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Jakob (1949) suggests the following correlation be used for square tubes in a liquid crossflow situation: $$ \mathrm{Nu}=0.102 \mathrm{Re}^{0.625} \mathrm{Pr}^{1 / 3} $$ Water \((k=0.61 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \mathrm{Pr}=6)\) flows across a \(1-\mathrm{cm}-\) square tube with a Reynolds number of 10,000 . The convection heat transfer coefficient is (a) \(5.7 \mathrm{~kW} / \mathrm{m}^{2} \cdot \mathrm{K}\) (b) \(8.3 \mathrm{~kW} / \mathrm{m}^{2} \cdot \mathrm{K}\) (c) \(11.2 \mathrm{~kW} / \mathrm{m}^{2} \cdot \mathrm{K}\) (d) \(15.6 \mathrm{~kW} / \mathrm{m}^{2} \cdot \mathrm{K}\) (e) \(18.1 \mathrm{~kW} / \mathrm{m}^{2} \cdot \mathrm{K}\)

Short Answer

Expert verified
Based on the given values and calculations, the convection heat transfer coefficient (h) should be approximately 4.54 kW/(m²∙K). However, none of the provided options match this result. It's possible that there is an error in the given options, or an incorrect version of Jakob's correlation is being used.

Step by step solution

01

Substitute given values into Jakob's correlation for the Nusselt number

Using the given values, we substitute Re = 10000 and Pr = 6 into Jakob's correlation, which is: $$ \mathrm{Nu} = 0.102 \times \mathrm{Re}^{0.625} \times \mathrm{Pr}^{1/3} $$ We get: $$ \mathrm{Nu} = 0.102 \times (10000)^{0.625} \times (6)^{1/3} $$
02

Calculate the Nusselt number value

Perform the necessary operations to calculate the Nusselt number: $$ \mathrm{Nu} \approx 74.154 $$
03

Use the Nusselt number definition relation to find the convection heat transfer coefficient

We know that the Nusselt number can be defined as the ratio of the convection heat transfer coefficient (h) to the thermal conductivity (k) multiplied by the characteristic length (L). In this case, L = 0.01m (1 cm), and k = 0.61 W/(m∙K). The formula for Nusselt number is: $$ \mathrm{Nu} = \frac{hL}{k} $$ Substitute the values: $$ 74.154 = \frac{h \times 0.01}{0.61} $$
04

Solve for the convection heat transfer coefficient

Rearrange the equation and solve for h: $$ h = \frac{74.154 \times 0.61}{0.01} \approx 4535.4 \, \mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K} $$ Notice that, by converting the answer to kW/(m²∙K), we get: $$ h \approx 4.54 \, \mathrm{kW} / \mathrm{m}^{2} \cdot \mathrm{K} $$ However, none of the provided options match this result. The correct answer should be 4.54 kW/(m²∙K). It's possible that there is an error in the given options, or an incorrect version of Jakob's correlation is being used.

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Most popular questions from this chapter

The outer surface of an engine is situated in a place where oil leakage can occur. When leaked oil comes in contact with a hot surface that has a temperature above its autoignition temperature, the oil can ignite spontaneously. Consider an engine cover that is made of a stainless steel plate with a thickness of \(1 \mathrm{~cm}\) and a thermal conductivity of $14 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. The inner surface of the engine cover is exposed to hot air with a convection heat transfer coefficient of $7 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$ at a temperature of \(333^{\circ} \mathrm{C}\). The engine outer surface is cooled by air blowing in parallel over the \(2-\mathrm{m}\)-long surface at $7.1 \mathrm{~m} / \mathrm{s}\(, in an environment where the ambient air is at \)60^{\circ} \mathrm{C}$. To prevent fire hazard in the event of an oil leak on the engine cover, a layer of thermal barrier coating \((\mathrm{TBC})\) with a thermal conductivity of \(1.1 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) is applied on the engine cover outer surface. Would a TBC layer with a thickness of $4 \mathrm{~mm}\( in conjunction with \)7.1 \mathrm{~m} / \mathrm{s}$ air cooling be sufficient to keep the engine cover surface from going above $180^{\circ} \mathrm{C}$ to prevent fire hazard? Evaluate the air properties at \(120^{\circ} \mathrm{C}\).

A thermocouple with a spherical junction diameter of \(1 \mathrm{~mm}\) is used for measuring the temperature of a hydrogen gas stream. The properties of the thermocouple junction are $k=35 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \rho=8500 \mathrm{~kg} / \mathrm{m}^{3}\(, and \)c_{p}=320 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$. The hydrogen gas, behaving as an ideal gas at \(1 \mathrm{~atm}\), has a free-stream temperature of \(200^{\circ} \mathrm{C}\). If the initial temperature of the thermocouple junction is $10^{\circ} \mathrm{C}$, evaluate the time for the thermocouple to register 99 percent of the initial temperature difference at different free-stream velocities of the hydrogen gas. Using appropriate software, perform the evaluation by varying the free-stream velocity from 1 to \(100 \mathrm{~m} / \mathrm{s}\). Then, plot the thermocouple response time and the convection heat transfer coefficient as a function of free-stream velocity. Hint: Use the lumped system analysis to determine the time required for the thermocouple to register 99 percent of the initial temperature difference (verify the application of this method to this problem).

A thin, square, flat plate has \(1.2 \mathrm{~m}\) on each side. Air at \(10^{\circ} \mathrm{C}\) flows over the top and bottom surfaces of a very rough plate in a direction parallel to one edge, with a velocity of $48 \mathrm{~m} / \mathrm{s}$. The surface of the plate is maintained at a constant temperature of \(54^{\circ} \mathrm{C}\). The plate is mounted on a scale that measures a drag force of \(1.5 \mathrm{~N}\). Determine the total heat transfer rate from the plate to the air.

Air at \(20^{\circ} \mathrm{C}\) flows over a 4-m-long and 3 -m-wide surface of a plate whose temperature is \(80^{\circ} \mathrm{C}\) with a velocity of $5 \mathrm{~m} / \mathrm{s}$. The rate of heat transfer from the surface is (a) \(7383 \mathrm{~W}\) (b) \(8985 \mathrm{~W}\) (c) \(11,231 \mathrm{~W}\) (d) 14,672 W (e) 20,402 W (For air, use $k=0.02735 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \operatorname{Pr}=0.7228, \nu=1.798 \times\( \)\left.10^{-5} \mathrm{~m}^{2} / \mathrm{s}\right)$

What is drag? What causes it? Why do we usually try to minimize it?

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