UO1-Topic 1 (Part 5) Particle Motion AY2021
Particle Motion 1
Objectives
Define drag force.
Calculate drag force for flow past various solid bodies such as spheres, cylinders, and discs.
What is Drag Force?
Definition: When a solid body moves through a fluid or a fluid flows past a solid body, the fluid resists the motion of the object.
Opposing Force: The force opposing the motion of the object is termed drag force, which acts to retard the object's motion.
Parameters Affecting Drag Force
Velocity: The speed of the object or fluid.
Size: The dimensions of the object.
Shape: The geometry of the object affects the flow around it.
Density of Fluid: The mass density of the fluid influences drag.
Viscosity of Fluid: The fluid's resistance to flow affects drag; higher viscosity usually results in higher drag.
Types of Flow
Laminar Flow: Smooth and orderly fluid motion.
Turbulent Flow: Chaotic and irregular fluid motion.
Flow Past A Cylinder
Conditions: If the fluid is incompressible and the cylinder is small, the kinetic and pressure energy remains constant across the surface of the cylinder.
Bernoulli's Equation
Represents the conservation of energy in fluid flow:
( PA + \frac{1}{2} \rho U^2 + \rho gh = constant )
Energy Change
Kinetic Energy: Maximum at points B and C, zero at A and D.
Pressure Variation: Pressure decreases from A to B and A to C; it rises from B to D and C to D, remaining equal at A and D.
Calculation of Drag Force
Formula: [ F_D = C_D \cdot \rho \cdot A_P \cdot \frac{U_0^2}{2} ]
Where:
( F_D ): Drag force
( C_D ): Drag coefficient
( A_P ): Projected area
( U_0 ): Velocity of the flow
Finding Drag Coefficient
Common Values:
Spheres: ( C_D = 0.5 )
Cylinders: ( C_D = 0.33 )
Disks: ( C_D = 1.12 )
Flow Characteristics
Flow past a Sphere: ( T_{ap} = 4 \pi )
Flow Parallel to Cylinder: ( T_{A2} = \frac{P}{4} )
Flow Perpendicular to Cylinder: ( dp L A = dp \times L )
Example Problem 1.11
Scenario: Air at 37.8 °C and 101.3 kPa flows past a 45 mm diameter sphere at 25 m/s.
Drag Coefficient Calculation:
From CD chart for spheres, ( C_D = 0.5 )
Calculated Parameters:
Diameter: ( dp = 0.045 m )
Velocity: ( U_0 = 25 m/s )
Projected Area Calculation for Sphere
[ A_P = \frac{\pi (0.045^2)}{4} \approx 1.59 \times 10^{-3} m^2 ]
Example Problem 1.12
Scenario: A cylindrical steam boiler stack with diameter 1.0 m and height 30 m is exposed to air.
Parameters given:
Temperature: 37.8 °C, Velocity: 180 km/h = 50 m/s
Density: 1.137 kg/m³, Viscosity: 1.9 x 10⁻⁵ Pa·s
Drag Force Calculation: [ F_D = C_D \cdot p \cdot (D_P imes L) \cdot \frac{U_0^2}{2} ]
With calculated drag force ( F = 14070 N ) at ( C_D = 0.33 )