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,