roughness coefficient & piping schedule no22.pptx

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    Roughness Coefficient , Equivalent Length &

    Piping Schedule No.

    Joon EeoSchool of Chemical Engineering

    University of Ulsan

    26- NOV -2015

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    Commercial pipes comes in many different materials and many different sizes. The

    internal roughness of a pipe is an important factor when considering the friction

    losses of a fluid moving through the pipe.

    For each pipe material either a single pipe roughness value or a range of roughness

    values is normally provided by the manufacturer. The roughness value, usually

    denoted as e, is used in the calculating the relative roughness of a pipe against the

    size of its diameter

    Absolute Roughness : The roughness of a pipe is normally specified

    in either mm or inches and common values range from .!" mm

    for #$C pipes through to %. mm for rough concrete pipes.

    The relative roughness of a pipe is its roughness divided by itsinternal diameter or e&', and this value is used in the calculation

    of the pipe friction factor, which is then used in the 'arcy()eisbach

    e*uation to calculate the friction loss in a pipe for a flowing fluid.

    Roughness Coefcient

    Roughness Coefcient

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    Roughness Coefcient

    Roughness Coefcient

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    Roughness Coefcient

    Roughness Coefcient

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    Roughness Coefcient

    Roughness Coefcient

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    Factors to affect the head loss in pipe

    - Viscosity to be handled

    - Size of the pipe

    - Resistance through various valves and fittings- Roughness of the internal surface of the pipe

    - Changes in elevation

    - Length of travel of the fluid

    Friction Loss

    Friction Loss

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    Darcy Weisbach !uation"his for#ula recognized that pipe friction is dependent on

    condition li$e roughness of pipe internal surface% internal

    dia#eter% internal velocity and viscosity&

    where ' friction loss% ft or # of li!uid ' friction factor

    L ' (ipe length % ft or #D ' (ipe inside dia#eter% ft or #

    V ' )verage pipe velocity in ft*sec or #*sec

    g ' +ravitational constant ,.&/01 ft*2

    ,3&4#*2

    Friction LossFriction Loss

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    , which is 4 times greater than the Fanning Friction actorused with Weisbach equation has now become the standard headloss equation or calculating head loss in pipes where the ow isturbulent

    !nitiall" the #arc"$Weisbach equation was difcult appl", since noelectronic calculators were a%ailable and man"calculations had to be carried out b" hand

    For laminar ow&Re"nolds 'o below ()))* the roughness has no

    e+ect and the riction actor

    Friction Loss #arc" Friction FactorFriction Loss #arc" Friction Factor

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    For laminar ow&Re"nolds 'o below ()))* the roughness has noe+ect and the riction actor

    For turbulent ow&Ra"nolds 'o abo%e 4)))* the riction actor isa+ected b" both the roughness and the Re"nolds 'o and can be

    determined rom an equation de%elopment b" CF Coolbroo-&./0/*

    = -2

    Where R = VD/

    /sec

    Friction Loss #arc" Friction FactorFriction Loss #arc" Friction Factor

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    1ince the Colebroo- equation is nonactorable in &* and thereoredifcult to sol%e, its solution is presented graphicall" on chart

    de%eloped b" CF 2ood"

    Friction Loss 2ood" ChartFriction Loss 2ood" Chart

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    +CA- obtaining complete test data on the pressure drop of every

    available size and type of valve and pipe fitting is impossible,

    a practical method for e/tending available information is useful.

    This techni*ue, 0nown as the e*uivalent(length method for calculating

    pressure losses, applies only to single phase, non(compressible, non(flashing li*uids.

    3qui%alent Length3qui%alent Length

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    3qui%alent Length3qui%alent Length

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    3qui%alent Length3qui%alent Length

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    1crewed ttings

    Flanged ttings

    3qui%alent Length3qui%alent Length

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    A pipe run consists of %1 ft of 2 inch diameter straight pipe,

    %(34 elbows, 5(wide open gate valves and !( wide open glove valve.

    )hat total e*uivalent length of straight pipe is used to calculate head

    loss6

    olution :

    From the table

    - traight pipe %1 ft- %(34 elbows : % 7 !! ft 8 %% ft

    -5(wide open gate valves : 5 7 5." 8 ". ft

    - !( wide open glove valve : !!" ft

    Total e*uivalent length : %1 9 %%9 " 9 !!" 8 !3 ft

    3qui%alent Length 35ample3qui%alent Length 35ample

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    1chedule 'o1chedule 'o

    For all pipe sizes the outside diameter ;.'.< remains relativelyconstant. The variations in wall thic0ness affects only the inside

    diameter =.'.

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    1chedule 'o1chedule 'o

    )elded and eamless )rought teel #ipe

    To distinguish different weights of pipe, it is common to use the chedule terminology

    from

    A>=&A? +%@.! )elded and eamless )rought teel #ipe ,

    ight wall : CB !, 5,%,2

    tandard )eighttd, T', T< : CB @/tra strong/tra Beavy, B, B, < : CB D,!,!5,!2

    'ouble /tra trong'ouble /tra Beavy, B,