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    Dr Ali Nokhodchi

    PARTICLE SIZEANALYSIS

    -Particle shape

    -Particle size distribution

    -Particle size measurements

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    Particle size Analysis

    Primary characteristics, relating tobasic material properties, particulate size,shape and surface area

    Secondary characteristics, behaviouralproperties such as flow, bulk and tappeddensity, compactibility, lubricity

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    The ideal particle and reality

    Sol id Sphere

    One dimension (radius) describessize, shape, surface area, volume

    Sol id Geometr ical Part ic les

    Two-three dimensions required todescribe size, shape, surface area,

    volume

    r

    r

    hh

    h

    wl r

    Solid Irregu lar Partic lesSize and shape can only be

    approximated, surface area and

    volume can be measured

    Porou s Irregular Part ic lesSize, shape, surface area and

    volume can only be approximated

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    Particle Shape TerminologyAcicular: needle-shaped

    Angular : sharp edged; having a roughly polyhedral shape

    Dendritic: having a branched crystalline shape

    Fibrous: thread-likeFlaky : plate-like

    Granular : irregular but of approximately spherical overall form

    Irregular : lacking any symmetry

    Modular : having a rounded, irregular shape

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    Particle shape

    The thickness is the height of the particlewhen it is resting in its position of maximumstability.

    The breadth is the minimum distance betweentwo tangential planes which are perpendicular

    to those defining the thickness and breadth.

    The length is the distance between two planeswhich are perpendicular to those defining thethickness and breadth.

    x

    yz

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    Shape factors

    Elongation ratio = length/breadth

    Flakiness ratio = breadth/thickness

    Bulkiness factor= projected area/(length xbreadth)

    The ratio of two equivalent diameters obtained by differentmethods is termed a shape factor.

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    Circularity

    Circumscribed circle (dc)

    Inscribed circle (di)

    dc=10 mmdi= 1 mm

    Circularity=0.1

    dc=10 mmdi= 5 mmCircularity=0.5

    P i l i i fl di l i

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    Particle size influences dissolution

    DissolutionSmall particles dissolves more rapidly than larger ones.

    Drug in Solid

    Dosage Form

    Drug Crystals

    Exposed to GI Fluids

    Drug Dissolved

    In GI Fluids

    Drug in

    Blood

    Dissolution Absorption

    Release from

    Dosage Form

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    Particle size effect on bioavailability of a poorly

    soluble drug

    Particle sizedissolution rate ?Bioavailability ?

    Other examples:

    Tetracycline

    Aspirin

    Sulphonamides

    Digoxin

    Dicoumarol

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    1 g

    1 cm

    1 cm

    1 cmSurface area = area/face 6 faces = 6 cm2

    Weight-specific surface area = Sw = [surface area/weight]

    Therefore , Sw = 6 cm2 /g

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    The total surface area in 1 g is now: [1012 cubes][6 x 10-8 cm2/cube]

    Sw = 6 104 cm2 = 60000 cm2

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    Range of particle size and units

    Pharmaceutical system usually are confined to anarrower size range

    Most pharmaceutical systems lie in the range 1mm to 10 mm

    Colloidal range is considered less than 1 mm 1 mm forms useful boundary since the properties

    of colloidal materials are often very different tothose of coarser systems, and the techniquesused to study them are quite distinct from thoseused for larger particulates

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    Individual particle characteristics

    The way that we characterise the particles largely

    depends on the technique used to measurethem.

    The way that we measure a particle size is as

    important as the value of the measured size. Forexample, how would you quantify yourself ifmeasured by

    1) Circumference around your waist?

    2) Diameter of a sphere of the same displacement

    volume as your body? 3) Length of your longest chord (height)?

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    As you can deduce, the measured values have different

    meanings and wil l be important relative to those meanings. I f

    you are sizing a li fe jacket belt you would be interested in the

    f irst size (circumference around your waist). I f you are

    buying a sleeping bag I suggest the last one (length of your

    longest chord) .We have already been using a length to describeparticle size, with the intention that it indicatesthe distance from one side of the particle to itsopposite side.The description is unambiguous in the case of aspherical particle, example: emulsion droplet or

    microsphere.

    Measures of Particle size

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    The ideal particle and reality

    Sol id Sphere

    One dimension (radius) describessize, shape, surface area, volume

    Sol id Geometr ical Part ic les

    Two-three dimensions required todescribe size, shape, surface area,

    volume

    r

    r

    hh

    h

    wl r

    Solid Irregu lar Partic lesSize and shape can only be

    approximated, surface area and

    volume can be measured

    Porou s Irregular Part ic lesSize, shape, surface area and

    volume can only be approximated

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    Particle sizing of powders

    1 cm

    1 cm

    1 cm

    Large, geometric objects:Size is described in three

    dimensions (minimum)

    Small, irregular particles:Three dimensional size

    description is impractical,

    only one dimension

    (average diameter) is used.

    1 m

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    What is the diameter of this particle?

    1

    23

    4

    What should we do if the particle is irregular?

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    Measures of Particle size

    The problem can be solved by quoting theparticle size of a non-spherical particle asthe diameter of a sphere which is in some

    way equivalent to the particle; such asphere is termed an equivalent sphereand the diameter is an equivalentdiameter.

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    Measures of Particle size Example:

    Weigh a particle

    measure its density

    Find the particle volume

    The volume equivalent sphere is the spherewhich has the same volume as the irregularparticle, and is characterised by the volumeequivalent diameter.

    Mass= 1gDensity=2 g/cm3

    Volume= 0.5 cm3

    V=(4/3)r3

    0.5= (4/3) 3.14r3

    R3= (0.5/4.19)=0.119r=0.49 cmDiameter = 0.98 cm

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    r

    h

    r

    h

    r

    h

    Size of cylinder Aspect

    ratio

    Equivalent

    spherical

    diameter

    (m)

    Height

    (m)

    Diameter

    (m)

    20 20 1:1 22.9

    40 20 2:1 28.8

    100 20 5:1 39.1

    For cylinder:

    Radius= 10 m, h= 100 m

    Volume of cylinder

    Volume of cylinder = 3.14 (10)2x100

    Volume of cylinder = 3.14 x 10000

    Volume of sphere =

    Volume of sphere =(4/3) 3.14 x r3

    In equivalent assumption both volume

    should be the same

    (4/3) x 3.14 x r3 =3.14 x 10000

    4r3 = 3x10000

    r3= 30000/4

    r3= 7500 r=19.5 diameter= 2 x r

    diameter = 39.1 m

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    Selected ESDs

    da (the projected area diameter): the diameterof a sphere having the same projected area asthe particle in question

    dv (the volume diameter) the diameter of a

    sphere having the same volume as the particle ds (the surface diameter) the diameter of a

    sphere having the same surface area as theparticle

    dst (the stokes diameter) the diameter of a

    sphere having the same density and free-fallvelocity in given fluid as the particle

    dsieve (the sieve diameter) the diameter of asphere that is just able to pass through thesame square aperture as the particle

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    Illustrations of equivalent diameters

    dp da dv dsa dmass ds

    xm/s2dst

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    Selected EDSs (continued)

    dF (Ferets diameter) the (mean) value betweenpairs of parallel tangents to the projected outlineof the particle

    dM (Martins diameter) the (mean) chord lengthof the projected outline of the particle

    dd (aerodynamic diameter) the diameter of asphere with the same viscous drag as a particlein a fluid at the same viscosity

    dM1

    dF1

    dM2

    dF2

    dM3

    dF3

    * Ferets and Martins diameters are

    taken from a statistical mean of

    diameters measured from different

    particle orientations.

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    There are many different ways of defining equivalent

    diameters. All of these diameters will generally be

    different-unless the particle really is a sphere:

    Projected area diameter da Projected perimeter diameter dp

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    ESDs for a simple shape

    Bear in mind that all equivalent diameters available to us will be differentfor a given irregular particle.

    Select an equivalent diameter (and associated measurement technique)which is relevant to the property of the particle that we are interested in.

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    To obtain a good description of the particle system, we must selectan equivalent diameter (and associated measurement technique)

    which is relevant to the property of the particle in which we are

    interested.

    e.g. Paint pigment particles: Projected area diameter

    measured by microscopy.

    Aerosol deposition in the lungs: Aerodynamic diameter

    measured by inertial impaction methods.

    Sedimentation properties of the material: Stokesdiameter

    Which equivalent diameter do you

    use?

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    Arithmetic mean

    The mean value is the center of gravity of thedistribution. It is calculated using thefollowing equation:

    1

    21 2 3 4 5 6 7 8 9 10 11

    6 6 6 6 6 6 6 6 6 6 6

    Calculate the arithmetic mean for the particle populations 1 & 2.

    Arithmetic Mean (d = ESD)

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    Arithmetic Mean (d = ESD)

    Number-length mean diameter which is

    arithmetic mean of a number distribution

    of length; D [1, 0]

    1 m 3 m 5 m 8 m 10 m

    Calculate the arithmetic mean for the above particle populations.

    3x1 + 1x3 + 5x5 + 2x8 + 2x10 = 67Dav = [67/13] = 5.15 m

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    Assume a simple situation of 10particles having the following length

    (i.e., ESDs) in m :

    1, 3, 3, 4, 5, 2, 2, 6.5, 6, 5

    What are the arithmetic and geometric means?

    Arithmetic

    mean

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    Geometric mean

    Thegeometric mean is calculated using thefollowing equation:

    Calculate the geometric mean for the particle populations 1 & 2.

    1

    21 2 3 4 5 6 7 8 9 10 11

    6 6 6 6 6 6 6 6 6 6 6

    Geometric Mean (d =ESD)

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    Geometric Mean (d =ESD)

    1 um 3 um 5 um 8 um 10 um

    Calculate the geometric mean for the particle populations 1 & 2.

    log dg = 1/12 x [3xlog1 + 1xlog3 + 4xlog5 + 2xlog8 + 2xlog10]log dg = 1/12 x [0 + 0.48 +2.80 + 1.81 + 2 ]log dg = 0.59

    dg = 3.89 m

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    Geometric mean

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    Number Surface area mean diameter

    D [2, 0]

    Thesurface mean diameter (SMD) isthe calculated using the followingequation:

    Calculate the SMD for the particle populations 1 & 2.

    SMD = n1d12 + n2d22 + n3d32 + = nd

    2

    n n

    where n1, n2, = number of particles in size

    groups d1, d2 , and n is the total number

    of particles (i.e., n1 + n2 + )

    N b V l /M di

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    Number-Volume/Mass mean diameter

    D [3, 0]

    The volume-number mean diameter is the diameter of a particle having

    average weight (i.e. weight = volume density)

    therefore, dnv is uniquely related to Nw, the specific particle number

    VMD =n1d13 + n2d23 + n3d33 +

    =nd3

    n n

    where n1, n2, = number of particles in size

    groups d1, d2 , and n is the total number of

    particles (i.e., n1 + n2 + )

    3 3

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    Volume-surface mean diameter; D [3, 2]

    Surface area moment mean (Sauter mean diameter)

    The volume surface mean diameter(VSMD) is calculated using the followingequation:

    Calculate the VMD for the particle populations 1 & 2.

    VSMD =n1d13 + n2d23 + n3d33 +

    =nd3

    where n1, n2, = number of particles in size

    groups d1, d2

    n1d12 + n2d22 + n3d32 + nd2

    It is defined as the diameter of a sphere that has the samevolume/surface area ratio as a particle of interest

    Typical statistics (d= ESD)

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    Typical statistics (d= ESD)

    d=(0.5 + 1)/2 = 0.75 m

    nd = 2 x 0.75 = 1.5

    nd2 = 2 x (0.75)2 = 1.13

    nd3

    = 2 x (0.75)3

    = 0.85

    dnl=265.5/118 = 2.25 m D[1, 0]

    dns =(640.89/118)1/2 = 2.33 m D[2, 0]

    dnv = (1645.25/118)1/3 = 2.41 m D[3, 0

    dvs = 1645.25/640.89 = 2.57 m D[3, 2]

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    Particle size distribution

    A particle population which consists of spheres or equivalent

    spheres with uniform dimensions is monosized and its

    characteristics can be described by a single diameter or equivalent

    diameter.

    Unusual for the particles to be completely monosized in a batch:

    most powders contain particles with a large number of different

    equivalent diameters.

    What do we do to compare the characteristics of two or more

    powders consisting of particles with many different diameters?

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    Particle size distribution

    No. ofparticles

    Particlesize (m)

    No. ofparticles

    Particle size(m)

    50

    50

    Mean

    5

    15

    10

    10

    10

    10

    mean

    5

    10

    15

    10

    1

    2

    1 2 3 4 5 6 7 8 9 10 11

    6 6 6 6 6 6 6 6 6 6 6

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    Particle size distribution

    We would not only want to know aboutthe characteristics of the average'particle, but have some idea of the

    variation between the particles. Divide the data into size classes

    Draw a histogram of the number of particles ineach size class.

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    Particle size distributionsFrequency Distribution Data

    ESD(m)

    Number ofparticles

    (frequency)

    Per centparticles

    (% frequency)

    0-1 0 0

    1-2 4 0.92-3 25 5.4

    3-4 50 10.7

    4-5 86 18.5

    5-6 93 20.0

    6-7 88 18.9

    7-8 67 14.4

    8-9 39 8.4

    9-10 14 3.0

    0

    4

    25

    50

    86

    93

    88

    67

    39

    14

    0-1

    1-2

    2-3

    3-4

    4-5

    5-6

    6-7

    7-8

    8-9

    9-10 Frequency histogram

    466

    F(%) = (4/466) x100 = 0.9%

    S h hi t

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    Such a histogram:

    - reflect the distribution of particle sizes.

    - presents an interpretation of the particle size distribution.

    - enables the percentage of particles having equivalent.

    diameter to be determined.- allows different particle size distribution to be compared.

    Normal: symmetrical about mean (+) skewed Bimodal

    Commonly encountered distributions

    % per mm

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    Particle size [mm]

    % per mm

    % per mm

    Particle size [mm]

    Distributions may have apointed or rounded shape,

    this is quantified as the kurtosis of the distribution.

    A distribution which ispointedis termed leptokurtic.

    A distribution which isflattenedis termedplatykurtic.

    l b

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    Particlesize[mm]

    Numberofparticles

    In band

    Percentagein range

    d

    Percentageunder size

    Percentageover size

    1-2 4 0.86 99.14

    2-3 25 5.36 93.78

    3-4 50 10.73 16.95 83.05

    4-5 86 18.45 35.40 64.6

    5-6 93 19.96 55.36 44.646-7 88 18.89 74.24 25.76

    7-8 67 14.38 88.62 11.38

    8-9 39 8.37 96.99 3.01

    9-10 14 3.00 100 0

    %in range= (4/466)*100= %undersize=(0.86+5.36)=6.220.86

    0.86

    6.22

    Total particles= 466

    Less than 2 m

    Larger than 2 m

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    The graph shows, at any

    size, what fraction of the

    particles are smaller than

    that size, and so is termed

    apercentage undersize graph.

    The two curves are

    mirror images aroun

    a horizontal axis.The graphs shows, at any

    size, what fraction of theparticles are larger than

    that size, and so termed

    apercentage oversize graph.

    Typical statistics (d = ESD)

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    Typical statistics (d = ESD)

    %n=(2/118)x100= 1.69

    Cumulative undersize = 1.69+8.47=10.69=10.69+18.64=28.80

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    Particle

    size

    (m)number of

    particles

    10 1

    20 2

    30 3

    40 450 3

    60 2

    70 1

    Plot Cumulative % undersize and oversize (number and massdistributions) against particle size. Determine the median ofeach distribution.

    Question?

    T th d f l tti di t ib ti

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    Two methods of plotting distributions:

    Incremental & cumulative

    0

    25

    50

    75

    100

    1-2 2-3 3-4 4-5 5-6 6-7 7-8 8-9 9-10

    No. of particles

    in band

    Particle size [micrometers]

    0

    25

    50

    75

    100

    0 1 2 3 4 5 6 7 8 9 10

    Cumulative % undersize

    Cumulative % oversize

    Micrometers

    The histogram is termed

    an incrementaldistribution

    because it shows how many

    particles fall within a given

    size increment.

    A cumulat ivedistribution

    shows how much material

    lies above or below a

    particular size.

    Cumulative(%)

    Incremental? C m lati e?

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    Incremental? Cumulative?

    Which to use?

    Both are widely used, since various particle sizeanalysis methods lead to one or the other.

    Examples:

    Sieving: sorts out the material which issufficiently small to fall through one sieve, but toolarge to fall through a finer one, and so sorts theparticles into increments. Plotting this dataleads to an incremental distribution.

    Sedimentation: where all the material largerthan a certain size has sedimented at a particulartime, naturally leads to a cumulativedistribution.

    Representing the size distribution:

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    Representing the size distribution:

    Number, Area & Mass distributions

    It is important to realise that, for aparticular sample of material, the curvesdescribing the distribution of particle

    number, area, and mass will not beidentical in SHAPE.

    One million 1 micrometer sphericalparticles will occupy the same volume as

    one 100 micrometer (the number/volumerelationship)

    V= 4/3r3

    30

    (1/10)x100 = 10%

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    0

    10

    20

    1 2 3 4 5 6 7 8 9 10

    Particle s ize [micrometer]

    %

    Number distribution

    Area distribution

    Volume distribution

    It is evident from this example that we need to specify which type of

    distribution we are using.

    The particular type of distribution obtained depends on thesizing method used.

    - Sievingandsedimentation: provide the mass of material in a

    given size band.

    - Coulter counter: measure the number of particles in a given

    band.

    2 m

    (1/10)x100 = 10%

    Area = [(2)2/385]x100=1%

    Total surface area for 10particles

    Number of Particle size Surface Mass dist.

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    Number ofparticles

    Particle size(mm)

    Surfacearea (mm2)

    Mass dist.(mm3)

    1

    11

    1

    1

    11

    1

    1

    1

    1

    23

    4

    5

    67

    8

    9

    10

    1

    49

    16

    25

    3649

    64

    81

    100

    ?

    ?27

    ?

    ?

    ??

    512

    ?

    ?

    53

    Total 10 particlesF(%) = (no. particles/total)x 100F (%) = (1/10)x 100 = 10%

    Total surface area is 385F(%) = (surface area of 1st Particle/total)x 100F (%) = (1/385)x 100 = 0.26%

    Total 10 particlesF(%) = (no. particles/total)x 100

    F (%) = (1/10)x 100 = 10%

    Total surface area is 385F(%) = (surface area of 1st Particle/total)x 100

    F (%) = (100/385)x 100 = 26%

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    Difference between number distribution and mass

    distribution

    Dr Ali Nokhodchi 54

    % by number %by massSize (cm) Number of

    objects

    10-1000 7000 0.2 99.961-10 17500 0.5 0.03

    0.1-1 3500000 99.3 0.01

    Total 3524500 100 100

    Number mean diameter =1.6 cm

    Mass mean diameter = 500 cm

    So, which one is correct or important?

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    Characterization of particle size

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    Characterization of particle size

    distributions

    Histograms contain a great amount of

    data, which may be summarized by

    statistics to yield a measure of:

    Central tendency Dispersion

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    Measures of central tendency

    Central tendency = the tendency of the particle sizeto cluster around a particular value. Such values areevident as a peak in the particle size distribution.These values are normally known as averages ormeans of set of data.

    Three different quantities are in common use:

    1. Mode

    2. Median

    3. Mean

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    Median

    The median value is the size which splits thedistribution into two halves, with 50% of the mass orparticle number larger, and 50% of the mass or particlenumber smaller. It is always given the symbol D50.

    The easiest way to find the D50 is to construct a

    cumulative graph, from which the 50% point can beread off directly.

    0

    25

    50

    75

    100

    0 5 10 15 20 25 30 35 40 45 50 55

    Cumulative

    (%)

    Particle size (um)

    0

    25

    50

    75

    100

    0 20 40 60

    16 um

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    Median

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    Mode

    The value of the peak of the distribution ( Themode of the distribution is the most commonvalue occurring in distribution). If the distributionhas two or more peaks, it is said to be bimodal

    or multimodal.

    0

    1

    2

    3

    4

    5

    6

    7

    0 10 20 30 40 50 60

    Particle size

    Percentage/micron

    Mode

    Unimodal distribution

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    Number of

    Particles

    particle size

    (um) Frequency

    (%)

    Cumulative

    under size(%)

    Mean

    diameter

    3 50

    5 100

    10 150

    20 200

    25 250

    20 300

    10 350

    5 400

    2 450

    1. Arithmetic mean?

    2. Determine mode and median?

    3. Plot Cumulative undersize against particle size?

    4. Plot Frequency against particle size?

    Span = D -D /D

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    Span = D90% -D10%/D50%

    Span for A= (340-20)/100Span A= 3.2

    Span for B= (340-30)/150Span B = 2.1

    2

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    Model Distributions

    Particle size distributions may take many forms,but there are small number of model distributionswhich are of particular interest.

    may allow us to infer something about the

    material or the processes through which it haspassed

    Normal distribution

    lognormal distribution

    0 2CumulativeIncremental

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    0

    184%

    50%

    16%

    3 5 7

    Mean - Mean Mean +

    Normal distribution with X=5 and s = 2.

    0

    0.2

    The standard deviation is the difference between

    the 16% and 50%, or the 50% and 84% points.

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    Positively skewed

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    Positively skewed

    distribution

    Normal

    a: lognormal distribution with

    Mode =5 and =2.

    lognormal distribution of fig. a. plotted on a

    logarithmic x axis.

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    The lognormal distribution

    Examples:

    Particles reduced by grinding follow lognormal

    distribution.-Emulsion made by valve homogenizer

    Particles grown by crystallisation often show alognormal distribution of size.

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    Normal and lognormal distributions on linear probability

    paper.

    Normal and lognormal distributions on log- probability

    paper.

    Number Cumulative

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    Number

    of Particle %frequency particle size

    Cumulative

    (%)

    3 3 50 3

    5 5 100 8

    10 10 150 18

    20 20 200 38

    25 25 250 63

    20 20 300 83

    10 10 350 93

    5 5 400 97

    2 2 450 100

    Total 100 100

    Question? Determine the type of distribution.

    99.99

    Probability graph

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    Particle size diameter (um)

    99.9

    99.8

    99

    98

    95

    90

    80

    70

    60

    50

    4030

    20

    10

    5

    2

    1

    0.5

    0.2

    0.1

    0.05

    0.01

    Cumulative

    (%)

    100 200 300 400 500 600 700 800 900 1000 1100

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    Particle size diameter (um)

    10 20 30 40 50 60 70 80 90 200 300 400 500 600 800 1000

    100 700 900

    99.99

    99.9

    99.8

    9998

    95

    90

    80

    70

    60

    5040

    30

    20

    10

    5

    2

    1

    0.5

    0.2

    0.1

    0.05

    0.01

    Cumulative

    (%)

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    Techniques

    Technique ESD Sizerange

    Wet /dry

    Manual /automatic

    Speed

    Sieving ds > 45

    m

    Dry /

    wet

    Manual Slow

    Microscopy dp > 1nm

    Dry /wet

    Manual Slow

    Sedimentation dst > 0.5

    m

    Wet Manual Medium

    Coulter

    counter

    dv >0.1

    m

    Wet Automatic Fast

    Laser light

    scattering

    dv,

    da

    > 1

    nm

    Wet Automatic Fast

    Dry sieving

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    y g

    The results are expressed in the form of a cumulat ive und ersize

    percentage distr ibu t ion.

    Fill seal agitate weighStacking the sieves in order of ascending aperture size and placing thepowder on the top sieve and agitating, the powder is classified intofractions.A closed pan, a receiver, is placed at the bottom of the stack to collectthe fines and a lid is placed on top to prevent loss of powder.Agitation may be manual or mechanical.

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    What does sieving measure?The sieve equivalent diameter(d

    s) is defined as the size

    of a sphere that will just pass through the aperture of a

    particular sieve. This is a two-dimensional value.

    ds ds

    ds ds

    Types of dry sieves

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    Types of dry sieves

    Punched sieves:

    Usually circular, 1 mm to 10 cm apertures

    Woven sieves:

    Apertures are square, > ~50 m

    This type of sieve was originally specified in terms of themesh number, which is the number of wires to the inchof mesh cloth; e.g. a 120 mesh sieve has 120 wires perinch.

    Etched sieves:

    Circular, finer sieves ( ~5 mm).

    Remember!It i i t t t if th h f th i

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    It is important to specify the shape of the sieve

    mesh, i.e. square-meshed or round-hole.

    Example:A 100 mm sphere will just pass through the hole of 100 mm

    square or round-hole sieve, but an irregular particle may

    pass through one sieve and not the other.

    The part ic le wou ld have dif ferent sieve diameters (ds ) in

    round o r square hole sieves!

    In practice dry sieving is predominant

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    p y g p

    Sieving times:It is recommended that sieving be continued until less than 0.2%

    of material passes a given sieve aperture in any 5-minute interval.

    The material separated in the sieves is measured on a weight basis

    providing a mass (or volume distribution). The results are usually

    presented as a percentage mass against sieve equivalent diameter.

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    Sieving time

    90%

    10 20

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    Wet sieving

    When?

    Fine powder (

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    When to use sieving

    Sieving is a basic technique and is employed wheneverany of the following conditions, or combination ofthem, hold:

    Separates fractions

    Excellent method for powders with agood flowability

    (coarse powders) Excellent method for powders that exhibit a range of

    different densities (causes difficulties for sedimentationtechniques)

    Excellent method for powders that exhibit different

    refractive indices (causes difficulties for light scatteringtechniques)

    Excellent method for water-soluble or conductivepowders (causes difficulties for Coulter countermeasurements).

    Sieving is best avoided when:

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    Sieving is best avoided when:

    Cannot be used when powder is too fine Cannot be used when particles are fragile

    and may break during sieving

    Not an appropriate method for particles in

    the form ofelongated needles Cannot be used when powder adheres to

    the sieve

    Cannot be used when powder forms

    clumps Cannot be used when powder easily

    acquires an electrostatic charge

    Powder must be relatively robust

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    Sieving errors may arise fromFactors influencing the probability that a particle will

    correctly present itself at an aperture include:

    Theparticle size distribution of the powder The number of particles on the sieve (load):A good

    starting point is 50-100g for 100 mm sieves and 200g for200 mm sieves.

    Thephysical properties of the particles (e.g., surface) The method of shaking the sieve The dimension and shape of the particles

    Obtaining a correct size distribution during a sievingoperation also depends on the following variables:

    Durat ionof sieving

    Variation of sieve aperture