x2
2 find M E1 = Ax1x2
2(2 − 3x1) and M E2 = Ax2
1 x2(2 − 3x2)
Note that at both x1 = 0 (x2 = 1) and x1 = 1 (x2 = 0), M E1 = M E
2 = 0
In particular, (M E1 )∞ = (M E
2 )∞ = 0
Although M E has the same sign over the whole composition range, both M E1 and M E
2 changesign, which is unusual behavior. Find also that
d M E1
dx1= 2Ax2(1 − 6x1x2) and
d M E2
dx1= −2Ax1(1 − 6x1x2)
The two slopes are thus of opposite sign, as required; they also change sign, which is unusual.
For x1 = 0d M E
1
dx1= 2A and
d M E2
dx1= 0
For x1 = 1d M E
1
dx1= 0 and
d M E2
dx1= −2A
(b) For M E = A sin(πx1) find:
M E1 = A sin(πx1) + Aπx2 cos(πx1) and M E
2 = A sin(πx1) − Aπx1 cos(πx1)
d M E1
dx1= −Aπ2x2 sin(πx1) and
d M E2
dx1= Aπ2x1 sin(πx1)
The two slopes are thus of opposite sign, as required. But note the following, which is unusual:
For x1 = 0 and x1 = 1d M E
1
dx1= 0 and
d M E2
dx1= 0
PLOTS OF THE FUNCTIONS ARE SHOWN ON THE FOLLOWING PAGE.
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Pb. 11.45 (a) A 10 i ..0 100 xi .00001 ..01 i
MEi..A xi
2 1 xi2 MEbar1i
..A xi 1 xi2 2 .3 xi
MEbar2i....A xi xi 1 xi 2 .3 1 xi
0 0.2 0.4 0.6 0.8 10.5
0
0.5
1
1.5
2
MEi
MEbar1i
MEbar2i
xi
Pb. 11.45 (b) MEi.A sin .p xi (pi prints as bf p)
MEbar1i.A sin .p xi
...A p 1 xi cos .p xi
MEbar2i.A sin .p xi
...A p xi cos .p xi
0 0.2 0.4 0.6 0.8 110
0
10
20
30
40
MEi
MEbar1i
MEbar2i
xi
sin
687A
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11.46 By Eq. (11.7), Mi =
[
∂(nM)
∂ni
]
T,P,n j
= M + n(
∂ M∂ni
)
T,P,n j
At constant T and P , d M =∑
k
(
∂ M∂xk
)
T,P,x j
dxk
Divide by dni with restriction to constant n j ( j �= i):
(
∂ M∂ni
)
T,P,n j
=∑
k
(
∂ M∂xk
)
T,P,x j
(
∂xk
∂ni
)
n j
With xk =nk
n
(
∂xk
∂ni
)
n j
=
−nk
n2(k �= i)
1n
−ni
n2(k = i)
(
∂ M∂ni
)
T,P,n j
= −1n
∑
k �=i
xk
(
∂ M∂xk
)
T,P,x j
+1n(1 − xi )
(
∂ M∂xi
)
T,P,x j
=1n
(
∂ M∂xi
)
T,P,x j
−1n
∑
k
xk
(
∂ M∂xk
)
T,P,x j
Mi = M +
(
∂ M∂xi
)
T,P,x j
−∑
k
xk
(
∂ M∂xk
)
T,P,x j
For species 1 of a binary mixture (all derivatives at constant T and P):
M1 = M +
(
∂ M∂x1
)
x2
− x1
(
∂ M∂x1
)
x2
− x2
(
∂ M∂x2
)
x1
= M + x2
[
(
∂ M∂x1
)
x2
−
(
∂ M∂x2
)
x1
]
Because x1 + x2 = 1, the partial derivatives in this equation are physically unrealistic; however, theydo have mathematical significance. Because M = M(x1, x2), we can quite properly write:
d M =
(
∂ M∂x1
)
x2
dx1 +
(
∂ M∂x2
)
x1
dx2
Division by dx1 yields:
d Mdx1
=
(
∂ M∂x1
)
x2
+
(
∂ M∂x2
)
x1
dx2
dx1=
(
∂ M∂x1
)
x2
−
(
∂ M∂x2
)
x1
wherein the physical constraint on the mole fractions is recognized. Therefore
M1 = M + x2d Mdx1
The expression for M2 is found similarly.
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11.47 (a) Apply Eq. (11.7) to species 1: M E1 =
[
∂(nM E)
∂n1
]
n2
Multiply the given equation by n and eliminate the mole fractions in favor of mole numbers:
nM E= An1n2
(
1n1 + Bn2
+1
n2 + Bn1
)
M E1 = An2
{(
1n1 + Bn2
+1
n2 + Bn1
)
+ n1
(
−1(n1 + Bn2)2
−B
(n2 + Bn1)2
)}
Conversion back to mole fractions yields:
M E1 = Ax2
{(
1x1 + Bx2
+1
x2 + Bx1
)
− x1
(
1(x1 + Bx2)2
+B
(x2 + Bx1)2
)}
The first term in the first parentheses is combined with the first term in the second parenthesesand the second terms are similarly combined:
M E1 = Ax2
{
1x1 + Bx2
(
1 −x1
x1 + Bx2
)
+1
x2 + Bx1
(
1 −Bx1
x2 + Bx1
)}
Reduction yields:
M E1 = Ax2
2
[
B(x1 + Bx2)2
+1
(x2 + Bx1)2
]
Similarly,
M E2 = Ax2
1
[
1(x1 + Bx2)2
+B
(x2 + Bx1)2
]
(b) The excess partial properties should obey the Gibbs/Duhem equation, Eq. (11.14), when writtenfor excess properties in a binary system at constant T and P:
x1d M E
1
dx1+ x2
d M E2
dx1= 0
If the answers to part (a) are mathematically correct, this is inevitable, because they were derivedfrom a proper expression for M E . Furthermore, for each partial property M E
i , its value andderivative with respect to xi become zero at xi = 1.
(c) (M E1 )∞ = A
(
1B
+ 1)
(M E2 )∞
= A(
1 +1B
)
11.48 By Eqs. (11.15) and (11.16), written for excess properties, find:
d M E1
dx1= x2
d2 M E
dx21
d M E2
dx1= −x1
d2 M E
dx21
At x1 = 1, d M E1 /dx1 = 0, and by continuity can only increase or decrease for x1 < 1. Therefore the
sign of d M E1 /dx1 is the same as the sign of d2 M E/dx2
1 . Similarly, at x1 = 0, d M E2 /dx1 = 0, and by
the same argument the sign of d M E2 /dx1 is of opposite sign as the sign of d2 M E/dx2
1 .
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11.49 The claim is not in general valid.
β ≡1V
(
∂V∂T
)
PV id =
∑
i
xi Vi
β id =1
�i
xi Vi
∑
i
xi
(
∂Vi
∂T
)
P=
1
�i
xi Vi
∑
i
xi Viβi
The claim is valid only if all the Vi are equal.
690PROPRIETARY MATERIAL. © 2005 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers
and educators for course preparation. If you are a student using this Manual, you are using it without permission.