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A \(0.083\)-in-diameter electrical wire at \(90^{\circ} \mathrm{F}\) is covered by \(0.02\)-in-thick plastic insulation $\left(k=0.075 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}\right)$. The wire is exposed to a medium at \(50^{\circ} \mathrm{F}\), with a combined convection and radiation heat transfer coefficient of $2.5 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F}$. Determine if the plastic insulation on the wire will increase or decrease heat transfer from the wire. Answer: It helps

Short Answer

Expert verified
Answer: The plastic insulation on the electrical wire decreases the heat transfer from the wire.

Step by step solution

01

Calculate the surface area of the wire

The first thing we need to do is calculate the surface area of the wire. The surface area of the wire cylinder can be calculated using the formula \(A = 2\pi r L\), where \(r\) is the radius and \(L\) is the length of the wire. Since we don't have the length, we can assume a length of 1 ft and the result will be in terms of heat transfer per foot. The radius of the wire can be calculated by dividing the diameter by 2. $$r_{wire} = \frac{0.083}{2} = 0.0415\, \mathrm{ft}$$ Now, plug in the value of \(r\) into the formula: $$A = 2\pi(0.0415)(1) = 0.261\, \mathrm{ft}^2$$
02

Calculate the heat transfer rate without insulation

Now let's calculate the heat transfer rate without insulation. We use the formula for the heat transfer rate due to combined convection and radiation: $$q = hA(T_{wire} - T_{medium})$$ Here, \(h\) is the combined convection and radiation heat transfer coefficient, \(A\) is the surface area of the wire, \(T_{wire}\) is the temperature of the wire, and \(T_{medium}\) is the temperature of the surrounding medium. Plug in the values: $$q_{no\_insulation} = 2.5(0.261)(90 - 50) = 26.1\, \mathrm{Btu/h}$$
03

Calculate equivalent thermal resistance for insulation

To calculate the heat transfer rate with the insulation, we first need to calculate the equivalent thermal resistance for the insulation. The formula for the thermal resistance of insulation is: $$R_{insulation} = \frac{r_{outer} - r_{inner}}{2\pi k L}$$ where \(r_{inner}\) is the radius of the wire, \(r_{outer}\) is the radius of the insulated wire, and \(k\) is the thermal conductivity of the insulation material. First, compute \(r_{outer}\): $$r_{outer} = r_{inner} + 0.02 = 0.0415+0.02 = 0.0615\, \mathrm{ft}$$ Next, plug in the values into the formula: $$R_{insulation} = \frac{0.0615 - 0.0415}{2\pi (0.075)(1)} = 0.674\, \mathrm{h \cdot ft \cdot { }^{\circ}F/ Btu }$$
04

Calculate the heat transfer rate with insulation

To find the heat transfer rate with insulation, we'll use the formula: $$q_{insulation} = \frac{T_{wire} - T_{medium}}{R_{insulation} + \frac{1}{hA_{insulated}}}$$ First we need the surface area of the insulated wire: $$A_{insulated} = 2\pi(0.0615)(1) = 0.387\, \mathrm{ft}^2$$ Now plug in the values to solve for \(q_{insulation}\): $$q_{insulation} = \frac{90 - 50}{0.674 + \frac{1}{2.5(0.387)}} = 14.9\, \mathrm{Btu/h}$$
05

Compare the heat transfer rates with and without insulation

Now, compare the heat transfer rates: $$q_{no\_insulation} = 26.1\, \mathrm{Btu/h}$$ $$q_{insulation} = 14.9\, \mathrm{Btu/h}$$ Since the heat transfer rate without insulation (\(q_{no\_insulation}\)) is higher than the heat transfer rate with insulation (\(q_{insulation}\)), we can conclude that the plastic insulation on the wire decreases the heat transfer from the wire.

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Most popular questions from this chapter

Hot water $\left(c_{p}=4.179 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( flows through an 80 -m-long PVC \)(k=0.092 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\( pipe whose inner diameter is \)2 \mathrm{~cm}$ and outer diameter is \(2.5 \mathrm{~cm}\) at a rate of $1 \mathrm{~kg} / \mathrm{s}\(, entering at \)40^{\circ} \mathrm{C}$. If the entire interior surface of this pipe is maintained at \(35^{\circ} \mathrm{C}\) and the entire exterior surface at \(20^{\circ} \mathrm{C}\), the outlet temperature of water is (a) \(35^{\circ} \mathrm{C}\) (b) \(36^{\circ} \mathrm{C}\) (c) \(37^{\circ} \mathrm{C}\) (d) \(38^{\circ} \mathrm{C}\) (e) \(39^{\circ} \mathrm{C}\)

A 3-m-diameter spherical tank containing some radioactive material is buried in the ground \((k=1.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\). The distance between the top surface of the tank and the ground surface is $4 \mathrm{~m}$. If the surface temperatures of the tank and the ground are \(140^{\circ} \mathrm{C}\) and \(15^{\circ} \mathrm{C}\), respectively, determine the rate of heat transfer from the tank.

Circular cooling fins of diameter \(D=1 \mathrm{~mm}\) and length $L=30 \mathrm{~mm}\(, made of copper \)(k=380 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$, are used to enhance heat transfer from a surface that is maintained at temperature \(T_{s 1}=132^{\circ} \mathrm{C}\). Each rod has one end attached to this surface \((x=0)\), while the opposite end \((x=L)\) is joined to a second surface, which is maintained at \(T_{s 2}=0^{\circ} \mathrm{C}\). The air flowing between the surfaces and the rods is also at \(T_{\infty}=0^{\circ} \mathrm{C}\). and the convection coefficient is $h=100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. (a) Express the function \(\theta(x)=T(x)-T_{\infty}\) along a fin, and calculate the temperature at \(x=L / 2\). (b) Determine the rate of heat transferred from the hot surface through each fin and the fin effectiveness. Is the use of fins justified? Why? (c) What is the total rate of heat transfer from a \(10-\mathrm{cm}\) by \(10-\mathrm{cm}\) section of the wall, which has 625 uniformly distributed fins? Assume the same convection coefficient for the fin and for the unfinned wall surface.

A 5 -m-diameter spherical tank is filled with liquid oxygen $\left(\rho=1141 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=1.71 \mathrm{~kJ} / \mathrm{kg} \cdot{ }^{\circ} \mathrm{C}\right)\( at \)-184^{\circ} \mathrm{C}$. It is observed that the temperature of oxygen increases to \(-183^{\circ} \mathrm{C}\) in a 144-hour period. The average rate of heat transfer to the tank is (a) \(124 \mathrm{~W}\) (b) \(185 \mathrm{~W}\) (c) \(246 \mathrm{~W}\) (d) \(348 \mathrm{~W}\) (e) \(421 \mathrm{~W}\)

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.

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