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Week # 2 MR Chapter 2 Tutorial #2 MR # 2.1, 2.4, 2.8. To be discussed on Jan. 27, 2021. By either volunteer or class list. MARTIN RHODES (2008) Introduction to Particle Technology , 2nd Edition. Publisher John Wiley & Son, Chichester, West Sussex, England.

Week # 2 MR Chapter 2• Tutorial #2 • MR # 2.1, 2.4, 2.8. • To be discussed on Jan. 27, 2021. • By either volunteer or class list. MARTIN RHODES (2008) ... England. Motion of

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  • Week # 2

    MR Chapter 2

    • Tutorial #2

    • MR # 2.1, 2.4, 2.8.

    • To be discussed on Jan. 27, 2021.

    • By either volunteer or class list.

    MARTIN RHODES (2008)

    Introduction to Particle

    Technology , 2nd Edition.

    Publisher John Wiley & Son,

    Chichester, West Sussex,

    England.

  • Motion of solid particles in a fluid

    For a sphere

    Stoke’s law

  • Standard drag curve for motion of a sphere in a fluid

  • Reynolds number ranges for single

    particle drag coefficient correlations

    At higher relative velocity, the inertia of fluid begins to dominate.

    Four regions are identified: Stoke’s law, intermediate, newton’s law, boundary layer

    separation.

    Table 2.1 (Schiller and Naumann (1933) : Accuracy around 7%.

  • Single Particle Terminal Velocity

  • Special Cases

    • Newton’s law region:

    1

    2( )1.74

    p f

    T

    f

    x gU

    Intermediate region:

    0.7

    1.1 0.29 0.43, , ,T p f fU x

  • To calculate UT and x

    • (a) To calculate UT, for a given size x,

    • (b) To calculate size x, for a given UT,

    3

    2

    2

    ( )4Re

    3

    f p f

    D

    x gC

    Independent of UT

    3 2

    ( )4

    Re 3

    P fD

    P T f

    gC

    U

    Independent of size x

  • Particles falling under gravity through a fluid

    Method for estimating terminal velocity for a given size of particle and vice versa

  • Non-spherical particles

    Drag coefficient CD versus Reynolds number ReP for particles of sphericity

    ranging from 0.125 to 1.0

  • Effect of boundaries on terminal

    velocity

    Sand particles falling from rest in air (particle density, 2600 kg/m3)

    When a particle is falling through a fluid in the presence of a solid boundary the terminal

    Velocity reached by the particle is less than that for an infinite fluid.

    Following Francis (1933), wall factor ( )/w Df U U

  • Limiting particle size for Stoke’s law in water

  • Limiting particle size for Stoke’s law in air

  • 850

  • • Where the plotted line intersects the standard

    drag curve for a sphere (y = 1), Rep = 130.

    • The diameter can be calculated from:

    Re 130f v T

    P

    x U

    Hence sphere diameter, xv = 619 m.

    • For a cube having the same terminal velocity under the

    same conditions, the same CD vesus Rep relationship

    applies, only the standard drag curve is that for a cube

    (y = 0.806)