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The velocity profile in fully developed laminar flow of water at $40^{\circ} \mathrm{F}\( in a 140 -ft-long horizontal circular pipe, in \)\mathrm{ft} / \mathrm{s}\(, is given by \)u(r)=0.8\left(1-625 r^{2}\right)\( where \)r$ is the radial distance from the centerline of the pipe in \(\mathrm{ft}\). Determine (a) the volume flow rate of water through the pipe, \((b)\) the pressure drop across the pipe, and (c) the useful pumping power required to overcome this pressure drop.

Short Answer

Expert verified
#Answer# (a) To find the volume flow rate \(Q\), integrate the given velocity profile: $$Q = \int_{0}^{R} 0.8\left(1-625 r^{2}\right)(2\pi r dr) $$ (b) To calculate the pressure drop across the pipe, use the Hagen-Poiseuille equation: $$\Delta P = \frac{32 \mu Q L}{\pi R^4}$$ (c) To find the useful pumping power needed to overcome the pressure drop, use the expression: $$P_{\text{pumping}} = Q \Delta P$$ Plug in the expressions for \(Q\) and \(\Delta P\) from Steps 1 and 2 to calculate the required pumping power.

Step by step solution

01

Calculate the volume flow rate \(Q\)

To find the volume flow rate, first, let's integrate the velocity profile \(u(r)\) over the pipe's cross-sectional area. Recall that for a circular cross-section with radius \(R\), the area element is given by \(dA = 2\pi r dr\). The volume flow rate is then the integral of the product of \(u(r)\) and \(dA\): $$Q = \int_{0}^{R} u(r) dA = \int_{0}^{R} u(r) (2\pi r dr) $$ Now we will integrate the given velocity profile: $$Q = \int_{0}^{R} 0.8\left(1-625 r^{2}\right)(2\pi r dr) $$
02

Find the pressure drop

For laminar flow in a pipe, the pressure drop can be calculated using the Hagen-Poiseuille equation: $$\Delta P = \frac{32 \mu Q L}{\pi R^4}$$ Where \(\Delta P\) is the pressure drop, \(\mu\) is the dynamic viscosity of water, \(Q\) is the volume flow rate, \(L\) is the pipe length, and \(R\) is the pipe radius. We will use the provided temperature (\(40^{\circ}\mathrm{F}\)) to find the dynamic viscosity of water.
03

Calculate the useful pumping power required

The useful pumping power needed to overcome the pressure drop is determined by the product of the volume flow rate and the pressure drop: $$P_{\text{pumping}} = Q \Delta P$$ Using the expression obtained in Step 1 for \(Q\) and the Hagen-Poiseuille equation obtained in Step 2 for \(\Delta P\), calculate the useful pumping power required.

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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}\(, and \)k=0.58 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\( ) flows with an average velocity of \)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 \(T_{s}-T_{\text {m }}\), and (c) the value of \(T_{e}-T_{i}\).

Air \(\left(c_{p}=1000 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters a \(16-\mathrm{cm}\)-diameter and \(19-\mathrm{m}\)-long underwater duct at \(50^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\) at an average velocity of $7 \mathrm{~m} / \mathrm{s}$ and is cooled by the water outside. If the average heat transfer coefficient is $35 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$ and the tube temperature is nearly equal to the water temperature of \(5^{\circ} \mathrm{C}\), the exit temperature of the air is (a) \(6^{\circ} \mathrm{C}\) (b) \(10^{\circ} \mathrm{C}\) (c) \(18^{\circ} \mathrm{C}\) (d) \(25^{\circ} \mathrm{C}\) (e) \(36^{\circ} \mathrm{C}\)

How is the friction factor for flow in a tube related to the pressure drop? How is the pressure drop related to the pumping power requirement for a given mass flow rate?

In a food processing plant, hot liquid water is being transported in a pipe \((k=15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), $D_{i}=2.5 \mathrm{~cm}, D_{o}=3 \mathrm{~cm}\(, and \)L=10 \mathrm{~m}$.) The hot water flowing with a mass flow rate of \(0.15 \mathrm{~kg} / \mathrm{s}\) enters the pipe at \(100^{\circ} \mathrm{C}\) and exits at \(60^{\circ} \mathrm{C}\). The plant supervisor thinks that since the hot water exits the pipe at $60^{\circ} \mathrm{C}$, the pipe's outer surface temperature should be safe from thermal burn hazards. In order to prevent thermal burn upon accidental contact with skin tissue for individuals working in the vicinity of the pipe, the pipe's outer surface temperature should be kept below \(45^{\circ} \mathrm{C}\). Determine whether or not there is a risk of thermal burn on the pipe's outer surface. Assume the pipe outer surface temperature remains constant.

In fully developed laminar flow inside a circular pipe, the velocities at \(r=0.5 R\) (midway between the wall surface and the centerline) are measured to be 3,6 , and \(9 \mathrm{~m} / \mathrm{s}\). (a) Determine the maximum velocity for each of the measured midway velocities. (b) By varying \(r / R\) for $-1 \leq r / R \leq 1$, plot the velocity profile for each of the measured midway velocities with \(r / R\) as the \(y\)-axis and \(V(r / R)\) as the \(x\)-axis.

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