1
46 GAS PIPELINE HYDRAULICS Figure 2.3 Moody diagram. Relative roughness e D = 0.000,001 e D = 0.000,005 e D Reynolds number Re = VD n Friction factor f 0.008 10 3 2 3 4 56 8 10 4 2 3 4 56 8 10 5 2 3 4 56 8 10 6 2 3 4 56 8 10 7 2 3 4 56 8 10 8 0.009 0.01 0.015 0.02 0.03 0.04 0.05 0.06 0.07 0.08 0.09 0.10 0.025 0.000,05 0.0001 0.0002 0.0004 0.0006 0.0008 0.001 0.002 0.004 0.006 0.008 0.01 0.015 0.02 0.03 0.04 0.05 0.000,01 ×10 3 ×10 4 ×10 5 ×10 6 Smooth pipes Laminar flow f = 64/Re Laminar Flow Critical Zone Transition Zone Complete turbulence, rough pipes Copyright 2005 by Taylor & Francis Group, LLC

Tabla de Rugosidad

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Tablade Rugosidades

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Page 1: Tabla de Rugosidad

46G

AS

PIP

ELIN

E H

YD

RA

ULIC

SFigure 2.3 Moody diagram.

Rel

ativ

e ro

ughn

ess

e D

= 0.000,001

eD = 0.000,005

eD

Reynolds number Re = VDn

Fric

tion

fact

or f

0.008103 2 3 4 56 8104 2 3 4 56 8105 2 3 4 56 8106 2 3 4 56 8107 2 3 4 56 8108

0.0090.01

0.015

0.02

0.03

0.04

0.05

0.06

0.07

0.08

0.090.10

0.025

0.000,05

0.00010.0002

0.00040.00060.00080.001

0.002

0.004

0.0060.0080.01

0.0150.02

0.03

0.040.05

0.000,01

×103 ×104 ×105 ×106

Smooth pipes

Laminar flow

f = 64/R

e

LaminarFlow

CriticalZone Transition

Zone Complete turbulence, rough pipes

2785_C002.fm

Page 46 F

riday, April 1, 2005 3:23 P

M

Copyright 2005 by T

aylor & Francis G

roup, LL

C