Calculate the change in entropy when #"1 mol"# of argon gas is heated from #"300 K"# to #"1200 K"#, assuming that #C_P = "20.8 J/mol"cdot"K"# and is constant in the temperature range?
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If you really want to be exact, look up the Shomate equation for argon, and integrate that instead:
#DeltaS ("const. P") -= int_(T_1)^(T_2) (C_P(T))/TdT#
#= int_(T_1)^(T_2) [20.78600/T + 2.825911 xx 10^(-10) - 1.464191 xx 10^(-13)T + 1.092131 xx 10^(-17) T^2 - (3.661371 xx 10^(-2))/T^3] dT#
#~~ int_(T_1)^(T_2) 20.78600/T dT# when ignoring the higher-order terms. The most exact answer is
#28.8_(155)color(white)(.)"J/K"# , and the approximated answer is#28.8_(35)# #"J/K"# . Pretty good!
DERIVING THE RELATIONSHIP BETWEEN ENTROPY AND HEAT CAPACITY
Well, the influence on the entropy due to a change in temperature at constant pressure is given by:
#((delS)/(delT))_P# ,the partial derivative of
#S# (entropy) with respect to#T# (temperature) at constant pressure (#P# ).
Recall that the differential entropy is given by:
#dS = (deltaq_(rev))/T# #" "bb((1))# where
#"rev"# indicates the process is reversible, i.e. that is done infinitesimally slowly.
At constant pressure, the differential heat flow
#dH = overbrace(dE)^"Internal Energy" + d(PV)#
#= overbrace(deltaq_(rev) + deltaw_(rev))^("First Law of Thermodynamics") + PdV + VdP#
#= deltaq_(rev) cancel(- PdV + PdV) + VdP#
#= deltaq_(rev) + cancel(VdP)^(0)# at const. pressure,where
#w_(rev)# is the reversible work done from the perspective of the system.
Furthermore, by definition, for a reversible process, the constant-pressure heat capacity
#C_P = ((delH)/(delT))_P = ((delq_(rev))/(delT))_P# #" "bb((2))#
Therefore, we use
#T((delS)/(delT))_P = ((delq_(rev))/(delT))_P = C_P# #" "bb((3))#
As a result, we have that:
#color(blue)(barul(|stackrel(" ")(" "((delS)/(delT))_P = C_P/T" ")|))# #" "# #ul"at constant pressure"# .
(If you have done the derivation before, you can feel free to just memorize this result.)
FINDING THE CHANGE IN ENTROPY
Keeping that in mind, separate the variables and integrate as follows:
#int_((1))^((2))dS = int_(T_1)^(T_2) C_P/TdT#
Assuming that the constant-pressure heat capacity
#color(blue)(DeltaS) ~~ C_Pln(T_2/T_1)#
#~~ nbarC_Pln(T_2/T_1)# #" "" "# (where#barC_P = C_P/n# )
#~~# #cancel"1 mol" cdot "20.8 J/"cancel"mol"cdot"K" cdot ln("1200 K"/"300 K")#
#~~# #color(blue)(ul"28.8 J/K")#