Module : Review of Fluid Mechanics Basic Principles for Water Resources Engineering Robert Pitt University of Alabama and Shirley Clark Penn State - Harrisburg Mass quantity of matter that a substance contains Weight effect of the force of gravity upon a substance Density mass of a substance per unit volume Viscosity measure of a fluid s resistance to flow Mass Density (density) (): For water at 4 o C, = 1000 kg/m 3 or 1.94 slugs/ft 3. Specific weight (γ): gravitational force per unit volume of water. For water at 4 o C, γ = 9810 N/m 3 or.4 lb/ft 3. γ = g where g = gravitational constant Specific Gravity: Density of substance Specific Gravity = Density of water γ = g specific gravity = Specific weight of a fluid is defined as the weight per unit volume and is related to density. Specific gravity of a fluid is the ratio of the density of the fluid to the density of pure water at standard conditions (such as at 15 o C). fluid H 0@15 o C Hydraulics for Operators, Barbara Hauser, Lewis Publishers, Boca Raton, FL. 1993. 1
Newton s equation of viscosity: dµ τ = µ dy Viscosity is the proportionality constant between shear stress and strain rate of a fluid element: Dynamic Viscosity (µ): ratio of the shear stress to the velocity gradient between two thin sheets of fluid Kinematic Viscosity (ν): ratio of the dynamic viscosity to the density Kinematic viscosity related to (dynamic) viscosity: µ ν = Fluid characterized by: Temperature, T Density, (units: mass/volume) Absolute/Dynamic Viscosity, µ (units: force-time/area) Fluid flow characterized by: Velocity, V (units: length/time) Kinematic Viscosity, ν (units: area/time) µ ν = Where ν = kinematic viscosity µ = absolute/dynamic viscosity = fluid density According to the table of the physical properties of water, the specific weight of water at 0 o C is 9789 N/m 3, what is its density? γ = g 4 1kg m/sec 998 N sec /m = N 3 = 998 kg/m 3 9789 N/m = 9.81 m/sec
Properties of Water in U.S. Customary (English) Units Properties of Water in SI (Metric) Units Temp. ( o F) 3 40 50 0 70 80 100 10 140 10 180 1 Specific Weight γ (lb/ft 3 ).4.43.41.37.30..00 1.71 1.38 1.00 0.80 59.83 Mass Density (lb-sec /ft 4 or slugs/ft 3 ) 1.940 1.940 1.940 1.938 1.93 1.934 1.97 1.918 1.908 1.89 1.890 1.80 Absolute Viscosity µ (x 10 5 lb-sec/ft ) 3.74 3.9.735.359.050 1.799 1.44 1.18 0.981 0.838 0.780 0.593 Kinematic Viscosity ν (x10 5 sec/ft ) 1.931 1.4 1.410 1.17 1.059 0.930 0.739 0.09 0.514 0.44 0.413 0.319 Vapor Pressure p v (psi) 0.09 0.1 0.18 0. 0.3 0.51 0.95 1.9.89 4.74 5.99 14.70 Temp. ( o C) 0 5 10 15 0 5 30 40 0 80 100 Specific Weight γ (kn/m 3 ) 9.805 9.807 9.804 9.798 9.789 9.777 9.74 9.730 9.4 9.530 9.399 Mass Density (kg/m 3 ) 999.8 1000.0 999.7 999.1 998. 997.0 995.7 99. 983. 971.8 958.4 Absolute Viscosity µ (x 10 3 kg/m-sec or 10 3 N-sec/m ) 1.781 1.518 1.307 1.139 1.00 0.890 0.798 0.53 0.4 0.354 0.8 Kinematic Viscosity ν (x10 m /sec) 1.785 1.519 1.30 1.139 1.003 0.893 0.800 0.58 0.474 0.34 0.94 Vapor Pressure p v (kpa) 0.1 0.87 1.3 1.70.34 3.17 4.4 7.38 19.9 47.34 101.33 From: George Tchobanoglous (Metcalf & Eddy, Inc.). Wastewater Engineering: Collection and Pumping of Wastewater. McGraw-Hill, Inc., New York, NY. 1981. Table B-. Warren Viessman, Jr. and Mark J. Hammer. Water Supply and Pollution Control, Sixth Edition. Addison Wesley, Menlo Park, CA. 1998. Table A.8. Larry W. Mays. Water Resources Engineering, 1st Edition. John Wiley & Sons, Inc. New York, NY. Table.1.1. From: George Tchobanoglous (Metcalf & Eddy, Inc.). Wastewater Engineering: Collection and Pumping of Wastewater. McGraw-Hill, Inc., New York, NY. 1981. Table B-. Warren Viessman, Jr. and Mark J. Hammer. Water Supply and Pollution Control, Sixth Edition. Addison Wesley, Menlo Park, CA. 1998. Table A.8. Larry W. Mays. Water Resources Engineering, 1st Edition. John Wiley & Sons, Inc. New York, NY. Table.1.1. Reynolds Number, Re or N R : Vd Vd N R = = µ ν Where V = fluid velocity D or d = diameter of equivalent pipe = fluid density µ = absolute viscosity ν = kinematic viscosity THE REYNOLDS NUMBER SHOULD BE DIMENSIONLESS: All units must cancel out!! Calculate the Reynolds number for the following water flow conditions: V = 0.10 ft/sec D = 1 inch Solution: Convert the pipe diameter to feet since V is in ft/sec. D = 1 inch/(1 in/ft) = 0.083 ft Since T is not given, assume T = 70 o F, and look up the density, absolute viscosity, and kinematic viscosity at 70 o F. = 1.93 lb-sec /ft 4 µ =.050 x 10-5 lb-sec/ft ν = 1.059 x 10-5 ft /sec 3
Solution: Substituting: 4 (0.10 ft /sec)(0.083 ft)(1.93lb sec / ft ) 5.050x10 lb sec/ ft 784 OR (0.10 ft /sec)(0.083 ft) 5 1.059x10 ft /sec 784 Steady Flow assumes constant flow rate throughout the analysis. Flow velocity does not change with respect to time at a given location. Unsteady Flow does not assume a constant flow rate throughout the analysis. Flow velocity likely does change with respect to time at a given location. Can assume Steady Flow for the analyses performed in this class. Unsteady flow assumptions used for floodplain analysis, for example. Velocity Distribution in Pipe and Open-Channel Flow Streamlines paths of single fluid particles. 4
Laminar Flow Streamlines are parallel, smooth and predictable No mixing occurs between layers Reynolds number < 100 to 4000 What is the maximum velocity (ft/sec) for laminar flow (assuming 4000) in a 1-inch pipe (water is the fluid, 0 o F is the temperature)? Vd µ Substituting : 4 V (1inch)(1ft/1 in)(1.934 lb - sec /ft ) 4000 = -5.359 x 10 lb - sec/ft V = 0.59 ft/ sec Maximum Velocity of Laminar Flow or Water in Circular Pipes ( N R = 4000) millimeters 1 5 50 150 300 Diameter inches 0.5 0.5 1 1 Maximum Velocity of Laminar Flow meters/sec 0.71 0.3 0.18 0.09 0.03 0.01 feet/sec.34 1.17 0.59 0.9 0.10 0.05 Turbulent Flow (calculated as steady flow although not) Streamlines are not parallel or predictable Mixing occurs across pipe diameter Reynolds number > 100 to 4000 Eddies may occur in flow profile Reference: McGhee, Chapter 3 5
Water flows full in a 5-foot diameter pipe at a velocity of 10 ft/sec. What is the Reynolds number? The temperature is 50 o F. From table, at 50 o F, ν = 1.41 x 10-5 ft /sec. VD ν (10 ft / sec)(5 ft) 5 1.41x10 ft / sec From: Introduction to Fluid Mechanics, Third Edition. James E. John and William L. Haberman. Prentice-Hall, Englewood Cliffs, NJ. 1988. 3.55x10