[Thermodynamics] Transient Analysis of an air-filled tank

Click For Summary
SUMMARY

The discussion focuses on the transient analysis of an air-filled tank undergoing a process where the pressure decreases from 300 kPa to 100 kPa, following the relation pv1.2 = constant. The user seeks clarification on how to accurately account for varying enthalpy during the integration of the energy balance for a control volume. Key insights include the necessity of using the energy equation in differential form to accommodate changes in enthalpy over time and the importance of considering mass flow rates and heat transfer at the control volume boundaries.

PREREQUISITES
  • Understanding of ideal gas behavior and specific heats
  • Familiarity with energy balance equations in thermodynamics
  • Knowledge of transient analysis in control volumes
  • Ability to perform integration with respect to time in thermodynamic processes
NEXT STEPS
  • Study the application of the energy equation in differential form for transient systems
  • Learn about the implications of varying enthalpy in thermodynamic processes
  • Research mass flow rate calculations in control volume analysis
  • Explore heat transfer mechanisms at the boundaries of control volumes
USEFUL FOR

Thermodynamics students, engineers involved in fluid dynamics, and professionals conducting transient analysis of thermal systems will benefit from this discussion.

dav2008
Gold Member
Messages
589
Reaction score
1
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[tex]\Delta[/tex]u=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.
 
Physics news on Phys.org
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.
 

Similar threads

  • · Replies 4 ·
Replies
4
Views
3K
  • · Replies 14 ·
Replies
14
Views
3K
  • · Replies 8 ·
Replies
8
Views
2K
  • · Replies 3 ·
Replies
3
Views
2K
  • · Replies 56 ·
2
Replies
56
Views
6K
  • · Replies 10 ·
Replies
10
Views
2K
Replies
17
Views
3K
  • · Replies 12 ·
Replies
12
Views
4K
  • · Replies 3 ·
Replies
3
Views
3K
Replies
12
Views
3K