/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 60 A spherical vessel used as a rea... [FREE SOLUTION] | 91Ó°ÊÓ

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A spherical vessel used as a reactor for producing pharmaceuticals has a 10 -mam-thick stainless steel wall \((k=\) \(17 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) and an inner diameter of \(1 \mathrm{~m}\). The exteria surface of the vessel is exposed to ambient air \(\left(T_{z}=\right.\) \(25^{\circ} \mathrm{C}\) ) for which a convection coefficient of \(6 \mathrm{~W} / \mathrm{m}^{2}+\mathrm{K}\) may be assumed. (a) During steady-state operation, an inner surfact temperature of \(50^{\circ} \mathrm{C}\) is maintained by enengy geneated within the reactor. What is the heat loss from the vessel? (b) If a 20-mm-thick layer of fiberglass insulation \((k=\) \(0.040 \mathrm{~W} / \mathrm{m}\) - K) is applied to the exterior of the ve sel and the rate of thermal energy generation is inchanged, what is the inner surface temperature of the vessel?

Short Answer

Expert verified
Heat loss without insulation is calculated using conduction and convection. With insulation, calculate temperature change using total thermal resistance.

Step by step solution

01

Understand the Problem

We have a spherical reactor with an inner diameter of 1 m, surrounded by a steel wall 10 mm thick and then by an ambient air. First, we need to calculate the heat loss when the inner surface is at 50°C without insulation and then find the new inner surface temperature when a 20 mm fiberglass layer is added.
02

Calculate the Heat Loss without Insulation

The heat loss, denoted as \( Q \), through the steel wall can be calculated using the formula for conductive heat transfer through a sphere: \[ Q = \frac{4 \pi k_{steel} r_{inner}^2 (T_{inner} - T_{outer})}{d_{steel}} \]where:- \( r_{inner} \) is the inner radius, 0.5 m,- \( T_{inner} \) is the inner surface temperature, 50°C,- \( T_{outer} \) is the outer surface temperature, assumed to be the air temperature, 25°C,- \( d_{steel} \) is the thickness, 0.01 m,- \( k_{steel} \) is the thermal conductivity, 17 W/m⋅K.
03

Calculate the Convection Heat Transfer

The formula for convection is:\[ Q = h \cdot A \cdot (T_{outer} - T_{ambient}) \]where:- \( h \) is the convection coefficient, 6 W/m²⋅K,- \( A \) is the outer surface area of the sphere, \( 4\pi r_{outer}^2 \);- \( T_{ambient} \) is ambient temperature, 25°C.
04

Calculate New Inner Surface Temperature with Insulation

After adding the fiberglass insulation, we first calculate the resistance of each layer of material: resistances due to steel, insulation, and convection. Then we sum them to find the total resistance:\[ R_{total} = R_{steel} + R_{insulation} + R_{conv} \]where:- \( R_{steel} = \frac{1}{4 \pi k_{steel} r_{inner}^2} \)- \( R_{insulation} = \frac{d_{insulation}}{4 \pi k_{insulation} r_{avg}^2} \)- \( R_{conv} = \frac{1}{h \cdot 4 \pi r_{outer}^2} \)where \( k_{insulation} \) is the thermal conductivity of insulation, 0.040 W/mK; \( d_{insulation} \) is insulation thickness, 0.02 m; \( r_{avg} \) is the average radius for insulation, \( r_{inner} + \frac{d_{steel} + d_{insulation}}{2} \). Solve for the temperature drop across these resistances to find \( T_{inner\_new} \).
05

Solve for Heat Loss and New Temperature

Substitute the known values into each formula, calculate the heat loss \( Q \) without insulation, then use the total resistance to solve for the temperature difference and find the new inner surface temperature after insulation is added.

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Key Concepts

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

Conduction in Spherical Coordinates
When dealing with heat conduction through a spherical structure, such as the walls of a spherical reactor, the heat transfer process requires a unique approach compared to flat surfaces. This is because the geometry of a sphere impacts how heat flows through its material.
Conduction in spherical coordinates takes into account the curvature of the sphere. The formula for this type of conduction is different from the one used for flat plates or cylinders. In a sphere, heat transfer is influenced by the radius and thickness of the material. This makes it essential to use the proper formula for calculating heat loss or gain.
The equation used for conduction in a sphere is:\[ Q = \frac{4\pi k r_{inner}^2 (T_{inner} - T_{outer})}{d} \]where:
  • "\( k \)" represents the thermal conductivity of the material, reflecting how well it conducts heat.
  • "\( r_{inner} \)" is the inner radius of the sphere, determining the starting point of measurement.
  • "\( T_{inner} \)" and "\( T_{outer} \)" are the temperatures of the inner and outer surfaces, respectively.
  • "\( d \)" is the thickness of the wall, a critical factor influencing heat transfer rate.
This method ensures you capture the variable thickness of the sphere and the radial change in temperature across it. Understanding how to apply this formula allows for accurate assessments of how heat is conducted through spherical walls.
Thermal Insulation
Thermal insulation is a crucial element when dealing with heat transfer in any structure, spherical or otherwise. Its primary role is to reduce the amount of heat transfer between the inside and outside of the vessel.
For the spherical reactor case, adding a layer of insulation, such as fiberglass, is an effective way to minimize heat loss and enhance energy efficiency. This additional layer traps heat, thereby slowing down the rate at which it escapes to the surrounding environment.
When insulation is applied, it's essential to calculate its impact through thermal resistance. Thermal resistance indicates how well a material resists heat conduction. For the insulation layer, it can be calculated as: \[ R_{insulation} = \frac{d_{insulation}}{4 \pi k_{insulation} r_{avg}^2} \]where:
  • "\( d_{insulation} \)" is the thickness of the insulation.
  • "\( k_{insulation} \)" is the thermal conductivity of the insulation material.
  • "\( r_{avg} \)" is the average radius of the insulation layer.
By considering the thermal resistance of the insulation, one can predict how much the inner surface temperature will be affected once the insulation is applied. This understanding is fundamental for ensuring the effectiveness of thermal insulation strategies.
Convection Heat Transfer
In thermal transfer processes involving gases or liquids, convection plays a significant role. It involves the transfer of heat between a solid surface and a fluid (like air), concerned primarily with boundary surfaces. The spherical reactor's external surface exemplifies such a situation.
Convection heat transfer depends significantly on the fluid's properties and the condition of the surface. For this spherical vessel, the convection coefficient \( h \) is provided, which determines the rate of heat loss to the environment.
The formula to calculate the heat transfer due to convection is given by: \[ Q = h \cdot A \cdot (T_{outer} - T_{ambient}) \]where:
  • "\( h \)" is the convection heat transfer coefficient, representing the heat transfer rate per unit area per degree of temperature difference.
  • "\( A \)" is the surface area of the sphere from which heat is being exchanged.
  • "\( T_{outer} \)" is the temperature of the outer surface.
  • "\( T_{ambient} \)" is the ambient or surrounding air temperature.
This approach allows for the estimation of thermal energy lost due to convection, crucial for maintaining energy efficiency and determining insulation requirements. Understanding both conduction and convection is key to effectively managing heat transfer in spherical systems.

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Most popular questions from this chapter

The walls of a refrigerator are typically constructed by sandwiching a layer of insulation between shect metal pancls. Consider a wall made from fiberglass insulation of thermal conductivity \(k_{1}=0.046 \mathrm{~W} / \mathrm{m}-\mathrm{K}\) and thickness \(I_{-}=50 \mathrm{~mm}\) and steel parels, each of thermal conductivity \(k_{p}=60\) W/m \(: \mathrm{K}\) and thickness \(L_{7}=3 \mathrm{~mm}\). If the wall separates refrigerated air at \(T_{x, j}=4^{\circ} \mathrm{C}\) from ambient air at \(T_{2,0}=25^{\circ} \mathrm{C}\), what is the heat gain per unit surface area? Cocfficicnts associated with natural convection at the inner and outer surfaces may be approximated as \(h_{y}=h_{g}=5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\).

The energy transferred from the anterior chamber of the eye through the cornea varies considerably depending on whether a contact lens is worm. Treat the eye as a splerical system and assume the system to be at steady state. The convection coefficient \(h_{e}\) is unchanged with and without the contact lens in place. The cornea and the lens cover one-third of the spherical surface area. Values of the parameters representing this situation are as follows: \(\begin{array}{ll}r_{1}=10.2 \mathrm{~mm} & r_{2}=12.7 \mathrm{~mm} \\\ r_{3}=16.5 \mathrm{~mm} & T_{-a}=21^{\circ} \mathrm{C} \\ T_{s 1}=37^{\circ} \mathrm{C} & k_{2}=0.80 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K} \\\ k_{1}=0.35 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K} & h_{n}=6 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K} \\ h_{4}=12 \mathrm{~W} / \mathrm{m}^{2}-\mathrm{K} & \end{array}\) (a) Construct the thermal circuits, labeling all potentials and flows for the systems excluding the contact lens and including the contact lens. Write resistance elements in terms of appropriate parameters. (b) Determine the heat loss from the anterior chamber with and without the contact lens in place. (c) Discuss the implication of your results.

A thin flat plate of length \(L\) thickness \(t\), and width \(W=L\) is thermally joined to two large heat sinks that are maintained at a temperature \(T_{e}\). The bottom of the plate is well insulated, while the net heat flux to the top surface of the plate is known to have a uniform value of \(q^{*}\) - (a) Derive the differential equation that determines the steady-state temperature distribution \(T(x)\) in the plate. (b) Solve the foregoing equation for the temperature distribution, and obtain an expression for the rate of heat transfer from the plate to the heat sinks.

An annular aluminum fin of rectangular profile is attached to a circular tube having an outside diameter of \(25 \mathrm{~mm}\) and a surface temperature of \(250^{\circ} \mathrm{C}\). The fin is \(1 \mathrm{~mm}\) thick and \(10 \mathrm{~mm}\) long, and the temperature and the convection coefficient associated with the adjoining fluid are \(25^{\circ} \mathrm{C}\) and \(25 \mathrm{~W} / \mathrm{m}^{2}\) + \(\mathrm{K}\), respectively. (a) What is the heat loss per fin? (b) If 200 such fins are spaced at 5-mm increments along the tube length, what is the heat loss per meter of tube length?

A thin electrical heater is wrapped around the outer surface of a long cylindrical tube whose inner surface is maintained at a temperature of \(5^{\circ} \mathrm{C}\). The tube wall has inner and outer radii of 25 and \(75 \mathrm{~mm}\), respectively, and a thermal conductivity of \(10 \mathrm{~W} / \mathrm{m}+\mathrm{K}\). The thermal contact resistance between the heater and the outer surface of the tube (per unit length of the tube) is \(R_{\text {Le }}^{\prime}=0.01 \mathrm{~m} \cdot \mathrm{K} / \mathrm{W}\). The outer surfice of the heater is exposed to a fluid with \(T_{n}=-10^{\circ} \mathrm{C}\) and a convecticn cocfficient of \(h=\) \(100 \mathrm{~W} / \mathrm{m}^{2}\) - K. Determine the heater power per unit length of tube required to maintain the heater in \(T_{e}=25^{\circ} \mathrm{C}\).

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