How Is Entropy Calculated During Isothermal Expansion in a Carnot Engine?

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Homework Help Overview

The discussion revolves around calculating the entropy change during the isothermal expansion phase of a Carnot engine operating with methane as an ideal gas. Participants are exploring the implications of constant temperature on the equations relevant to entropy and work in thermodynamic processes.

Discussion Character

  • Exploratory, Conceptual clarification, Mathematical reasoning, Assumption checking

Approaches and Questions Raised

  • The original poster attempts to relate entropy to heat transfer while questioning the applicability of various equations due to the constant temperature condition. Some participants suggest using a P-V diagram to visualize the process and clarify relationships between variables. Others raise concerns about the implications of isothermal conditions on efficiency and the definitions of heat transfer.

Discussion Status

The discussion is active, with participants providing insights and questioning assumptions. Some have offered guidance on using diagrams and equations, while others are still grappling with the relationships between temperature, heat, and efficiency in the context of the Carnot cycle.

Contextual Notes

Participants note the complexity of applying traditional equations for entropy and efficiency in an isothermal process, highlighting the challenge of reconciling these with the Carnot engine's operational principles.

Emspak
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Homework Statement


A Carnot engine operates with 1 kg of methane, which we will consider an ideal gas.

The ratio of specific heat capacities \gamma is 1.35.

The ratio of maximum volume to minimum volume is 4 and the cycle efficiency is 25%.

Find the entropy increase during the isothermal expansion.

Homework Equations



The temperature is constant if the expansion. I wasn't sure which equations to start with, though, because the equations I saw int he text all seem to be predicated on the temperature being different.

Now, I could put T in terms of P for the ideal gas, so if PV = nRT and I keep T constant, T = \frac{PV}{nR} and then use the following for entropy, since this is a Carnot engine and it's a reversible process:

$$S_b - S_a = \int^a_b \frac{d'Q_T}{T} = \int^a_b \frac{d'Q_T nR}{PV} = nR \int^a_b \frac{d'Q_T}{PV}$$

But I have no idea if I am even on the right track with this. So really I am hoping someone can tell me if I am going in the right direction. Because I am really not sure.

Thanks in advance.
 
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Start by drawing a picture of the process.

In isothermal expansion, ΔU=0.

Now, W=\int_b^c PdV = \int_b^c \frac{nRT}{V}dV = nRT\ln(\frac{V_c}{V_b})

Do you see what you have to do from here?Also, I don't think this belongs in "advanced physics".
 
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I am not sure. I can use the work function and say it is Q2-Q1, but all of the functions I see that relate S to Q depend on temperature. Unless I can just plug in what T is in terms of P and go from there.

I put it in advanced because it said upper level undergrad and a lot of Carnot engine problems here. So I went with that. If it belongs in beginner phys then so be it.
 
Emspak said:
I am not sure. I can use the work function and say it is Q2-Q1, but all of the functions I see that relate S to Q depend on temperature. Unless I can just plug in what T is in terms of P and go from there.

I put it in advanced because it said upper level undergrad and a lot of Carnot engine problems here. So I went with that. If it belongs in beginner phys then so be it.

How does efficiency relate to Q and T?
 
well let's see. In a Carnot with two different temperatures thermal efficiency \eta = \frac{W}{Q} but that's the thing that gets me here, because Q = c_P(T_2-T_1). But the process is isothermal. I could plug in pressure instead, assuming T constant as I did at the beginning. But that's where this whole problem sort of ceases making sense to me because the whole way a Carnot works is moving heat between reservoirs of two different temperatures and a free expansion of gas does no work at all...
 
\eta = 1-\frac{T_1}{T_2}
\eta = 1+\frac{Q_1}{Q_2}

You can use this along with the adiabatic expansion equation to get Vc/Vb.


Draw a picture of the process.
 
Drawing a picture should be on a P-V diagram, yes? And I should have a diagram in which the let side is Vb and the right side is Vc, and the top is P2 and the bottom p1, yes?

Also, in the second expression with eta, Q1 and Q2 are both dependent on T are they not? And if the process is isothermal T2-T1 is zero! That means η=1. Well ok then, but the original problem says it isn't!

What am I missing here?
 
Emspak said:
Drawing a picture should be on a P-V diagram, yes? And I should have a diagram in which the let side is Vb and the right side is Vc, and the top is P2 and the bottom p1, yes?

Also, in the second expression with eta, Q1 and Q2 are both dependent on T are they not? And if the process is isothermal T2-T1 is zero! That means η=1. Well ok then, but the original problem says it isn't!

What am I missing here?

If you set them equal to each other you'll see that Q1/Q2=-T1/T2=-3/4, since the efficiency is .25. With this relationship and the adibatic expansion equation TV^{\gamma -1} \implies T_{2}V_{c}^{\gamma -1}=T_{1}V_{b}^{\gamma -1}
Now rearrange so that you have Vc/Vb
 
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thanks a lot - i actually figured it out once I looked at my diagram and realized what you were getting at with the b and c subscripts... stupid of me.
 
  • #10
Emspak said:
thanks a lot - i actually figured it out once I looked at my diagram and realized what you were getting at with the b and c subscripts... stupid of me.

Good job :)
 

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