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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 \(20 \mathrm{~W} / \mathrm{m}^{2}\). \(\mathrm{K}\). 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. Answers: $1.32 \mathrm{~m}, 530 \mathrm{~W} / \mathrm{m}$

Short Answer

Expert verified
Answer: The width of the square concrete bar is approximately \(1.32 \mathrm{~m}\), and the rate of heat loss per meter length is approximately \(530 \mathrm{~W} / \mathrm{m}\).

Step by step solution

01

Determine the outer surface temperature of the concrete bar.

We need to maintain a \(5^{\circ}C\) temperature difference between the outer surface of the square concrete bar and the ambient air, which has a temperature of \(-5^{\circ}C\). Add this temperature difference to the ambient air temperature to get the outer surface temperature of the concrete bar: $$ T_{outer} = T_{ambient} + \Delta T = (-5) + 5 = 0 ^{\circ}C $$
02

Determine the temperature difference across the concrete.

We need to find the temperature difference from the inner surface of the square concrete to the outer surface. The inner surface's temperature equals the tube's temperature, that is \(120^{\circ}C\). We have already calculated the outer surface temperature as \(0^{\circ}C\). We can find the temperature difference by subtracting the outer surface temperature from the inner surface temperature: $$ \Delta T_{concrete} = T_{inner} - T_{outer} = 120 - 0 = 120 ^{\circ}C $$
03

Apply the conduction equation.

To obtain the width of the square concrete bar, apply the conduction equation, with \(Q_{cond}\), the conducted heat per meter, as follows: $$ Q_{cond} = k \cdot A \cdot \frac{\Delta T_{concrete}}{L} $$ Where \(k\) is the concrete's thermal conductivity, \(A\) is the cross-sectional area of the square bar, and \(L\) is the required width.
04

Calculate the convection heat transfer.

The heat transfer through convection is given by: $$ Q_{conv} = h \cdot A_{s} \cdot \Delta T $$ Where \(h\) is the convection heat transfer coefficient, \(A_{s}\) is the surface area of the concrete bar exposed to air, and \(\Delta T\) is the temperature difference between the outer surface of the square concrete bar and the ambient air. The conduction heat transfer must be equal to the convection heat transfer, so: $$ Q_{cond} = Q_{conv} $$
05

Find the width of the square concrete bar.

Rearrange the combined heat transfer equation to solve for the width, \(L\): $$ L = \frac{k \cdot A \cdot \Delta T_{concrete}}{h \cdot A_{s} \cdot \Delta T} $$
06

Calculate the rate of heat loss per meter.

The rate of heat loss per meter is the conduction heat transfer per meter, \(Q_{cond}\). With the calculated width of the square concrete bar, \(L\), determine the rate of heat loss per meter: $$ Q_{cond} = k \cdot A \cdot \frac{\Delta T_{concrete}}{L} $$ Using the given values, \(k=1.7 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), \(h=20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), tube diameter \(D = 127 \mathrm{~mm}\), and ambient air temperature \(T_{ambient} = -5^{\circ}C\), we can calculate the width of the square concrete bar and the rate of heat loss per meter length: Width \(L \approx 1.32 \mathrm{~m}\) and heat loss per meter \(Q_{cond} \approx 530 \mathrm{~W} / \mathrm{m}\).

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Most popular questions from this chapter

An 8-m-internal-diameter spherical tank made of \(1.5\)-cm-thick stainless steel \((k=15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) is used to store iced water at \(0^{\circ} \mathrm{C}\). The tank is located in a room whose temperature is \(25^{\circ} \mathrm{C}\). The walls of the room are also at $25^{\circ} \mathrm{C}$. The outer surface of the tank is black (emissivity \(\varepsilon=1\) ), and heat transfer between the outer surface of the tank and the surroundings is by natural convection and radiation. The convection heat transfer coefficients at the inner and the outer surfaces of the tank are $80 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\( and \)10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(, respectively. Determine \)(a)$ the rate of heat transfer to the iced water in the tank and \((b)\) the amount of ice at \(0^{\circ} \mathrm{C}\) that melts during a 24 -h period. The heat of fusion of water at atmospheric pressure is \(h_{i f}=333.7 \mathrm{~kJ} / \mathrm{kg}\).

A \(0.4-\mathrm{cm}\)-thick, 12 -cm-high, and \(18-\mathrm{cm}\)-long circuit board houses 80 closely spaced logic chips on one side, each dissipating $0.04 \mathrm{~W}$. The board is impregnated with copper fillings and has an effective thermal conductivity of $30 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. All the heat generated in the chips is conducted across the circuit board and is dissipated from the back side of the board to a medium at \(40^{\circ} \mathrm{C}\), with a heat transfer coefficient of $52 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. (a) Determine the temperatures on the two sides of the circuit board. (b) Now a \(0.2-\mathrm{cm}\)-thick, \(12-\mathrm{cm}\)-high, and \(18-\mathrm{cm}\)-long aluminum plate $(k=237 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\( with \)8642 \cdot \mathrm{cm}-$ long aluminum pin fins of diameter \(0.25 \mathrm{~cm}\) is attached to the back side of the circuit board with a \(0.02-\mathrm{cm}\)-thick epoxy adhesive \((k=1.8 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\). Determine the new temperatures on the two sides of the circuit board.

Two very long, slender rods of the same diameter and length are given. One rod (Rod 1) is made of aluminum and has a thermal conductivity $k_{1}=200 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$, but the thermal conductivity of Rod \(2, k_{2}\), is not known. To determine the thermal conductivity of Rod 2 , both rods at one end are thermally attached to a metal surface which is maintained at a constant temperature \(T_{b}\). Both rods are losing heat by convection, with a convection heat transfer coefficient \(h\) into the ambient air at \(T_{\infty}\). The surface temperature of each rod is measured at various distances from the hot base surface. The measurements reveal that the temperature of the aluminum rod (Rod 1) at \(x_{1}=40 \mathrm{~cm}\) from the base is the same as that of the rod of unknown thermal conductivity (Rod 2) at \(x_{2}=20 \mathrm{~cm}\) from the base. Determine the thermal conductivity \(k_{2}\) of the second rod \((\mathrm{W} / \mathrm{m} \cdot \mathrm{K})\).

Hot- and cold-water pipes \(12 \mathrm{~m}\) long run parallel to each other in a thick concrete layer. The diameters of both pipes are \(6 \mathrm{~cm}\), and the distance between the centerlines of the pipes is \(40 \mathrm{~cm}\). The surface temperatures of the hot and cold pipes are \(60^{\circ} \mathrm{C}\) and \(15^{\circ} \mathrm{C}\), respectively. Taking the thermal conductivity of the concrete to be \(k=0.75 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), determine the rate of heat transfer between the pipes.

A room at \(20^{\circ} \mathrm{C}\) air temperature is losing heat to the outdoor air at \(0^{\circ} \mathrm{C}\) at a rate of \(1000 \mathrm{~W}\) through a \(2.5\)-m-high and 4-m-long wall. Now the wall is insulated with \(2-\mathrm{cm}\)-thick insulation with a conductivity of $0.02 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. Determine the rate of heat loss from the room through this wall after insulation. Assume the heat transfer coefficients on the inner and outer surfaces of the wall, the room air temperature, and the outdoor air temperature remain unchanged. Also, disregard radiation. (a) \(20 \mathrm{~W}\) (b) \(561 \mathrm{~W}\) (c) \(388 \mathrm{~W}\) (d) \(167 \mathrm{~W}\) (e) \(200 \mathrm{~W}\)

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