Fluid flow out of pressurized vessel

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SUMMARY

The discussion focuses on calculating fluid flow rates from a pressurized non-rigid vessel, specifically using principles of fluid dynamics. The relationship between pressure drop and flow rate is established through the Hagen-Poiseuille equation for laminar flow and the Darcy-Weisbach equation for turbulent flow. Key parameters include the Reynolds number (Re), pressure drop (ΔP), and tube characteristics such as length (L) and diameter (D). The iterative nature of the calculations is emphasized, requiring adjustments to the Reynolds number until convergence is achieved.

PREREQUISITES
  • Understanding of fluid dynamics principles, including laminar and turbulent flow.
  • Familiarity with the Hagen-Poiseuille equation for laminar flow.
  • Knowledge of the Darcy-Weisbach equation for turbulent flow.
  • Ability to calculate Reynolds number (Re) and friction factor (λ).
NEXT STEPS
  • Study the Hagen-Poiseuille equation in detail for laminar flow calculations.
  • Learn about the Darcy-Weisbach equation and its application in turbulent flow scenarios.
  • Explore methods for calculating the friction factor (λ) in various flow conditions.
  • Investigate iterative numerical methods for solving fluid dynamics equations.
USEFUL FOR

Engineers, fluid dynamics researchers, and anyone involved in the design and analysis of fluid transport systems, particularly in applications involving pressurized vessels.

koch15
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I have a non-rigid vessel holding a fluid with a tube for fluid flow out. It is initially at equilibrium pressure with the atmosphere. (Think a water bladder for a camelback hydration system) A pressure is then applied to the bag to cause fluid to flow out the tube. Is there a way to relate the fluid flow rate to the pressure applied?

Thanks
 
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Yes, there is. The pressure drop over the tube is known (pressure in the bladder/vessel minus ambient pressure at the end of the hose). Knowing that pressure drop, you know is has to be equal to the pressure drop due to viscous forces acting inside the tube.

Note, it changes whether you are in the laminar or turbulent regime. It is very difficult to calculate if the length is equal to or shorter than the development length.

[itex]Re=\frac{\rho D V_{avg}}{\mu}[/itex]

Laminar: Re < 2300
L_developing = 0.03*Re*D
[itex]Q=\frac{-\pi R^{4}}{8 \mu}\frac{\Delta P}{L}[/itex]
(ΔP is pressure drop, L is length of tube, Q is volume flow rate, or V_avg*A_cross sectional).

Source: http://faculty.poly.edu/~rlevicky/Handout12_6333.pdf

Turbulent: Re > 2300
L_developing ≈ 10*D
[itex]\frac{1}{\sqrt{\lambda}}=-2LOG\left(\frac{2.51}{Re\sqrt{\lambda}}+0.269\frac{k}{D}\right)[/itex]
[itex]\Delta P=\lambda \frac{L}{D}\frac{\rho}{2}V_{avg}^{2}[/itex]
(ΔP is pressure drop, L is length of tube, λ is the friction factor, k is the absolute roughness of the tube where 0 is smooth).

Source: http://www.engineersedge.com/fluid_flow/pressure_drop/pressure_drop.htm

Note: It is iterative, and you will have to guess a value for Re, calculate the friction factor, calculate a new velocity, calculate a new Re, until your solution has converged.
 
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