Understanding Drag Force: Standard Formula vs. Alternative Formula Explained

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SUMMARY

The discussion focuses on two formulas for calculating drag force: the standard formula FD = 1/2 CD * ApV^2 and an alternative approximation FD = 1/4 AV^2. The standard formula incorporates the drag coefficient (CD), cross-sectional area (A), fluid density (ρ), and velocity (v), while the alternative formula simplifies the relationship by assuming CD⋅ρ = 0.5. The approximation is valid under specific conditions where area and velocity changes occur in a constant density fluid, but it fails when these conditions are not met, leading to inaccuracies in drag force calculations.

PREREQUISITES
  • Understanding of fluid dynamics principles
  • Familiarity with drag coefficient (CD) concepts
  • Knowledge of cross-sectional area (A) in fluid flow
  • Basic physics of motion and forces
NEXT STEPS
  • Research the implications of varying drag coefficients in different fluids
  • Explore the effects of cross-sectional area on drag force in practical applications
  • Study the relationship between velocity and drag force in turbulent vs. laminar flow
  • Learn about computational fluid dynamics (CFD) tools for drag force analysis
USEFUL FOR

Students in physics or engineering, researchers in fluid dynamics, and professionals involved in aerodynamics or automotive design will benefit from this discussion.

jason bourne
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I know that standard formula is, FD = 1/2 CD *ApV^2


FD = Drag Force. SI: N
CD = Drag Coefficient. SI: Dimensionless (Typical Values)
A = Coss-sectional Area perpendicular to the flow. SI: m2
r = Density of the medium. SI: kg/m3
v = Velocity of the body relative to the medium. SI: m/s

But our prof also said there's another formula for drag force,

FD = 1/4 AV^2

(Its is not supposed to be equal but approximately)

So the question is when is the equation above false, what's the error in the equation that makes it approximate.
 
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Such a simple equation assumes that CD⋅ρ = 0.5
Where ∝ means proportional to; FD ∝ ¼⋅A⋅V2
can be further simplified to; FD ∝ A⋅V2
That can only be applied where changes to area or velocity occur, while maintaining a constant profile in a constant density fluid.
 

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