1 2 History Faces of Fluid Mechanics Archimedes (C. 287-212 BC) Navier (1785-1836) 3 Newton (1642-1727) Stokes (1819-1903) Leibniz (1646-1716) Reynolds (1842-1912) Bernoulli Euler (1667-1748) (1707-1783) Prandtl Taylor (1875-1953) (1886-1975) Vehicles Aircraft High-speed rail 4 Surface ships Submarines Environment Air pollution 5 River hydraulics Physiology and Medicine Blood pump 6 Ventricular assist device Sports & Recreation Water sports Auto racing 7 Cycling Offshore racing Surfing Turbofan Engine 8 Flow 9 Course contents • • • • • • • • Concepts and definitions. 1 week Fluid Static. 2 week Forces on submerged surfaces and bodies. 2 week Non-viscous flow. 2 week Conservation of mass. 1 week Momentum and energy. 1 week Bernoulli’s equation. 2 week Viscous flow ( flow past immersed bodies, pipe flow, losses in conduit) 2 week • Laminar and Turbulent flow. 2 week 10 REFERENCES • Frank M. White ” Fluid Mechanics” 4th Edition, McGraw-Hill, 2002. • Munson, Young and Okiish “Fundamentals of Fluid mechanics“John Wiley & Sons, Inc. 1999. • Michael J. Moran, Howard N. Shapiro, Bruce R. Munson, and David P. DeWitt “Introduction to Thermal Systems Engineering: Thermodynamics, Fluid Mechanics, and Heat Transfer” John Wiley & Sons, Inc. 2003. • Yunus A. Çengel, and Robert H. Turner “FUNDAMENTALS OF THERMAL-FLUID SCIENCES” McGraw-Hill Higher Education, 2004 11 Introduction Fluid mechanics is part of applied Mechanics concerned with the statics and dynamics of liquids and gases. Fluid Mechanics Fluid Statics Fluid Dynamics Hydro- Dynamics Hydro-Statics Aero-Statics 12 Hydraulics Gas Dynamics Hydro-Statics: Deals with the statics of incompressible fluids “ Liquids“. Aero-Statics: Deals with the statics of compressible fluids “ Gases “. Hydro-Dynamics: Deals with the dynamics of incompressible fluids “ Liquids “. Gas-Dynamics: Deals with the` dynamics of compressible fluids “ Gases “. 13 Fluid Free Surfaces Gas Liquid No free Surfaces Easy to compress 14 Difficult to compress DIMENSIONS AND UNITS • Any physical quantity can be characterized by dimensions. Length = 10 m The magnitudes assigned to the dimensions are called units. Unit • Primary or fundamental Dimension dimensions, mass m, length L, time t, and temperature T • Secondary dimensions, or derived dimensions. velocity V, energy E, and volume V are expressed in terms of the primary dimensions • The Metric System of units, m, kg, s. • The English system, which is also known as the United States Customary System (USCS). • The SI is being used for scientific and engineering work in most of the industrialized nations, including England. 16 Metric Unit S.I. British Length, L Mass, m m kg m kg Ft lbm Density, Force, F kg/m3 Kgf kg/m3 N lbm/ft3 lb Kgf/m3 ata, kgf/m2 kCal N/m3 bar, Pa kJ lb/ft3 psi BTU kCal/kg.C hp poise, kp.s/m2 kJ/kg.C kW N.s/m2 BTU/lb.f B.hp lb.S/ft2 C, K Sec C, K Sec f, R Sec Dimension Specific Weight, Pressure, p Heat, Q Specific heat, Cp Power, P Viscosity, Temperature, T 17 Time, • we consider force to be a secondary dimension whose unit is derived from Newton’s second law, that is, 18 Example • A commonly used equation for determining the volume rate of flow Q, of a liquid through an orifice located in the side of a tank is • Q = 0.61 A 2gh • Where A is the area of the orifice, g is the acceleration of gravity and h is the height of the liquid above the orifice. Investigate the dimensional homogeneity of this formula. Solution • • • • • 19 Left hand side Q = volume/ time = L3. t-1 Right hand side 0.61 A 2gh = L2 ( L /t2 L)1/2= L3.t-1 The formula is homogenous Properties of Fluids • Density • The density of a substance is that quantity of matter contained in unit volume of the substance. • Mass Density • Mass density ρ is defined as the mass of the substance per unit volume. mass Volume 3 • Units: kg/m • Dimensions: M L-3 • Typical values at p = 1.013 x 105 N/m2, T = 288.15 K: • Water, 1000 kg/m3; • Air, 1.23 kg/m3. Specific Volume: 20 volume 1 v mass • Specific Weight γ • Specific weight γ is defined as the weight per unit volume. Weight mass g N 3 volume Volume m • Weigh per unit volume = Mass per unit volume x g γ = ρ.g • • • • • 21 Units: N/m3 Dimensions: M L-2-2 Typical values at p = 1.013 x 105 N/m2, T = 288.15 K: Water, 9.81 x 103 N/m3; Air, 12.07 N/m3. Specific gravity Specific gravity is defined as the ratio between density and water density. S .G Example the substance subs tan ce water If the specific gravity of an oil is 0.8, find its specific weight in kg/m3. Solution: 22 N/m3 γ Viscosity: μ It is the property of a fluid, due to cohesion and interaction between molecules, which offers resistance to shear deformation. Shear Stress y u ( )B y B 23 x Newtonian Fluid u A b y No slip condition u u τ xy y b’ c Fluid a d F c’ u F A y u F μ A y u τ μ y Where 24 μ: Is the coefficient of viscosity or the dynamic viscosity. Dimension of dynamic viscosity ML1t 1 Units of dynamic viscosity (Poise) Poise dyne.s N 0 . 1 Pa . S 0 . 1 s 2 2 cm m Kinematics viscosity Dimension of Kinematic viscosity L2.t-1 Units of kinematic viscosity (Stoke) 2 cm 2 4 m 1stoke 1 10 , s s 25 ft 2 930 stoke s Example: A 6 Cm. diameter shaft runs in 12 Cm long bearing, if an oil viscosity 0.5 poise and 0.02 thick fills the space between the shaft and the bearing. Find the power lost due to friction when the shaft rotates at 200 r.p.m. L = 12 Cm. d = 6 Cm D = 6.02 26 Solution: A πdL π 6 12 226.19 (6.02 6.0) y 0.01 2 Cm 2 Cm 2 πN d 2 π 200 6 u ω r 62.832 60 2 60 2 Cm/sec u 62.832 F μ A 0.5 226.16 710598.5 y 0.01 dyne F u 710598.5 62.832 Power 0.00446 kW 5 2 3 Const . 10 10 10 27 σ Surface Tension: σ σ d θ h θ h Water Mercury θ : is the angle of contact between liquid and solid Upward pull due to surface tension equal σ π d cos θ h : is the height of liquid is raised 28 Weight of liquid raised = γ A h = γ π d2 h/4 σ π d cos θ = γ π d2 h/4 4 σ cosθ h γd For water in tube 6 mm in diameter h will be 4.5 mm For mercury the corresponding figure is – 1.5 mm. 7- Bulk Modulus of Elasticity: 29 K P2 P1 K V2 V1 V1 Fluid Statics That means: Fluid at rest and free of shearing stresses. Pressure Intensity: P1 P1 A P3Sinθ θ P2 C P3Cos θ A B θ B C Force on AB = P1 x AB x S Force on BC = P2 x BC x S 30 Force on AC = P3 x AC x S P2 P1 Fluid at rest Appling the forces balance : P 1 A P3Sinθ θ x AB x S = P3Cos θ x AC x S AB = AC x Cos θ P 1 P3Cos θ = P3 31 P2 = P3 P1 = P2 = P3 P2 C Appling the forces balance (Horizontally) : B Pressure Head: h in m P ρgh γh h Fluid (γ) P Variation of pressure along horizontal line: Fx 0 P1a P2a 32 P1 P2 P1 a P2 Variation of pressure along vertical line: P1 W γ a h Fh 0 P1 a γ a h P2 a P2 P1 γh W h P2 a 33 Absolute and Gauge Pressure: kg f Pressure 2 m 1 bar = 105 or N/m2 Patm = atmospheric pressure Patm = 1.013 bar = 760 mm.hg = 1.033 kgf /Cm2 34 Force Pressure Area N Pressure 2 m Pabs = Patm + Pgauge 35 Vacuum or Negative Pressure: If the pressure is blew the atmospheric negative or vacuum pressure it is called Vapor Pressure: The vapor pressure is the absolute pressure below which the liquid turns into vapor. 36 Example Convert a pressure of P = 5 bar into meters of : i- Water. ii- Mercury iii- Oil of specific gravity of S = 0.9 P γ h P P h γ g ρ i- For water: h water 5 105 50 1000 9.81 meter γ1 h1 γ 2 h 2 γ water S1 h1 γ water S2 h 2 37 S1 h1 S2 h 2 Measurements of pressure: The pressure is measured by a devices is called Manometers. Manometers can be classified into : Vacuum region a- Simple manometers: 1 – Barometer: h The barometer is a device for measuring the local atmospheric pressure. Mercury The Standard atmospheric pressure is 10.3 meter of water or 0.758 meter of mercury. 38 Piezometer: h Fluid ( water or oil ) The Piezometer tube is used to measure the static pressure head of the flowing liquid at any section of a pipe. Note that: The Piezometer tube would not work for negative pressure. It is not suitable for measuring high pressure. It is not suitable for measuring for gas pressure. 39 Differential manometers: Pgas First for positive pressure: PL = PR x y PL = Pgas + gas . x PR = 1 . y Pgas = 1.y - g . x g . x ≃ 0 ∴ Pgas = 1.y 40 L S1 R Second for negative pressure: ∵ PL = PR Pgas PL = Pgas + 1 . y y PR = 0 ∴ 0 = Pgas + 1 . y ∴ Pgas = - 1.y 41 L S1 R Third for liquids: PLiq In this case : S2 > S1 x S1,γ1 y ∵ PL = PR L PL = P + 1 . x S2 PR = 2 . y ∴ P = 2 . y - 1 . x 42 R The U-tube manometer can used to measure the difference in pressure In this case : S2 > S1 S1 ∵ PL = PR 1 x 2 PL = P1 + 1 . (x + y) y PR = P2 + 1 . x + 2. y L S2 P1 + 1(x + y) = P2 + (1x + 2.y) P1 – P2 = y (2 – 1) 43 P1 – P2 = water.y (S2 – S1) R In this case : S1 > S2 S2 L R ∵ PL = PR y ∴ PL = P1 ــ1(x + y) ∴ PR = P2 ( ــ1x + 2.y) P1 ــ1(x + y) = P2 ( ــ1x + 2.y) P1 ــP2 = y (1 ــ2) P1 ــP2 = water.y (S1 ــS2) 44 x S1 1 2 Inclined manometer: P1 P1 = . h θ θ Bourdon pressure tube: A A Section at A-A 45 ℓ h Transmission of pressure: F ∵ P1 = P2 a F W A 46 A a F P1 a W P2 A W P1 Oil P2 Hydraulic press: F a ∵ P1 = P2 f W γh P2 a A 47 P1 W A h P2 Hydraulic Jack: F L F1 F. L = F1. L1 a P1 Oil 48 W A L1 P2 Hydrostatic of pressure Introduction: When a surface is submerged in a fluid, forces develop on the surface due to the fluid. The determination of these forces is important in the design of storage tanks, ships, dams and other hydraulic structure. For fluids at rest we know that the force must be perpendicular to the surface since there are no shearing stresses present. 49 Hydrostatic Forces on Horizontal and Vertical Surfaces 50 1 F h. A 2 F h.A Fy p dF y . y sin .dA y F h.dA A A F . y. sin dA A A sin y 2 dA A sin I x F sin y.dA θ a y dA yc y dA A F yc sin A hc A 51 o h hc First Moment of Area hp F y yc yp cp dA x I x y dA 2 Second moment of Area I x I c y c2 A yp sin ( I c y A) 2 c F 2 sin ( I c yc A) yc sin A 52 Ic yc yc A Figure Rectangular h G G d/2 Area A 2nd moment of area Ic b.h b h 3 12 b h 2 b h 3 36 b Triangle h h/3 b Circle Semi-circle 53 G 4R/3π G π R2 π R4 4 R G π R2 2 0.1104 R 4 R G Pressure on Curved Surface: Problems involving the resultant pressure of a liquid on a curved surface can usually be solved most conveniently by considering the horizontal and vertical components of the resultant pressure separately.` D E C P A Liquid G H V (a) D E B B Liquid P G R Liquid O R A (b) R (c) H and V are the horizontal and vertical components of the resultant pressure R of the liquid on the surface. 54 D E C P A Liquid G H V B R (a) Figure (a), if ACE is vertical plane through A the section of fluid is in equilibrium horizontally under the action of H and the resultant pressure P of the liquid on AC, therefore H = P. But AC is the projection of AB on vertical plane, therefore Horizontal component H = resultant pressure on the projection of B on a vertical plane. 55 D E B Liquid P G R A (b) In Figure (b), if the surface AB is removed and the space ABDE is filled with liquid, this liquid would be in equilibrium under its weight and the vertical force V on the boundary AB, therefore; Vertical component V = weight of the fluid which would lie vertically above AB if AB were removed and V will act upwards through the centre of gravity G of the imaginary fluid. 56 Example The 4 –m diameter circular gate is located in the inclined wall (θ=60o) of a large reservoir containing water ( =9.8 kN/m3). The gate is mounted on a shaft along its horizontal diameter for a water depth of 10 m above the shaft, determine: A- the magnitude and location of the resultant force exerted on the gate by the water, and B- the moment that would have to be applied to the shaft to open the gate. 57 Solution • • • • • • • • • • • 58 F= hc A = 9800x10x(πx42/4) =1.23 MN yp = yc + I.c/(yc. A) Ic = πxR4/4 = πx24/4=4 π yp = (10/sin60)+4 π/((10/sin60)x πx42/4)=11.6 m yp –yc= 0.0866 m ∑Mc = 0 M = F(yp-yc)=123x1000x0.0866 =1.07x105 N.m 60 F h= 10 m O shaft 4m Example • A rectangular gate in the vertical side of a reservoir can turn freely about its upper edge which is horizontal and is fastened at its two lower corners. The gate is 1.0 m wide and 2.0 m high and its upper edge is 2.0 m below the water level. Determine the reactions at the lower corners assuming them to be equal. 59 Solution • • • • • • • FH=γ hc A = 9810*3*(1*2)= 58750 N hp =hc + Ic/ (hc*A) I c=1*23/12=0.67 hp =3+0.75/[3x(1x2)]=3.11 m FH* (3.11-2)=2R*2.0 R=58750*1.11/4=16340 N 60 2m hb 2m hc = 3 m 1m 2m FH R Determine the resultant force due to water acting on the 1 m by 2 m rectangular area AB and on 1.25 m by 2 m triangle area CD shown in Figure below. The apex of triangle is at C. 1- For rectangular area AB Let the Resultant Force P A F 9810 (1.22 1) (1 2) 43560 N 2.0 m B 1m The resultant force Acts on the center of pressure 61 1.0 m C 2m F ρ g h C.G A 1.22 m 45o D 2- For triangle area AB F ρ g h C.G A 2 1 F 9810 (1 0.707 2) ( 1.25 2) 23.8 103 N 3 2 The resultant force Acts on the center of pressure 62 Determine and locate the components of force due to the water acting on the curved area AB in Figure per meter of its length. 1- For the horizontal component PH PH : is the force on vertical projection CB. A PH ρ g h C.G A CB C y PH 9810 (1) (2 1) 19620 N x PH B 2- For the Vertical component PV PV : is the weight of water above area AB. PV π 22 PV ρ gV 9810 ( 1) 30820 N 4 R PH2 PV2 (19620) 2 (30820) 2 63 29275067368000 Hinge N Fluids at rest Floating bodies (buoyance and stability) As pressure increases with depth, the fluid exerts a resultant upward (buoyancy) force on a body wholly or partially immersed in a fluid. If the buoyancy force equals the weight of the body then it will float. No horizontal component of the buoyancy force because the vertical projection of a body is the same in both directions. 64 Fluids at rest Floating bodies Upward thrust on M Water surface Q P S N lower surface PSR weight of fluid in volume PSRNM R Downward thrust on upper surfacePQR weight of fluid in volume PQRNM 65 M Water surface Q N buoyancy, FB : FB weight PSRNM weight PQRNM R P Resultant upward force due to FB weight PQRS S Buoyancy force weight of displaced fluid 66 • Buoyancy force acts through the centre of gravity of the volume of fluid displaced. This is called the centre of buoyancy. The centre of buoyancy does not in general correspond to the centre of gravity of the body. If the density is constant the centre of gravity of the displaced fluid is at the centroid of the immersed volume. G B 67 Fluids at rest Floating bodies - Archimedes Principle • The buoyancy force is equal to gV where is the density and V the volume of fluid displaced. • For equilibrium the buoyancy force must equal the weight of the body: FB W equilibriu m FB W body rises (bubbles of air in water) FB W body sinks (stone in water) 68 Stability and Metacentre: M G θ B R=W W R 1. If M lies above G a righting moment is produced, GM is as positive, equilibrium is stable. 2. Ifregarded M lies below G anand overturning moment is produced, GM is regarded as negative, and equilibrium is unstable. 3. 69 If M and G coincide the body is in neutral equilibrium. W G W G M M M W G B B1 B B1 FB1 FB1 GM is +ve positive Stable 70 B′ B GM is -ve positive Unstable FB GM is Neutral 0 Determination of the Metacentric height W M FB = ρ g V BB1 = BM sin dθ G B dθ B1 BB1 = BM . dθ FB1 GM = BM - BG BM Where: I V 71 I BG V Is the Area Moment of Inertia of the top view about the vertical axis Is the volume of liquid displaced by the body. Example A block of wood 0.2 x 0.5 m cross-section and 0.8 m long has a mass of 64 kg. Can the block float with 0.5 m side vertical? 0.5 m Solution: 0.5 m G 0.2 m 0.25 m 0.4 m Water Level B 0.2 m 0.8 m Volume of displaced water 64 V 0.064 m3 1000 The height of submergence 0.064 h 0.4 m 0.2 0.8 72 The center of buoyancy is 0.2 m from the base. The Metacentric height I BM BG V 0.8 0.23 I 0.00053 m 4 12 BG = 0.25 – 0.2 = 0.05 m GM = BM - BG The Metacentric height ∵ GM < 0 73 0.00053 GM 0.05 0.042 m 0.064 The Block is unstable with its 0.5 m side vertical • Worked Example • A cube of side 35 mm is floating in water of density 1000 kg/m3. a) What is the density of the cube material if the depth of submersion is 27 mm? b) A hemispherical scoop, diameter 15 mm, is removed from the top face (volume of a sphere = ). What is the new depth of immersion? 74 74 • Worked Example a) 27 mm When the cube is floating in a stable position the buoyancy force is equal to the weight of the cube: 75 75 • Worked Example Weight of cube : W mg cubeVcube g 0.035 cube g 4.21x10 4 cube 3 But, the buoyancy force is also equal to the weight of displaced fluid : FB waterVdisplaced g 10000.0352 x 0.027 g 0.324 N where 0.027 is depth of immersion. 76 76 • Worked Example Equate : W FB 4.21x10 4 cube 0.324 cube 770 kg / m3 77 77 • Worked Example b) h 78 78 • Worked Example Find the new weight of the cube: W 0.324 12 43 0.00753 cube g 0.317 N When the depth of immersion is h, the buoyancy force is : F B 0.0352 h water g Equate : FB W 79 12.017h 0.317 h 26.4 mm 79 LIQUID IN RELATIVE EQUILIBRIUM - If the vessel containing a liquid is at rest or moving with constant linear velocity, the liquid is not affected by the motion - But if the container is given continuous acceleration this will be imparted to the liquid which will take up a new position. - Fluid pressure is every where normal to the surface on which it acts. 5.2 Horizontal acceleration: at rest or moving with constant linear velocity W B A 80 1.5 m C 1.5 m W P m f f g R f P For equilibrium P = W . tan θ 1.5 m f W tan θ P W g W B A f tan θ g C 1.5 m 1.5 m and is constant for all points on the free surface. Example If the linear acceleration is given by f = 3 m/sec2, the tank is 3 m long and the depth of water when the tank is at rest is 1.5 m. Calculate: a- The angle of the water surface to the horizontal. b- The maximum pressure intensity on the bottom. 81 c- The minimum pressure intensity on the bottom. Solution: (a) (b) f 3 tan θ 0.306 g 9.81 θ 17 o Maximum pressure intensity occurs at point A hA = 1.5 + 1.5 tan = 1.96 m The pressure intensity at A = h A = 9.81 x 103 x 1.96 = 19.2 KN/m2 (c) The minimum intensity of pressure occurs at point B. hB = 1.5 – 1. 5 tan = 1.04 82 The pressure intensity at B = h B = 9.81 x 103 x 1.04 = 10.2 KN/m2 5.3 Vertical acceleration: Prism cross-section area is = a A f B h Accelerating force at X = P force due to pressure weight of prism = P . a - X . h .a By Newton's 2nd law h a f P = mass x acceleration = g h a Pa γ h a f g 83 f Pa γ h 1 g C dy tan θ dx For a constant value of ω , P will vary with x, since the centrifugal acceleration is ω2. x and, W 2 P ω x g dy ω 2 x tan θ dx g x P R A O W ω2 x ω2 x 2 y dx Constant g 2g 0 84 D B Integrating the x Axis of rotation 5.4 Forced vortex: If y is measured from the AB, i.e, ∴ Constant = 0 y = 0 when x = 0 . ω2 x 2 y 2g Example A cylindrical tank is spun at 300 r.p.m. with its vertical axis. The tank is 0.6 m high and 45 Cm. diameter and filled of water before spinning. Show that the water surface will take the form of paraboloid when the container is spun and calculate: (a) The speed at which the water surface will just touch the top rim and the center bottom of the tank. (b) The level to which the water will return when the tank stops spinning and the amount of water lost. 85 Solution: (a) When the surface just touched the rim of the base: y = 0.6 m and x = 0.225 m 2g y ω 15.25 2 x N = 145.6 rad . /sec. r.p.m (b) In figure the volume of the paraboloid will be half that of the containing cylinder ABCD . When the water surface touches the rim and the center of the bottom, volume of water left in tank = half of the original volume = ½ π (0.225)2 x 0.6 = 0.0475 m3 Depth when tank ceases to rotate = 0.3 86 ∴ Amount of water thrown out = 0.0475 m m3 The figure shows a semicircular gate of 1.2 m diameter and length 0.9m in the wall of a tank containing water. If the gate has a mass of 1000 kg, what force, F, is required to lift the gate? Resultant force R = pressure at centroid × area, 2 m π 42 R ρg(2 2) 43104 N 4 1.2 m Depth to centre of pressure, the point where the resultant force acts 87 I CG y Cp y CG y CG A π 4 12.566 y Cp 4.25 m 4 π4 4 4 4 2 Moment of R about pivot MR = 493104 (4.25-4.0) = 123276 N.m Moment required from F applied at base is MF is equal to MR MF = M R F x 2 = 123267 88 F = 61638 N b) Force Down = weight of water above gate (volume A) + weight of gate Force Up = F + Weight of water in volume B 2.6 m A 0.6 m 89 2.6 m B 0.6 m π 0.62 FD 2.6 0.6 0.9 1000 9.81 21087 N 4 π 0.62 FV 2.6 0.6 0.9 1000 9.81 F 16270 4 FD FV 21087 F16270 F 2108716270 4817 N 90 91 92 93