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What fluid property is responsible for the development of the velocity boundary layer? For what kinds of fluids will there be no velocity boundary layer in a pipe?

Short Answer

Expert verified
Answer: The fluid property responsible for the development of the velocity boundary layer is viscosity. Fluid types with no boundary layer in a pipe will be the ones with zero viscosity, called inviscid fluids. However, ideal inviscid fluids are only theoretical approximations, and all real fluids exhibit some level of viscosity.

Step by step solution

01

Understanding the concept of the velocity boundary layer

The velocity boundary layer is a region near a solid boundary in which the fluid velocity changes rapidly due to the viscous effects of the fluid. The viscous property of a fluid is responsible for the formation of the boundary layer, which affects the momentum transfer in the fluid flow and creates a drag effect on the solid surfaces.
02

Identifying the fluid property responsible for the velocity boundary layer

The fluid property responsible for the development of the velocity boundary layer is viscosity. Viscosity is a measure of a fluid's resistance to deformation or the ease with which the layers of fluid flow over one another. It determines the fluid's ability to deform and absorb the momentum of adjacent fluid layers, causing the velocity profile to change near the boundary.
03

Determining the fluid types with no boundary layer in a pipe

The type of fluids with no velocity boundary layer in a pipe will be the ones with zero viscosity, called inviscid fluids. In inviscid fluids, the layers flow over one another without any resistance, resulting in a smooth flow and no formation of the velocity boundary layer. However, it is important to note that ideal inviscid fluids are only theoretical approximations used for certain calculations, while in reality, all fluids exhibit some level of viscosity.

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Most popular questions from this chapter

In a manufacturing plant that produces cosmetic products, glycerin is being heated by flowing through a \(25-\mathrm{mm}-\) diameter and 10 -m-long tube. With a mass flow rate of \(0.5 \mathrm{~kg} / \mathrm{s}\), the flow of glycerin enters the tube at \(25^{\circ} \mathrm{C}\). The tube surface is maintained at a constant surface temperature of \(140^{\circ} \mathrm{C}\). Determine the outlet mean temperature and the total rate of heat transfer for the tube. Evaluate the properties for glycerin at \(30^{\circ} \mathrm{C}\).

The velocity profile in fully developed laminar flow in a circular pipe, in \(\mathrm{m} / \mathrm{s}\), is given by \(u(r)=4\left(1-100 r^{2}\right)\) where \(r\) is the radial distance from the centerline of the pipe in \(\mathrm{m}\). Determine \((a)\) the radius of the pipe, \((b)\) the mean velocity through the pipe, and \((c)\) the maximum velocity in the pipe.

Water at $10^{\circ} \mathrm{C}\left(\rho=999.7 \mathrm{~kg} / \mathrm{m}^{3}\right.\( and \)\mu=1.307 \times\( \)10^{-3} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}\( ) is flowing in a \)0.20-\mathrm{cm}$-diameter, 15 -m-long pipe steadily at an average velocity of $1.2 \mathrm{~m} / \mathrm{s}\(. Determine \)(a)\( the pressure drop and \)(b)$ the pumping power requirement to overcome this pressure drop. Assume flow is fully developed. Is this a good assumption? Answers: (a) \(188 \mathrm{kPa}\), (b) $0.71 \mathrm{~W}$

In the effort to find the best way to cool a smooth, thin-walled copper tube, an engineer decided to flow air either through the tube or across the outer tube surface. The tube has a diameter of \(5 \mathrm{~cm}\), and the surface temperature is held constant. Determine \((a)\) the convection heat transfer coefficient when air is flowing through its inside at $25 \mathrm{~m} / \mathrm{s}\( with a bulk mean temperature of \)50^{\circ} \mathrm{C}\( and \)(b)$ the convection heat transfer coefficient when air is flowing across its outer surface at \(25 \mathrm{~m} / \mathrm{s}\) with a film temperature of \(50^{\circ} \mathrm{C}\).

Consider a 25-mm-diameter and 15-m-long smooth tube that is maintained at a constant surface temperature. Fluids enter the tube at \(50^{\circ} \mathrm{C}\) with a mass flow rate of \(0.01 \mathrm{~kg} / \mathrm{s}\). Determine the tube surface temperatures necessary to heat water, engine oil, and liquid mercury to the desired outlet temperature of \(150^{\circ} \mathrm{C}\).

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