PDF Free Download | Chemical Engineering Fluid Mechanics 2nd Edition by Ron Darby

Contents of Chemical Engineering Fluid Mechanics

• BASIC CONCEPTS
• FUNDAMENTALS
• A Basic Laws
• B Experience
• OBJECTIVE
• PHENOMENOLOGICAL RATE OR TRANSPORT LAWS
• A Fourier’s Law of Heat Conduction
• B Fick’s Law of Diffusion
• C Ohm’s Law of Electrical Conductivity
• D Newton’s Law of Viscosity
• THE ‘‘SYSTEM’’
• TURBULENT MACROSCOPIC (CONVECTIVE) TRANSPORT MODELS
• PROBLEMS
• NOTATION
• DIMENSIONAL ANALYSIS AND SCALE-UP
• INTRODUCTION
• UNITS AND DIMENSIONS
• A Dimensions
• B Units
• C Conversion Factors
• CONSERVATION OF DIMENSIONS
• A Numerical Values
• B Consistent Units
• DIMENSIONAL ANALYSIS
• A Pipeline Analysis
• B Uniqueness
• C Dimensionless Variables
• D Problem Solution
• E Alternative Groups
• SCALE-UP
• DIMENSIONLESS GROUPS IN FLUID
• MECHANICS
• ACCURACY AND PRECISION
• PROBLEMS
• NOTATION
• FLUID PROPERTIES IN PERSPECTIVE CLASSIFICATION OF MATERIALS AND FLUID
• PROPERTIES
• DETERMINATION OF FLUID VISCOUS (RHEOLOGICAL) PROPERTIES
• A Cup-and-Bob (Couette) Viscometer
• B Tube Flow (Poiseuille) Viscometer
• TYPES OF OBSERVED FLUID BEHAVIOR
• A Newtonian Fluid
• B Bingham Plastic Model
• C Power Law Model
• D Structural Viscosity Models
• TEMPERATURE DEPENDENCE OF VISCOSITY
• A Liquids
• B Gases
• DENSITY
• PROBLEMS
• NOTATION
• REFERENCES
• FLUID STATICS
• STRESS AND PRESSURE
• THE BASIC EQUATION OF FLUID STATICS
• A Constant Density Fluids
• B Ideal Gas—Isothermal
• C Ideal Gas—Isentropic
• D The Standard Atmosphere
• MOVING SYSTEMS
• A Vertical Acceleration
• B Horizontally Accelerating Free Surface
• C Rotating Fluid
• BUOYANCY
• V STATIC FORCES ON SOLID BOUNDARIES
• PROBLEMS
• NOTATION
• CONSERVATION PRINCIPLES
• THE SYSTEM
• CONSERVATION OF MASS
• A Macroscopic Balance
• B Microscopic Balance
• CONSERVATION OF ENERGY
• A Internal Energy
• B Enthalpy
• IRREVERSIBLE EFFECTS
• A Kinetic Energy Correction
• CONSERVATION OF MOMENTUM
• A One-Dimensional Flow in a Tube
• B The Loss Coefficient
• C Conservation of Angular Momentum
• D Moving Boundary Systems and Relative Motion
• E Microscopic Momentum Balance
• PROBLEMS
• NOTATION
• PIPE FLOW
• FLOW REGIMES
• GENERAL RELATIONS FOR PIPE FLOWS
• A Energy Balance
• B Momentum Balance
• C Continuity
• D Energy Dissipation
• NEWTONIAN FLUIDS
• A Laminar Flow
• B Turbulent Flow
• C All Flow Regimes
• POWER LAW FLUIDS
• A Laminar Flow
• B Turbulent Flow
• C All Flow Regimes
• V BINGHAM PLASTICS
• A Laminar Flow
• B Turbulent Flow
• C All Reynolds Numbers
• PIPE FLOW PROBLEMS
• A Unknown Driving Force
• B Unknown Flow Rate
• C Unknown Diameter
• D Use of Tables
• TUBE FLOW (POISEUILLE) VISCOMETER
• TURBULENT DRAG REDUCTION
• PROBLEMS
• NOTATION
• REFERENCES
• INTERNAL FLOW APPLICATIONS
• NONCIRCULAR CONDUITS
• A Laminar Flows
• B Turbulent Flows
• MOST ECONOMICAL DIAMETER
• A Newtonian Fluids
• B Non-Newtonian Fluids
• FRICTION LOSS IN VALVES AND FITTlNGS
• A Loss Coefficient
• B Equivalent L=D Method
• C Crane Method
• D -K (Hooper) Method
• E -K (Darby) Method
• NON-NEWTONIAN FLUIDS
• PIPE FLOW PROBLEMS WITH FITTINGS
• A Unknown Driving Force
• B Unknown Flow Rate
• C Unknown Diameter
• SLACK FLOW
• PIPE NETWORKS
• PROBLEMS
• NOTATION
• REFERENCES
• PUMPS AND COMPRESSORS
• PUMPS
• A Positive Displacement Pumps
• B Centrifugal Pumps
• PUMP CHARACTERISTICS
• PUMPING REQUIREMENTS AND PUMP
• SELECTION
• A Required Head
• B Composite Curves
• CAVITATION AND NET POSITIVE SUCTION
• HEAD (NPSH)
• A Vapor Lock and Cavitation
• B NPSH
• C Specific Speed
• D Suction Specific Speed
• V COMPRESSORS
• A Isothermal Compression
• B Isentropic Compression
• C Staged Operation
• D Efficiency
• PROBLEMS
• NOTATION
• REFERENCES
• COMPRESSIBLE FLOWS
• GAS PROPERTIES
• A Ideal Gas
• B The Speed of Sound
• PIPE FLOW
• A Isothermal Flow
• B Adiabatic Flow
• C Choked Flow
• D The Expansion Factor
• E Ideal Adiabatic Flow
• GENERALIZED EXPRESSIONS
• A Governing Equations
• B Applications
• C Solution of High-Speed Gas Problems
• PROBLEMS
• NOTATION
• REFERENCES
• FLOW MEASUREMENT AND CONTROL
• SCOPE
• THE PITOT TUBE
• THE VENTURI AND NOZZLE
• THE ORIFICE METER
• A Incompressible Flow
• B Compressible Flow
• LOSS COEFFICIENT
• ORIFICE PROBLEMS
• A Unknown Pressure Drop
• B Unknown Flow Rate
• C Unknown Diameter
• CONTROL VALVES
• A Valve Characteristics
• B Valve Sizing Relations
• C Compressible Fluids
• D Viscosity Correction
• PROBLEMS
• NOTATION
• REFERENCES
• EXTERNAL FLOWS
• DRAG COEFFICIENT
• A Stokes Flow
• B Form Drag
• C All Reynolds Numbers
• D Cylinder Drag
• E Boundary Layer Effects
• FALLING PARTICLES
• A Unknown Velocity
• B Unknown Diameter
• C Unknown Viscosity
• CORRECTION FACTORS
• A Wall Effects
• B Drops and Bubbles
• NON-NEWTONIAN FLUIDS
• A Power Law Fluids
• B Wall Effects
• C Carreau Fluids
• D Bingham Plastics
• PROBLEMS
• NOTATION
• REFERENCES
• FLUID–SOLID SEPARATIONS BY FREE SETTLING
• FLUID–SOLID SEPARATIONS
• GRAVITY SETTLING
• CENTRIFUGAL SEPARATION
• A Fluid–Solid Separation
• B Separation of Immiscible Liquids
• CYCLONE SEPARATIONS
• A General Characteristics
• B Aerocyclones
• C Hydrocyclones
• PROBLEMS
• NOTATION
• REFERENCES
• FLOW IN POROUS MEDIA
• I DESCRIPTION OF POROUS MEDIA
• A Hydraulic Diameter
• B Porous Medium Friction Factor
• C Porous Medium Reynolds Number
• II FRICTION LOSS IN POROUS MEDIA
• A Laminar Flow
• B Turbulent Flow
• C All Reynolds Numbers
• PERMEABILITY
• MULTIDIMENSIONAL FLOW
• PACKED COLUMNS
• FILTRATION
• A Governing Equations
• B Constant Pressure Operation
• C Constant Flow Operation
• D Cycle Time
• E Plate-and-Frame Filters
• F Rotary Drum Filter
• G Compressible Cake
• PROBLEMS
• NOTATION
• REFERENCES
• FLUIDIZATION AND SEDIMENTATION
• FLUIDIZATION
• A Governing Equations
• B Minimum Bed Voidage
• C Nonspherical Particles
• SEDIMENTATION
• A Hindered Settling
• B Fine Particles
• C Coarse Particles
• D All Flow Regimes