2.6 Calculation of Enthalpy Changes of Processes without Chemical Reactions 83
only onnandT,∆Hfor the first step vanishes. For the second step
∆H 2
∫T 2
T 1
CPdTnCP, m∆T
( 1 .000 mol)
(
5
2
)(
8 .3145 J K−^1 mol−^1
)
( 75 .00 K)1559 J
∆H∆H 1 +∆H 2 0 +1559 J1559 J
Although∆His the same for any process with the same initial and final states as
the overall process in Example 2.26,qandware dependent on the path of a particular
process. If the pressure is not constant during the entire process,qis not necessarily
equal to∆H.
EXAMPLE2.27
Findqandwfor the process used in the calculation of Example 2.26.
Solution
We first findV 2 andP 2 , the volume and pressure at the end of step 2. From the ideal gas law,
V 2 (10.00 L)
298 .15 K
373 .15 K
7 .990 L
P 2
( 1 .000 mol)
(
8 .3145 J K−^1 mol−^1
)
( 298 .15 K)
0 .007990 m^3
3. 103 × 105 Pa
q 1 ( 1 .000 mol)
(
8 .3145 J K−^1 mol−^1
)
( 298 .15 K)ln
(
7 .990 L
5 .000 L
)
1162 J
Because the pressure was constant during step 2,
q 2 ∆H 2 1559 J
qq 1 +q 2 1162 J+1559 J2721 J
This differs considerably from the value of∆H, 1559 J.
We can calculatewfor the process. For the first step
w 1 ∆U 1 −q 1 −q 1 −1162 J
For the second step, we letV 3 be the final volume
w 2 −
∫V 3
V 2
PdV−P
∫V 3
V 2
dV−P∆V
−
(
3. 103 × 105 Pa
)(
0 .01000 m^3 − 0 .007990 m^3
)
− 623 .6J
ww 1 +w 2 −1162 J−624 J−1786 J