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
