v-bbarbara.cm.utexas.edu/courses/ch353/files/hw3s10key.pdf · 2018-08-24 · -r-lzi 00r >i /j...
TRANSCRIPT
686
-5.13 x 10-a bar'm3'mol-r
-5i.3 J'mol t
Chapter 22
Using Equation 16.41,
2n ot n'
B2v(T):'+ [1 - (r'- t)(e'zk"r - t)ldBru _2ro3No (rr _ t) n,t*"r (.+)dr 3 \RBI-/
Substitute into the equation fbr AZ to find
Lc : -'"oir ^ ,r, - tr#ntkur (Pz- P,) +
For Nr(g) under the conditions specified'
^ I rr2tto No." r _ ly.€_r, ,urlp,LU : ---J-(n Rrr
2r(32'/.7 x 10-12 m1316'022 x - ', (H) aos I roo(lo o - t.oor I-
22-8. Determine Z" - Zu for a gas that obeys the cquation of state P lV - b\ : RT
We can write, from the equation of state'
P(V - b)
/aP\t;l/ay\[*l\0r / p
RTD
-v -bR
v
Now we substitute into Equation 22'23:
e ,_e ,: r (#)"(#)" RT
v-b (;) :^
22-9" The coefficient of thermal expanslon of water at25'C
compressibility is 4.525 x 10 5 bar i Calculate thc value
25'C. The densrty of water aL25'C is 0'99705 g'mL ''
The molar volume of watcr ts
_ 1 \ \/l8.ol5g\/ ldm:,\:o.ol8o68dmlv:(o*6;;;)( '* i \rooo'L)-"
We can now substitute into Equation 22'27 to find C" - Cu' For one mole'
is 2.512 x 10-a
of C ,, - C,, for
atT vC,-C,,:-.K
- (2"572 x 10 * r-')'(z9g'ts r)(0'otg0og amt)
4.525 x 10-s bar r
dm3.bar-r .K-l
and its thet'mimole of water
1.815 x
-r-
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724 Chapter 23
23-6. The slope of the melting curve of methane is given by
dP - (0.08446our'a-r es)To8s
dT
from the triple point to arbitrary temperatures' Using the fact that the temperature and pressurc
the triple point are 90.68 K and 0.1 : ',:4bat,calculate the melting pressure of methane at 300 K
Integrating from the triple point to 300 K gives
^ P, 1":t00 K
[ ' d, : l^^. ,.0'08446 bar'K-rssrossdr
Jo.ttTq b", Jq0.o8 K
0.08446 bar'K-r'8s[{:oo r)"t - (90.68 K)"']Pz- 0 l714bar :
1.85
Pr: l556bar
This is the melting pressure of methane at 300 K'
23-7 . Thevapor pressure of methanol along the entire liquid-vapor coexistence curve can be express- -
very accurately by the empirical equation
ln(P/bar) - -10'7?849
* 4.373232x
where x -- T lr,' and { : 512'60 K' Use
methanol is 337.67 K.
+ 16.158201 - 3.603425x
, - 2.38t3jj x3 + 4.5l.2199(1 - x)'io
this formula to show that the normal boiling point;=Hrh
''F
t;r
At the normal boiling point, P - 1 atm : 1.01325 bar. If the normal boiling point of methanol i'
331 .67 K, then the equality below should hold when x :337 '61 1512'60:
, l0 15.8491n(1.01325) : _ '"'' :" + r6Js8201 - 3'603425x
+ 4.313232xt - Z.3gtzll x3 + +.512t99(1 - x)1 70
0.013163 :0.013163 =
-16'323364+|6158201-2.313.|19+1.891112-0.6801220+07351410.0132546
23-8. The standard boiling point of a liquid is the temperature at which the vapor pressure is exactll
one bar. Use the ".pi.I"l formula given in the previous problem to show that the standard boiling
point of methanol is 337'33 K'
we do this in the same way as the previous problem' but substitute x : 331 '33 l512'60 into
" -10'"752849 + rc158201 - 3'603425x
x* 4.373232x2 - z.zgt3ll *' + 4'572t99(1 - x)r 70
ln(1)
?
0
0^,- t6.33g820 + 16.1 58207 - 2.31 1329 + 1 .893892 - 0.678668 + 0'1 31 5'/ 2
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742 Chapter 23
To find the standard molar Gibbs entropy, we use the Maxwell relation (Equation 22.46)/^
A. s" : _ eA : _3.:03 J.mor I' \ ar /,Substitutinginto A,Go: A,E _ TL,s'(Equation 22.13),wefindthatA.H': 1g95J.mol-r.Because both graphite and diamond are incompressible, we can write (as in Problem 23-18\
and
Gi.upr' : ci.*n + V *urn(P - Po)
4,u' : do,"' * {,",{e - ro)
Combining these two equations gives
A,G - l,d + (%,", - T r_r)( p * po)
When graphite and diamond are in equilibrium, A,G : 0. Substituting into the equation given inthe problem, we see that at 25'C, L,G' : 2898 J.mol-t. Then
0: A,G'. (#-;= - t-h;=) rt,ot g mol-r)1P - l bar)
:2898 J.mol-r - (1.916 x 10-3 dm3.mol-r)1p - 1 bar)
P- | /?RqRr.-^r-r1/o'o82o6dml- t.916 x l0 r 6r:--^1-r
(zals l'mot- ) ( ,ffi !1) +ru-: 15 000 bar
23-37. Use Equation23.36 to calculate k" - En for Kr(g) at298.15 K. The literature value is
-42.12 kJ.mol-r.
lt" - Eo: -RZ ln
We do this in the same way we found p' - Eofor A
qo(V.Tl (2rmk"T\3'2-r-lv\r'/
l({\wlL\y/ P" )r(g) in Section 23-5. First,
(23.36)
_l (2n)(1.391 x 10-25 kg.mol-')(t.381 x l0-23 J.K-')(298.15 K)lt/'_|l
L (6.626 x 10-34 J.s;2 |
:7 .422 x 1032 m-3
kuT _ (1.381 x 10-r3 J.K-')(298.15 K)Po 1"0 x 105 Pa
Substituting into Equation 23.34 giv es
: 4.716 " 16*26 --3
ti" - En: -Rr," If4) g-l' u L\Y/ P"): -R(298.15 K) lnt(7 422 x 1032 m-,) {+.t t6 x 10-26 m-3)l
: -4.212 x 104 J.mol-l
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