CHE 454A
Unit Operations Involving Particulate Solids for
                 Chemical Engineers
Dr. Raju Kumar Gupta,
Associate Professor,
Department of Chemical Engineering,
Indian Institute of Technology Kanpur,
Kanpur 208016, India
                         Cletus                    (                Lecture l             -
                                                                                              2)
                                                   -
    unit       process
    unit       operation
-
*
        upstream process :
        -
        unit operation :
                         crushing                           ,       grinding              ,
                                     washing                        filtration                drying
        -
                                                    ,                                 ,
                                      mining       ,
                                                                    etc   .
*        Reaction    :
                         chemical                  Mxn                   takes        place
                                         material
        -
                            raw                             →
                                                                              products
        Downstream
                            processes
*
                                               :
        unit    operation   :       Distillation                ,
                                                                     evaporation              ,
                                    extraction
                                                        ,           settling      ,   centrifugation
                                     etc   .
    United                  :
                                     physical               /       or        mechanical
                                     procedure                       occurring
                         individually                   or           parallel to chemical
                            Mxn      .
          physical       steps            of preparing                           reactants
    -
           separating           a
                                         purifying                   products
    -
           Recycling            unconverted reactants
                                                                                      into
-
          controlling               energy          transfer                                       or
          out      of       the      reactor
mechanism                                                       .
     purely                 based        on
                                                physical       or
     mechanical                        forces      such       as
    *         Gravitational                   force
    *         centrifugal                     face
    *     mechanical & kinetic                               forces
          arising from flow
*        Final              property          of    product depend
         on         unit
                                      operation    used
⑨        solid
         -
                    -
                            solid        operations   :
         crushing                 ,     gain ding     ,     sieving   ,
        compaction                ,
                                        cutting ,         storage     4
        transport of                       bulk       solids        etc   .
⑤       solid   -
                        fluid operations :
        -
    Filtration          ,
                                sedimentation ,           centrifugation      ,
    floatation              .
                                 cyclone separators
                                                  61 Dp
 sphericity               :
                                                                                      ④
                                            -
                                  4S
                                                                      -
                                       =
                                                  setup
 -
   Dp   -
                 nominal               alia   .
                                                        of        particle
   SP
                     surface                                               battle
         -
                                      area
                                                    of       one
   Up                volume             of                    particle
         -
                                                   one
 For    a
                 sample                of          uniform                     particles of    dis   .
                                                                                                         Dp
                                                                                                          ,
                          FT                            m
                                                                  total
                                                                                           of sample
                                                             -
   µ up              =                                                              mass
                                                        Pp   -
                                                                      density of particle
Total   surface               area
                                            of          particle           ,
                 A   =    N
                                  Sp
                                                              M                      6 up
                                  Msp
                 A
                                                                                .
                                                             -
                                                                                    -
                     =                             =
                                                                 Ep
                          -
                                                                      Up            Dp %
                              Ep up
             a-⇐gseT④*
                                  6   m
specific surface                        area
                                                         of       mixture
( total surface                                              per       mass
                                                                                      of particles)
                                           area
                                       62 ,                                                        6am
 Ass        =
                     Aw       =
                                                         +
                                                                 GRI
                                                                                     t
                                      Ep
                                                                                               +
                                                                  -4g
                                                                                           -
                                                    ,              Cp Dps & GDI
        ki       -
                     mass         faction           in       a
                                                                      given          increment
        n    -       no
                          of          increment
                Dpi   -
                          Average            particle    dia
                                                               ,
                                                                    taken   as
                          arithmetic                                 smallest
                                              average        of
                          &
                                   largest      particle diameters          in
                          increment
                :/ I
             opening
           mesh      Average particle
                          screen
           D#¥m
                Y                 4699                       4.699
÷: :                          ::                         :::¥o                   .
    8+10    I   O
                              l 65
                              -
                                     I   }              2.007
           -
           E¥i:÷                                   .
                                                         dig
            Volume
            -
             mean
                  ,           surface
                    DTs   =
                                  qA÷p=E¥
                                                        it         Bpi
                                                                             ]
Problem      1   :
                          Pp    =          O    '
                                                        00265
                                                                   81mm
-
                          As    =
                                            O
                                                    '
                                                        571
For    the       material                  b/w           4   -
                                                                 mesh   of       200   mesh
in
       particle          size               calculate specific surface
                                   ,
                          -
            in
area                 mm
                              1g       .
                                            h
                     6
                                                          ki
 Ass    -
                                           E
             E
        -
                                           El            Dpi
                           Particle
      Understanding of Particle SizeSize Distribution
                                       and
               Particle Shape
Particle Size
  Particle size or grain size refers to the diameter of a grain of
                         granular material
                                   Particle
❑ The size of a spherical homogeneous particleSize Distribution
                                                is uniquely
defined by its diameter.
   ❑ For regular, compact particles such as cubes or regular
     tetrahedra, a single dimension can be used to define size.
   ❑ With some regular particles it may be necessary to specify
     more than one dimension: For a cone the base diameter
     and height are required whilst for a cuboid three
     dimensions are needed.
❑ For irregular particles, it is desirable toParticle Size
                                              quote the     Distribution
                                                         size of a
particle in terms of a single quantity, and the expression most
often used is the "equivalent diameter".
    ❑ The assigned equivalent diameter usually depends on the
      method of measurement.
    ❑ Several equivalent diameters are commonly encountered.
      For example, the Stokes' diameter is measured by
      sedimentation and elutriation techniques; the projected
      area diameter is measured microscopically and the sieve-
      aperture diameter is measured by means of sieving.
Influences of Particle Size                            Particle Size Distribution
❑ Particle size influences dissolution
           Small particles dissolve more rapidly than large ones, which is important
in various manufacturing processes.
❑ Particle size influences flow properties of powders
          The flow properties of powders are strongly dependent on particle size
and, in particular, particle shape. Since most powders are moved from one place to
another by flowing, control of flow behavior is highly important. Generally, coarse,
roughly spherical particles flow much more easily than small or elongated particles.
❑ Particle size influences stability of dispersions
          The stability of dispersions, such as suspensions and emulsions,
depends on the size of the dispersed material. The forces between colloidal
particles depend on their dimensions, and the settling.
                                         Particle Size Distribution
Effect of Particle Shape
❑ Particle shape influences such properties as:
    ➢ Flowability of powders
    ➢ Packing
    ➢ Interaction with fluids
❑ The variation between the diameters increases as the particles
diverge more from the spherical shape.
❑ Different results from different techniques can be compared by
applying shape factors and shape coefficients.
                                            Particle Size Distribution
Particle Size Distribution
❑ The particle size distribution (PSD) may be defined as
 “Particle size distribution (PSD) of a powder, or granular material,
or particles dispersed in fluid, is a list of values or a mathematical
function that defines the relative amounts of particles present,
sorted according to size.”
                                 Particle Size Distribution
Significance of Particle Size Distribution (PSD)
❑ The PSD of a material can be important in understanding its
physical and chemical properties.
❑ It affects the strength and load-bearing properties of rocks and
soils.
❑ It affects the reactivity of solids participating in chemical
reactions, and needs to be tightly controlled in many industrial
products such as the manufacture of printer toner and cosmetics.
                                          Particle Size Distribution
Sieve Analysis
❑ Sieve analysis is one of the oldest methods of size analysis.
❑ Sieve analysis is accomplished by passing a known weight of
sample material successively through finer sieves and weighing
the amount collected on each sieve to determine the percentage
weight in each size fraction.
❑ Sieving is carried out with wet or dry materials and the sieves
are usually agitated to expose all the particles to the openings.
                                         Particle Size Distribution
Process of Sieving
❑ The process of sieving may be divided into two stages.
❑ First, the elimination of particles considerably smaller than the
screen apertures, which should occur rapidly and, second, the
separation of the so-called "near-size" particles, which is a
gradual process rarely reaching final completion.
❑ The effectiveness of a sieving test depends on the amount of
material put on the sieve (the "charge") and the type of movement
imparted to the sieve.
                                            Particle Size Distribution
❑ The woven sieve is the oldest design, and it is normally made
by weaving fine metal wire into a square pattern, then soldering
the edges securely into a flattish cylindrical Container.
❑ Woven-wire sieves were originally designated by a mesh
number (the number of wires per inch or the number of square
apertures per square inch)
16 Mesh   6 Mesh   3 Mesh
 Screen Analysis & Standard Screen Series
 ❑ Testing sieves are made of woven wire screens, the mesh and
 dimensions of which are carefully standardized. The openings are
 square. Each screen is identified in meshes per inch.
 ❑ The actual openings are smaller than those corresponding to mesh
 numbers because of thickness of the wires.
Tyler standard screen scale
Tyler standard screen scale
  Typical Screen Analysis
The notation 14/20 means ‘through 14 mesh and on 20 mesh’
Dpi means the particle diameter equal to the mesh opening of screen i
Screening equipment
                                                            Gyrations at one end,
Gyrations in horizontal plane Gyrations in vertical plane
                                                            shaking at other
             Shaking                Mechanically vibrated     Electrically vibrated