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Water at an average temperature of \(180^{\circ} \mathrm{F}\) and an average velocity of \(4 \mathrm{ft} / \mathrm{s}\) flows through a thin-walled \(\frac{3}{4}\)-indiameter tube. The water is cooled by air that flows across the tube with a velocity of \(12 \mathrm{ft} / \mathrm{s}\) at an average temperature of \(80^{\circ} \mathrm{F}\). Determine the overall heat transfer coefficient.

Short Answer

Expert verified
Use the provided steps in the solution to determine the heat transfer coefficients for the fluids, dimensions of the tube, and calculate the overall heat transfer coefficient.

Step by step solution

01

Compute the heat transfer coefficient of the water

To compute the heat transfer coefficient of the water, we can use the Sieder-Tate equation in the form: \$ h_w = k_w * Nu \$, where \$h_w\$ is the heat transfer coefficient of the water, \$k_w\$ is the thermal conductivity of the water, and \$Nu\$ is the dimensionless Nusselt number. The thermal conductivity of the water at the given average temperature will have to be found from a reference table or a correlation. Similarly, the Nusselt number depends on the dimensionless Reynolds and Prandtl numbers. Use available correlations to compute these dimensionless numbers and the corresponding heat transfer coefficient for water.
02

Compute the heat transfer coefficient of the air

We can also compute the heat transfer coefficient of the air using the same Sieder-Tate equation for air: \$ h_a = k_a * Nu \$, where \$h_a\$ is the heat transfer coefficient of the air, \$k_a\$ is the thermal conductivity of the air, and \$Nu\$ is the Nusselt number for air. Again, the thermal conductivity of the air at the given average temperature can be found from reference tables or correlations. Similarly, use appropriate correlations for determining the dimensionless numbers and corresponding heat transfer coefficient for air.
03

Calculate the overall heat transfer coefficient

The overall heat transfer coefficient (\$ U \$) can be found using the following equation for a concentric pipe arrangement: \$ \frac{1}{U} = \frac{1}{h_w} + \frac{D_o}{D_i*h_a} \$, where \$D_i\$ is the inner diameter of the tube, and \$D_o\$ is the outer diameter of the tube (assumed to be the same as the inner diameter in a thin-walled tube). Using the heat transfer coefficients obtained in Step 1 and Step 2, along with the given diameter for the tube, we can calculate the overall heat transfer coefficient. Calculate the overall heat transfer coefficient using the values obtained in the previous steps and the given tube diameter, and that will be the final answer.

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Most popular questions from this chapter

Consider the flow of saturated steam at \(270.1 \mathrm{kPa}\) that flows through the shell side of a shell-and-tube heat exchanger while the water flows through four tubes of diameter \(1.25 \mathrm{~cm}\) at a rate of $0.25 \mathrm{~kg} / \mathrm{s}$ through each tube. The water enters the tubes of the heat exchanger at \(20^{\circ} \mathrm{C}\) and exits at $60^{\circ} \mathrm{C}$. Due to the heat exchange with the cold fluid, steam is condensed on the tube's external surface. The convection heat transfer coefficient on the steam side is \(1500 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), while the fouling resistance for the steam and water may be taken as \(0.00015\) and \(0.0001 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\), respectively. Using the \(\mathrm{NTU}\) method, determine \((a)\) effectiveness of the heat exchanger, (b) length of the tube, and (c) rate of steam condensation.

Write an interactive computer program that will give the effectiveness of a heat exchanger and the outlet temperatures of both the hot and cold fluids when the types of fluids, the inlet temperatures, the mass flow rates, the heat transfer surface area, the overall heat transfer coefficient, and the type of heat exchanger are specified. The program should allow the user to select from the fluids water, engine oil, glycerin, ethyl alcohol, and ammonia. Assume constant specific heats at about room temperature.

A single-pass crossflow heat exchanger with both fluids unmixed has water entering at \(16^{\circ} \mathrm{C}\) and exiting at \(33^{\circ} \mathrm{C}\), while oil $\left(c_{p}=1.93 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right.\( and \)\left.\rho=870 \mathrm{~kg} / \mathrm{m}^{3}\right)$ flowing at \(0.19 \mathrm{~m}^{3} / \mathrm{min}\) enters at $38^{\circ} \mathrm{C}\( and exits at \)29^{\circ} \mathrm{C}$. If the surface area of the heat exchanger is \(20 \mathrm{~m}^{2}\), determine \((a)\) the NTU value and \((b)\) the value of the overall heat transfer coefficient.

Consider a double-pipe heat exchanger with a tube diameter of $10 \mathrm{~cm}$ and negligible tube thickness. The total thermal resistance of the heat exchanger was calculated to be \(0.025 \mathrm{k} / \mathrm{W}\) when it was first constructed. After some prolonged use, fouling occurs at both the inner and outer surfaces with the fouling factors $0.00045 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\( and \)0.00015 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}$, respectively. The percentage decrease in the rate of heat transfer in this heat exchanger due to fouling is (a) \(2.3 \%\) (b) \(6.8 \%\) (c) \(7.1 \%\) (d) \(7.6 \%\) (e) \(8.5 \%\)

A shell-and-tube heat exchanger with two shell passes and eight tube passes is used to heat ethyl alcohol $\left(c_{p}=2670 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( in the tubes from \)25^{\circ} \mathrm{C}\( to \)70^{\circ} \mathrm{C}\( at a rate of \)2.1 \mathrm{~kg} / \mathrm{s}$. The heating is to be done by water $\left(c_{p}=4190 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( that enters the shell at \)95^{\circ} \mathrm{C}$ and leaves at \(60^{\circ} \mathrm{C}\). If the overall heat transfer coefficient is $800 \mathrm{~W} / \mathrm{m}^{2} . \mathrm{K}$, determine the heat transfer surface area of the heat exchanger using \((a)\) the LMTD method and \((b)\) the \(\varepsilon-\mathrm{NTU}\) method. Answer: \((a) 11.4 \mathrm{~m}^{2}\)

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