1. An incompressible fluid of kinematic viscosity v= p/p = 10-4 m²/s flows steadily through a circular pipe of diameter d = 10 cm. The pipe flow is fully developed. If the average velocity V is 2 m/s, is the flow laminar or turbulent? What is the value of the friction factor, f? Friction Factor If the pipe is perfectly smooth on its internal surface and V is 20 m/s, the pipe flow is turbulent (double check yourself). Evaluate its friction factor using the Moody chart below. Repeat (c) by numerically solving the Colebrook formula (using, for example, Matlab). Attach the source code you used. Suppose that the pipe internal surface is rough. Also suppose that increasing V up to 200 m/s yields no change in the value of f found in (a). Determine the relative roughness, e/d, using the Colebrook formula. 0.1 0.09 0.08 0.07 0.06 0.05 0.04 0.03 0.02 0.015 0.01 Laminar Flow Material Concrete, coarse Concrete, new smooth Drawn tubing Glass, Plastic Perspex Iron, cast e (mm) 0.25 0.025 0.0025 0.0025 0.15 3.0 Sewers, old Steel, mortar lined 0.1 Steel, rusted 0.5 Steel, structural or forged 0.025 Water mains, old 1.0 10³ 104 Moody Diagram WEEEEEE Transition Region Complete Turbulence Friction Factor=AP. 105 106 Reynolds Number, Re = PVd Smooth Pipe 107 0.05 0.04 0.03 0.02 0.015 0.01 0.005 0.002 0.001 5x10-4 2x10-4 10-4 5x10-5 10-5 5x10-6 10-6 108 Relative Pipe Roughness
1. An incompressible fluid of kinematic viscosity v= p/p = 10-4 m²/s flows steadily through a circular pipe of diameter d = 10 cm. The pipe flow is fully developed. If the average velocity V is 2 m/s, is the flow laminar or turbulent? What is the value of the friction factor, f? Friction Factor If the pipe is perfectly smooth on its internal surface and V is 20 m/s, the pipe flow is turbulent (double check yourself). Evaluate its friction factor using the Moody chart below. Repeat (c) by numerically solving the Colebrook formula (using, for example, Matlab). Attach the source code you used. Suppose that the pipe internal surface is rough. Also suppose that increasing V up to 200 m/s yields no change in the value of f found in (a). Determine the relative roughness, e/d, using the Colebrook formula. 0.1 0.09 0.08 0.07 0.06 0.05 0.04 0.03 0.02 0.015 0.01 Laminar Flow Material Concrete, coarse Concrete, new smooth Drawn tubing Glass, Plastic Perspex Iron, cast e (mm) 0.25 0.025 0.0025 0.0025 0.15 3.0 Sewers, old Steel, mortar lined 0.1 Steel, rusted 0.5 Steel, structural or forged 0.025 Water mains, old 1.0 10³ 104 Moody Diagram WEEEEEE Transition Region Complete Turbulence Friction Factor=AP. 105 106 Reynolds Number, Re = PVd Smooth Pipe 107 0.05 0.04 0.03 0.02 0.015 0.01 0.005 0.002 0.001 5x10-4 2x10-4 10-4 5x10-5 10-5 5x10-6 10-6 108 Relative Pipe Roughness
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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
Transcribed Image Text:### Educational Transcription
#### Problem Statement
1. An incompressible fluid of kinematic viscosity \( \nu = \mu / \rho = 10^{-4} \, \text{m}^2/\text{s} \) flows steadily through a circular pipe of diameter \( d = 10 \, \text{cm} \). The pipe flow is fully developed.
- If the average velocity \( V \) is \( 2 \, \text{m/s} \), is the flow laminar or turbulent? What is the value of the friction factor, \( f \)?
- If the pipe is perfectly smooth on its internal surface and \( V \) is \( 20 \, \text{m/s} \), the pipe flow is turbulent (double check yourself). Evaluate its friction factor using the Moody chart below.
- Repeat (c) by numerically solving the Colebrook formula (using, for example, Matlab). Attach the source code you used.
- Suppose that the pipe internal surface is rough. Also suppose that increasing \( V \) up to \( 200 \, \text{m/s} \) yields no change in the value of \( f \) found in (a). Determine the relative roughness, \( \epsilon/d \), using the Colebrook formula.
#### Moody Diagram
The Moody Diagram provided is a plot of the friction factor versus the Reynolds number \( Re \) for various levels of relative pipe roughness, \( \epsilon/d \).
- **Vertical Axis (Friction Factor):** Ranges from 0.01 to 0.1.
- **Horizontal Axis (Reynolds Number, \( Re \)):** Ranges from \( 10^3 \) to \( 10^8 \).
- **Regions on the Curve:**
- **Laminar Flow Region:** For \( Re < 2000 \), characterized by a linear decrease.
- **Transition Region:** Illustrated by dashed lines indicating instability in flow between laminar and turbulent regimes.
- **Complete Turbulence Region:** For higher \( Re \), where friction factor values stabilize but vary with roughness.
- **Smooth Pipe Curve:** A distinct line which illustrates the behavior of pipes with negligible roughness.
- **Lines Indicating Roughness Values:** Several curves represent different relative roughness values \( \epsilon/d \), from \( 10^{-6} \
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