Slurry Transport Using Centrifugal Pumps, Third Edition | by K. C. Wilson, G. R. Addie, A. Sellgren and R. Clift | ISBN: 9780387232621. Fluid and Particle Mechanics. Principles of Particulate Slurry Flow. Motion and Deposition of Settling Solids. Components of Slurry Systems.

January 30, 2010 by kutenk
Filed under: Engineering Books 

Slurry Transport Using Centrifugal Pumps, Third Edition

by K. C. Wilson, G. R. Addie, A. Sellgren and R. Clift
ISBN:9780387232621

Discussing the behaviors of various sorts of slurry flow, this unique text deals with the behavior of centrifugal pumps handling slurries, and with how pumps and pipelines interact as a system.

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Slurry Transport Using Centrifugal Pumpsm, Third Edition









Chapter 1 – Introduction
1.1: Applications of Slurry Transport
1.2: Topics Covered in This Book
1.3: List of Symbols
References

Chapter 2 – Review of Fluid and Particle Mechanics
2.1: Introduction
2.2: Basic Relations for Flow of Simple Fluids
2.3: Friction in Laminar and Turbulent Flow of Simple Fluids
2.4: Basic Relations for Slurry Flow
2.5: Settling of Solids in Liquids
References

Chapter 3 – Flow of Non-Settling Slurries
3.1: Introduction
3.2: Rheometry and Rheological Models
3.3: Turbulent Flow of Non-Newtonians
3.4: Scale-up of Laminar Flow
3.5: Scale-up of Turbulent Flow
3.6: Effects of Solids Concentration
3.7: Transition from Laminar to Turbulent Flow
3.8: Case Study
References

Chapter 4 – Principles of Particulate Slurry Flow
4.1: Introduction
4.2: Homogeneous and Pseudo-Homogeneous Flow
4.3: Flow of Settling Slurries
4.4: Physical Mechanisms Influencing Type of Flow
4.5: Stationary Deposits of Solids
4.6: Heterogeneous Flow
4.7: Specific Energy Consumption
References

Chapter 5 – Motion and Deposition of Settling Solids
5.1: Introduction
5.2: Resisting and Driving Forces
5.3: Velocity at the Limit of Stationary Deposition
5.4: Effect of Solids Concentration on Deposit Velocity
5.5: Fully Stratified Coarse-Particle Transport
5.6: Case Studies
References





Chapter 6 – Heterogeneous Slurry Flow in Horizontal Pipes
6.1: Introduction
6.2: Concepts of Near-Wall Hydrodynamic Lift
6.3: Stratification Ratio and Scale-up
6.4: Effect of Particle Size Distribution
6.5: Simplified Approach for Estimating Solids Effect
6.6: Effect of Large Pipe Diameter
6.7: Effect of High Concentration of Solids
6.8: Case Studies
References




Chapter 7 – Complex Slurries
7.1: Introduction
7.2: Broad-graded Slurries with Newtonian Carrier Fluids
7.3: The ‘Stabflo’ Debate
7.4: Particle Settling in non-Newtonian Fluids
7.5: Particle Settling in Laminar non-Newtonian Pipeline Flow
7.6: Turbulent Flow of Slurries with non-Newtonian Carrier Fluids
7.7: Example Problems and Case Study
References

Chapter 8 – Vertical and Inclined Slurry Flow
8.1: Introduction
8.2: Analysis of Vertical Flow
8.3: Applications of Vertical Flow
8.4: Effect of Pipe Inclination on Deposition Limit
8.5: Effect of Pipe Inclination on Friction Loss
8.6: Worked Examples and Case Study
References

Chapter 9 – Centrifugal Pumps
9.1: Introduction: Basic Concepts and Affinity Laws
9.2: Hydraulic Design and Specific Speed
9.3: Cavitation and Net Positive Suction Head
9.4: Mechanical Design
9.5: Performance Testing
9.6: Case Studies
References



Chapter 10 – Effect of Solids on Pump Performance
10.1: Introduction and Previous Correlations
10.2: Effect of Pump Size
10.3: Effect of Solids Concentration
10.4: Effect of Particle Properties
10.5: Non-settling Slurries
10.6: Suction Performance
10.7: Generalised Solids-Effect Diagram for Settling Slurries
References

Chapter 11 – Wear and Attrition
11.1: Introduction
11.2: Wear-Resistant Materials
11.3: Combined Erosion and Corrosion
11.4: Experimental Testing Methods
11.5: Numerical Modelling of Flow and Wear
11.6: Pump and Wear Variables
11.7: Variation of Wear with Design Geometry
11.8: Variation of Component Wear with Different Duties
11.9: Practical Considerations and Field Experience
11.10: Particle Attrition
References



Chapter 12 – Components of Slurry Systems
12.1: Introduction
12.2: Pump Suction Piping Considerations
12.3: Pump Drive Trains
12.4: Pump Layout and Spacing
12.5: Flow Control and Valving
12.6: Instrumentation
References

Chapter 13 – System Design and Operability
13.1: Introduction
13.2: Homogeneous Slurries
13.3: Effect of Solids Concentration in Settling Slurries
13.4: Effect of Particle Size
13.5: Case Study
References

Chapter 14 – Pump Selection and Cost Considerations
14.1: General Concepts of Pump Selection
14.2: Wear Considerations
14.3: Economic Considerations
14.4: Downtime Costs
14.5: Effect of System Size
14.6: Selection Procedure
References

Chapter 15 – Practical Experience with Slurry Systems
15.1: Introduction
15.2: Pumps in Series
15.3: Pumps in Parallel
15.4: Suction Problems
15.5: Pumping Frothy Mixtures
15.6: Flow Instability
15.7: Operation with a Stationary Bed
15.8: Transient Conditions
References

Chapter 16 – Environmental Aspects of Slurry Systems
16.1: Introduction
16.2: The Benefits of Integrated Processing
16.3: Energy Consumption and Associated Emissions
16.4: A Cautionary Tale – Velenje and its Lakes
References

Worked Examples and Case Studies in U.S. Customary Units
Example 2.A – Flow of Water in a Pipe
Example 2.B – Calculation of Terminal and Hindered Settling Velocities
Worked Examples of Vertical Hoisting from Chapter 8
Worked Examples from Chapter 10



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