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13.021 – Marine Hydrodynamics, Fall 2004 Lecture 4

Copyright °c 2004 MIT - Department of Ocean Engineering, All rights reserved.

13.021 - Marine Hydrodynamics Lecture 4

Introduction Governing Equations so far:

Knowns Number of Equations Number of Unknowns ρ Continuity(conservation of 1 vi 3 ) Fi Euler (conservation of 3 τij 6 3 of 9 eliminated by ) symmetry 4 9

Therefore, some constitutive relationships are needed to relate vi to τ ij.

1.7 Newtonian

1. Consider a fluid at rest (vi ≡ 0). Then according to Pascal’s Law:

τij = −psδij (Pascal’s Law)   −ps 0 0 τ =  0 −ps 0  ∼ 0 0 −ps

where ps is the hydrostatic and δij is the Kroenecker delta function, equal to 1 if i = j and 0 if i 6= j. 2. Consider a fluid in . The fluid is defined as:

τij = −pδij +τ ˆij

1 where p is the thermodynamic pressure andτ ˆij is the dynamic stress, which is related to the empirically.

Experiments with a wide class of fluids, ”Newtonian” fluids, obtain that:

τˆij ≈ linear function of the rate of strain ≡ z µ ¶ }| µ ¶{ z}|{ ∂ ∂X ∂ ∂X ∂u = k ∂t ∂x ∂x ∂t ∂x | {z } m u

∂uk i.e.τ ˆij ≈ αijkm i, j, k, m = 1, 2, 3 | {z } ∂xm 34=81 empirical coefficients (constants for Newtonian fluids) Note that the is proportional to the rate of strain.

τ ij NewtonianFluid

Fluid

∂ uk ∂ xm

For isotropic fluids, this reduces to: µ ¶ µ ¶ ∂u ∂u ∂u τˆ = µ i + j + λ l , ij ∂x ∂x ∂x j i | {zl } ∇·~v where the fluid properties are:

• µ - (coefficient of) dynamic .

• λ - bulk , ‘second’ coefficient of viscosity

2 For incompressible flow, ∂ul = 0. Therefore, for an incompressible, isotropic, Newtonian fluid the viscous ∂xl stressτ ˆij is given as µ ¶ ∂ui ∂uj τˆij = µ + ∂xj ∂xi

1.8 Navier-Stokes equations

Equations Number of Unknowns Number of Equations Unknowns Euler 3 ui 3 continuity 1 p 1 constitutive 6 (symmetry) τij 6 (Newtonian) 10 10 | {z } closure

Substitute the equation for the stress µ ¶ ∂ui ∂uj τij = −pδij + µ + ∂xj ∂xi for a Newtonian fluid into Euler’s equation:

Dui ∂τij ρ = Fi + Dt ∂xj where µ ¶ ∂τ ∂p ∂ ∂u ∂u ij = − + µ i + j ∂x ∂x ∂x ∂x ∂x j i | j {zj i }

2 ∂uj ∂ ui + ∂ ∂xj ∂xj ∂xi ∂x |{z}j 0 and ∂uj = 0 due to continuity. Finally, ∂xj

3 2 Dui ∂ui ∂ui 1 ∂p ∂ ui 1 = + uj = − + ν + Fi Tensor form Dt ∂t ∂xj ρ ∂xi ∂xj∂xj ρ D~v ∂~v 1 1 = + ~v · ∇~v = − ∇p + ν∇2~v + F~ Vector form Dt ∂t ρ ρ

µ 2 where ν ≡ ρ denoted as the Kinematic viscosity [ L /T ].

• Navier-Stokes equations for incompressible, Newtonian fluids

Number of Number of Equations Unknowns continuity 1 p 1 Navier-Stokes 3 (symmetry) ui 3 4 4

1.9 Boundary Conditions 1. Kinematic Boundary Conditions: Specifies (position, velocity, . . . ) On a boundary, velocity of the fluid = velocity of the body. i.e. velocity continuity.

~v = ~u ”no-slip” boundary condition where ~v is the fluid velocity at the body and ~u is the body surface velocity

• ~v · nˆ = ~u · nˆ no flux – continuous flow • ~v · tˆ= ~u · tˆ no slip – finite shear stress

G v G u

4 2. Dynamic Boundary Conditions: Specifies ( pressure, sheer stress, . . . )

Stress continuity:

0 p = p + pinterface 0 τij = τij + τij interface The most common example of interfacial stress is .

τ p interface , ij interface τ ' 'p ij τ p ij

Surface Tension • Notation: Σ [Tension / Length] ≡ [Surface / Area].

• Surface tension is due to the inter molecular attraction forces in the fluid.

• At the interface of two fluids, surface tension implies in a pressure jump across the interface. Σ gives rise to ∆p across an interface.

• For a /air interface: Σ = 0.07 N/m. This is a function of temperature, impurities etc. . .

• 2D Example:

dθ dθ dθ cos · ∆p · Rdθ = 2Σsin ≈ 2Σ 2 | {z2} | {z2} ≈1 dθ ≈ 2 Σ ∴ ∆p = R Higher curvature implies in higher pressure jump at the interface.

5 p θ p’=p+ ∆p d /2

Σ R Σ

• 3D Example: Compound curvature µ ¶ 1 1 ∆p = + Σ R1 R2

where R1 and R2 are the principle radii of curvature.

1.10 Body Forces – Gravity • Conservative force:

F~ = −∇ϕ for some ϕ, where ϕ is the force potential.

I Z 2 Z 2 ~ ~ F · d~x = 0 or F · d~x = − ∇ϕ · d~x = ϕ(~x1) − ϕ(~x2) 1 1 • A special case of a conservative force is gravity.

F~ = −ρgk,ˆ with gravitational potential:

ϕ = ρgz → F~ = −∇ϕ = ∇(−ρgz) = −ρgk,ˆ

where −ρgz is the hydrostatic pressure ps = −ρgz = −ϕ.

6 Navier-Stokes equation:

D~v ρ = −∇p + F~ + ρν∇2~v Dt = −∇p − ∇ρgz + ρν∇2~v = −∇ (p + ρgz) + ρν∇2~v,

but p − ps = pd and ps = −ρgz, where p is the total pressure and pd is the dynamic pressure. Therefore,

D~v ρ = −∇p + ρν∇2~v Dt d

• Presence of gravity body force is equivalent to replacing total pressure p by dynamic pressure pd in the Navier-Stokes(N-S) equation.

• Solve the N-S equation with pd, then calculate p = pd + ps = pd − ρgz.

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