48 2 Work, Heat, and Energy: The First Law of Thermodynamics
Exact and Inexact Differentials
The differential of a function of two or more independent variables is called anexact
differential.Iffis a function ofxandy, the differential
df
(
∂f
∂x
)
y
dx+
(
∂f
∂y
)
x
dx (exact differential) (2.1-19)
is an exact differential. There is an important theorem of mathematics concerning
the line integral of an exact differential:A line integral of an exact differential is
equal to the function evaluated at the final point of the integration curve minus the
function evaluated at the initial point of the curve. The line integral of an exact
differential therefore depends only on the end points, and not on the curve connect-
ing them.The line integral of an exact differential is said to bepath-independent.
The converse of this theorem is also true.If the integral of a differential is path-
independent for all paths between the same end points, the differential must be an exact
differential.
Since the pressurePis a state function,dPis an exact differential. The line integral
ofdPin part b of Example 2.2 is equal to the value ofPat the end of the process minus
the value ofPat the beginning of the process:
∫
c
dP∆PP(final)−P(initial)
Exercise 2.3
Verify that∆Pin Example 2.2 is equal to the final pressure minus the initial pressure.
Work Is an Inexact Differential
A differential that is not exact is called aninexact differential. The differential
duM(x,y)dx+N(x,y)dy (2.1-20)
is an inexact differential ifMandNare not the appropriate partial derivatives of
the same function. The line integral of an inexact differential depends on the path of
integration as well as on the initial point and the final point. We will show thatdwis an
inexact differential by showing that two processes with the same initial and final states
can correspond to different amounts of work done on the system.
EXAMPLE 2.7
Consider a reversible process with the same initial and final states as the process of
Example 2.2, but with a different path. Calculate the work done on the ideal gas system
of Example 2.2 if it is reversibly cooled at constant volume of 5.000 L from 298.15 K