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What is the generally accepted value of the Reynolds number above which the flow in smooth pipes is turbulent?

Short Answer

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Answer: The critical Reynolds number value is Re > 4000.

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01

Generally Accepted Reynolds Number Value for Turbulent Flow

The generally accepted value of the Reynolds number above which the flow in smooth pipes is considered turbulent is Re > 4000.

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Laminar and Turbulent Flow
Understanding the distinction between laminar and turbulent flow is crucial for students studying fluid mechanics.

Laminar flow is characterized by fluid particles moving along smooth paths in layers, with little to no mixing between the layers. This type of flow is orderly and predictable. Imagine how syrup flows down the side of a pancake - it’s steady and smooth. Laminar flow occurs at lower speeds and viscosity plays a significant role in maintaining the ordered flow state.

Visualizing Laminar Flow

You might visualize it like a deck of cards neatly stacked; when slid across a table, the cards move as one layered unit.

In contrast, turbulent flow is characterized by random, chaotic fluid motion. Fluid particles mix vigorously and the flow is unpredictable. Picture a rapidly flowing river - the water’s surface is rough and disturbed. Turbulent flow typically happens at higher flow speeds, and inertia is the dominant factor, overpowering viscosity.

Chaos in Motion

To envision turbulent flow, think of it as shuffling the card deck; the cards (or fluid particles) are in disorder, moving irregularly and mixing.
Reynolds Number Significance
The Reynolds number is a fundamental dimensionless quantity in fluid dynamics with profound importance. It helps predict the flow regime, be it laminar or turbulent, without the need for complex calculations or experiments.

The Reynolds number is obtained by the formula \(Re = \frac{\rho VD}{\mu}\) where \(\rho\) is the fluid's density, \(V\) is the flow velocity, \(D\) is the characteristic length (diameter of the pipe), and \(\mu\) is the dynamic viscosity of the fluid. It effectively compares the inertial forces to the viscous forces in a flowing fluid. When inertial forces dominate, the flow tends to be turbulent; when viscous forces prevail, the flow is laminar.

Threshold of Turbulence

A Reynolds number greater than 4000 generally indicates turbulent flow in smooth pipes. This threshold helps engineers design systems that either minimize or enhance turbulence, according to the needs of the application, such as in the mixing of chemicals or the reduction of friction in pipelines.
Flow in Smooth Pipes
The behavior of fluid flow in smooth pipes is governed by both the Reynolds number and the physical conditions of the pipe. Since the interior of a smooth pipe lacks roughness, it doesn't disrupt the fluid flow as much as a rough pipe would.

For smooth pipes, critical transitions from laminar to turbulent flow occur around the Reynolds number threshold of 4000. However, this is an approximation; the actual transition can be influenced by other factors like pipe vibrations, temperature, or irregularities in the fluid.

Optimizing Fluid Transport

Engineers leverage the concept of smooth pipe flow to enhance efficiency in transport systems by minimizing resistance and ensuring predictable flow patterns. Whether it’s a municipal water supply system or an intricate chemical processing plant, understanding the flow behavior in smooth pipes is essential for designing an effective and economic system.
Maintaining laminar flow in processing industries can be desirable to ensure uniform mixing and prevent damage to sensitive fluids. On the other hand, turbulent flow is used in heat exchangers because it enhances heat transfer efficiency due to the mixing action of the fluid.

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Most popular questions from this chapter

A fluid \(\left(\rho=1000 \mathrm{~kg} / \mathrm{m}^{3}, \mu=1.4 \times 10^{-3} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}\right.\), \(c_{p}=4.2 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\), and \(\left.k=0.58 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\right)\) flows with an average velocity of \(0.3 \mathrm{~m} / \mathrm{s}\) through a \(14-\mathrm{m}\) long tube with inside diameter of \(0.01 \mathrm{~m}\). Heat is uniformly added to the entire tube at the rate of \(1500 \mathrm{~W} / \mathrm{m}^{2}\). Determine \((a)\) the value of convection heat transfer coefficient at the exit, \((b)\) the value of \(T_{s}-T_{m}\), and (c) the value of \(T_{e}-T_{i}\).

Water enter a 5-mm-diameter and 13-m-long tube at \(45^{\circ} \mathrm{C}\) with a velocity of \(0.3 \mathrm{~m} / \mathrm{s}\). The tube is maintained at a constant temperature of \(5^{\circ} \mathrm{C}\). The required length of the tube in order for the water to exit the tube at \(25^{\circ} \mathrm{C}\) is (a) \(1.55 \mathrm{~m}\) (b) \(1.72 \mathrm{~m}\) (c) \(1.99 \mathrm{~m}\) (d) \(2.37 \mathrm{~m}\) (e) \(2.96 \mathrm{~m}\) (For water, use \(k=0.623 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \operatorname{Pr}=4.83, v=0.724 \times\) \(10^{-6} \mathrm{~m}^{2} / \mathrm{s}, c_{p}=4178 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}, \rho=994 \mathrm{~kg} / \mathrm{m}^{3}\).)

Inside a condenser, there is a bank of seven copper tubes with cooling water flowing in them. Steam condenses at a rate of \(0.6 \mathrm{~kg} / \mathrm{s}\) on the outer surfaces of the tubes that are at a constant temperature of \(68^{\circ} \mathrm{C}\). Each copper tube is \(5-\mathrm{m}\) long and has an inner diameter of \(25 \mathrm{~mm}\). Cooling water enters each tube at \(5^{\circ} \mathrm{C}\) and exits at \(60^{\circ} \mathrm{C}\). Determine the average heat transfer coefficient of the cooling water flowing inside each tube and the cooling water mean velocity needed to achieve the indicated heat transfer rate in the condenser.

How does the friction factor \(f\) vary along the flow direction in the fully developed region in (a) laminar flow and (b) turbulent flow?

A concentric annulus tube has inner and outer diameters of \(25 \mathrm{~mm}\) and \(100 \mathrm{~mm}\), respectively. Liquid water flows at a mass flow rate of \(0.05 \mathrm{~kg} / \mathrm{s}\) through the annulus with the inlet and outlet mean temperatures of \(20^{\circ} \mathrm{C}\) and \(80^{\circ} \mathrm{C}\), respectively. The inner tube wall is maintained with a constant surface temperature of \(120^{\circ} \mathrm{C}\), while the outer tube surface is insulated. Determine the length of the concentric annulus tube. Assume flow is fully developed.

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