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Consider a tube for transporting steam that is not centered properly in a cylindrical insulation material (k= 0.73 W/mK). The tube diameter is D1=20 cm and the insulation diameter is D2=40 cm. The distance between the center of the tube and the center of the insulation is z=5 mm. If the surface of the tube maintains a temperature of 100C and the outer surface temperature of the insulation is constant at 30C, determine the rate of heat transfer per unit length of the tube through the insulation.

Short Answer

Expert verified
Answer: The rate of heat transfer per unit length of the tube through the insulation is approximately 466.67 W/m.

Step by step solution

01

Calculate the temperature drop through the insulation

The temperature difference between the inner surface of the tube and the outer surface of the insulation is the driving force for heat transfer. We can calculate it as follows: ΔT=T1T2=100C30C=70C
02

Calculate the equivalent thermal resistance of the insulation

The insulation is not centered on the pipe; thus, the heat flow in the insulation is not radial. However, since its diameter (D2) is large compared to the pipe diameter (D1), it is reasonable to approximate the flow as radial. We can calculate the equivalent thermal resistance (Rth) of the insulation using the equation: Rth=ln(D2D1)2πk Using the given values, we get: Rth=ln(0.4 m0.2 m)2π(0.73 W /mK)=ln(2)4.581=0.150 mK/W
03

Calculate the rate of heat transfer per unit length

Now that we have the equivalent thermal resistance and the temperature drop, we can calculate the rate of heat transfer per unit length (q) using Fourier's Law: q=ΔTRth Substituting the values, we get: q=70C0.150 mK/W=466.67 W/m Thus, the rate of heat transfer per unit length of the tube through the insulation is approximately 466.67 W/m.

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Key Concepts

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

Fourier's Law
Fourier's Law is the fundamental principle that governs heat conduction. It states that the rate at which heat energy is transferred through a material is directly proportional to the negative of the temperature gradient and the cross-sectional area through which heat is flowing, and is inversely proportional to the material's thickness. In simpler terms, heat flows from hot regions to cold ones, and the flow rate increases with larger temperature differences and cross-sectional areas, but decreases with greater distances.

Mathematically, Fourier's Law for one-dimensional heat flow can be expressed as: q=kAdTdx where q is the heat transfer rate, k is the thermal conductivity of the material, A is the cross-sectional area perpendicular to the heat flow, and dTdx is the temperature gradient along the direction of heat flow. In the context of the textbook exercise, this law helps us calculate the heat transfer rate per unit length once we know the thermal resistance and temperature difference.
Thermal Resistance
Thermal resistance, analogous to electrical resistance, is a measure of a material's ability to resist the flow of heat. When considering heat transfer through a material, thermal resistance describes how well the material insulates against the movement of heat. The higher the thermal resistance, the slower the heat flows through the material, and vice versa.

Thermal resistance can be calculated using the formula: Rth=ΔxkA where Rth is the thermal resistance, Δx is the thickness of the material, k is the thermal conductivity, and A is the cross-sectional area. In practice, when dealing with non-uniform geometries like the insulation in the exercise, we make reasonable approximations to simplify calculations. Here, a radial heat flow assumption allows us to represent the thermal resistance of cylindrical insulation as an equivalent resistance, which is a crucial step in determining the heat transfer rate.
Radial Heat Flow
Radial heat flow refers to the movement of heat in a radial direction outward or inward through a cylindrical or spherical object. This type of heat flow is prevalent in systems where there is a non-uniform geometry such as pipes or tubes.

In the case of radial heat flow through a cylindrical object, the thermal resistance is different from that in one-dimensional heat flow situations, due to the varying cross-sectional area as heat moves radially. The formula to calculate thermal resistance for radial heat flow in a cylinder is: Rth=ln(r2r1)2πkL where r1 and r2 are the inner and outer radii of the cylindrical layer through which heat is flowing, k is the thermal conductivity, and L is the length of the cylinder. This concept is crucial in the step-by-step solution provided, where approximating the insulation as a radially conducting layer allows us to calculate the heat transfer rate using the modified equation for thermal resistance in cylindrical coordinates.

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Most popular questions from this chapter

Two 3-m-long and 0.4cm-thick cast iron (k= 52 W/mK) steam pipes of outer diameter 10 cm are connected to each other through two 1 -cm-thick flanges of outer diameter 20 cm. The steam flows inside the pipe at an average temperature of 200C with a heat transfer coefficient of 180 W/m2K. The outer surface of the pipe is exposed to an ambient at 12C, with a heat transfer coefficient of 25 W/m2K. (a) Disregarding the flanges, determine the average outer surface temperature of the pipe. (b) Using this temperature for the base of the flange and treating the flanges as the fins, determine the fin efficiency and the rate of heat transfer from the flanges. (c) What length of pipe is the flange section equivalent to for heat transfer purposes?

A plane wall surface at 200C is to be cooled with aluminum pin fins of parabolic profile with blunt tips. Each fin has a length of 25 mm and a base diameter of 4 mm. The fins are exposed to an ambient air condition of 25C and the heat transfer coefficient is 45 W/m2K. If the thermal conductivity of the fins is 230 W/mK, determine the heat transfer rate from a single fin and the increase in the rate of heat transfer per m2 surface area as a result of attaching fins. Assume there are 100 fins per m2 surface area.

Consider the conditions of Example 314 in the text except that the ambient air is at a temperature of 30C. A person with skin/fat layer thickness of 0.003 m is doing vigorous exercise which raises the metabolic heat generation rate from 700 to 7000 W/m3 over a period of time. Calculate the perspiration rate required in lit/s so as to maintain the skin temperature at 34C. Use the perspiration properties to be the same as that of liquid water at the average surface skin temperature of 35.5C.

One wall of a refrigerated warehouse is 10.0-m-high and 5.0-m-wide. The wall is made of three layers: 1.0-cm-thick aluminum (k=200 W/mK),8.0-cm-thick fibreglass (k= 0.038 W/mK), and 3.0cm thick gypsum board (k= 0.48 W/mK). The warehouse inside and outside temperatures are 10C and 20C, respectively, and the average value of both inside and outside heat transfer coefficients is 40 W/m2K. (a) Calculate the rate of heat transfer across the warehouse wall in steady operation. (b) Suppose that 400 metal bolts (k=43 W/mK), each 2.0 cm in diameter and 12.0 cm long, are used to fasten (i.e., hold together) the three wall layers. Calculate the rate of heat transfer for the "bolted" wall. (c) What is the percent change in the rate of heat transfer across the wall due to metal bolts?

Hot- and cold-water pipes 8 m long run parallel to each other in a thick concrete layer. The diameters of both pipes are 5 cm, and the distance between the centerlines of the pipes is 40 cm. The surface temperatures of the hot and cold pipes are 60C and 15C, respectively. Taking the thermal conductivity of the concrete to be k=0.75 W/mK, determine the rate of heat transfer between the pipes.

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