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An engineer who is working on the heat transfer analysis of a house in English units needs the convection heat transfer coefficient on the outer surface of the house. But the only value he can find from his handbooks is $14 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, which is in SI units. The engineer does not have a direct conversion factor between the two unit systems for the convection heat transfer coefficient. Using the conversion factors between \(\mathrm{W}\) and \(\mathrm{Btu} / \mathrm{h}, \mathrm{m}\) and \(\mathrm{ft}\), and \({ }^{\circ} \mathrm{C}\) and \({ }^{\circ} \mathrm{F}\), express the given convection heat transfer coefficient in Btu/h \(\mathrm{ft}^{2}{ }^{\circ} \mathrm{F}\). Answer: \(2.47\) Btu/h $\cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}$

Short Answer

Expert verified
Question: Convert the given convection heat transfer coefficient \(14 \mathrm{~W} / \mathrm{m}^2 \cdot \mathrm{K}\) to \(\mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^2 \cdot { }^{\circ} \mathrm{F}\). Answer: The equivalent convection heat transfer coefficient is approximately \(2.47 \mathrm{Btu/h} \cdot \mathrm{ft}^2{ }^{\circ} \mathrm{F}\).

Step by step solution

01

Write down the given convection heat transfer coefficient and conversion factors

The given convection heat transfer coefficient is \(14 \mathrm{~W} / \mathrm{m}^2 \cdot \mathrm{K}\). We are given the following conversion factors: 1. Watts (W) to Btu/h: \(1\mathrm{~W} = 3.412\mathrm{~Btu/h}\) 2. Meters (m) to feet (ft): \(1\mathrm{~m} = 3.281\mathrm{~ft}\) 3. Kelvin (K) to Fahrenheit (F): \(1\mathrm{~K} = 1.8 { }^{\circ} \mathrm{F}\)
02

Multiply the convection heat transfer coefficient value with conversion factors

Using the given conversion factors, we can convert each unit in the convection heat transfer coefficient individually. \(\frac{14\mathrm{~W}}{\mathrm{m}^2 \cdot \mathrm{K}} \times \frac{3.412\mathrm{~Btu/h}}{1\mathrm{~W}} \times \frac{1\mathrm{~m}}{3.281\mathrm{~ft}} \times \frac{1\mathrm{~m}}{3.281\mathrm{~ft}} \times \frac{1.8 { }^{\circ} \mathrm{F}}{1\mathrm{~K}}\)
03

Simplify the expression

Now, we will cancel out the units and simplify the expression: \(\frac{14\times 3.412\mathrm{~Btu/h}}{3.281^2 \mathrm{ft}^2 \cdot 1.8 { }^{\circ} \mathrm{F}}\)
04

Calculate the equivalent convection heat transfer coefficient

Performing the calculation, we get: \(\frac{47.768\mathrm{~Btu/h}}{35.7254\mathrm{~ft}^2 \times { }^{\circ} 1.8\mathrm{F}} = \frac{47.768}{64.3057} \mathrm{Btu/h} \cdot \mathrm{ft}^2{ }^{\circ} \mathrm{F} \approx 2.47 \mathrm{Btu/h} \cdot \mathrm{ft}^2{ }^{\circ} \mathrm{F}\) So, the convection heat transfer coefficient in Btu/h \(\cdot \mathrm{ft}^2{ }^{\circ} \mathrm{F}\) is approximately \(2.47\) Btu/h \(\cdot \mathrm{ft}^2{ }^{\circ} \mathrm{F}\).

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Most popular questions from this chapter

The critical heat flux (CHF) is a thermal limit at which a boiling crisis occurs whereby an abrupt rise in temperature causes overheating on a fuel rod surface that leads to damage. A cylindrical fuel rod \(2 \mathrm{~cm}\) in diameter is encased in a concentric tube and cooled by water. The fuel generates heat uniformly at a rate of \(150 \mathrm{MW} / \mathrm{m}^{3}\). The average temperature of the cooling water, sufficiently far from the fuel rod, is \(80^{\circ} \mathrm{C}\). The operating pressure of the cooling water is such that the surface temperature of the fuel rod must be kept below \(300^{\circ} \mathrm{C}\) to prevent the cooling water from reaching the critical heat flux. Determine the necessary convection heat transfer coefficient to prevent the critical heat flux from occurring.

A \(4-\mathrm{m} \times 5-\mathrm{m} \times 6-\mathrm{m}\) room is to be heated by one ton \((1000 \mathrm{~kg})\) of liquid water contained in a tank placed in the room. The room is losing heat to the outside at an average rate of $10,000 \mathrm{~kJ} / \mathrm{h}\(. The room is initially at \)20^{\circ} \mathrm{C}$ and \(100 \mathrm{kPa}\) and is maintained at an average temperature of \(20^{\circ} \mathrm{C}\) at all times. If the hot water is to meet the heating requirements of this room for a \(24-\mathrm{h}\) period, determine the minimum temperature of the water when it is first brought into the room. Assume constant specific heats for both air and water at room temperature. Answer: 77.4 \(\mathrm{C}\)

Heat treatment of metals is commonly done using electrically heated draw batch furnaces. Consider a furnace that is situated in a room with a surrounding air temperature of \(30^{\circ} \mathrm{C}\) and an average convection heat transfer coefficient of \(15 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The outer furnace front surface has an emissivity of \(0.7\), and the inside surface is subjected to a heat flux of \(5 \mathrm{~kW} / \mathrm{m}^{2}\). To ensure safety and avoid thermal burns to people working around the furnace, the outer front surface of the furnace should be kept below \(50^{\circ} \mathrm{C}\). Based on the information given about the furnace, does the furnace front surface require insulation to prevent thermal burns?

What is stratification? Is it more likely to occur at places with low ceilings or places with high ceilings? How does it cause thermal discomfort for a room's occupants? How can stratification be prevented?

The inner and outer surfaces of a \(4-\mathrm{m} \times 7-\mathrm{m}\) brick wall of thickness \(30 \mathrm{~cm}\) and thermal conductivity $0.69 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\( are maintained at temperatures of \)20^{\circ} \mathrm{C}\( and \)5^{\circ} \mathrm{C}$, respectively. Determine the rate of heat transfer through the wall in W.

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