1.5 - Limitations of Power Law Profiles
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Understanding Power Law Velocity Profiles
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Today, let's explore the power law velocity profile. Does anyone remember the formula for it?
Isn't it u/u_max = (y/R)^(1/n)?
Great! Now, can anyone tell me what the variable n represents?
I think n depends on the Reynolds number, right?
Exactly! And as the Reynolds number increases, n also increases. Remember, higher n gives a steeper profile. But, unfortunately, there are limitations. What do you think happens at the center of the pipe?
It doesn't give a zero slope there.
Correct! So keep in mind, power law profiles cannot predict wall shear stress either as it leads to infinite velocity gradients at the wall. That's crucial!
Applications of Power Law Profiles
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Let's talk about how we apply these power law profiles in real-world situations. What do we need to consider when using them?
We have to account for the pipe surface texture, whether it's smooth or rough.
Good point! And remember, despite those differences, the velocity profile at any point minus the average remains the same for both types of pipes. Why might that be significant?
It shows that the fundamental behavior of fluid flow doesn't change that much.
Exactly! Lastly, can anyone summarize why we can't use power law profiles to calculate wall shear stress?
Because they give us an infinite velocity gradient at the wall.
Spot on! Let's summarize the key limitations we discussed today.
Deriving Average Velocities from Power Law Profiles
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Now, let’s derive the average velocity from our power law profile. Can anyone remind us how we express the average velocity mathematically?
I think we integrate the velocity profile over the cross-sectional area.
Correct, we use A = πR² for the area and integrate. What’s the expression for the average velocity from u_max?
It's V_bar = 2u_max times the integral of the power law expression.
Exactly! And remember, after integrating and applying boundaries, we find the average velocity. Who remembers the final expression for average velocity using n=7?
That would be V_bar = 0.816u_max.
Perfect! Remember this value, as it can be critical in practical applications.
Introduction & Overview
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Quick Overview
Standard
The limitations of power law profiles in turbulent flow through pipes are highlighted, especially regarding the calculations for wall shear stress and the behavior of velocity gradients. The section explores how both smooth and rough pipes exhibit similar differences between local and average velocities but face challenges in accurately modeling shear conditions.
Detailed
In this section, we explore the limitations of power law profiles for turbulent flow in pipes. The key focus is on how the average velocity divided by the frictional velocity reveals insights into local flow conditions. The difference between any point velocity and the average velocity remains consistent across smooth and rough pipes, which implies similarities in fluid behavior despite the surface texture differences.
Furthermore, the power law velocity profile, expressed as u/u_max = (y/R)^(1/n), lacks the capability to predict zero slope at the pipe center and fails to calculate wall shear stress accurately. This is primarily due to the indication that the velocity gradient approaches infinity at the wall (r = R), highlighting a fundamental limitation in the analytical frameworks used. Moreover, calculations involving the average velocity demonstrate a systematic approach to address these velocity profiles, culminating in a practical example that showcases the method of integrating the power law expression to derive average velocities.
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Introduction to Velocity Profiles
Chapter 1 of 3
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Chapter Content
Now, about the power law velocity profile, a little bit on that. So, the power law velocity profile for smooth pipes can be expressed as, it is, u by u max can be written as y by R to the power 1 by n.
Detailed Explanation
In fluid mechanics, the velocity profile describes how the velocity of fluid varies across a cross-section of the pipe. The power law velocity profile is a specific equation that shows this relationship for smooth pipes, where 'u' is the fluid's velocity, 'u max' is the maximum velocity at the center of the pipe, 'y' is the vertical distance from the centerline, and 'R' is the radius of the pipe. The exponent 'n' indicates how rapidly the velocity changes with distance from the center.
Examples & Analogies
Think of the fluid flowing through a pipe as similar to a group of people walking through a narrow hallway. The people (fluid particles) in the center move faster than those near the edges. The power law represents this difference in speed as it projects how fast someone moves based on their distance from the hallway's center.
Dependence on Reynolds Number
Chapter 2 of 3
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This 1/n depends upon the Reynolds number, putting n is equal to 7 in the above equation gives one-seventh power law velocity profile. This is one of the very famous velocity profiles.
Detailed Explanation
The exponent 'n' in the power law velocity profile is influenced by the flow regime specified by the Reynolds number, which categorizes flow as laminar, transitional, or turbulent. As the Reynolds number increases, the value of 'n' also tends to increase. When 'n' equals 7, it represents a widely recognized velocity distribution, known as the one-seventh power law velocity profile, typically applicable in many practical scenarios.
Examples & Analogies
Imagine a river with different flow rates due to varied speeds at different areas. Just as a gentle stream on a calm day (laminar flow) would have a different flow profile compared to a fast-moving turbulent river, the Reynolds number helps us understand how to interpret the velocity profile in different conditions.
Limitations of Power Law Profiles
Chapter 3 of 3
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The value of n will increase with increasing Reynolds number. Power law velocity profiles cannot give 0 slope at the pipe center. So, power law velocity profiles also cannot calculate the wall shear stress. Why? Because the power law profiles give a velocity gradient of infinity at the walls.
Detailed Explanation
While power law profiles are useful for estimating velocity distribution in pipes, they have limitations. For instance, as the Reynolds number increases, the power law profile suggests an increasingly steep gradient at the walls, which results in an infinite velocity gradient. This is unrealistic, as it implies that fluid velocity would change instantaneously at the boundary, which doesn't happen in reality. Additionally, because power law profiles cannot achieve a zero slope at the center of the pipe, they are inadequate for calculating the shear stress at the wall, a critical parameter in fluid mechanics.
Examples & Analogies
Consider the way a train moves on tracks. If suddenly, the tracks at the center change steeply, the train would derail. Similarly, in fluid flow, if the velocity changes too abruptly at the pipe walls, it becomes an unrealistic scenario, just like the train scenario, leading to an improper assessment of shear stresses at the boundaries.
Key Concepts
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Velocity Difference: The difference between a point velocity and average velocity in pipes is consistent for smooth and rough surfaces.
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Limitations of Power Law: Power law profiles cannot predict zero slope at the pipe center or calculate wall shear stress accurately due to infinite gradients.
Examples & Applications
In a turbulent water flow in a pipeline, the velocity at the center might reach maximum levels, while the average would fall short, illustrating the practical application of velocity profiles.
Considering Reynolds number changes with flow rates, the behavior of the power law profile can influence the design of piping systems significantly.
Memory Aids
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Rhymes
Power laws don't show zero slope, at centers, they can't help us cope.
Stories
Imagine a smooth and a rough pipe side by side, both carrying water. They both have differences in their average and point velocities, but their velocity behavior is surprisingly similar, meaning we have distinct design considerations!
Memory Tools
Remember 'Smoothness Saves Stress' - smooth pipes have a predictable behavior while rough pipes can lead to unpredictable shear stress.
Acronyms
RAPID - Recognize Average Point Interactions Derive - remember the average velocity interaction when considering turbulent flows.
Flash Cards
Glossary
- Power Law Velocity Profile
A mathematical model representing velocity distribution in a turbulent flow characterized by a governing exponent dependent on flow conditions.
- Reynolds Number
A dimensionless number used to predict flow patterns in different fluid flow situations.
- Wall Shear Stress
The force per unit area exerted by a fluid at the interface with a solid surface.
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