Change in entropy of an irreversible adiabatic process

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The discussion focuses on calculating the change in entropy for an irreversible adiabatic process, emphasizing that entropy is not zero and requires a reversible path for accurate calculation. Participants express difficulty in determining final pressure (P2) and temperature (T2), with suggestions to use heat capacities and internal energy changes to find ΔT and subsequently T2. The ideal gas law is recommended for calculating P2, ensuring consistency with enthalpy changes. There is a collaborative tone, with an invitation for others to engage in the problem-solving process. The conversation highlights the complexities involved in thermodynamic calculations and the need for careful analysis.
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Homework Statement
We have 5.32 L of an ideal diatomic gas at 16.3 bar and 371 K. The gas is in an insulated cylinder contained with an insulated piston. We unlock the piston and the gas expands against a constant external pressure of 1.43 bar until the piston is locked again at triple the original volume. Calculate the values of the parameters below for this process. Express all energies in J and entropy in J/K.
Relevant Equations
W= PexdV
delta U = q+ w
ds= dq/T
Screen Shot 2021-03-02 at 6.56.49 PM.png

I have been able to get everything except entropy. I know it's not zero. I know I have to find a reversible path to calculate it, but keep coming up with strange values so I don't think I'm doing it correctly.
can I do CpdT/T + CvdT/T = ds? I am having trouble calculating my P2 (I know my final pressure is not the constant external pressure) and T2.
 
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Please show us how you calculated T2. Also, how did you get the change in enthalpy if you do not know P2?

Please describe for us the alternative reversible process you devised to determine the change in entropy (it may involve two process steps).
 
I agree with your calculated internal energy change. For an enthalpy change, I get 1.4 times as much, or -2123 J. The next step is to determine the final temperature. You know the internal energy change, the number of moles of gas, and the heat capacity of the gas. From that, you can determine ΔT. What value do you get, and what do you get for the final temperature.

You can get the final pressure P2 knowing the final temperature and employing the ideal gas law, or from the enthalpy change, since you know ΔU, P1, V1, and V2. The values you get from both these methods should agree.
 
It doesn't look like the OP is going to return to complete this. If anyone else would like to continue for practice, please feel free to do so. I will continue to look on.

Chet
 
If have close pipe system with water inside pressurized at P1= 200 000Pa absolute, density 1000kg/m3, wider pipe diameter=2cm, contraction pipe diameter=1.49cm, that is contraction area ratio A1/A2=1.8 a) If water is stationary(pump OFF) and if I drill a hole anywhere at pipe, water will leak out, because pressure(200kPa) inside is higher than atmospheric pressure (101 325Pa). b)If I turn on pump and water start flowing with with v1=10m/s in A1 wider section, from Bernoulli equation I...

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