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57:020 Chapter 3 Professor Fred Stern Fall 2005 16 3.4 Hydrostatic on Plane Surfaces

For a static fluid, the shear is zero and the only stress is the normal stress, i.e., p. Recall that p is a scalar, which when in contact with a surface exerts a normal towards the surface.

Fp = − ∫ pndA A

For a plane surface n = constant such that we can separately consider the magnitude and line of action of Fp.

Fp = F = ∫ pdA A

Line of action is towards and normal to A through the center of pressure (xcp, ycp).

57:020 Chapter 3 Professor Fred Stern Fall 2005 17

Unless otherwise stated, throughout the chapter assume patm acts at surface. Also, we will use gage pressure so that p = 0 at the liquid surface.

Horizontal Surfaces

horizontal surface with area A

p = constant

F

F = ∫ pdA = pA

Line of action is through centroid of A, i.e., (xcp, ycp) = (x, y)

57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 18 Inclined Surfaces g z

dp =−γ dz ∆=−γ∆pz F

(x,y) = centroid of A x

(xcp,ycp) = center of pressure

y

dF = pdA = γy sin α dA p γ and sin α are constants F= ∫ pdA = γsin α ∫ ydA A A 1 y = ∫ ydA yA A

F = γsin α yA 1st of area

p = pressure at centroid of A

F = pA

Magnitude of resultant hydrostatic force on plane surface is product of pressure at centroid of area and area of surface. 57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 19 Center of Pressure

Center of pressure is in general below centroid since pressure increases with depth. Center of pressure is determined by equating the moments of the resultant and distributed forces about any arbitrary axis.

Determine ycp by taking moments about horizontal axis 0-0

ycpF = ∫ ydF A ∫ ypdA A ∫ y(γysin α)dA A 2 = γsin α ∫ y dA A

nd Io = 2 moment of area about 0-0 = moment of inertia

2 transfer equation: Io = y A + I

I = moment of inertia with respect to horizontal centroidal axis

57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 20 2 ycpF = γsin α(y A + I)

2 y (pA) = γsin α(y A + I) cp

2 ycpγsin α yA = γsin α(y A + I)

2 ycp yA = y A + I I yycp =+ yA

ycp is below centroid by I / yA

ycp → y for large y

For po ≠ 0, y must be measured from an equivalent located po/γ above y.

57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 21

Determine xcp by taking moment about y axis

xcpF = ∫ xdF A ∫ xpdA A

x cp (γysin αA) = ∫ x(γysin α)dA A

x cp yA = ∫ xydA A

Ixy = product of inertia

= Ixy + xyA transfer equation

x cp yA = Ixy + xyA

Ixy x cp = + x yA

For plane surfaces with symmetry about an axis normal to

0-0, Ixy = 0 and xcp = x.

57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 22 57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 23 3.5 Hydrostatic Forces on Curved Surfaces

Free surface

p = γh

F = − ∫ pndA h = distance below A free surface

Horizontal Components (x and y components) ˆ ˆ Fx = F⋅i = − ∫ pn ⋅idA A

dAx = projection of ndA onto = − ∫ pdA x plane ⊥ to x-direction Ax

ˆ ˆ Fy = F⋅ j = − ∫ pdA y dA y = n ⋅ jdA Ay = projection ndA onto plane ⊥ to y-direction

Therefore, the horizontal components can be determined by some methods developed for submerged plane surfaces.

The horizontal component of force acting on a curved surface is equal to the force acting on a vertical projection of that surface including both magnitude and line of action. 57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 24 Vertical Components

ˆ ˆ Fz = F⋅k = − ∫ pn ⋅kdA A

=− ∫ pdAz p = γh Az h=distance below free surface

=γ ∫ hdAz = γV Az = weight of fluid above surface A

The vertical component of force acting on a curved surface is equal to the net weight of the column of fluid above the curved surface with line of action through the centroid of that fluid volume.

57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 25 Example: Drum Gate

Pressure Diagram p = γh = γR(1-cosθ) n = −sin θˆi + cosθkˆ dA = A Rdθ π F = −∫ γR(1− cosθ)(−sin θˆi + cosθkˆ)ARdθ 0 p n dA

π ˆ 2 F⋅i = Fx = +γAR ∫(1− cosθ)sin θdθ 0 π 2 ⎡ 1 2 = γ AR ⎢− cosθ + cos2θ = 2γAR ⎣ 4 0 = (γR)(2R A ) ⇒ same force as that on projection of p A area onto vertical plane π 2 Fz = −γ AR ∫(1− cosθ)cosθdθ 0 π 2 ⎡ θ sin 2θ =− γ AR ⎢sin θ − − ⎣⎢ 2 4 0 π ⎛ πR 2 ⎞ 2 ⎜ ⎟ = γ AR = γA⎜ ⎟ = γV 2 ⎝ 2 ⎠ ⇒ net weight of water above surface 57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 26 3.6

Archimedes Principle

FB = Fv2 – Fv1

= fluid weight above Surface 2 (ABC) – fluid weight above Surface 1 (ADC)

= fluid weight equivalent to body volume V

FB = ρgV V = submerged volume

Line of action is through centroid of V = center of buoyancy

Net Horizontal forces are zero since FBAD = FBCD

57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 27 Hydrometry

A hydrometer uses the buoyancy principle to determine specific weights of .

Stem

Bulb

W = mg = γfV = SγwV

W = γwV o = Sγw(Vo − ∆V) = Sγw(Vo − a∆h) γf V a = cross section area stem

Vo/S = Vo − a∆h a∆h = Vo – Vo/S V ⎛ 1⎞ ∆h = o ⋅⎜1− ⎟=∆h(S) a ⎝ S⎠

V S −1 ∆h = o ⋅ calibrate scale using of known S a S

V S = o V0 − a∆h

57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 28 Example (apparent weight)

King Hero ordered a new crown to be made from pure gold. When he received the crown he suspected that other metals had been used in its construction. discovered that the crown required a force of 4.7# to suspend it when immersed in water, and that it displaced 18.9 in3 of water. He concluded that the crown was not pure gold. Do you agree?

∑Fvert = 0 = Wa + Fb – W = 0 ⇒ Wa = W – Fb = (γc - γw)V W=γcV, Fb = γwV Wa Wa + γ w V or γc = + γ = V w V

4.7 + 62.4×18.9/1728 γ = = 492.1 = ρ g c 18.9/1728 c

3 ⇒ ρc = 15.3 slugs/ft

∼ ρsteel and since gold is heavier than steel the crown can not be pure gold 57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 29 3.7 Stability of Immersed and Floating Bodies

Here we’ll consider transverse stability. In actual applications both transverse and longitudinal stability are important.

Immersed Bodies

Static equilibrium requires: ∑Fv = 0 and ∑M = 0

∑M = 0 requires that the centers of gravity and buoyancy coincide, i.e., C = G and body is neutrally stable

If C is above G, then the body is stable (righting moment when heeled)

If G is above C, then the body is unstable (heeling moment when heeled)

57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 30 Floating Bodies

For a floating body the situation is slightly more complicated since the center of buoyancy will generally shift when the body is rotated depending upon the shape of the body and the position in which it is floating.

Positive GM Negative GM

The center of buoyancy (centroid of the displaced volume) shifts laterally to the right for the case shown because part of the original buoyant volume AOB is transferred to a new buoyant volume EOD.

The point of intersection of the lines of action of the buoyant force before and after heel is called the metacenter M and the distance GM is called the metacentric height. If GM is positive, that is, if M is above G, then the ship is stable; however, if GM is negative, the ship is unstable.

57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 31 Floating Bodies

α = small heel angle x = CC′ = lateral displacement of C C = center of buoyancy i.e., centroid of displaced volume V

Solve for GM: find x using (1) basic definition for centroid of V; and (2) trigonometry Fig. 3.17

(1) Basic definition of centroid of volume V

xV = ∫ xdV = ∑ xi∆Vi moment about centerplane

xV = moment V before heel – moment of VAOB + moment of VEOD = 0 due to symmetry of original V about y axis i.e., ship centerplane

xV=−∫∫ ( − x)dV + xdV tan α = y/x AOB EOD dV = ydA = x tan α dA 22 xV=α+α∫∫ xtandA xtandA AOB EOD 57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 32 2 xV = tan α∫ x dA ship waterplane area

moment of inertia of ship waterplane about z axis O-O; i.e., IOO

IOO = moment of inertia of waterplane area about centerplane axis

(2) Trigonometry

xV = tan αIOO tan αI CC′ = x = OO = CM tan α V

CM = IOO / V

GM = CM – CG

I GM = OO − CG V

GM > 0 Stable

GM < 0 Unstable

57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 33 3.8 Fluids in Rigid-Body Motion

For fluids in motion, the pressure variation is no longer hydrostatic and is determined from application of Newton’s 2nd Law to a fluid element.

τij = viscous stresses net surface force in X direction p = pressure Ma = inertia force ⎛ ∂p ∂τxx ∂τyx ∂τzx ⎞ Xnet = ⎜− + + + ⎟V W = weight (body force) ⎝ ∂x ∂x ∂y ∂z ⎠

Newton’s 2nd Law pressure viscous

Ma = ∑F = FB + FS

per unit (÷ V) ρa = fb + fs volume DV ∂V a = = + V ⋅∇V Dt ∂t

fs = body force = − ρgkˆ

fs = surface force = fp + fv fp = surface force due to p = −∇p fv = surface force due to viscous stresses τij 57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 34 DV Neglected in this chapter and ρ = f b + f p + f v included later in Section 6.4 Dt when deriving complete Navier-Stokes equations DV ρ = −ρgkˆ − ∇p Dt

inertia force = body force due + surface force due to to gravity pressure

Du ∂p x: ρ = − Note: for V = 0 Dt ∂x ∇p = −ρgkˆ ∂p ∂p = = 0 ⎡∂u ∂u ∂u ∂u⎤ ∂p ∂x ∂y ρ + u + v + w = − ⎢ ⎥ ∂p ⎣ ∂t ∂x ∂y ∂z ⎦ ∂x = −ρg = −γ ∂z

Dv ∂p y: ρ = − Dt ∂y

⎡∂v ∂v ∂v ∂v⎤ ∂p ρ⎢ + u + v + w ⎥ = − ⎣ ∂t ∂x ∂y ∂z⎦ ∂y

57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 35 Dw ∂p ∂ z: ρ = −ρg − = − ()p + γz Dt ∂z ∂z

⎡∂w ∂w ∂w ∂w ⎤ ∂p ρ⎢ + u + v + w ⎥ = − ()p + γz ⎣ ∂t ∂x ∂y ∂z ⎦ ∂z

or ρa = −∇(p + γz) Euler’s equation for inviscid flow

∇ ⋅ V = 0 for

4 equations in four unknowns V and p

57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 36 Examples of Pressure Variation From Acceleration

Uniform Linear Acceleration: ρa = −ρgkˆ − ∇p

∇p = −ρ()a + gkˆ = ρ()g − a g = −gkˆ ˆ ˆ ˆ ˆ ∇p = −ρ[a x i + ()g + a z k] a = a x i + a zk ∂p ∂p = −ρa = −ρ()g + a ∂x x ∂z z sˆ= unit vector in direction of ∇p =∇p /⏐∇p⏐ − a ˆi + ()g + a kˆ = [ x z ] 2 2 1/ 2 []a x + ()g + a z nˆ = unit vector in direction of p = constant = sˆ ׈j ijkijk ⊥ to ∇p − a kˆ + (g + a )ˆi by definition lines = x z of constant p are 2 2 1/ 2 []a x + (g + a z ) normal to ∇p

-1 θ = tan ax / (g + az) = angle between nˆ and x

dp 2 2 1/ 2 = ∇p⋅sˆ = ρ[]a x + ()g + a z > ρg ds G p = ρGs + constant ⇒ pgage = ρGs 57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 37 Rigid Body Rotation:

Consider a cylindrical tank of liquid rotating at a constant rate Ω = Ωkˆ Ω = ω in text

a = Ω×(Ω× ro ) centripetal acceleration

2 = − rΩ eˆ r V2 = − eˆ r r

∂ 1 ∂ ∂ ∇p = ρ(g − a) ∇ = eˆ + eˆ + eˆ ∂r r r ∂θ θ ∂z z ˆ 2 = − ρgk + ρrΩ eˆ r grad in cylindrical coordinates

∂p ∂p ∂p i.e., = ρrΩ2 = −ρg = 0 ∂r ∂z ∂θ C (r) along path of a = 0 pressure distribution is hydrostatic ρ and p = r 2Ω2 + f (z) + c 2 pz = -ρg p = -ρgz + C(r) + c

ρ p V2 p = r 2Ω2 − ρgz + constant + z − =constant 2 γ 2g V = rΩ 57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 38 The constant is determined by specifying the pressure at one point; say, p = po at (r, z) = (0, 0)

1 2 2 p = po − ρgz + r Ω 2

Note: pressure is linear in z and parabolic in r

Curves of constant pressure are given by

p − p r 2Ω2 z = 1 o + = a + br 2 ρg 2g which are paraboloids of revolution, concave upward, with their minimum point on the axis of rotation

Free surface is found by requiring volume of liquid to be constant (before and after rotation)

The unit vector in the direction of ∇p is − ρgkˆ + ρrΩ2eˆ sˆ = r 2 1/ 2 ⎡()ρg 2 + ()ρrΩ2 ⎤ ⎣⎢ ⎦⎥

dz g tan θ = = − slope of sˆ dr rΩ2

⎛ Ω2z ⎞ ⎜ ⎟ i.e., r = C1exp⎜− ⎟ equation of ∇p surfaces ⎝ g ⎠ 57:020 Fluid Mechanics Chapter 3 Professor Fred Stern Fall 2005 39