Helmholtz and Gibbs free energy for an adiabatic process

In summary, In case 1, if ##S=S_1## at (T1, P1), what is the value of S at (T2,P2)?I can get the changes in S for the processes above, so if I already know S1, S2 = delta_S + S1 respectively.Is it a hint for calculating the delta_A and delta_G for processes in which temperature changes?
  • #1
wwildlifee
7
1

Homework Statement


Calculate changes in A and G of one mole of an ideal gas that undergoes the following processes respectively.
1. adiabatic expansion from (T1, P1) to (T2, P2)
2. isobaric expansion from (P, V1, T1) to (P, V2, T2) (if it is not isothermal)
3. isochoric expansion from (V, P1, T1) to (V, P2, T) (if it is not isothermal)

2. The attempt at a solution
I can get a solution for isothermal processes, but for cases that temperature changes, I cannot calculate changes of A and G because I cannot even find a clue for handling d(TS) = TdS + SdT.
I tried to solve these by using the Gibbs-Helmholtz equation, but I failed.
And also I separated the path into two steps, but I failed again.

How can I calculate the change in A and G for processes in which temperature changes?

Thank you.
 
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  • #3
In case 1, if ##S=S_1## at (T1, P1), what is the value of S at (T2,P2)?
 
  • #4
stevendaryl said:
Well, the various types of energy are all inter-related through:

[itex]dU = T dS - P dV[/itex]
[itex]dA= -S dT - P dV[/itex]
[itex]dG = -S dT + V dP[/itex]

This Wikipedia article tells how to compute the change in volume for an adiabatic process if you know the initial and final pressures:

https://en.wikipedia.org/wiki/Adiabatic_process#Ideal_gas_.28reversible_process.29
Thanks[emoji2]
However this is not what I do not know.
What I want to know is how to handle the integration of (-SdT) in dA or dG for the processes above(adiabatic, isobaric, isochoric).
 
  • #5
Chestermiller said:
In case 1, if ##S=S_1## at (T1, P1), what is the value of S at (T2,P2)?
I can get the changes in S for the processes above, so if I already know S1, S2 = delta_S + S1 respectively.
Is it a hint for calculating the delta_A and delta_G for processes in which temperature changes?
 
  • #6
wwildlifee said:
I can get the changes in S for the processes above, so if I already know S1, S2 = delta_S + S1 respectively.
Is it a hint for calculating the delta_A and delta_G for processes in which temperature changes?
Sure.

Is this for a class in classical thermodynamics or a class in statistical thermodynamics?

What is the equation for ##\Delta G## in terms of ##\Delta H## and ##\Delta(TS)##?
 
  • #7
Chestermiller said:
Sure.

Is this for a class in classical thermodynamics or a class in statistical thermodynamics?

What is the equation for ##\Delta G## in terms of ##\Delta H## and ##\Delta(TS)##?

This course is the classical thermodynamics.
So all I've got are
dU = Tds - pdV
dH = Tds + Vdp
dA = d(U-TS) = dU - TdS - SdT = -pdV - SdT
dG = d(H-TS) = dH - TdS - SdT = Vdp - SdT
Maxwell relations, and the Gibbs-Helmholtz equation.

I I tried to solve case 1 by separating the adiabatic process into two steps: an isothermal process and then an isochoric process.
In other words,
A: (T1, P1, V1)
B: (T1, P`, V`)
C: (T2, P2, V2)
A -> C (adiabatic process) = A -> B -> C
But in this case, I still need to calculate ΔA and ΔG for another isochoric process...

In order to solve this problem, the statistical thermodynamics is needed?
 
  • #8
wwildlifee said:
This course is the classical thermodynamics.
So all I've got are
dU = Tds - pdV
dH = Tds + Vdp
dA = d(U-TS) = dU - TdS - SdT = -pdV - SdT
dG = d(H-TS) = dH - TdS - SdT = Vdp - SdT
Maxwell relations, and the Gibbs-Helmholtz equation.

I I tried to solve case 1 by separating the adiabatic process into two steps: an isothermal process and then an isochoric process.
In other words,
A: (T1, P1, V1)
B: (T1, P`, V`)
C: (T2, P2, V2)
A -> C (adiabatic process) = A -> B -> C
But in this case, I still need to calculate ΔA and ΔG for another isochoric process...

In order to solve this problem, the statistical thermodynamics is needed?
No. Just checking.

You still haven't answered my question regarding the definition of the Gibbs Free Energy G: What is the equation for ##\Delta G## in terms of ##\Delta H## and ##\Delta(TS)##?

Another question: If you know the initial and final states of an ideal gas, do the details of the process that took you from the initial to the final state matter in determining the changes in U, H, S, A, and G between these states?
 
  • #9
Chestermiller said:
No. Just checking.

You still haven't answered my question regarding the definition of the Gibbs Free Energy G: What is the equation for ##\Delta G## in terms of ##\Delta H## and ##\Delta(TS)##?

Another question: If you know the initial and final states of an ideal gas, do the details of the process that took you from the initial to the final state matter in determining the changes in U, H, S, A, and G between these states?

The definition of G is G = H - TS, so ΔG is ΔG = ΔH - Δ(TS) = ΔH - TΔS - SΔT

I'm not sure that I understand your question correctly, but U, H, S, A and G are state functions, so if I know the initial and final state, I think the details of the process do not matter.:rolleyes:
 
  • #10
wwildlifee said:
The definition of G is G = H - TS, so ΔG is ΔG = ΔH - Δ(TS) = ΔH - TΔS - SΔT
ΔH - Δ(TS) = ΔH - TΔS - SΔT? This is not correct mathematically.
I'm not sure that I understand your question correctly, but U, H, S, A and G are state functions, so if I know the initial and final state, I think the details of the process do not matter.:rolleyes:
So, since you are told the initial and final states, why are you worried about "adiabatic," "isochoric," and "isobaric?"

For an ideal gas, what is the change in entropy between the two end states of processes 1, 2, and 3? What is the change in internal energy? What is the change in enthalpy?
 
  • #11
Chestermiller said:
ΔH - Δ(TS) = ΔH - TΔS - SΔT? This is not correct mathematically.

So, since you are told the initial and final states, why are you worried about "adiabatic," "isochoric," and "isobaric?"

For an ideal gas, what is the change in entropy between the two end states of processes 1, 2, and 3? What is the change in internal energy? What is the change in enthalpy?

So, is it enough to express ΔG as ΔH - Δ(TS) ?

I assume the processes are all reversible. And I think it is okay to use Cv and Cp here.
1) ΔU = Cv (T2 - T1), ΔH = Cp (T2 - T1), ΔS = 0 (because dq = 0)
2) ΔU = Cv (T2 - T1), ΔH = Cp (T2 - T1), ΔS = Cp ln(T2/T1) - R ln(P2/P1) (from dH = TdS + Vdp)
3) ΔU = Cv (T2 - T1), ΔH = Cp (T2 - T1), ΔS = Cv ln(T2/T1) (from dU = TdS - pdV)

I'm getting confused more and more:cry:
 
  • #12
wwildlifee said:
So, is it enough to express ΔG as ΔH - Δ(TS) ?

I assume the processes are all reversible. And I think it is okay to use Cv and Cp here.
1) ΔU = Cv (T2 - T1), ΔH = Cp (T2 - T1), ΔS = 0 (because dq = 0) cl
2) ΔU = Cv (T2 - T1), ΔH = Cp (T2 - T1), ΔS = Cp ln(T2/T1) - R ln(P2/P1) (from dH = TdS + Vdp)
3) ΔU = Cv (T2 - T1), ΔH = Cp (T2 - T1), ΔS = Cv ln(T2/T1) (from dU = TdS - pdV)

I'm getting confused more and more:cry:
You are very close now. I'll be back tomorrow.
 
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  • #13
wwildlifee said:
So, is it enough to express ΔG as ΔH - Δ(TS) ?
yes.
I assume the processes are all reversible. And I think it is okay to use Cv and Cp here.
1) ΔU = Cv (T2 - T1), ΔH = Cp (T2 - T1), ΔS = 0 (because dq = 0)
If the actual process was irreversible, then, even if it was adiabatic, ##\Delta S## would not be zero. It is impossible to find an adiabatic reversible path that gives the same change in entropy as an irreversible adiabatic path; the reversible path between the same two end states must always involve some heat transfer. For the adiabatic path to be reversible, the temperatures and pressures at the two end points must be related by Cp ln(T2/T1) - R ln(P2/P1)=0. This is not necessarily the case here. For this case, the most we can say is that ΔS = Cp ln(T2/T1) - R ln(P2/P1)

2) ΔU = Cv (T2 - T1), ΔH = Cp (T2 - T1), ΔS = Cp ln(T2/T1) - R ln(P2/P1) (from dH = TdS + Vdp)
The problem statements says that ##P_2=P_1=P##. Therefore, for this case, ΔS = Cp ln(T2/T1), without the pressure term.

3) ΔU = Cv (T2 - T1), ΔH = Cp (T2 - T1), ΔS = Cv ln(T2/T1) (from dU = TdS - pdV)
Correct!

Now for the changes in A and G. Considering Case 2, $$\Delta G=\Delta H-\Delta (TS)=\Delta H-T_2(S_1+\Delta S)+T_1S_1$$So,
$$\Delta G=C_p(T_2-T_1)-S_1(T_2-T_1)-C_pT_2\ln(T_2/T_1)$$
This can also be written as:
$$\Delta G=C_p(T_2-T_1)-\left(S_1+\frac{C_p\ln(T_2/T_1)}{2}\right)(T_2-T_1)-\frac{(T_1+T_2)}{2}C_p\ln(T_2/T_1)$$
Note that, in neither version is it possible to eliminate the entropy in the initial state ##S_1## from the equation for the change in G.
 
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  • #14
I also thought that the entropy of the initial state S1 (and final state) might be needed.
However, I thought that there is a way to express ΔA and ΔG only in terms of the variables which are given in the problems.
So I tried, but it is an impossible work (at this point)!

Thanks for your kind explanation despite my bad English.
I express my gratitude (probably) halfway around the world.
 
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  • #15
wwildlifee said:
I also thought that the entropy of the initial state S1 (and final state) might be needed.
However, I thought that there is a way to express ΔA and ΔG only in terms of the variables which are given in the problems.
So I tried, but it is an impossible work (at this point)!

Thanks for your kind explanation despite my bad English.
I express my gratitude (probably) halfway around the world.

I think you are right, that [itex]\Delta A[/itex] involves the quantity [itex]S_1 \Delta T[/itex] (for an adiabatic change). So it seems to me that you need to know the original entropy in order to solve for [itex]\Delta A[/itex].
 

1. What is Helmholtz and Gibbs free energy?

Helmholtz and Gibbs free energy are thermodynamic potentials that measure the amount of energy available to do work in a system. They take into account both the internal energy and entropy of a system.

2. What is the difference between Helmholtz and Gibbs free energy?

The main difference between Helmholtz and Gibbs free energy is that Helmholtz free energy is used for systems at constant temperature and volume, while Gibbs free energy is used for systems at constant temperature and pressure.

3. How is Helmholtz and Gibbs free energy related to an adiabatic process?

In an adiabatic process, there is no exchange of heat between the system and its surroundings. This means that the change in internal energy is equal to the work done by the system. Helmholtz and Gibbs free energy take into account both the internal energy and work done, making them useful for analyzing adiabatic processes.

4. What is the equation for Helmholtz and Gibbs free energy?

The equation for Helmholtz free energy is A = U - TS, where A is Helmholtz free energy, U is internal energy, T is temperature, and S is entropy. The equation for Gibbs free energy is G = H - TS, where G is Gibbs free energy, H is enthalpy, T is temperature, and S is entropy.

5. What are the applications of Helmholtz and Gibbs free energy?

Helmholtz and Gibbs free energy are important concepts in thermodynamics and have many applications in various fields such as chemistry, physics, and engineering. They are used to determine the stability of a system, predict phase changes, and calculate the maximum work that can be obtained from a system.

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