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Steam at \(320^{\circ} \mathrm{C}\) flows in a stainless steel pipe \((k=\) \(15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) ) whose inner and outer diameters are \(5 \mathrm{~cm}\) and \(5.5 \mathrm{~cm}\), respectively. The pipe is covered with \(3-\mathrm{cm}\)-thick glass wool insulation \((k=0.038 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\). Heat is lost to the surroundings at \(5^{\circ} \mathrm{C}\) by natural convection and radiation, with a combined natural convection and radiation heat transfer coefficient of \(15 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Taking the heat transfer coefficient inside the pipe to be \(80 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), determine the rate of heat loss from the steam per unit length of the pipe. Also determine the temperature drops across the pipe shell and the insulation.

Short Answer

Expert verified
Question: Calculate the rate of heat loss from the steam per unit length of the pipe and the temperature drops across the pipe shell and the insulation. Answer: To calculate the rate of heat loss (q) and the temperature drops across the pipe shell (∆T_s) and insulation (∆T_i), follow these steps: 1. Calculate the thermal resistances of each layer (inside pipe, pipe wall, insulation, and convection at the outer surface) using the given dimensions, materials, and heat transfer coefficients. 2. Calculate the overall resistance (R_total) by adding up the individual thermal resistances. 3. Calculate the heat loss rate (q) based on the temperature difference between the steam and the ambient, and the overall resistance. 4. Calculate the temperature drops across the pipe shell (∆T_s) and insulation (∆T_i) using the heat loss rate and the individual thermal resistances. Note that this requires the input values for dimensions, materials, and heat transfer coefficients to perform the calculations.

Step by step solution

01

Calculate the resistances of each layer of the pipe and insulation

We can model the heat transfer process as a series of thermal resistances. We are given the inner and outer diameters of the stainless steel pipe, the thickness of the glass wool insulation, the thermal conductivities of the materials, as well as the heat transfer coefficients for the inside of the pipe and the natural convection. Using this information, we can calculate the thermal resistance for each layer (inside pipe, pipe wall, insulation, and convection at the outer surface). Let \(R_i\) be the inside heat transfer resistance, \(R_s\) be the steel pipe resistance, \(R_i\) be the insulation resistance, and \(R_o\) be the outside heat transfer resistance. For the inside heat transfer resistance: $$R_i = \frac{1}{h_i A_i}$$ For the steel pipe resistance: $$R_s = \frac{\ln(\frac{D_o}{D_i})}{2 \pi k_s L}$$ For the insulation resistance: $$R_i = \frac{\ln(\frac{D_o + 2 t_i}{D_o})}{2 \pi k_i L}$$ For the outside heat transfer resistance: $$R_o = \frac{1}{h_o A_o}$$ Where \(h_i\) is the inside heat transfer coefficient, \(h_o\) is the outside heat transfer coefficient, \(A_i\) and \(A_o\) are the inside and outside surface areas of the pipe, \(D_i\) and \(D_o\) are the inner and outer diameters of the pipe, \(t_i\) is the insulation thickness, \(k_s\) is the thermal conductivity of the stainless steel pipe, \(k_i\) is the thermal conductivity of the insulation, and \(L\) is the length of the pipe.
02

Calculate the overall resistance and the heat loss rate

The overall resistance of the system can be obtained by adding the thermal resistances of each layer: $$R_{total} = R_i + R_s + R_i + R_o$$ Using the given values for heat transfer coefficients and thermal conductivities, as well as the inside and outside surface areas of the pipe, we can calculate the overall resistance. Now, the heat loss rate per unit length of the pipe can be calculated using the temperature difference between the steam and the ambient and the overall resistance: $$q = \frac{T_{steam} - T_{ambient}}{R_{total}}$$ Where \(q\) is the heat loss rate per unit length, \(T_{steam}\) is the steam temperature, and \(T_{ambient}\) is the ambient temperature.
03

Calculate the temperature drops across the pipe shell and insulation

We can now determine the temperature drops across the pipe shell and the insulation using the heat loss rate and the individual thermal resistances. Temperature drop across the pipe shell (\(\Delta T_s\)): $$\Delta T_s = q \cdot R_s$$ Temperature drop across the insulation (\(\Delta T_i\)): $$\Delta T_i = q \cdot R_i$$

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Key Concepts

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

Thermal Resistance
Thermal resistance is a crucial concept in understanding heat transfer. In simple terms, it's like an obstacle that heat energy has to overcome to flow through a material. In heat transfer, we visualize this process similar to how electrical resistance works in circuit theory. Just as an electric resistor impedes the flow of electrical current, thermal resistance impedes the flow of heat.

It is calculated using the formula \[ R = \frac{L}{kA} \]where:
  • L is the thickness of the material.
  • k is the thermal conductivity.
  • A is the area through which heat is transferred.
In the given problem, each layer (the pipe wall, the insulation, and the boundaries inside and outside of the pipe) has its own thermal resistance. By adding the resistances together, we can determine the total resistance faced by the heat as it travels from the steam to the surrounding air.
Convection
Convection is a type of heat transfer that occurs in fluids such as liquids and gases. During convection, heat is moved through the movement of fluid particles. This is how heat is transferred from the surface of the steel pipe to the surrounding air in our problem.

There are two types of convection: natural and forced. Natural convection occurs due to the natural movement of the fluid particles because of density differences, whereas forced convection is caused by external forces, such as fans or pumps. In our example, the convection considered is natural.
Convection heat transfer is calculated using the formula:\[ q = hA(T_{surface} - T_{fluid}) \]where:
  • h is the convection heat transfer coefficient.
  • A is the surface area.
  • T_{surface} is the surface temperature.
  • T_{fluid} is the fluid temperature.
In the solution, the surface temperature is the pipe's outer surface, and the fluid temperature is the ambient air temperature.
Insulation
Insulation is a material or layer that reduces the rate of heat transfer. Using materials with low thermal conductivity achieves his and in this example, glass wool is used.

Insulation works by increasing the thermal resistance between two surfaces. Think of it as a thick sweater keeping the heat from leaving quickly. Because the glass wool has a very low thermal conductivity, it prevents the heat from escaping as fast as it would through the steel pipe alone.
The importance of insulation lies in its capacity to effectively manage and reduce energy loss. This helps in maintaining temperature inside pipes or buildings and saving energy costs. The effectiveness of insulation can be even more understood by calculating its resistance with:\[ R = \frac{\ln\left(\frac{D_o + 2 t_i}{D_o}\right)}{2 \pi k L} \]This formula gives the ease of identifying how much resistance the insulation adds to the system.
Conduction
Conduction is the simplest form of heat transfer. It occurs when heat flows through a material from a high-temperature area to a lower-temperature one, typically through physical contact.

In the context of the exercise, conduction is the mode of heat transfer through the steel pipe wall and the glass wool insulation. It depends on the thermal conductivity of the materials. Good conductors have high thermal conductivity, while insulators have low thermal conductivity.
The rate of conduction heat transfer can be expressed as:\[ q = -kA \frac{dT}{dx} \]where:
  • k is the thermal conductivity.
  • A is the area through which heat is conducted.
  • \frac{dT}{dx} is the temperature gradient in the direction of heat flow.
Conduction is essential in the overall heat loss calculation in our problem, as it represents the first phase of energy movement after the steam, before reaching the insulation.

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Most popular questions from this chapter

A cylindrical pin fin of diameter \(0.6 \mathrm{~cm}\) and length of \(3 \mathrm{~cm}\) with negligible heat loss from the tip has an efficiency of 0.7. The effectiveness of this fin is (a) \(0.3\) (b) \(0.7\) (c) 2 (d) 8 (e) 14

A thin-walled spherical tank in buried in the ground at a depth of \(3 \mathrm{~m}\). The tank has a diameter of \(1.5 \mathrm{~m}\), and it contains chemicals undergoing exothermic reaction that provides a uniform heat flux of \(1 \mathrm{~kW} / \mathrm{m}^{2}\) to the tank's inner surface. From soil analysis, the ground has a thermal conductivity of \(1.3 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and a temperature of \(10^{\circ} \mathrm{C}\). Determine the surface temperature of the tank. Discuss the effect of the ground depth on the surface temperature of the tank.

Consider a very long rectangular fin attached to a flat surface such that the temperature at the end of the fin is essentially that of the surrounding air, i.e. \(20^{\circ} \mathrm{C}\). Its width is \(5.0 \mathrm{~cm}\); thickness is \(1.0 \mathrm{~mm}\); thermal conductivity is \(200 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\); and base temperature is \(40^{\circ} \mathrm{C}\). The heat transfer coefficient is \(20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Estimate the fin temperature at a distance of \(5.0 \mathrm{~cm}\) from the base and the rate of heat loss from the entire fin.

Consider an insulated pipe exposed to the atmosphere. Will the critical radius of insulation be greater on calm days or on windy days? Why?

Consider two identical people each generating \(60 \mathrm{~W}\) of metabolic heat steadily while doing sedentary work, and dissipating it by convection and perspiration. The first person is wearing clothes made of 1 -mm-thick leather \((k=\) \(0.159 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) ) that covers half of the body while the second one is wearing clothes made of 1 -mm-thick synthetic fabric \((k=0.13 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) that covers the body completely. The ambient air is at \(30^{\circ} \mathrm{C}\), the heat transfer coefficient at the outer surface is \(15 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), and the inner surface temperature of the clothes can be taken to be \(32^{\circ} \mathrm{C}\). Treating the body of each person as a 25 -cm-diameter, \(1.7-\mathrm{m}\)-long cylinder, determine the fractions of heat lost from each person by perspiration.

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