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 2T 1CPdTnCP, 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 JAlthough∆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 LP 2 ( 1 .000 mol)(
8 .3145 J K−^1 mol−^1)
( 298 .15 K)
0 .007990 m^3 3. 103 × 105 Paq 1 ( 1 .000 mol)(
8 .3145 J K−^1 mol−^1)
( 298 .15 K)ln(
7 .990 L
5 .000 L)
1162 JBecause the pressure was constant during step 2,q 2 ∆H 2 1559 Jqq 1 +q 2 1162 J+1559 J2721 JThis differs considerably from the value of∆H, 1559 J.
We can calculatewfor the process. For the first stepw 1 ∆U 1 −q 1 −q 1 −1162 JFor the second step, we letV 3 be the final volumew 2 −∫V 3V 2PdV−P∫V 3V 2dV−P∆V−(
3. 103 × 105 Pa)(
0 .01000 m^3 − 0 .007990 m^3)
− 623 .6Jww 1 +w 2 −1162 J−624 J−1786 J