Calculating entropy for an adiabatic system

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Discussion Overview

The discussion revolves around calculating entropy for an adiabatic process involving a gas, specifically addressing the work done on the system, the calculation of entropy production, and the nature of the process (whether it is reversible). Participants explore different approaches to these calculations and clarify the relevant equations.

Discussion Character

  • Homework-related
  • Mathematical reasoning
  • Debate/contested

Main Points Raised

  • One participant presents a scenario involving the adiabatic compression of gas and attempts to calculate work done using the first law of thermodynamics.
  • Another participant questions the calculation of work, suggesting that the change in internal energy should be used instead.
  • There is a discussion about the correct formula for calculating entropy in an adiabatic process, with some participants advocating for using Cv ln(T2/T1) while others suggest using Cp ln(T2/T1) - R ln(P2/P1).
  • One participant calculates entropy production and finds a negative value, prompting further discussion about the validity of their approach.
  • Later replies clarify that the correct approach involves considering both temperature and pressure changes, and that the entropy change should be positive.
  • Participants share their calculations and results, with some noting arithmetic errors in their previous attempts.

Areas of Agreement / Disagreement

Participants do not reach a consensus on the correct method for calculating entropy, as differing opinions on the appropriate equations persist throughout the discussion. There is also uncertainty regarding the interpretation of the results, particularly in relation to the reversibility of the process.

Contextual Notes

Participants express uncertainty about the assumptions underlying their calculations, particularly regarding the conditions for reversibility and the implications of negative entropy production values. There are also unresolved mathematical steps in the calculations presented.

Who May Find This Useful

This discussion may be useful for students or individuals interested in thermodynamics, particularly those studying adiabatic processes and entropy calculations in ideal gases.

hinjab

Homework Statement



  1. A container of 1.5 Kg of gas is at a temperature and pressure of 293 K and 1 bar respectively. The gas is adiabatically compressed until its temperature and pressure are 450 K, 4.49 bars. Adiabatic processes are processes with no heat transfer. The properties of this gas are cv = 10.3 KJ/(Kg K) and R = 4.158 KJ/(Kg K). Neglect kinetic and potential energy terms.

Homework Equations



a) Use the first law to determine the work into the system.

b) Calculate the entropy production for this process.

c) Is this a reversible process?

The Attempt at a Solution



I solved A by saying that the work done = the change in internal energy. So Work done = P1V1 - P2V2 / Y-1 where Y = Cp/Cv = 1.403.
Since P1V1 = NRT1 and P2V2 = nRT2 , I calculated Work done as nRT1-nRT2 / 1.403 - 1 = -2427.79 kJ. The negative sign representing work being done on the system.

I am having trouble calculating B. My understanding would be that the change in entropy for an adiabatic process where volume is constant would be calculated as Cv ln (T2/T1), However I am finding conflicting ideas online, where people are actually calculating it as Cp ln (T2/T1) - R ln (P2/P1). When I calculate it that way, I get a negative number of -61.71 J/K for entropy production.

Can anyone explain if that is the right way to calculate it, or if I should be doing it the way I originalyl thought was correct (Entropy production = Cv ln (T2/T1)?Thanks!
 
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You calculated the work incorrectly. What is the equation for the change in internal energy of an ideal gas?
 
the change in internal energy of an ideal gas would be Δ U = n Cv Δ T . . . since there is no heat transfer for this, should I be saying that work actually equals this equation?
 
Chestermiller said:
You calculated the work incorrectly. What is the equation for the change in internal energy of an ideal gas?

the change in internal energy of an ideal gas would be Δ U = n Cv Δ T . . . since there is no heat transfer for this, should I be saying that work actually equals this equation?
 
hinjab said:
the change in internal energy of an ideal gas would be Δ U = n Cv Δ T . . . since there is no heat transfer for this, should I be saying that work actually equals this equation?
Sure
 
Chestermiller said:
Sure

Okay, thanks.

My other question is in regards to part B. Can you please help me understand which equation I should be using in the two that I listed above to solve for entropy?
 
hinjab said:
Okay, thanks.

My other question is in regards to part B. Can you please help me understand which equation I should be using in the two that I listed above to solve for entropy?
You should be using the one that the other people are using, not the one you wanted to use. The one they are using is, of course, per unit mass, so you have to multiply by the mass of gas. The reason their equation is correct is that, in addition to the temperature changing, the pressure and volume also changed. The answer should come out positive, so maybe you made a mistake in arithmetic. Please show your work.

Chet
 
Chestermiller said:
You should be using the one that the other people are using, not the one you wanted to use. The one they are using is, of course, per unit mass, so you have to multiply by the mass of gas. The reason their equation is correct is that, in addition to the temperature changing, the pressure and volume also changed. The answer should come out positive, so maybe you made a mistake in arithmetic. Please show your work.

Chet
Hi Chet,

Thanks for your response. You are very helpful.

Here is my math:
Cp - Cv = R
Cp = R + Cv
Cp = 4.158 KJ/Kg*K + 10.3 KJ/Kg*k = 14.458 KJ/Kg*k

Entropy production calculation:
Delta S = M*Cp*ln(T2/T1) - M*R*ln (P2/P1)
Delta S = (1.5 Kg)*(14.458 KJ/Kg*K)*ln(450K/293K) - (1.5 Kg)*(4.158 KJ/Kg*K)*ln(449000 pascals/100000 pascals)
Delta S = 9.305 - 9.948 KJ/K
Delta S = -0.643 KJ/K
 
hinjab said:
Hi Chet,

Thanks for your response. You are very helpful.

Here is my math:
Cp - Cv = R
Cp = R + Cv
Cp = 4.158 KJ/Kg*K + 10.3 KJ/Kg*k = 14.458 KJ/Kg*k

Entropy production calculation:
Delta S = M*Cp*ln(T2/T1) - M*R*ln (P2/P1)
Delta S = (1.5 Kg)*(14.458 KJ/Kg*K)*ln(450K/293K) - (1.5 Kg)*(4.158 KJ/Kg*K)*ln(449000 pascals/100000 pascals)
Delta S = 9.305 - 9.948 KJ/K
Delta S = -0.643 KJ/K
For the 2nd term, I get 9.367, not 9.948. So, for the change in entropy, I get ##\Delta S=-0.0617##. This is pretty close to zero, so I would call it reversible.

That being the case, the result you got for the work using the equation that applies only for an adiabatic reversible change (i.e., in your original post) should come very close to matching the result you got using the relationship for the internal energy change. Does it?
 
  • #10
Hi Chet,

Sorry about that. I did mess up the arithmetic! I also got the same answer as you for the second term. I didn't know that it was OK to consider an entropy change that is very close to zero as zero, thus making it reversible. Thank you for the info.

When I calculated the work done by using the internal energy change (the way you suggested) I get 2425.65 KJ, as opposed to the 2429.79 KJ in my original attempt.
 
  • #11
hinjab said:
Hi Chet,

Sorry about that. I did mess up the arithmetic! I also got the same answer as you for the second term. I didn't know that it was OK to consider an entropy change that is very close to zero as zero, thus making it reversible. Thank you for the info.

When I calculated the work done by using the internal energy change (the way you suggested) I get 2425.65 KJ, as opposed to the 2429.79 KJ in my original attempt.
Looks good. Nice job.
 
  • #12
Chestermiller said:
Looks good. Nice job.

Thank you so much for your help!
 

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