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Calculate the pressure drop for a straight pipe of length L 40m, the data for this problem is given to you below: Pipe diameter D=0.01m • Flow velocity v=1.20 m/s Pipe absolute roughness €=0.00003 m Pipe length, L= 40m Dynamic viscosity=0.000354 Pa.s (dynamic viscosity of water at 80degC) Fluid density=971.79 kg/m^3 • Pressure at pipe entry, P1=1,535,922 Pa Pipe inclination =0.03 radians, the conversion factor between radians and degrees is 1 rad =57.29° • Assume acceleration of gravity 9.80 8² ● ● ● D=0.01m P1 ΔΡ =? e inclination P2 Flow direction indicated by blue arrow

Calculate the pressure drop for a straight pipe of length L 40m, the data for this problem is given to you below: Pipe diameter D=0.01m • Flow velocity v=1.20 m/s Pipe absolute roughness €=0.00003 m Pipe length, L= 40m Dynamic viscosity=0.000354 Pa.s (dynamic viscosity of water at 80degC) Fluid density=971.79 kg/m^3 • Pressure at pipe entry, P1=1,535,922 Pa Pipe inclination =0.03 radians, the conversion factor between radians and degrees is 1 rad =57.29° • Assume acceleration of gravity 9.80 8² ● ● ● D=0.01m P1 ΔΡ =? e inclination P2 Flow direction indicated by blue arrow

Elements Of Electromagnetics
Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
ChapterMA: Math Assessment
Section: Chapter Questions
Problem 1.1MA
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I have attached the given moody diagram in this question, how do I complete this question accuractely?

2hDg LV² Darcy-Weisbach friction factor f = 0.00 10-¹ 9 8 7 6 5.5 5 45 3.5 3 2.5 2 18 1.6 1.4 12 102 9 8 91 Laminar flow 92 Critical zone Material Riveted steel Concrete D.4 0.0 0.5 Wood stave Cast Iron Galvanized Iron Asphalted cast Iron Commercial steel Drawn tubing Fluid at 20°C Water Air (101.325 kPa) □ ID e (mm) 0.9-9 0.3-3 0.18-0.9 0.25 0.15 0.12 0.046 0.0015 v (m²/s) TTT Transition zone 1.003e-006 1.511e-005 Latitude (WGS84) g(m/s) 0.0 Sea level 9.78033 45.5 Standard 9.80665 90.0" Sea level 9.83219 i 6 78 10 2 3 4 5 6 7 8 10* Moody Diagram 40 80 VD for water at 20°C (V in m/s, D in cm) 10 20 I 40 eo VD for atmospheric air at 20°C 200 GOD 1000 100 Smooth pipes, r-o 1NT-2 log(RF)-0.8) Hagen-Polsseuille equation A ≤ 2300, 1-64/R Colebrook equation, ♬ ≥ 2300 1Nr-2 log(r/3.7 +2.51/(√)) Continuity equation, Q - AV A-D²14, V-4Q/(xD²) 2 3 4 5 6 7 8 10³ Reynolds number R = 400 2 VD V 100 2000 r-5e-006 200 4000 400 Complete turbulence, rough pipes, R3500/r, 1/f-1.14-2 logr eaco + 3 4 5 6 7 8 10⁰ (V in m/s, Din m, v in m/s) r-1e-006 pa IL 10000 1000 2 3 4 5 6 7 8 107 20000 2000 4000 40000 0000 0000 10000 TI 1 DODOO 0.07 0.06 0.05 0.045 0.04 0.035 0.03 0.025 0.02 0.0175 0.015 0.0125 O 0.01 0.008 0.006 0.002 0.0015 0.004 || 0.003 0.001 0.0008 0.0006 0.0004 0.0002 0.0001 WID 5e-005 Relative roughness r= ( in mm, D in mm) 2e-005 1e-005 2 3 4 5 6 7 8 10" Metzger & Willard, Inc. http://www.metzgerwillard.com
Transcribed Image Text:2hDg LV² Darcy-Weisbach friction factor f = 0.00 10-¹ 9 8 7 6 5.5 5 45 3.5 3 2.5 2 18 1.6 1.4 12 102 9 8 91 Laminar flow 92 Critical zone Material Riveted steel Concrete D.4 0.0 0.5 Wood stave Cast Iron Galvanized Iron Asphalted cast Iron Commercial steel Drawn tubing Fluid at 20°C Water Air (101.325 kPa) □ ID e (mm) 0.9-9 0.3-3 0.18-0.9 0.25 0.15 0.12 0.046 0.0015 v (m²/s) TTT Transition zone 1.003e-006 1.511e-005 Latitude (WGS84) g(m/s) 0.0 Sea level 9.78033 45.5 Standard 9.80665 90.0" Sea level 9.83219 i 6 78 10 2 3 4 5 6 7 8 10* Moody Diagram 40 80 VD for water at 20°C (V in m/s, D in cm) 10 20 I 40 eo VD for atmospheric air at 20°C 200 GOD 1000 100 Smooth pipes, r-o 1NT-2 log(RF)-0.8) Hagen-Polsseuille equation A ≤ 2300, 1-64/R Colebrook equation, ♬ ≥ 2300 1Nr-2 log(r/3.7 +2.51/(√)) Continuity equation, Q - AV A-D²14, V-4Q/(xD²) 2 3 4 5 6 7 8 10³ Reynolds number R = 400 2 VD V 100 2000 r-5e-006 200 4000 400 Complete turbulence, rough pipes, R3500/r, 1/f-1.14-2 logr eaco + 3 4 5 6 7 8 10⁰ (V in m/s, Din m, v in m/s) r-1e-006 pa IL 10000 1000 2 3 4 5 6 7 8 107 20000 2000 4000 40000 0000 0000 10000 TI 1 DODOO 0.07 0.06 0.05 0.045 0.04 0.035 0.03 0.025 0.02 0.0175 0.015 0.0125 O 0.01 0.008 0.006 0.002 0.0015 0.004 || 0.003 0.001 0.0008 0.0006 0.0004 0.0002 0.0001 WID 5e-005 Relative roughness r= ( in mm, D in mm) 2e-005 1e-005 2 3 4 5 6 7 8 10" Metzger & Willard, Inc. http://www.metzgerwillard.com
Calculate the pressure drop for a straight pipe of length L 40m, the data for this problem is given to you below: ● Pipe diameter D=0.01m • Flow velocity v=1.20 m/s Pipe absolute roughness €=0.00003 m Pipe length, L= 40m Dynamic viscosity=0.000354 Pa.s (dynamic viscosity of water at 80degC) • Fluid density=971.79 kg/m^3 • Pressure at pipe entry, P1=1,535,922 Pa • Pipe inclination 0 =0.03 radians, the conversion factor between radians and degrees is 1 rad =57.29° • Assume acceleration of gravity 9.80 D=0.01m P1 m ΔΡ =? L 0 inclination P2 Flow direction indicated by blue arrow Z
Transcribed Image Text:Calculate the pressure drop for a straight pipe of length L 40m, the data for this problem is given to you below: ● Pipe diameter D=0.01m • Flow velocity v=1.20 m/s Pipe absolute roughness €=0.00003 m Pipe length, L= 40m Dynamic viscosity=0.000354 Pa.s (dynamic viscosity of water at 80degC) • Fluid density=971.79 kg/m^3 • Pressure at pipe entry, P1=1,535,922 Pa • Pipe inclination 0 =0.03 radians, the conversion factor between radians and degrees is 1 rad =57.29° • Assume acceleration of gravity 9.80 D=0.01m P1 m ΔΡ =? L 0 inclination P2 Flow direction indicated by blue arrow Z
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