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Steam at \(235^{\circ} \mathrm{C}\) is flowing inside a steel pipe \((k=\) \(61 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) whose inner and outer diameters are \(10 \mathrm{~cm}\) and \(12 \mathrm{~cm}\), respectively, in an environment at \(20^{\circ} \mathrm{C}\). The heat transfer coefficients inside and outside the pipe are \(105 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and \(14 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), respectively. Determine ( \(a\) ) the thickness of the insulation \((k=0.038 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) needed to reduce the heat loss by 95 percent and \((b)\) the thickness of the insulation needed to reduce the exposed surface temperature of insulated pipe to \(40^{\circ} \mathrm{C}\) for safety reasons.

Short Answer

Expert verified
To determine this, follow the steps below: 1. Calculate the current heat transfer rate (Q) using the given parameters and the overall heat transfer coefficient (U). 2. Determine the insulation thickness that reduces heat loss by 95%, considering the new heat transfer rate (Q_reduced) and a redefined thermal resistance (R'_{total}). 3. Calculate the insulation thickness required for an exposed surface temperature of 40°C using a redefined thermal resistance (R''_{total}). After performing the calculations mentioned in the given solution, you will obtain the insulation thickness required for both conditions.

Step by step solution

01

Calculate the current heat transfer

First, let's convert the diameters to meters: \(d_{in}=0.1\,\text{m}\) and \(d_{out}=0.12\,\text{m}\). Now, we can use the thermal circuit analogy to determine the overall heat transfer coefficient \(U\). The total thermal resistance to heat transfer from inside to outside is given by: \(R_{total} = \frac{1}{h_{in}A_{in}} + \frac{\ln{(r_{out}/r_{in})}}{2\pi k_{steel}L} + \frac{1}{h_{out}A_{out}}\) Next, we need to calculate the heat transfer rate inside and outside the pipe: \(A_{in}=2\pi r_{in}\,L\) \(A_{out}=2\pi r_{out}\,L\) \(r_{in} = \frac{d_{in}}{2} =0.05\,\text{m}\) \(r_{out} = \frac{d_{out}}{2} =0.06\,\text{m}\) Now plug the values into \(R_{total}\) and calculate the overall heat transfer coefficient, U: \(R_{total} = \frac{1}{h_{in}2\pi r_{in} L} + \frac{\ln{(r_{out}/r_{in})}}{2\pi k_{steel} L} + \frac{1}{h_{out}2\pi r_{out} L}\) \(U = \frac{1}{R_{total}}\) Heat transfer rate, \(Q = UA(T_{steam} - T_{env})\)
02

Determine insulation thickness to reduce heat loss by 95%

To reduce the heat loss by 95%, we want the heat transfer rate to be: \(Q_{reduced} =Q(1-0.95)=0.05Q\) Redefine the thermal resistance to include the insulation: \(R'_{total} = \frac{1}{h_{in}A_{in}} + \frac{\ln{(r_{out}/r_{in})}}{2\pi k_{steel}L} + \frac{\ln{(r_{insulation}/r_{out})}}{2\pi k_{insulation}L} + \frac{1}{h_{out}A_{insulation}}\) \(Q_{reduced} = U'A(T_{steam}-T_{env}) \implies U' = \frac{Q_{reduced}}{A(T_{steam}-T_{env})}\) Now we can solve for the insulation thickness using the equation: \(\frac{\ln{(r_{insulation}/r_{out})}}{2\pi k_{insulation} L} = \frac{1}{U'} - \frac{1}{h_{in}A_{in}} - \frac{\ln{(r_{out}/r_{in})}}{2\pi k_{steel} L} - \frac{1}{h_{out}A_{insulation}}\) Calculate the thickness of the insulation, \(t_{insulation} = r_{insulation} - r_{out}\).
03

Determine insulation thickness to reduce exposed surface temperature to 40°C

To achieve an exposed surface temperature of \(40\,^{\circ}\mathrm{C}\), we can use the following relationship: \(T_{insulation} - T_{env} = U'R'_{total} (T_{steam} - T_{insulation})\) In this case, \(T_{insulation} = 40\,^{\circ}\mathrm{C}\) and \(T_{env}=20\,^{\circ}\mathrm{C}\). Redefine the thermal resistance as before: \(R''_{total} = \frac{1}{h_{in}A_{in}} + \frac{\ln{(r_{out}/r_{in})}}{2\pi k_{steel}L} + \frac{\ln{(r_{insulation}/r_{out})}}{2\pi k_{insulation}L} + \frac{1}{h_{out}A_{insulation}}\) Now we can solve for the insulation thickness using the equation: \(\frac{\ln{(r_{insulation}/r_{out})}}{2\pi k_{insulation}L} = \frac{1}{U''} - \frac{1}{h_{in}A_{in}} - \frac{\ln{(r_{out}/r_{in})}}{2\pi k_{steel}L} - \frac{1}{h_{out}A_{insulation}}\) Calculate the thickness of the insulation, \(t_{insulation} = r_{insulation} - r_{out}\).

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Key Concepts

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

Heat Transfer
Heat transfer is a fundamental concept in thermodynamics that involves the movement of thermal energy from one place to another. It is crucial in analyzing how well heating or cooling systems perform and in calculating the insulation thickness for pipes or buildings. In the given exercise, we are examining a scenario where steam is flowing inside a steel pipe, and our goal is to minimize heat loss.

There are three modes of heat transfer: conduction, convection, and radiation. In our scenario, conduction occurs through the metal of the pipe, and convection is happening on both the inside and outside surfaces of the pipe due to the difference in temperature between the steam, the pipe material, and the surrounding environment. The exercise focuses on calculating the necessary insulation to achieve a significant reduction in heat loss by 95% and ensure safety by keeping the exterior pipe temperature at 40°C.
Thermal Resistance
Thermal resistance refers to the ability of a material or system to resist the flow of heat. It's an analogous concept to electrical resistance, but instead of impeding electrical current, it hinders the transfer of heat. The higher the thermal resistance, the less heat is lost over time, making it a critical factor in insulation.

When performing insulation thickness calculation, as in our textbook exercise, we must understand the various resistances heat encounters as it moves from the hot steam inside the pipe, through the pipe's steel wall, the insulation, and eventually to the cooler environment outside. These resistances are then combined to form a total system resistance, which helps us to quantify the efficiency of the insulation. In the solution steps, we are provided with a formula that incorporates the thermal resistances of the pipe and insulation to solve for the heat transfer rate reduction and the necessary insulation thickness.
Overall Heat Transfer Coefficient
The overall heat transfer coefficient, symbolized by 'U', is a measure that incorporates all forms of heat transfer (conduction, convection, and radiation) in a system. It is an indicator of how well a series of materials can transfer heat. The overall heat transfer coefficient is inversely proportional to the total thermal resistance of the system.

Let's apply this to our exercise, where calculating the 'U' factor allows us to understand the heat transfer characteristics of the pipe with and without insulation. When insulation is added, we calculate a new 'U' to reflect the additional resistance. By comparing the original and the new 'U' values, we can determine the effectiveness of different insulation thicknesses and choose the one that meets our goal—either the 95% heat loss reduction or the specific exterior temperature condition for safety.

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Most popular questions from this chapter

Consider a tube for transporting steam that is not centered properly in a cylindrical insulation material \((k=\) \(0.73 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\). The tube diameter is \(D_{1}=20 \mathrm{~cm}\) and the insulation diameter is \(D_{2}=40 \mathrm{~cm}\). The distance between the center of the tube and the center of the insulation is \(z=5 \mathrm{~mm}\). If the surface of the tube maintains a temperature of \(100^{\circ} \mathrm{C}\) and the outer surface temperature of the insulation is constant at \(30^{\circ} \mathrm{C}\), determine the rate of heat transfer per unit length of the tube through the insulation.

A 25 -cm-diameter, 2.4-m-long vertical cylinder containing ice at \(0^{\circ} \mathrm{C}\) is buried right under the ground. The cylinder is thin-shelled and is made of a high thermal conductivity material. The surface temperature and the thermal conductivity of the ground are \(18^{\circ} \mathrm{C}\) and \(0.85 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) respectively. The rate of heat transfer to the cylinder is (a) \(37.2 \mathrm{~W}\) (b) \(63.2 \mathrm{~W}\) (c) \(158 \mathrm{~W}\) (d) \(480 \mathrm{~W}\) (e) \(1210 \mathrm{~W}\)

Consider a short cylinder whose top and bottom surfaces are insulated. The cylinder is initially at a uniform temperature \(T_{i}\) and is subjected to convection from its side surface to a medium at temperature \(T_{\infty}\), with a heat transfer coefficient of \(h\). Is the heat transfer in this short cylinder one- or twodimensional? Explain.

In a combined heat and power (CHP) generation process, by-product heat is used for domestic or industrial heating purposes. Hot steam is carried from a CHP generation plant by a tube with diameter of \(127 \mathrm{~mm}\) centered at a square crosssection solid bar made of concrete with thermal conductivity of \(1.7 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). The surface temperature of the tube is constant at \(120^{\circ} \mathrm{C}\), while the square concrete bar is exposed to air with temperature of \(-5^{\circ} \mathrm{C}\) and convection heat transfer coefficient of \(20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). If the temperature difference between the outer surface of the square concrete bar and the ambient air is to be maintained at \(5^{\circ} \mathrm{C}\), determine the width of the square concrete bar and the rate of heat loss per meter length.

A 1-m-inner-diameter liquid-oxygen storage tank at a hospital keeps the liquid oxygen at \(90 \mathrm{~K}\). The tank consists of a \(0.5-\mathrm{cm}\)-thick aluminum ( \(k=170 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) shell whose exterior is covered with a 10 -cm-thick layer of insulation \((k=\) \(0.02 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\). The insulation is exposed to the ambient air at \(20^{\circ} \mathrm{C}\) and the heat transfer coefficient on the exterior side of the insulation is \(5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The temperature of the exterior surface of the insulation is (a) \(13^{\circ} \mathrm{C}\) (b) \(9^{\circ} \mathrm{C}\) (c) \(2^{\circ} \mathrm{C}\) (d) \(-3^{\circ} \mathrm{C}\) (e) \(-12^{\circ} \mathrm{C}\)

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