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TK3201 Transport Phenomena I Dewa Gede Arsa Putrawan Chemical Engineering ITB Shell Momentum & Velocity Distribution in Laminar Flow8-Jan-13 TK3201 DGA/1 Outcomes Students are able to derive microscopic balances for simple problems on momentum transfer. Students are able to estimate flux and velocity profiles from microscopic balances. Students are understand the application of transport phenomena in viscosity measurement. 8-Jan-13 TK3201 DGA/2

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  • TK3201

    Transport Phenomena

    I Dewa Gede Arsa Putrawan

    Chemical Engineering ITB

    Shell Momentum & Velocity Distribution

    in Laminar Flow

    8-Jan-13 TK3201 DGA/1

    Outcomes

    Students are able to derive microscopic balances for simple

    problems on momentum transfer.

    Students are able to estimate flux and velocity profiles from

    microscopic balances.

    Students are understand the application of transport

    phenomena in viscosity measurement.

    8-Jan-13 TK3201

    DGA/2

  • Momentum Flux: diffusive

    (x-component)

    xx

    yx zx

    y

    xx yx zxy z x z x y

    x

    y z

    8-Jan-13 TK3201

    DGA/3

    z

    Momentum Flux: convective

    (x-component)

    x

    y

    z

    v

    volumetric flow rate v

    v

    x

    y z

    v x z

    x y

    x

    y

    z

    ( v )( )

    ( v )( )

    ( v )( )

    x

    x

    x

    y z v

    x z v

    x y v

    Qx

    Qy Qz

    xy

    8-Jan-13 TK3201

    DGA/4

  • Momentum Balance

    = +

    +

    +

    8-Jan-13 TK3201

    DGA/5

    Forces

    Forces acting on fluid

    Generation (same direction to fluid flow)

    Consumption (opposite direction to fluid flow)

    Gravity

    F = m g

    Pressure

    F = P A

    8-Jan-13 TK3201

    DGA/6

  • Methodology

    Problem analysis

    Microscopic balances

    Newtons law

    Boundary conditions

    Profiles of transfer flux, transfer rate, and other variables

    Values of average, maximum, etc.

    8-Jan-13 TK3201

    DGA/7

    Boundary Conditions

    No slip at solid-fluid interfaces

    Continuity on flux and velocity at a liquid-

    liquid interfacial plane

    Zero flux at a liquid-gas interfacial plane

    8-Jan-13 TK3201

    DGA/8

  • Flow of a falling film

    8-Jan-13 TK3201

    DGA/9

    Flow Through A Circular Tube

    8-Jan-13 TK3201

    DGA/10

  • Average Velocity

    dr

    d

    d r

    r d dA = r dr d

    2

    0 0 0 0 0

    2

    0 0 0 0 0

    V L A R

    z z z

    z V L A R

    v dV v dzdA v rdrd

    v

    dV dzdA rdrd

    8-Jan-13 TK3201

    DGA/11

    Cannon-Fenske Viscometer

    From analysis of flow in a circular tube

    attVL

    hRg

    QL

    hRg

    L

    RhgQ

    8

    88

    )(

    4

    44

    Taking into account kinetic energy

    = at + b/t (note: b/t at)

    8-Jan-13 TK3201

    DGA/12

  • Cone-Plate Viscometer

    Shear rate:

    dvx/dy = / sin , sin = c / r (by manufacturer) Shear stress:

    yx = Tp / [(2/3) r3]

    8-Jan-13 TK3201

    DGA/13

    Homework II

    1. Problem 2B.3

    2. Problem 2B.11

    3. Problem 2C.7

    R. B. Bird et al, Transport phenomena, John

    Willey & Sons, 2002.

    8-Jan-13 TK3201

    DGA/14