BookAX: Particle Size Measurement Powder Technology Series
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Particle Size Measurement Powder Technology Series


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Contents:
  • Acknowledgements
  • Preface to the the fifth edition
  • Preface to the the first edition
  • Editor's foreword
  • 1 Powder sampling
  • 1.1 Introduction
  • 1.2 Sample selection
  • 1.3 Sampling stored material
  • 1.3.1 Sampling stored non-flowing
  • material
  • 1.3.2 Sampling stored free-flowing
  • material
  • 1.4 Sampling flowing streams
  • 1.4.1 Sampling from a conveyor belt
  • 1.4.2 Point samplers
  • 1.4.3 Sampling from falling streams
  • 1.4.4 Stream sampling ladles
  • 1.4.5 Traversing cutters
  • 1.4.6 Sampling dusty material
  • 1.4.7 Moving flap sampler
  • 1.5 Sample reduction
  • 1.5.1 Scoop sampling
  • 1.5.2 Cone and quartering
  • 1.5.3 Table sampling
  • 1.5.4 Chute splitting
  • 1.5.5 The rotary sample divider
  • 1.5.6 Miscellaneous sampling devices
  • 1.6 Slurry sampling
  • 1.7 Reduction of laboratory sample to
  • measurement sample
  • 1.8 Number of samples required
  • 1.9 Theoretical statistical errors on a number basis
  • 1.10 Practical statistical errors on a number basis
  • 1.11 Theoretical statistical errors on a weight basis
  • 1.12 Practical statistical errors on a weight basis
  • 1.13 Experimental tests of sampling techniques
  • 1.14 Weight of sample required
  • 1.14.1 Gross sample
  • 1.14.2 Sampling by increments
  • 2 Data presentation and interpretation
  • 2.1 Introduction
  • 2.2 Particle size
  • 2.3 Average diameters
  • 2.4 Particle dispersion
  • 2.5 Particle shape
  • 2.5.1 Shape coefficients
  • 2.5.2 Shape factors
  • 2.5.3 Shape regeneration by Fourier analysis
  • 2.5.4 Fractal dimensions
  • characterization of textured surfaces
  • 2.5.5 Other methods of shape analysis
  • 2.5.6 Sorting by shape
  • 2.6 Determination of specific surface from
  • size distribution data
  • 2.6.1 from a number count
  • 2.6.2 from a surface count
  • 2.6.3 from a volume (mass) count
  • 2.7 Tabular presentation of particle size
  • distribution
  • 2.8 Graphical presentation of size
  • distribution data
  • 2.8.1 Presentation on linear graph paper
  • 2.9 Standard forms of distribution functions
  • 2.10 Arithmetic normal distribution
  • 2.10.1 Manipulation of the normal equation
  • 2.11 The log-normal distribution
  • 2.11.1 Relationship between number mean
  • sizes for a log-normal distribution
  • 2.11.2 Derived mean sizes
  • 2.11.3 Transformation between log-normal
  • distributions
  • 2.11.4 Relationship between median and
  • mode of a log-normal equation
  • 2.11.5 An improved equation and graph
  • paper for log-normal evaluations
  • 2.11.6 Application
  • 2.12 Johnson's SB distribution
  • 2.13 Rosin-Rammler, Bennet-Sperling formula
  • 2.14 Other distribution laws
  • 2.14.1 Simplification of two-parameter equations
  • 2.14.2 Comments
  • 2.15 The law of compensating errors
  • 2.16 Evaluation of non linear
  • distributions on log-normal paper
  • 2.16.1 Bimodal intersecting distributions
  • 2.16.2 Bimodal non-intersecting
  • distributions
  • 2.16.3 Other distributions
  • 2.16.4 Applications of log-normal plots
  • 2.16.5 Curve fitting
  • 2.17 Alternative notations for frequency
  • distribution
  • 2.17.1 Notation
  • 2.17.2 Moment of a distribution
  • 2.17.3 Transformation from qt(x) to qr(x).
  • 2.17.4 Relation between moments
  • 2.17.5 Means of distributions
  • 2.17.6 Standard deviations
  • 2.17.7 Coefficient of variation
  • 2.17.8 Applications
  • 2.17.9 Transformation of abscissae
  • 2.18 Phi-notation
  • 3 Particle size by image analysis
  • 3.1 Introduction
  • 3.2 Optical microscopy
  • 3.2.1 Upper size limit
  • 3.2.2 Lower size limit
  • 3.3 Sample preparation
  • 3.4 Measurement of plane sections through packed beds
  • 3.5 Particle size
  • 3.6 Calibration
  • 3.6.1 Linear eyepiece graticules
  • 3.6.2 Globe and circle graticules
  • 3.7 Training of operators
  • 3.8 Experimental techniques
  • 3.9 Determination of particle size
  • distribution by number
  • 3.10 Conditions governing a weight size
  • determination
  • 3.10.1 Illustrative example of the
  • calculation of a size distribution by weight
  • 3.11 Quantitative image analysis
  • 3.11.1 Calibration of image analyzers
  • 3.11.2 Experimental procedures
  • 3.11.3 Commercial quantitative image analysis systems.
  • 3.11.4 On-line microscopy
  • 3.12 Electron microscopy
  • 3.13 Transmission electron microscopy
  • 3.13.1 Specimen preparation for TEM
  • 3.13.2 Replica and shadowing techniques
  • 3.13.3 Chemical analysis
  • 3.14 Scanning electron microscopy
  • 3.15 Other scanning electron microscopy techniques
  • 3.16 Errors involved in converting a
  • number to a volume count
  • 4 Particle size analysis by sieving
  • 4.1 Introduction
  • 4.2 Woven-wire and punched plate sieves
  • 4.3 Electroformed micromesh sieves
  • 4.4 Standard sieves
  • 4.5 Mathematical analysis of the sieving process
  • 4.6 Calibration of sieves
  • 4.7 Sieving errors
  • 4.8 Methods of sieving
  • 4.9 Amount of sample
  • 4.10 Hand sieving
  • 4.11 Machine sieving
  • 4.12 Wet sieving
  • 4.12.1 Manual
  • 4.12.2 Wet sieving by machine
  • 4.13 Air-Jet sieving
  • 4.14 The Sonic Sifter
  • 4.15 The Seishin Robot Sifter
  • 4.16 Automatic systems
  • 4.16.1 The Gradex particle size analyzer
  • 4.16.2 Labcon automatic sieve system
  • 4.17 Ultrasonic sieving
  • 4.18 The sieve cascadograph
  • 4.19 Felvation
  • 4.20 Self organized sieves (SORSI)
  • 4.21 Shape separation
  • 4.22 Correlation with light scattering data
  • 4.23 Conclusions
  • 5 Fluid classification
  • 5.1 Introduction
  • 5.2 Assessment of classifier efficiency
  • 5.3 Systems
  • 5.4 Counter-flow equilibrium classifiers
  • in a gravitational field-elutriators
  • 5.5 Cross-flow gravitational classification
  • 5.5.1 The Warmain Cyclosizer
  • 5.5.2 The Humboldt particle size analyzer TDS
  • 5.6 Counter-flow centrifugal classifiers
  • 5.7 Cross-flow centrifugal classifiers
  • 5.8 Zig-zag classifiers
  • 5.9 Cross-flow elbow classifier
  • 5.10 Fractionation methods for particle
  • size measurement
  • 5.11 Hydrodynamic chromatography
  • 5.12 Capillary hydrodynamic fractionation
  • 5.13 Capillary zone electrophoresis
  • 5.14 Size exclusion chromatography
  • 5.15 Field flow fractionation
  • 5.15.1 Sedimentation field flow fractionation
  • 5.15.2 Time-delayed-exponential SF3
  • 5.15.3 Thermal field flow fractionation
  • 5.15.4 Magnetic field flow fractionation
  • 5.15.5 Flow field flow fractionation
  • 5.15.6 Steric field flow fractionation
  • 5.16 The Matec electro-acoustic system EAS-8000
  • 5.17 Continuous SPLIT fractionation
  • 5.18 Classification by decantation
  • 6 Interaction between fluids and particles
  • 6.1 Introduction
  • 6.2 Settling of a single homogeneous sphere under a gravitational force
  • 6.2.1 Relationship between settling
  • velocity and particle size
  • 6.2.2 Calculation of particle size in
  • the laminar flow region
  • 6.3 Size limits for gravity sedimentation
  • 6.3.1 Upper size limit
  • 6.3.2 Lower size limit
  • 6.4 Time for terminal velocity to be attained
  • 6.5 Wall effects
  • 6.6 Errors due to discontinuity of the fluid
  • 6.7 Viscosity of a suspension
  • 6.8 Non-rigid spheres
  • 6.9 Non-spherical particles
  • 6.9.1 Stokes region
  • 6.9.2 Transition region
  • 6.10 Relationship between drag coefficient
  • and Reynolds number in the transition region
  • 6.11 The turbulent flow region
  • 6.12 Concentration effects
  • 6.13 Hindered settling
  • 6.13.1 Low concentration effects
  • 6.13.2 High concentration effects
  • 6.14 Electro-viscosity
  • 6.15 Dispersion of powders
  • 6.15.1 Dry powder dispersion
  • 6.15.2 The use of glidants to improve
  • flowability of dry powders
  • 6.15.3 Wet powder dispersion
  • 6.15.4 Role of dispersing agents
  • 6.15.5 Wetting a powder
  • 6.15.6 Determination of contact angle (Theta)
  • 6.15.7 Deagglomerating wetted clumps
  • 6.15.8 Suspension stability
  • 6.15.9 Tests of dispersion quality
  • 7 Sedimentation theory
  • 7.1 Powder density
  • 7.2 Liquid viscosity
  • 7.3 Resolution of sedimenting suspensions
  • 7.4 Concentration changes in a suspension settling under gravity
  • 7.5 Relationship between density gradient
  • and concentration
  • 7.5.1 Hydrometers
  • 7.6 Theory for the gravity photosedimentation technique
  • 7.6.1 The Beer-Lambert law
  • 7.6.2 The extinction coefficient
  • 7.7 Theory for concentration determination
  • with the x-ray gravitational sedimentation technique
  • 7.8 Theory for mass oversize distribution
  • determination for cumulative, homogeneous, gravitational sedimentation
  • 7.9 Stokes equation for centrifugal sedimentation
  • 7.9.1 General theory
  • 7.10 Stokes diameter determination for
  • cumulative and incremental line-start techniques
  • 7.10.1 Incremental, line-start,
  • centrifugal technique
  • 7.10.2 Homogeneous, cumulative,
  • centrifugal technique
  • 7.10.3 Sedimentation distance small
  • compared with distance from centrifuge axis
  • 7.11 Line-start technique using a photocentrifuge
  • 7.11.1 Introduction
  • 7.11.2 Homogeneous mode
  • 7.11.3 Line-start mode
  • 7.12 Theory for mass oversize distribution
  • determination for cumulative, homogeneous,
  • centrifugal sedimentation
  • 7.13 Theory for mass oversize distribution
  • determination for incremental, homogeneous,
  • centrifugal sedimentation
  • 7.13.1 General theory
  • 7.13.2 Variable time method
  • 7.13.3 Variable inner radius (pipette withdrawal)
  • 7.13.4 Variable measurement radius
  • (scanning x-ray centrifuge)
  • 8 Sedimentation methods of particle size
  • measurement
  • 8.1 Introduction
  • 8.2 Homogeneous incremental gravitational sedimentation
  • 8.2.1 The pipette method of Andreasen
  • 8.2.2 The photosedimentation technique
  • 8.2.3 X-ray sedimentation
  • 8.2.4 Hydrometers and divers
  • 8.3 Homogeneous cumulative gravitational sedimentation
  • 8.3.1 Introduction
  • 8.3.2 Balances
  • 8.3.3 Sedimentation columns
  • 8.4 Line-start incremental gravitational sedimentation
  • 8.4.1 Photosedimentation
  • 8.5 Line-start cumulative gravitational sedimentation
  • 8.5.1 Introduction
  • 8.5.2 Methods
  • 8.6 Homogeneous incremental centrifugal sedimentation
  • 8.6.1 Introduction
  • 8.6.2 The Simcar pipette disc centrifuge
  • 8.6.3 The Ladal pipette disc centrifuge
  • 8.6.4 The Ladal x-ray disc centrifuge
  • 8.6.5 The Du Pont/Brookhaven?Create scanning
  • x-ray disc centrifugal sedimentometer (BI-XDC)
  • 8.6.6 The BI-DCP disc (photo)centrifuge
  • 8.7 Cuvet photocentrifuges
  • 8.8 Homogeneous cumulative centrifugal sedimentation
  • 8.8.1 Methods
  • 8.9 Line-start incremental centrifugal sedimentation
  • 8.9.1 Disc photocentrifuges
  • 8.10 Line-start cumulative centrifugal sedimentation
  • 8.10.1 MSA analyzer
  • 8.11 Particle size analysis using
  • non-invasive dielectric sensors
  • 8.12 Conclusions
  • 9 Stream scanning methods of particle size
  • measurement
  • 9.1 Introduction
  • 9.2 The electrical sensing zone method
  • (The Coulter Principle)
  • 9.2.1 Introduction
  • 9.2.2 Operating principle
  • 9.2.3 Theory for the electrical sensing
  • zone method
  • 9.2.4 Effect of particle shape and orientation
  • 9.2.5 Pulse shape
  • 9.2.6 Effect of coincidence
  • 9.2.7 Multiple aperture method for powders having a wide size range
  • 9.2.8 Calibration
  • 9.2.9 Carrying out a mass balance
  • 9.2.10 Oversize counts on a mass basis
  • using the Coulter Counter
  • 9.2.11 Apparatus
  • 9.2.12 Limitations of the method
  • 9.2.13 Coulter Multisizer mass balance
  • calculation for BCR 70 standard quartz powder
  • 9.3 Fiber length analysis
  • 9.4 Optical particle counters
  • 9.4.1 Aerometrics Eclipse particle size analyzer
  • 9.4.2 Hiac/Royco
  • 9.4.3 Kratel Partascope
  • 9.4.4 Kratel Partograph
  • 9.4.5 Climet
  • 9.4.6 Particle Measuring Systems
  • 9.4.7 Flowvision
  • 9.4.8 Polytec HC (high concentration
  • optical counter)
  • 9.4.9 Lasentec
  • 9.4.10 Galai CIS
  • 9.4.11 Spectrex Prototron
  • 9.4.12 Spectrex PCT-1 laser particle
  • counter
  • 9.4.13 Procedyne
  • 9.4.14 Kane May
  • 9.4.15 Met One
  • 9.4.16 Erdco acoustical counter
  • 9.4.17 Micro Pure Systems acoustic
  • particle monitors (Monitek)
  • 9.4.18 Rion laser based liquidborne
  • particle counter
  • 9.4.19 Faley Status 8000
  • 9.4.20 Kowa Nanolyzer(TM) PC-30 and PC-500
  • 9.4.21 Malvern Autocounters
  • 9.4.22 Particle Sizing Systems
  • Accusizer(TM)
  • 9.4.23 AWK electronic sieve analyzer
  • 9.4.24 PMT universal size distribution
  • measuring systems
  • 9.4.25 Canty Vision System
  • 9.4.26 Contamination Control Systems
  • 9.5 Aerodynamic time-of flight measurement
  • 9.5.1 Amherst API Aerosizer
  • 9.5.2 The TSI Aerodynamic Particle Sizer
  • APS 33B
  • 9.6 Laser phase/Doppler principle
  • 9.6.1 BIRAL PD-Lisatek and L2F
  • 9.6.2 Hosokawa Mikropul E-Spart Analyzer
  • 9.6.3 Aerometrics phase/Doppler particle analyzer (APDPA)
  • 9.6.4 Dantec Particle Dynamic Analyzer
  • 9.7 Interferometers
  • 9.7.1 The TSI Liquitrak(TM)
  • interferometer
  • 9.8 Flow ultramicroscope
  • 9.8.1 ISPA image analysis system
  • 9.9 Measurement of the size distribution
  • of drops in dispersions
  • 9.10 Dupont electrolytic grain size analyzer
  • 9.11 TSI condensation particle counter
  • 9.12 TSI diffusion battery
  • 9.13 TSI diffusional particle sizer
  • 9.14 Differential mobility analyzer (DMA)
  • 9.15 Scanning mobility particle sizer (SMPS)
  • 9.16 Atmospheric particle counters
  • 10 Field scanning methods of particle size
  • measurement
  • 10.1 Introduction
  • 10.2 Effect of comminution on particle
  • size distribution
  • 10.3 Single point analyzers
  • 10.3.1 Static noise measurement
  • 10.3.2 Ultrasonic attenuation.
  • 10.3.3 Beta-ray attenuation
  • 10.3.4 X-ray attenuation and fluorescence
  • 10.3.5 Counter-flow classifiers
  • 10.3.6 Hydrocyclones
  • 10.3.7 The cyclosensor
  • 10.3.8 Automatic sieving machines
  • 10.3.9 Gas flow permeametry
  • 10.3.10 Correlation techniques
  • 10.4 Low angle laser light scattering (LALLS)
  • 10.4.1 Introduction
  • 10.4.2 Theoretical basis for LALLS
  • instruments
  • 10.4.3 Commercial instruments
  • 10.5 Optical incoherent space frequency analysis
  • 10.6 Small angle x-ray scattering (SAXS)
  • 10.7 Ultrasonic attenuation
  • 10.8 Photon correlation spectroscopy (PCS)
  • 10.8.1 Introduction
  • 10.8.2 Principles
  • 10.8.3 Through dynamic light scattering
  • 10.8.4 Particle size
  • 10.8.5 Concentration effects
  • 10.8.6 Particle interaction
  • 10.8.7 Particle size effects
  • 10.8.8 Polydispersity
  • 10.8.9 The controlled reference method
  • 10.8.10 Commercial equipment
  • 10.8.11 Discussion
  • 10.8.12 Diffusion wave spectroscopy (DWS)
  • 10.9 Insitec Ensemble Particle
  • Concentration-Size (EPCS) Systems
  • 10.10 Turbo-Power Model TPO-400
  • 10.11 Turbidity
  • 10.12 Transient turbidity
  • 10.13 Concentration monitors
  • 10.14 Shape discrimination
  • 11 Industrial applications of particle size
  • measurement
  • 11.1 Introduction
  • 11.2 Industrial diamonds
  • 11.3 Control of oversize particles
  • 11.4 Starry night
  • 11.5 Control of adhesive additives
  • 11.6 Video-tape
  • 11.7 Curve fitting
  • 11.8 Effect of size distribution on filter efficiency
  • 11.9 Predicting pigment gloss and hiding power
  • 11.10 Strength of engineering plastics
  • 11.11 Homogeneity control of ceramic paste
  • 11.12 Flowability
  • 11.13 Elimination of intra-lot variability
  • by mixing
  • 11.14 Mixing and segregation
  • 11.15 Comminution
  • 11.16 Attrition
  • 11.17 Instrument evaluation
  • 11.17.1 Introduction
  • 11.17.2 Evaluation procedure
  • 11.17.3 Definition of accuracy
  • 11.17.4 Definition of reproducibility
  • 11.17.5 Mean accuracy and reproducibility
  • 11.17.6 Discussion
  • 11.18 Summary
  • Appendix Manufacturers and suppliers
  • Author index


Particle Size Measurement Powder Technology Series

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