Entropy Change of a Monatomic Ideal Gas Compressed Adiabatically

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SUMMARY

The discussion centers on calculating the entropy change (ΔS) of a monatomic ideal gas compressed adiabatically. The initial conditions include 1.00 mole of gas, an initial volume of 10.00 L, a final volume of 4.00 L, and a constant external pressure of 50.00 atm. The user initially assumed ΔS to be zero due to the adiabatic nature of the process but was corrected that ΔS cannot be zero for irreversible processes. The final temperature was calculated to be 322.06 K using the equation ΔU = -PextΔV, but unit conversions were necessary for accurate results.

PREREQUISITES
  • Understanding of thermodynamic principles, specifically adiabatic processes.
  • Familiarity with the ideal gas law and related equations.
  • Knowledge of unit conversions between atmospheres and Pascals, as well as liters and cubic meters.
  • Ability to calculate changes in internal energy (ΔU) and entropy (ΔS).
NEXT STEPS
  • Learn about the equations for entropy change in ideal gases, specifically in terms of volume and temperature ratios.
  • Study the principles of reversible versus irreversible processes in thermodynamics.
  • Explore the implications of adiabatic processes in real-world applications, such as internal combustion engines.
  • Review unit conversion techniques to ensure accuracy in thermodynamic calculations.
USEFUL FOR

Students and professionals in thermodynamics, particularly those studying or working with ideal gases and adiabatic processes, as well as anyone needing to understand entropy changes in various thermodynamic scenarios.

Basis
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Homework Statement



A monatomic ideal gas is compressed adiabatically. What is ΔS of the gas?

n = 1.00
vi = 10.00 L
vf = 4.00 L
Constant External Pressure = 50.00 atm


Homework Equations



ΔU = q + w = 0 + (-PextΔV)
ΔS = ∫[(qrev)/T]dQ


The Attempt at a Solution



In order to calculate ΔS you have connect two thermodynamic states with a reversible path. I assumed that the ΔS of the system is 0 because dQ is 0 for adiabatic processes). Then second state focuses on ΔS of the surroundings that has an external pressure associated with it.

I found Tf = 322.06 K by using the ΔU equation

I am not sure what to do at this point, because every single attempt I made has led me to a negative ΔS.
 
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Basis said:

Homework Statement



A monatomic ideal gas is compressed adiabatically. What is ΔS of the gas?

n = 1.00
vi = 10.00 L
vf = 4.00 L
Constant External Pressure = 50.00 atm

Homework Equations



ΔU = q + w = 0 + (-PextΔV)
ΔS = ∫[(qrev)/T]dQ

The Attempt at a Solution



In order to calculate ΔS you have connect two thermodynamic states with a reversible path. I assumed that the ΔS of the system is 0 because dQ is 0 for adiabatic processes). Then second state focuses on ΔS of the surroundings that has an external pressure associated with it.

I found Tf = 322.06 K by using the ΔU equation

I am not sure what to do at this point, because every single attempt I made has led me to a negative ΔS.
You cannot assume that the ΔS = 0 because the process is not reversible. Since external pressure is constant and internal pressure varies, the compression is not quasi-static. A reversible path between the initial and final states is not adiabatic - there is heat flow.

I am not sure how you are calculating the final temperature. Are you given the initial temperature or the initial (internal) pressure of the gas?

AM
 
Yeah I started thinking it over and it wouldn't make sense. I thought I had read somewhere that if it is reversible it is 0. I am sorry I thought I had specified that initial temperature. It is at 298 K

I used

ΔU = -PextΔV
ΔU = =-(50.00 atm)(4.00 L - 10.00 L) = 300 J
300 J = n(3/2)R(Tf - Ti)
300 J = (1.00 mole)(3/2)(8.314 J/Kmol)(Tf - 298 K)
Tf = 322.06 K

But the question is given that it is compressed adiabatically so that's where my problem lies
 
Basis said:
Yeah I started thinking it over and it wouldn't make sense. I thought I had read somewhere that if it is reversible it is 0. I am sorry I thought I had specified that initial temperature. It is at 298 K
If the process is reversible the ΔS of the system + surroundings will be 0. As I said, this is not a reversible process. To calculate entropy change you have to first find a reversible path between the beginning and end states. So you have to find the pressure, volume and temperature of the gas initially and at the end and then find a reversible path from the initial to final states.

I used

ΔU = -PextΔV
ΔU = =-(50.00 atm)(4.00 L - 10.00 L) = 300 J
Whoa! You need MKS units to get an answer in Joules: Pressure is in Pascals and Volume is in m3. 1 atm = 101.325 x 103 Pa. and 1 L = 10-3 m3.

300 J = n(3/2)R(Tf - Ti)
300 J = (1.00 mole)(3/2)(8.314 J/Kmol)(Tf - 298 K)
Tf = 322.06 K

But the question is given that it is compressed adiabatically so that's where my problem lies
Your method is ok. You are just out by a few orders of magnitude with the units. (R = 8.314 J/mol-K). Tf is much higher than 322K.

Apart from the units, I am not sure where you are having a problem. Adiabatic processes do not have to be quasi-static. Compression in an internal combustion engine is a good example of an irreversible adiabatic compression.

Welcome to PF by the way!

AM
 
I came to that realization not too long ago thankfully. I am glad for the clarification. I thought I was going mad for a second. Thank you so much!
 
You still need to get the entropy change. You have all the information you need about the initial and final states. You just need to figure out a reversible path from the initial to the final state and calculate dq/T for that path, or (less preferably) you need to remember the equation for the change of entropy for an ideal gas in terms of the volume ratio and the temperature ratio. Have you seen an equation like that?

Chet
 

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