Faculty of Coastal Engineering Faculty of Coastal Engineering

BED, BANK & SHORE BED, BANK & SHORE PROTECTION PROTECTION

Lecturer: PhamThu Lecturer:

Huong PhamThu Huong

Chapter 2 Chapter 2 Loads Flow -- Loads Flow

(3 class hours)

Content Content

2.1 Introduction

2.2 Turbulence

2.3 Wall flow

2.4 Free flow

2.5 Combination of wall flow and free flow

2.6 Load reduction

2.1 Introduction

forces

Structure

regular

Hour

tides

Flow

Fluctuation

Seconds

short waves

seconds

turbulence

Velocity field in various situations

averaged velocity values (ū = Q/A) Chezy's law for uniform flow: ū = C√(Ri)

Reynolds dye experiment Reynolds dye experiment

Reynolds number Reynolds number

vs - mean fluid velocity, L - characteristic length (h: water depth) μ - (absolute) dynamic fluid viscosity ν - kinematic fluid viscosity: ν = μ / ρ = 10-6 m2/s (water) ρ - fluid density

• Laminar flow occurs at low Reynolds numbers (Re<1000)

• Turbulent flow occurs at high Reynolds numbers (Re>2000)

2.2 Turbulence

Turbulence motion: velocity and pressure show irregular fluctuations

Turbulence variations:

u = u + u v = v + v w = w + w p = p + p

Turbulence variations:

u = u + u v = v + v w = w + w p = p + p

Turbulence can then be expressed in various ways, such as:

2

2

2

2

2

2

k

u

v

′ w

,

,

,

=

+

+

=

=

=

r u

r v

r w

(

)

1 2

u u

v u

′ w u

total kinetic energy in a turbulent flow

fluctuation intensities of u, v and w, relatively

Velocity Velocity

m * a = F

u

w

+

+

= −

+

u x

p x

u ∂ t ∂

∂ ∂

u ∂ z ∂

∂ ∂

2 u ∂ μ 2 z ∂

⎞ ⎟ ⎠

⎛ ρ ⎜ ⎝ inertia

press.

visc.

Reynolds stresses:

m * a = F

2

2

∂ u w ρ μ + + = − + − + u x u z p x u 2 z u ∂ t ∂ ∂ ∂ ∂ ∂ ∂ ∂ ∂ ∂ ′ u ∂ x ∂ ′ ′ u w z ∂ ⎛ ⎜ ⎝ ⎞ ⎟ ⎠ ⎛ ρ ⎜ ⎜ ⎝ ⎞ ⎟ ⎟ ⎠

inertia press. visc. Reynolds stresses

− − − − − − − − − − − − − − − − − − − − − − − − − − − − − − −

mean values turb. fluctuations

Exchange of momentum due to turbulence

2

Flow resistance:

u fc τ ρ=

In laminar flow the resistance, expressed as a shear stress, is proportional with the flow velocity.

In turbulent flow, the quadratic terms in equation become dominant and the relation between τand u becomes quadratic

Resistance in laminar and turbulent flow

2.3 Uniform wall flow 2.3 Uniform wall flow

Wall flow Wall flow

2

(

)

g h I

c

u

u

g h I

= τ ρ

=

ρ

=

=

ρ

⇒ =

2 u ρ *

b

f

' ' u w b b

1 c

f

u

g C /

=

u *

u* is the shear “velocity”

u C R I

C

Chezy:

with:

=

=

g c

f

c

2 / 3

1/ 6

Manning:

with:

u

R

I

=

n R =

f g

1 n

Nikuradse-Colebrook roughness:

C =

k (

is equivalent roughness )

r

R 12 ln k

R 12 18 log ≈ k

g κ

r

r

Example Example

20 m3/s of water flows in a 10 m wide channel with vertical banks, s, (cid:190)(cid:190) 20 m3/s of water flows in a 10 m wide channel with vertical bank a bed slope of 1/1000 and a roughness of 0.2 m. What is the a bed slope of 1/1000 and a roughness of 0.2 m. What is the Chezy--value, the relative turbulence depth, the velocity, the Chezy value, the relative turbulence depth, the velocity, the intensity and the relative turbulent shear stress? intensity and the relative turbulent shear stress?

Assume h

R =bh/(b+2h)

C=18log(12R/kr)

u= C√RI

Q* = bhu

Q* = Q

Stop

non uniform flow non uniform flow

The growth of a boundary layer when an infinitely thin plate is placed in a flow with u = u0.

Influence of pressure gradient on velocity Influence of pressure gradient on velocity profile profile

Uniform

accelerated

Decelerated

Turbulence in windtunnel Turbulence in

contraction windtunnel contraction

The total amount of turbulent kinetic energy, k, remains approximately constant.

Due to the increased velocity in the contraction, the relative turbulence, r, using the local mean velocity decreases.

2.4 Free flow 2.4 Free flow

50 100

Z

Flow, velocities and turbulence in mixing layer

Flow and velocities in jets Flow and velocities in jets

2

0.693

z b

⎛ ⎜ ⎝

⎞ ⎟ ⎠

3.5

⎛ ⎜ ⎜ ⎝

⎞ ⎟ ⎟ ⎠

Plane jets : u =

b =

0.1

x u = u e

m

m

u 0 x B

2

0.693

R b

⎛ ⎜ ⎝

⎞ ⎟ ⎠

⎛ ⎜ ⎜ ⎝

⎞ ⎟ ⎟ ⎠

Circular jets : u =

b =

x u = u e

0.1

m

m

u 6.3 0 x D

Turbulent fluctuations in circular jet Turbulent fluctuations in circular jet

instability of an axisymmetric instability of an

jet axisymmetric jet

effect of strong pressure gradients effect of strong pressure gradients

2.5 Combination of wall flow and Free flow 2.5 Combination of wall flow and Free flow

Flow separation around blunt and round body

Vertical constriction and expansion (sill) Vertical constriction and expansion (sill)

Vertical expansion Vertical expansion facing step) (backward--facing step) (backward

Horizontal expansion Horizontal expansion

Horizontal constriction and expansion Horizontal constriction and expansion (groyne)) (groyne

Detached Detached bodies bodies

Reduction 2.6 Load Reduction 2.6 Load

The end Chapter 2 The end Chapter 2