Finding ##U## given information about an adiabatic process (Callen)

In summary, the conversation discusses the concept of constant variables in a thermodynamic process, specifically in an adiabatic process where heat is not exchanged. They talk about the first law of thermodynamics and how it relates to the change in internal energy of a system. They also mention the importance of considering extensive variables and homogeneous functions in order to determine the appropriate integration constants.
  • #1
EE18
112
13
Homework Statement
Callen tells us the following:
Show that if a single-component system is such that ##PV^k## is constant in an
adiabatic process (k is a positive constant) the energy is given by
$$U = \frac{PV}{k-1} +Nf(\frac{PV^k}{N^k})$$
where ##f## is an arbitrary function.
Hint: ##PV^k## must be a function of S, so that ##\left( \frac{\partial U}{\partial V}
\right)_{S} = g(S)V^{-k}## where ##g(S)## is an unspecified function.
Relevant Equations
See my attempt below:
I was unable show that ##PV^k## must indeed equal some function of the entropy, ##g(S)##; maybe doing so would make things easier? I proceeded as below.
If we assume (as is almost surely intended by Callen) that in the given adiabatic (##d Q = 0##) process we are taking ##N## as constant and that the process is quasistatic, then we have both that ##dU = d W = -pdV## (from energy conservation/the first law) and that ##dU = TdS - pdV## (from the total differential of ##U## during this process). Thus ##TdS = 0## in such a process so that\footnote{I think we can take ##T \neq 0## as a reasonable assumption for any real process.} ##dS = 0## and thus ##S = const## during the process.

Now observe that if ##S## is held constant in a quasistatic process in which ##N## is constant, then we have ##dU = TdS - pdV +\mu dN = -pdV## while, also, ##dU = d Q -pdV## (first law for systems not changing ##N##) so that ##d Q = 0##. Thus by hypothesis, ##PV^k = const## in such a process. We'll call this constant ##C##, and note that in general it being "constant" means constant with respect to ##V##: ##C = C(S,N)## in general (why?).

Now we recall that
$$P := -\left( \frac{\partial U}{\partial V}
\right)_{S,N};$$
thus, "integrating"\footnote{See the discussion \href{https://math.stackexchange.com/ques...r-a-function-given-a-particular-partial-deriv}{here} for what this means. \label{this}} the above leads to
$$U = -\int P dV = \frac{CV^{1-k}}{k-1} + h(S,N) \stackrel{(1)}{=} \frac{PV}{k-1} + h(S,N)$$
where $h$ is some other constant function.

I can't see how to go further than this though?

Edit: I've added the following argument but am not sure why ##c## below should be invertible?
Now we note that
##u = U/N## should be zeroth order homogeneous.Thus we have that (since each term of a first order homogeneous function -- here ##U## -- must itself be fst order homogeneous) ##H## must be first-order homogeneous. Thus we see that ##H(S,N) = NH(S/N,1) \equiv Nh(s).## Analyzing ##PV^k = C(S,N)## we see that since the left-side is ##k##th order homogeneous, so too must be the right hand side. So in particular ## C(S,N) = N^kC(S/N,1) \equiv N^kc(s)##. We now argue physically that ##c## should be invertible, so that ##s = c^{-1}(Pv^k)$##so that, inserting this to the above gives
$$U = \frac{PV}{k-1} + Nh(s) = \frac{PV}{k-1} + Nh(c^{-1}(Pv^k)) \equiv \frac{PV}{k-1} + Nf(PV^k/N^k)$$
where ##f = g \circ c^{-1}##.
 
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  • #2
Are we allowed to bump?
 
  • #3
EE18 said:
Are we allowed to bump?
Yes. Maybe @Chestermiller can help.
 
  • #4
Hint: The "natural" independent thermodynamical variables for the internal energy, ##U##, for a one-component system are ##S##, ##V##, and ##N##, i.e., you have ##U=U(S,V,N)##.

Then you need the 1st Law
$$\mathrm{d} U=T \mathrm{d} S -P \mathrm{d} V +\mu \mathrm{d}N.$$
For an adiabatic change at constant ##N## you have given that
$$P V^k=C(S,N)=\text{const}.$$
Then you see from the 1st Law
$$\partial_V U(S,V,N)=-P.$$
This you can use to integrate the corresponding differential equation
$$-V^k \partial_V U=C(S,N).$$
Don't forget that the integration constant also depends on ##S## and ##N##.

Then you have to take into account that ##U##, ##S##, and ##V## are extensive variables, i.e., ##U## must be a homogeneous function of its variables of rank 1, i.e., you have
$$U(\lambda S, \lambda V,\lambda N)=\lambda U(S,V,N),$$
from which you learn more about the shape the integration constant(s) must take.
 
  • #5
vanhees71 said:
Hint: The "natural" independent thermodynamical variables for the internal energy, ##U##, for a one-component system are ##S##, ##V##, and ##N##, i.e., you have ##U=U(S,V,N)##.

Then you need the 1st Law
$$\mathrm{d} U=T \mathrm{d} S -P \mathrm{d} V +\mu \mathrm{d}N.$$
For an adiabatic change at constant ##N## you have given that
$$P V^k=C(S,N)=\text{const}.$$
Then you see from the 1st Law
$$\partial_V U(S,V,N)=-P.$$
This you can use to integrate the corresponding differential equation
$$-V^k \partial_V U=C(S,N).$$
Don't forget that the integration constant also depends on ##S## and ##N##.

Then you have to take into account that ##U##, ##S##, and ##V## are extensive variables, i.e., ##U## must be a homogeneous function of its variables of rank 1, i.e., you have
$$U(\lambda S, \lambda V,\lambda N)=\lambda U(S,V,N),$$
from which you learn more about the shape the integration constant(s) must take.
Thank you so much for your answer! If it's possible to follow-up, I think everything up to "Don't forget that the integration constant also depends on ##S## and ##N##." gets us to
$$U = \frac{PV}{k-1} + H(S,N)$$ as I state in the OP. Admittedly, your method seems much more rigorous to arrive here.

For simplifying the arguments for the constant as you suggest in your last paragraph, does my edit in the OP correspond to what you had in mind?
 
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  • #6
Yes, that looks good!
 
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Related to Finding ##U## given information about an adiabatic process (Callen)

What is an adiabatic process in thermodynamics?

An adiabatic process is a thermodynamic process in which there is no heat exchange between the system and its surroundings. This means that the system is perfectly insulated, and any change in its internal energy is due to work done on or by the system.

How do you find the internal energy (U) in an adiabatic process?

To find the internal energy (U) in an adiabatic process, you can use the first law of thermodynamics, which states that the change in internal energy (ΔU) is equal to the work done on the system (W) since there is no heat transfer (Q). Mathematically, ΔU = W. For an ideal gas, you can also use the specific heat capacities and the adiabatic condition (PV^γ = constant) to find U.

What is the significance of the adiabatic condition (PV^γ = constant)?

The adiabatic condition PV^γ = constant is a relationship that holds for an ideal gas undergoing an adiabatic process. Here, P is the pressure, V is the volume, and γ (gamma) is the adiabatic index or ratio of specific heat capacities (C_p/C_v). This condition helps in determining the final states of pressure and volume, which are crucial in calculating the internal energy change.

Can you use specific heat capacities to find U in an adiabatic process?

Yes, specific heat capacities can be used to find the internal energy change in an adiabatic process. For an ideal gas, the change in internal energy (ΔU) can be calculated using the molar specific heat capacity at constant volume (C_v) and the change in temperature (ΔT). The formula is ΔU = nC_vΔT, where n is the number of moles of the gas.

How does the work done on or by the system affect U in an adiabatic process?

In an adiabatic process, the work done on or by the system directly affects the internal energy (U). Since there is no heat exchange, any work done on the system increases its internal energy, while work done by the system decreases its internal energy. The relationship is given by ΔU = W, where W is the work done on the system. For an ideal gas, this work can be calculated using the adiabatic condition and the initial and final states of the gas.

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