Quasi-static, adiabatic problem

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Homework Help Overview

The discussion revolves around a quasi-static, adiabatic process involving a monatomic ideal gas. The original poster presents a problem where two moles of gas are expanded adiabatically from an initial temperature of 0°C to a final temperature of -50°C, seeking to determine the initial and final pressures and the final volume.

Discussion Character

  • Mixed

Approaches and Questions Raised

  • The original poster attempts to use the ideal gas law to find the initial pressure and applies the first law of thermodynamics to relate internal energy and work done. They express confusion regarding the final pressures and the work done during the process.
  • Some participants question the validity of the original poster's approach, particularly regarding the application of work done in adiabatic processes versus isothermal processes.
  • Others suggest integrating the first law of thermodynamics and checking the manipulation of logarithmic expressions related to temperature and volume ratios.
  • There is a discussion about potential errors in calculations and the possibility of typos in the reference material being used.

Discussion Status

The conversation is ongoing, with participants providing guidance on integrating equations and checking assumptions. There is recognition of a potential typo in the reference material, which may have contributed to confusion regarding the expected results. Multiple interpretations of the equations and their applications are being explored.

Contextual Notes

Participants note discrepancies in the expected versus calculated values, with specific attention to unit conversions and the implications of the adiabatic process on volume changes. There is an acknowledgment of possible errors in the provided reference material that could affect the discussion.

mateomy
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Two moles of a monatomic ideal gas are at a temperature of 0°C and a
(dQ = 0) and quasi-static volume of 45 liters. The gas is expanded adiabatically
until its temperature falls to - 50°C. What are its initial and final pressures and its final volume?

I've been beating my head against a wall for a while now on this one.

I know how to find the initial pressure. That's just an easy PV=nRT problem. I get an answer of 100,956 Pa (0.1MPa). I can't find the final pressures though, totally stuck.

So what I've done thus far is to utilize the first law in that I know dQ = 0. So I know that dU = -dW. Solving the U = cNRT for initial and final temperatures and taking the difference, I get an energy which I know must be attributed to the work done. This is where I get stuck.

Not sure what steps to take next. Need some assistance, thanks.

I thought I could try
<br /> W = - \int PdV<br />
which I could do some substitution to get to (eventually),
<br /> W = -nRTln\left(\frac{V_f}{V_i}\right)<br />
But when I do that and I set W to the difference in energy I found earlier, I get an answer that doesn't match my book's.
 
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No, but you almost have it. Going back to your equation for the first law:

dU=cNRdT=-PdV=-(NRT/V)dV

where c = 3/2

Cancel NR from both sides, divide both sides by T, and integrate.

Chet
 
mateomy said:
I thought I could try
<br /> W = - \int PdV<br />
which I could do some substitution to get to (eventually),
<br /> W = -nRTln\left(\frac{V_f}{V_i}\right)<br />
But when I do that and I set W to the difference in energy I found earlier, I get an answer that doesn't match my book's.
This doesn't work because that expression for the work done is for isothermal processes. That's not what you have here.
 
Chestermiller said:
dU=cNRdT=-PdV=-(NRT/V)dV

where c = 3/2

Cancel NR from both sides, divide both sides by T, and integrate.

Chet

So this is what I've done on your suggestion (asking for my work to be checked because my answer still isn't correct):

<br /> cNRdT = -\frac{NRTdV}{V}<br />

<br /> \frac{cdT}{T} = \frac{dV}{V}<br />

<br /> c \int_{T_i}^{T_f} \frac{dT}{T} = - \int_{V_i}^{V_f} \frac{dV}{V}<br />

<br /> c\,ln\left(\frac{T_f}{T_i}\right) = - ln\left(\frac{V_f}{V_i}\right)<br />

<br /> e^{c} (T_f - T_i) = -(V_f - V_i)\,\,\,\,\,\,negatives\,cancel\,here<br />

from which I get a result of 224.04. However, the answer is 61E3. Still unsure...
 
mateomy said:
<br /> c\,ln\left(\frac{T_f}{T_i}\right) = - ln\left(\frac{V_f}{V_i}\right)<br />

<br /> e^{c} (T_f - T_i) = -(V_f - V_i)\,\,\,\,\,\,negatives\,cancel\,here<br />
You exponentiated the LHS wrongly. eab is not eaeb.
 
I'm insanely confused then. Is it,
<br /> \left(\frac{T_f}{T_i}\right)^{c}<br />
 
mateomy said:
I'm insanely confused then. Is it,
<br /> \left(\frac{T_f}{T_i}\right)^{c}<br />
Now you're cookin'. Of course, you follow the same recipe on the RHS of the equation.

Chet
 
Now I'm becoming embarrassed...
<br /> \left(\frac{T_f}{T_i}\right)^{c} = \left(\frac{V_f}{V_i}\right)^{-1}<br />
<br /> \left(\frac{T_f}{T_i}\right)^{c} = \left(\frac{V_i}{V_f}\right)<br />
<br /> V_i \left(\frac{T_i}{T_f}\right)^{c} = V_f<br />
But I'm still not getting the correct answer.
 
  • #10
The given answer (from Callen) is 61 x 10^{3} m^{3}. My answer is 0.06095. It almost seems like there's a conversion error but I don't see it. From the initial values: 45 liters = 0.045 cubic meters, 0 C = 273K, and -50 C = 223K.
 
  • #11
Although...

I'm looking at my PDF (don't have the 'real' book) and it's entirely possible that the negative is smudged out. I've noticed a lot of cosmetic errors in this PDF. That seems reasonable if my equation is correct and I am off by that magnitude. Maybe someone could check my numbers to confirm?
 
  • #12
mateomy said:
The given answer (from Callen) is 61 x 10^{3} m^{3}. My answer is 0.06095. It almost seems like there's a conversion error but I don't see it. From the initial values: 45 liters = 0.045 cubic meters, 0 C = 273K, and -50 C = 223K.
No need to check the calculation in detail. It's quite clear that the volume would not expand by more than a factor of 10, probably much less. So 61 litres is reasonable.
 
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  • #13
mateomy said:
The given answer (from Callen) is 61 x 10^{3} m^{3}. My answer is 0.06095. It almost seems like there's a conversion error but I don't see it. From the initial values: 45 liters = 0.045 cubic meters, 0 C = 273K, and -50 C = 223K.

Yeah. That should be 10-3. You did a really nice job on this problem. Too bad the book had that typo.
 
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  • #14
Ugh. I can't believe it was a typo. At least I got some lessons out of it. Thank you, both.
 

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