Warning: foreach() argument must be of type array|object, bool given in /var/www/html/web/app/themes/studypress-core-theme/template-parts/header/mobile-offcanvas.php on line 20

A spherical vessel, \(3.0 \mathrm{~m}\) in diameter (and negligible wall thickness), is used for storing a fluid at a temperature of $0^{\circ} \mathrm{C}\(. The vessel is covered with a \)5.0$-cm-thick layer of an insulation \((k=0.20 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\). The surrounding air is at \(22^{\circ} \mathrm{C}\). The inside and outside heat transfer coefficients are 40 and 10 $\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}\(, respectively. Calculate \)(a)$ all thermal resistances, in \(\mathrm{K} / \mathrm{W},(b)\) the steady rate of heat transfer, and \((c)\) the temperature difference across the insulation layer.

Short Answer

Expert verified
Question: Calculate the thermal resistances, steady heat transfer rate, and temperature difference across the insulation layer of the spherical vessel. Answer: To find the thermal resistances, steady heat transfer rate, and temperature difference across the insulation layer, follow these steps: 1. Calculate the inner and outer radius of the vessel: \(R_1 = 1.5\,\text{m}\) and \(R_2 = 1.55\,\text{m}\). 2. Calculate the individual thermal resistances: \(R_{cond}\), \(R_{conv_1}\), and \(R_{conv_2}\). 3. Calculate the total thermal resistance: \(R_{tot} = R_{conv_1} + R_{cond} + R_{conv_2}\). 4. Calculate the steady rate of heat transfer: \(q = \frac{\Delta T}{R_{tot}}\), with \(\Delta T = T_{inside} - T_{outside}\). 5. Calculate the temperature difference across the insulation layer: \(\Delta T_{insulation} = q \times R_{cond}\). Using the given data, you will be able to calculate the thermal resistances, steady heat transfer rate, and temperature difference across the insulation layer for the given spherical vessel.

Step by step solution

01

Calculate the inner and outer radius of the vessel

We are given that the diameter of the spherical vessel is \(3.0\,\text{m}\). Considering negligible wall thickness, the radius of the inside sphere will be: \(R_1 = \frac{\text{diameter}}{2} = \frac{3.0}{2} = 1.5\,\text{m}\) The insulation layer is \(5.0\,\text{cm}\) thick. To find the radius of the outside sphere, we add this thickness to the inner radius: \(R_2 = R_1 + 5.0\,\text{cm} \times \frac{1\,\text{m}}{100\,\text{cm}} = 1.5\,\text{m} + 0.05\,\text{m} = 1.55\,\text{m}\)
02

Calculate the thermal resistances

There are three modes of heat transfer happening: conduction through the insulation, convection inside the vessel, and convection outside the vessel. The thermal resistance for conduction through the insulation, \(R_{cond}\), is given by: \(R_{cond} = \frac{1}{4 \pi k} \left(\frac{R_2^3 - R_1^3}{R_2 - R_1}\right)\) with \(k=0.20\,\frac{\text{W}}{\text{m}\cdot\text{K}}\), and \(R_1 = 1.5\,\text{m}\) and \(R_2 = 1.55\,\text{m}\) The thermal resistance for convection inside the vessel, \(R_{conv_1}\), is given by: \(R_{conv_1} = \frac{1}{h_1 A_1}\) with \(h_1=40\,\frac{\text{W}}{\text{m}^2\cdot\text{K}}\), and \(A_1 = 4 \pi R_1^2\) The thermal resistance for convection outside the vessel, \(R_{conv_2}\), is given by: \(R_{conv_2} = \frac{1}{h_2 A_2}\) with \(h_2=10\,\frac{\text{W}}{\text{m}^2\cdot\text{K}}\), and \(A_2 = 4 \pi R_2^2\)
03

Calculate the total thermal resistance

The total thermal resistance \(R_{tot}\) is given by the sum of the individual resistances: \(R_{tot} = R_{conv_1} + R_{cond} + R_{conv_2}\)
04

Calculate the steady rate of heat transfer

The formula for steady heat transfer through a system with the given total thermal resistance is: \(q = \frac{\Delta T}{R_{tot}}\) with the temperature difference \(\Delta T = T_{inside} - T_{outside}\), with \(T_{inside}=0\,\text{C}\) and \(T_{outside}=22\,\text{C}\).
05

Calculate the temperature difference across the insulation layer

The temperature difference across the insulation layer, \(\Delta T_{insulation}\), is given by: \(\Delta T_{insulation} = q \times R_{cond}\) Now that we have outlined the steps, we can use the given data to find the required thermal resistances, steady heat transfer rate, and temperature difference across the insulation layer.

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with Vaia!

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

A 2.2-m-diameter spherical steel tank filled with iced water at $0^{\circ} \mathrm{C}$ is buried underground at a location where the thermal conductivity of the soil is \(k=0.55 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). The distance between the tank center and the ground surface is \(2.4 \mathrm{~m}\). For a ground surface temperature of \(18^{\circ} \mathrm{C}\), determine the rate of heat transfer to the iced water in the tank. What would your answer be if the soil temperature were \(18^{\circ} \mathrm{C}\) and the ground surface were insulated?

Hot water at an average temperature of \(53^{\circ} \mathrm{C}\) and an average velocity of \(0.4 \mathrm{~m} / \mathrm{s}\) is flowing through a \(5-\mathrm{m}\) section of a thin-walled hot-water pipe that has an outer diameter of $2.5 \mathrm{~cm}\(. The pipe passes through the center of a \)14-\mathrm{cm}$-thick wall filled with fiberglass insulation $(k=0.035 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\(. If the surfaces of the wall are at \)18^{\circ} \mathrm{C}\(, determine \)(a)$ the rate of heat transfer from the pipe to the air in the rooms and \((b)\) the temperature drop of the hot water as it flows through this 5 -m-long section of the wall.

Circular fins of uniform cross section, with diameter of \(10 \mathrm{~mm}\) and length of \(50 \mathrm{~mm}\), are attached to a wall with surface temperature of \(350^{\circ} \mathrm{C}\). The fins are made of material with thermal conductivity of \(240 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), they are exposed to an ambient air condition of \(25^{\circ} \mathrm{C}\), and the convection heat transfer coefficient is $250 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Determine the heat transfer rate and plot the temperature variation of a single fin for the following boundary conditions: (a) Infinitely long fin (b) Adiabatic fin tip (c) Fin with tip temperature of \(250^{\circ} \mathrm{C}\) (d) Convection from the fin tip

A \(20-\mathrm{cm}\)-diameter hot sphere at \(120^{\circ} \mathrm{C}\) is buried in the ground with a thermal conductivity of $1.2 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. The distance between the center of the sphere and the ground surface is \(0.8 \mathrm{~m}\), and the ground surface temperature is \(15^{\circ} \mathrm{C}\). The rate of heat loss from the sphere is (a) \(169 \mathrm{~W}\) (b) \(20 \mathrm{~W}\) (c) \(217 \mathrm{~W}\) (d) \(312 \mathrm{~W}\) (e) \(1.8 \mathrm{~W}\)

Exposure to high concentrations of gaseous ammonia can cause lung damage. To prevent gaseous ammonia from leaking out, ammonia is transported in its liquid state through a pipe $\left(k=25 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, D_{i}=2.5 \mathrm{~cm}\right.\(, \)D_{o}=4 \mathrm{~cm}\(, and \)L=10 \mathrm{~m}$ ). Since liquid ammonia has a normal boiling point of $-33.3^{\circ} \mathrm{C}$, the pipe needs to be properly insulated to prevent the surrounding heat from causing the ammonia to boil. The pipe is situated in a laboratory, where the average ambient air temperature is $20^{\circ} \mathrm{C}$. The convection heat transfer coefficients of the liquid ammonia and the ambient air are \(100 \mathrm{~W} / \mathrm{m}^{2}, \mathrm{~K}\) and \(20 \mathrm{~W} / \mathrm{m}^{2}, \mathrm{~K}\), respectively. Determine the insulation thickness for the pipe using a material with $k=0.75 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$ to keep the liquid ammonia flowing at an average temperature of \(-35^{\circ} \mathrm{C}\), while maintaining the insulated pipe outer surface temperature at \(10^{\circ} \mathrm{C}\).

See all solutions

Recommended explanations on Physics Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.

Sign-up for free