[Thermodynamics] Transient Analysis of an air-filled tank

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The discussion revolves around a transient analysis problem involving an air-filled tank where the pressure decreases from 300 kPa to 100 kPa while maintaining a specific volume relationship. The user has calculated specific volumes and looked up relevant enthalpy and internal energy values but is uncertain about how to handle the varying enthalpy during integration. Suggestions include using the energy equation in differential form to account for changes in enthalpy over time and considering mass flow rates and heat transfer at the control volume boundaries. The user attempted to use the average of initial and final enthalpies but found it incorrect. Accurate handling of varying enthalpy is crucial for solving the energy balance correctly.
dav2008
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Hey I think I'm missing something fundamental in this problem.

The problem reads: a 1 m3 tank initially contains air at 300 kPa, 300K. The air slowly escapes until the pressure drops to 100 kPa, via a process where pv1.2=constant (v being specific volume)

Find the heat transfer for a control volume enclosing the tank, assuming ideal gas behavior with constant specific heats.

I have determined the specific volumes of the initial and final states and I have looked up enthalpy and internal energy values for initial and final states. This is more of a symbolic question I have so I'll leave those out.

The energy balance (all for control volume, so I don't have to write cv over and over)

dU/dt = dQ/dt +(dm/dt)he where he is the enthalpy at the outlet valve.

Integrating with respect to time from state 1 to 2 would give m\Deltau=Q+(mf-mi)he

Now this is where I have several questions. 1) It seems like since the enthalpy is varying and not constant that I should have somehow considered that in the integration. I'm just not sure how I would approach the fact that the enthalpy at the outlet is varying over time.

I considered using the average of the initial and final enthalpies but that didn't yield a correct answer.


Thanks.
 
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It's hard to answer this question without seeing the exact problem and what you have already tried. However, one thing to consider when dealing with a process where the enthalpy is changing over time is to use the energy equation in differential form. That way, you can account for any changes in enthalpy over time and get a more accurate result. You may also need to consider the mass flow rate and any heat transfer that occurs at the boundaries of the control volume.
 
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