Coefficient of Drag: Low Velocity Ellipsoids

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SUMMARY

The discussion focuses on determining the drag coefficient for prolate and tri-axial ellipsoids at low velocities (less than 0.5 m/s) in water. The standard drag equation can be linearized to F_d=γv, where γ represents the drag coefficient. For spheres, the drag coefficient at low velocities is given by C_d=24/Re, with the Reynolds number defined as Re=ρvD/μ. The drag force for a prolate ellipsoid oriented with its short axis in the flow direction is approximated by F_d=1.2πμ(4+E)a v, where E is the aspect ratio.

PREREQUISITES
  • Understanding of the drag equation and its components
  • Familiarity with Reynolds number calculations
  • Knowledge of Stokes' law and its application to fluid dynamics
  • Basic concepts of ellipsoidal geometry and aspect ratios
NEXT STEPS
  • Research the derivation of drag coefficients for non-spherical particles
  • Study the book "Bubbles, Drops and Particles" by Clift, Grace, and Weber
  • Examine the principles of low Reynolds number hydrodynamics in "Low Reynolds Number Hydrodynamics" by Happel and Brenner
  • Explore computational fluid dynamics (CFD) simulations for drag force analysis
USEFUL FOR

Researchers in fluid dynamics, engineers working with particle drag in fluids, and students studying low-velocity fluid interactions will benefit from this discussion.

omertech
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Hello,

I understood that in low velocities the standrad drag equation:
F_d=\frac{ρv^2C_dA}{2}
Could linearized to something like:
F_d=γv
I am looking for the drag coefficient(either γ or Cd) for either a prolate or a tri-axial ellipsoid at low velocities (less than 0.5 m/s) in water. I found some papers providing drag coefficients for relatively high velocities but none with drag coefficients for low velocities.

Best regards
 
Last edited:
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For spheres, the drag coefficient at low velocities can be determined analytically, see e.g. the book of Clift, Grace and Weber - Bubbles, Drops and Particles or Happel and Brenner, Low Reynolds number hydrodynamics. It is
\mathrm{C_d}=\frac{24}{\mathrm{Re}}
With the Reynolds number
\mathrm{Re}=\frac{\rho v D}{\mu}

Because A is the cross-sectional surface of the sphere, the force can be written as:
F_d=3\pi \mu D v, which is known as Stokes' law.

The drag of a nonspherical particle depends on its orientation with respect to the mean flow.

For a prolate with aspect ratio E=b/a and oriented such that that the short axis with length a (from center to edge) is in the direction of the flow, the drag component is approximately
F_d=1.2\pi \mu (4+E) a v.

Note that when E=1, then 2a=D and Stokes' result is recovered. The derivation is for instance in Happel and Brenner's book.
 

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