How Does a Pressurized Tank Empty Over Time Through a Hole?

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SUMMARY

This discussion focuses on modeling the pressure vs. time curve for a 10L tank of compressed air at 100 psi (114 psi absolute) as it empties through a hole with a cross-sectional area of 0.115 in². The analysis requires understanding two flow regimes: sonic flow when the internal pressure exceeds 1.9 times atmospheric pressure and subsonic flow at lower pressures. The LOHM concept is essential for calculating flow rates based on orifice size and pressure differentials. Resources such as pneumatic handbooks and valve manufacturer guidelines provide necessary engineering formulas for this analysis.

PREREQUISITES
  • Understanding of fluid dynamics principles
  • Familiarity with sonic and subsonic flow equations
  • Knowledge of the LOHM concept for flow rate calculations
  • Basic grasp of pressure measurement and conversion (psi to absolute pressure)
NEXT STEPS
  • Research the LOHM formula for calculating flow rates through orifices
  • Study sonic and subsonic flow equations in fluid dynamics
  • Explore pneumatic handbooks for additional engineering formulas
  • Investigate experimental methods for measuring pressure decay over time
USEFUL FOR

Engineers, fluid dynamics students, and anyone involved in pneumatic system design or analysis will benefit from this discussion, particularly those interested in pressure vessel behavior and flow rate calculations.

ab042896
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I having difficulty wrapping my head around a concept that I wish to solve. I have a 10L tank of compressed air at 100psi. When an outlet hole of cross-sectional area of 0.115 in^2 is opened, I wish to develop a curve of pressure vs. time from t=0 until pressure drops to atmospheric. Many things can be neglected in this situation, such as friction etc., since I would like a general curve to compare with experimental data. I am unsure of how to apply fluid dynamics to a vessel that empties simply due to its own pressure difference through an area.

Temperature can be assumed to be constant at 25C as well.
 
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You can find engineering formula in places such as valve manufacturers, pneumatic handbooks, etc. Here is an example http://www.theleeco.com/engineering/engineering.cfm#lohm-laws-working-with-gases

You have to be aware that you will need two regimes for your problem: initially the inside pressure is greater than 1.9 x atmospheric and you need a sonic formula. At lower pressures subsonic equations will do.
 
Doesn't
Henryk said:
You can find engineering formula in places such as valve manufacturers, pneumatic handbooks, etc. Here is an example http://www.theleeco.com/engineering/engineering.cfm#lohm-laws-working-with-gases

You have to be aware that you will need two regimes for your problem: initially the inside pressure is greater than 1.9 x atmospheric and you need a sonic formula. At lower pressures subsonic equations will do.
100psi relative is 114psi absolute, which is nearly eight times greater than atmospheric. Are you aware of any ways that this could be done to give a rugh estimate? After all I will be testing this and ultimately have the real data to compare this to.
 
Follow the link. You will find a number of pages with relevant information. Lee valve company uses LOHMS concept. Find how to calculate LOHM for a give size orifice and then the flow rate as a function of pressure.
 

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