The partial-derivative relations derived in Problems 1.46,3.33, and 5.12, plus a bit more partial-derivative trickery, can be used to derive a completely general relation between CPandCV.

(a) With the heat capacity expressions from Problem 3.33 in mind, first considerSto be a function of TandV.Expand dSin terms of the partial derivatives (S/T)Vand (S/V)T. Note that one of these derivatives is related toCV

(b) To bring in CP, considerlocalid="1648430264419" Vto be a function ofTand P and expand dV in terms of partial derivatives in a similar way. Plug this expression for dV into the result of part (a), then set dP=0and note that you have derived a nontrivial expression for (S/T)P. This derivative is related to CP, so you now have a formula for the difference CP-CV

(c) Write the remaining partial derivatives in terms of measurable quantities using a Maxwell relation and the result of Problem 1.46. Your final result should be

CP=CV+TVβ2κT

(d) Check that this formula gives the correct value of CP-CVfor an ideal gas.

(e) Use this formula to argue that CPcannot be less than CV.

(f) Use the data in Problem 1.46 to evaluateCP-CVfor water and for mercury at room temperature. By what percentage do the two heat capacities differ?

(g) Figure 1.14 shows measured values of CPfor three elemental solids, compared to predicted values of CV. It turns out that a graph of βvs.T for a solid has same general appearance as a graph of heat capacity. Use this fact to explain why CPand CVagree at low temperatures but diverge in the way they do at higher temperatures.

Short Answer

Expert verified

a) dS=SVTdV+STVdT

b) CP=TSVTVTP+CV

c) CP=β2TVκT+CV

d) CP=CV+Nk

e) CP>CV

f) CP-CV=0.0435J/K,CP-CV=3.576J/K

g)CP-CVTβ2

Step by step solution

01

Part (a) - Step 1: Solution

Let S be a function of V and T, that is S=S(V,T)Then, based on the derivative's definition, we get

role="math" localid="1648427685193" dS=SVTdV+STVdT......(1)

the heat capacity at constant volume and at constant pressure are given by:

role="math" localid="1648427702735" CV=TSTVCP=TSTP......(2)

so the first term of equation (1), is CV/T.

02

Part(b) Step 2: Solution

Let V be a function of P and T, that is V=V(P,T), then from the definition of the derivative we get:

dV=VPTdP+VTPdT

at constant pressure dpthe above equation becomes

dV=VTPdT

Substitute in equation (1) to get:

(dS)P=SVTVTPdT+STVdTSTP=SVTVTP+STV

Multiply T on the both side we get:

TSTP=TSVTVTP+TSTV

Substitute from equation (2) we get:

role="math" localid="1648428387185" CP=TSVTVTP+CV......(3)

03

Part (c) - Step 3: Solution

Consider the Helmholtz energy Maxwell relation we have:

SVT=PTV

substitute into (3) we get:

CP=TPTVVTP+CV

The following is the relationship between thermal expansion and isothermal compressibility:

βκT=PTV

Substitute in above expression:

CP=βTκTVTP+CV

The thermal expansion is determined by:

β=1VVTP

Substitute value in above equation we get:

CP=β2TVκT+CV......(4)

04

Part (d) - Step 4: Solution

PV=NkTis the ideal gas relation, hence the thermal expansion and isothermal compressibility are given by:

β=1VVTP=1VTNkTPP=NkPV=1TκT=-1VVPT=1VPNkTPT=NkTP2V

substitute into (4) to get:

CP=TVT2P2VNkT+CVCP=P2V2NkT2+CV

To use PV=NKTwe get:

CP=N2k2T2NkT2+CVCP=CV+Nk

05

Part (e) - Step 5: Solution

The thermal expansion can be negative, but it is squared, it will always be positive; however, the thermal compressibility cannot be negative because adding pressure to the system will increase its volume, which is impossible; hence, CP is always greater thanCV.

06

Part (f) - Step 6: Solution

Using the data from problem 1.46e The difference between the heat capacities at constant pressure and constant volume for one gram of water at room temperature is:

CP-CV=β2TVκT=2.57×10-4K-12(298K)10-6m34.52×10-10Pa-1=0.0435J/K

role="math" localid="1648429880211" this is just1%of the heat capacity4.186J/K. Now for one mole of mercury (from the data at page 405)we have:

CP-CV=β2TVκT=1.81×10-4K-12(298K)14.8×10-6m34.04×10-11Pa-1=3.576J/K

this is just under13%of the heat capacityCP=28.0J/K

07

Part (g) - Step 7: Solution

Since the volume of a solid is not totally dependent by its temperature,

CP-CVTβ2

As a result, the difference in heat capacity as the temperature approaches zero is zero, and the two curves of CPand CV diverge at high temperatures.

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Most popular questions from this chapter

Figure 5.35 (left) shows the free energy curves at one particular temperature for a two-component system that has three possible solid phases (crystal structures), one of essentially pure A, one of essentially pure B, and one of intermediate composition. Draw tangent lines to determine which phases are present at which values of x. To determine qualitatively what happens at other temperatures, you can simply shift the liquid free energy curve up or down (since the entropy of the liquid is larger than that of any solid). Do so, and construct a qualitative phase diagram for this system. You should find two eutectic points. Examples of systems with this behaviour include water + ethylene glycol and tin - magnesium.

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