Fluid Mechanics

External flows

Lecturer: Jakob Hærvig

Slides by Jakob Hærvig (AAU Energy) and Jacob Andersen (AAU Build)

Introduction to External Flows

External flows: Flow around bodies immersed in fluid


  • Air flow (aerodynamics) around:
    • Buildings
    • Wind turbine blade
    • Airplanes/drones
    • Cars

  • Water flow (hydrodynamics) around:
    • Offshore wind turbine foundation
    • Vessels
    • Submarines
    • Water turbine

External Flows Examples

Object categorisation

Categorisation of objects:

  • 2-D objects (infinitely long, constant cross-section)
  • Axisymmetric objects (cross-section rotated about symmetry axis)
  • 3-D objects

Note: Nominal 2-D objects may need to be modelled as 3-D depending on the flow characteristics

Further classification:

  • Streamlined objects - small fluid disturbance
    • Airfoils, ship hulls, some cars
  • Blunt/bluff objects - significant fluid disturbance
    • Buildings, bridges, some cars, stalled airfoils, parachutes

2-D flat plate

Total force on any object

Commonly split up in two different contributions

  • Surface normal force due to pressure:
  • $\displaystyle \boldsymbol{F}_p = \int p \cdot \mathbf{n} \, \text{d}A$
    • On all points on the surface, $\mathbf{F}_p$ acts in the normal direction

  • Surface shear force due to shear stress:
  • $\displaystyle \boldsymbol{F}_\tau = \int \tau_w \cdot \mathbf{t} \, \text{d}A$
    • On all points on the surface, $\mathbf{F}_\tau$ acts in the tangential direction

Total force on object is the sum:

$\displaystyle \boldsymbol{F} = \boldsymbol{F}_p + \boldsymbol{F}_\tau = \int (p \cdot \mathbf{n} + \tau_w \cdot \mathbf{t}) \, \text{d}A$
Lift and Drag - fig9-3a Lift and Drag - fig9-3b

Drag and lift forces on any object

Although, exact pressure and wall shear stress distributions are important and gives valuable information, it is often useful to describe drag and lift instead

  • Drag force: Force component of total force in the direction of the free-stream velocity
  • $\displaystyle \boldsymbol{F}_D = \int \text{d}F_x$ $\displaystyle = \int (p \cdot \mathbf{n} \cdot \text{cos}\theta + \tau_w \cdot \mathbf{t} \cdot \text{sin}\theta) \, \text{d}A$

  • Lift force: Force component of total force perpendicular to the direction of the free-stream velocity
  • $\displaystyle \boldsymbol{F}_L = \int \text{d}F_y$ $\displaystyle = \int (p \cdot \mathbf{n} \cdot \text{sin}\theta + \tau_w \cdot \mathbf{t} \cdot \text{cos}\theta) \, \text{d}A$

Note: pressure, $p$, and wall shear stress, $\tau_w$, distributions are almost impossible to measure

Pressure and friction drag

Drag is normally separated into two components:

  • Pressure drag caused by pressure differences
  • Friction drag caused by wall shear stress

Pressure drag dominates for blunt objects, while skin friction dominates for streamlined objects

Shape and Flow Pressure
drag
Friction
drag
Flow over plate $≈0 \%$ $≈100 \%$
Flow over foil $≈10 \%$ $≈90 \%$
Flow over sphere $≈90 \%$ $≈10 \%$
Flow over perpendicular plate $≈100 \%$ $≈0 \%$

Dimensionless drag and lift

Common to state dimensionless drag and lift

  • Drag coefficient: A dimensionless number that describes the drag force on an object in a fluid flow
  • $C_D = \dfrac{F_D}{\frac{1}{2} \rho U^2 A}$

  • Lift coefficient: A dimensionless number that describes the lift force on an object in a fluid flow
  • $C_L = \dfrac{F_L}{\frac{1}{2} \rho U^2 A}$

Note: $A$ is commonly frontal area (area seen from the front), but sometimes the planform area is used depending on object

Factors affecting drag and lift

Many factors affect drag and lift

$C_D = \phi(\Pi_1, \Pi_2, \ldots)$
$C_L = \phi(\Pi_1, \Pi_2, \ldots)$

Once the drag and lift coefficients ($C_D$ and $C_L$) are found, we may easily find the forces ($F_D$ and $F_L$)

Important factors include:

  1. Shape of object
  2. Orientation of object (angle of attack)
  3. Reynolds number (turbulence)
  4. Surface roughness
  5. Mach number (compressibility effects)
  6. Froude number (gravity effects)
  7. ... and more!

We may write:

$C_D = \phi(\text{shape}, \alpha, \text{Re}, \epsilon/l, \text{Ma}, \text{Fr}, ...)$
$C_L = \phi(\text{shape}, \alpha, \text{Re}, \epsilon/l, \text{Ma}, \text{Fr}, ...)$

Factors affecting drag: Shape of object

Obviously, the shape affects drag

  • To illustrate, varying $l/D$ of an elliptical shape:
    • $l/D \to 0$ (bluff object)
    • $l/D \to \infty$ (streamlined object)

  • To illustrate, two objects varying by factor 10 can have same drag

Factors affecting drag: Reynolds number (streamlined object)

Flow parallel to a flat plate at three $\text{Re}_l = \{$$0.1$$,\,$$10$$,\,$$10^7$$\}$.

  • Low Re ($\text{Re}_l = 0.1$)
    • Very large boundary layer
    • Flow deflected considerably
  • Intermediate Re ($\text{Re}_l = 10$)
    • Smaller boundary layer
    • Flow deflected somewhat
  • High Re ($\text{Re}_l = 10^7$)
    • Very small boundary layer
    • Flow almost not deflected

Factors affecting drag: Reynolds number (bluff object)

Flow past a circular cylinder at three $\text{Re}_D = \{$$0.1$$,\,$$50$$,\,$$10^5$$\}$.

  • Low Re ($\text{Re}_D = 0.1$)
    • Very large boundary layer
    • Viscous forces dominate
    • No separation
  • Intermediate Re ($\text{Re}_D = 50$)
    • smaller boundary layer
    • Mixed importance of viscous and inertial forces
    • Separation occurs, bubble forms
  • High Re ($\text{Re}_D = 10^5$)
    • Very small boundary layer
    • Viscous effects only important in wake and thin boundary layer
    • Boundary layer seperates

Factors affecting drag: Reynolds number (closer look at cylinders and spheres)

Closer inspection of the flow past a circular cylinder and sphere as a function of $\text{Re}$.

CD for circ cylinder and sphere
  • Note: Surface roughness can trigger turbulent BL at lower $\text{Re}$

Factors affecting drag: Surface roughness

Surface roughness can significantly impact the drag force experienced by an object in a fluid flow.

  • Typical golf balls: $10^4 < \text{Re}_D < 10^5$

Force coefficients: Gotta find em all

Force coefficients: Drag, lift coefficients have been determined experimentally or numerically for many typical geometries and flow conditions

  • Tables with force coefficients can be in books, reports, scientific papers etc.
  • - Hoerner (1965)