Entropy of a mole of an ideal gas

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SUMMARY

The entropy of one mole of an ideal gas is expressed as ΔS = ∫(C_v dT + PdV)/T. This relationship derives from the first law of thermodynamics, where ΔU = ΔQ - ΔW, leading to the conclusion that dQ = C_v dT + PdV. The discussion also clarifies that for a constant volume process, the work done (W) is zero, simplifying the equation to dU = nC_v dT. The bounds for the integrals of the change in entropy are confirmed to be different for temperature and volume, specifically ∫(PdV/T) from V1 to V2 and ∫(C_v dT/T) from T1 to T2.

PREREQUISITES
  • Understanding of the first law of thermodynamics
  • Familiarity with the concepts of molar entropy and molar volume
  • Knowledge of ideal gas behavior and properties
  • Basic calculus, particularly integration techniques
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  • Study the derivation of the first law of thermodynamics in detail
  • Learn about the specific heat capacities C_v and C_p for ideal gases
  • Explore the concept of entropy in thermodynamic processes
  • Investigate the implications of constant volume processes on thermodynamic equations
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Students and professionals in thermodynamics, particularly those studying ideal gas behavior, as well as educators looking to clarify concepts related to entropy and the first law of thermodynamics.

fluidistic
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Homework Statement

Show that the entropy of one mole of an ideal gas is given by \Delta S = \int \frac{C_v dT+PdV}{T}.
2. The attempt at a solution
\Delta S= \frac{dQ}{T}. From the 1st of Thermodynamics, \Delta U= \Delta Q - \Delta W, where W is the work done by the gas. Hence \Delta Q = \Delta U + \Delta W \Rightarrow dQ=dU+dW=C_vdT+PdV. So \Delta S= \int \frac{C_vdT+PdV}{T}.\square.
But this is cheat. By this I mean that I didn't know that dU=C_vdT. I deduced it because I had to fall over the result. How can I deduce dU=C_vdT, for an ideal gas?
Where did I supposed the 1 mol of the ideal gas?
Last question, what are the bounds of the integral of the change of entropy?
Because \Delta S = \int \frac{C_v dT+PdV}{T}=\int \frac{C_vdT}{T}+ \int \frac{PdV}{T} and I'm sure the bounds of the 2 integrals are different. For instance I think that the bounds of \int \frac{PdV}{T} are \int_{V_1}^{V_2} \frac{PdV}{T}. And I guess that the bounds of \int \frac{C_vdT}{T} are \int_{T_1}^{T_2} \frac{C_vdT}{T} but I'm not sure.
 
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fluidistic said:
How can I deduce dU=C_vdT, for an ideal gas?

By definition,

C_X=T\left(\frac{\partial S}{\partial T}\right)_X

where X is some constraint. This is easily combined with dU=T\,dS-P\,dV.

fluidistic said:
Where did I supposed the 1 mol of the ideal gas?

If you define S and V as the molar entropy and molar volume, respectively, then everything works out. You'll just multiply the answer by 1 mole.

fluidistic said:
Last question, what are the bounds of the integral of the change of entropy?

I don't believe it's possible to write a definite integral that contains both dT and dV. Combining them is a useful shorthand that works for the indefinite integral only.
 
Ok, thank you very much!
 
For a constant volume process, W = 0. From the first law, if W = 0, dQ = dU.

By definition dQ = nCvdT for a constant volume process. So dU = nCvdT.

AM
 
Andrew Mason said:
For a constant volume process, W = 0. From the first law, if W = 0, dQ = dU.

By definition dQ = nCvdT for a constant volume process. So dU = nCvdT.

AM

Thanks. I think I understand well now.
 

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