2 cylinders, pushing gas from one to another

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The discussion centers on the thermodynamic equations related to a gas system involving two cylinders. It clarifies that the equation Q=(3/2)nR(ΔT) is not universally applicable for ideal monatomic gases, while ΔU=(3/2)nR(ΔT) is valid. The process in question is identified as isobaric, not adiabatic, which affects the relationship between internal energy (U), work (W), and heat transfer (Q). Participants emphasize that U cannot simply equal W without considering heat transfer, particularly in non-equilibrium states. The final conclusion points to the need for careful application of thermodynamic principles to solve for variables like y and Tf/T.
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Homework Statement



I managed to do part (i) and first part to (ii):

Homework Equations



U = Q + W

The Attempt at a Solution

for the first part:
T/Tf = 1/(2 - y)

for (ii):
W = yVP

Given: (3/2)R = Q/(nΔT),

Q = (3/2)nR(ΔT)

Therefore U = Q + W

U = (3/2)nR(ΔT) + yVP

But then,

isn't U already equal to (3/2)nR(ΔT) since its a monoatomic gas?

Then that gives y = 0, so I'm utterly confused.Here's what the answer writes:

W = yVP

H = (3/2)nR(Tf - T) (does H here mean U?)

Does this imply that heat transferred Q, equals to zero? so W = U?
But there's no indication that this is an adiabatic process? How can we assume that?
 

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Hi unscientific! :smile:

I haven't worked through your entire problem yet, but I think I can answer your questions.

Q=(3/2)nR(ΔT) is not true in general (for ideal monatomic gasses).
What it true, is U=(3/2)nRT or ΔU=(3/2)nR(ΔT) for ideal monatomic gasses.

H would be "enthalpy" defined as H=U+PV.
But that formula would not be right. In this case it should be: H = (5/2)nR(Tf - T).
So perhaps they did intend U, or else you made a typo.

And no, it is not an adiabatic process. The problem specifies that it is an isobaric process.

For reference, here's a table with formulas:
http://en.wikipedia.org/wiki/Table_...ions#Equation_Table_for_a_monatomic_Ideal_Gas
Look at the column for isobaric processes.
 
I like Serena said:
Hi unscientific! :smile:

I haven't worked through your entire problem yet, but I think I can answer your questions.

Q=(3/2)nR(ΔT) is not true in general (for ideal monatomic gasses).
What it true, is U=(3/2)nRT or ΔU=(3/2)nR(ΔT) for ideal monatomic gasses.

H would be "enthalpy" defined as H=U+PV.
But that formula would not be right. In this case it should be: H = (5/2)nR(Tf - T).
So perhaps they did intend U, or else you made a typo.

And no, it is not an adiabatic process. The problem specifies that it is an isobaric process.

For reference, here's a table with formulas:
http://en.wikipedia.org/wiki/Table_...ions#Equation_Table_for_a_monatomic_Ideal_Gas
Look at the column for isobaric processes.


I understand how ΔU=(3/2)nR(ΔT), but i simply don't understand how they simply equate
U = W, in the process ignoring Q, as U = Q + W...
 
unscientific said:
I understand how ΔU=(3/2)nR(ΔT), but i simply don't understand how they simply equate
U = W, in the process ignoring Q, as U = Q + W...

Where do they do this?

You're right, you can't simply equate U=W.
It is only true in an adiabatic process.
 
It is not a quasi-equilibrium process as the gas in both containers are not in equilibrium during the motion of the piston: there is a pressure difference between the containers and a gas flow. The process is not isobaric as the pressure of the whole gas is not defined.

The gas was in equilibrium before opening the valve and reached equilibrium at the end when the temperature and the pressure became equal in both containers.

In the initial state, PV=nRT, in the final one, P(2-y)V=nRTf.

I think it was meant that the walls were adiabatic, not allowing heat transfer. The final temperature would be the same as the initial one otherwise.

So the change of internal energy is equal to the external work done on the whole system, PVy.

The change of internal energy is 3/2 nR(Tf-T).

So you have three equations:

PV=nRT
PV(2-y)=nRTf
3/2nR(Tf-T)= PVy
.

From these, you can find the numerical value of both y and Tf/T.

ehild
 
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