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Engine oil $\left(c_{p}=2100 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( is to be heated from \)20^{\circ} \mathrm{C}\( to \)60^{\circ} \mathrm{C}\( at a rate of \)0.3 \mathrm{~kg} / \mathrm{s}$ in a 2 -cm-diameter thin-walled copper tube by condensing steam outside at a temperature of \(130^{\circ} \mathrm{C}\) $\left(h_{f /}=2174 \mathrm{~kJ} / \mathrm{kg}\right)\(. For an overall heat transfer coefficient of \)650 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, determine the rate of heat transfer and the length of the tube required to achieve it. Answers: $25.2 \mathrm{~kW}, 7.0 \mathrm{~m}$

Short Answer

Expert verified
Answer: The rate of heat transfer is 25.2 kW, and the required tube length is 7.0 meters.

Step by step solution

01

Determine the heat required to raise the oil temperature.

Using the given information, we first need to calculate the heat required to raise the temperature of the oil from 20°C to 60°C using the formula: \(Q = mc_p\Delta T\) where \(Q\) = heat required in J \(m = 0.3 kg/s\) = mass flow rate of oil \(c_p = 2100 J/kg\cdot K\) = specific heat of oil \(\Delta T = (60-20) K = 40 K\) = change in temperature
02

Calculate the rate of heat transfer.

Now that we have the heat required, we can determine the rate of heat transfer (\(Q'\)) by dividing \(Q\) by the mass flow rate: \(Q' = \frac{Q}{\Delta t}\) So, using the values from step 1: \(Q' = \frac{0.3 kg/s \times 2100 J/kg\cdot K \times 40 K}{1s}\) Calculate \(Q'\) to obtain: \(Q' = 25.2 \times 10^3 W = 25.2 kW\)
03

Determine the length of the tube.

Next, we'll use the overall heat transfer equation to find the length of the tube required to achieve the heat transfer rate calculated in step 2: \(q' = U A \Delta T_m\) where \(q'\) = heat transfer rate per unit area = \(Q'/A\) \(U = 650 W/m^2\cdot K\) = overall heat transfer coefficient \(A = πDL\) = surface area of the tube \(\Delta T_m = 130°C - 60°C = 70K\) = temperature difference between steam and oil First, rearrange the equation as follows to find L: \(L = \frac{Q'}{U \times π \times D \times \Delta T_m}\) Inserting the given values: \(L = \frac{25.2\times 10^3 W}{650 W/m^2\cdot K \times π \times 0.02 m \times 70 K}\) Calculate \(L\) to obtain: \(L = 7.0 m\)
04

Report the results.

We've found the rate of heat transfer and the length of the tube needed to achieve it. So the final answer is: Rate of heat transfer: 25.2 kW Length of the tube: 7.0 m

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Most popular questions from this chapter

In a one-shell and two-tube heat exchanger, cold water with inlet temperature of \(20^{\circ} \mathrm{C}\) is heated by hot water supplied at the inlet at \(80^{\circ} \mathrm{C}\). The cold and hot water flow rates are $5000 \mathrm{~kg} / \mathrm{h}\( and \)10,000 \mathrm{~kg} / \mathrm{h}$, respectively. If the shell-andtube heat exchanger has a \(U A_{s}\) value of \(11,600 \mathrm{~W} / \mathrm{K}\), determine the cold water and hot water outlet temperatures. Assume $c_{p c}=4178 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\( and \)c_{p t}=4188 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$.

In a textile manufacturing plant, the waste dyeing water $\left(c_{p}=4295 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( at \)80^{\circ} \mathrm{C}$ is to be used to preheat fresh water $\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( at \)10^{\circ} \mathrm{C}$ at the same flow rate in a double-pipe counterflow heat exchanger. The heat transfer surface area of the heat exchanger is \(1.65 \mathrm{~m}^{2}\), and the overall heat transfer coefficient is $625 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. If the rate of heat transfer in the heat exchanger is \)35 \mathrm{~kW}$, determine the outlet temperature and the mass flow rate of each fluid stream.

A performance test is being conducted on a doublepipe counterflow heat exchanger that carries engine oil and water at a flow rate of $2.5 \mathrm{~kg} / \mathrm{s}\( and \)1.75 \mathrm{~kg} / \mathrm{s}$, respectively. Since the heat exchanger has been in service for a long time, it is suspected that fouling might have developed inside the heat exchanger that could affect the overall heat transfer coefficient. The test to be carried out is such that, for a designed value of the overall heat transfer coefficient of $450 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\( and a surface area of \)7.5 \mathrm{~m}^{2}\(, the oil must be heated from \)25^{\circ} \mathrm{C}$ to \(55^{\circ} \mathrm{C}\) by passing hot water at $100^{\circ} \mathrm{C}\left(c_{p}=4206 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)$ at the flow rates mentioned above. Determine if the fouling has affected the overall heat transfer coefficient. If yes, then what is the magnitude of the fouling resistance?

An air handler is a large unmixed heat exchanger used for comfort control in large buildings. In one such application, chilled water $\left(c_{p}=4.2 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)$ enters an air handler at \(5^{\circ} \mathrm{C}\) and leaves at \(12^{\circ} \mathrm{C}\) with a flow rate of \(1000 \mathrm{~kg} / \mathrm{h}\). This cold water cools $5000 \mathrm{~kg} / \mathrm{h}\( of air \)\left(c_{p}=1.0 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( which enters the air handler at \)25^{\circ} \mathrm{C}$. If these streams are in counterflow and the water-stream conditions remain fixed, the minimum temperature at the air outlet is (a) \(5^{\circ} \mathrm{C}\) (b) \(12^{\circ} \mathrm{C}\) (c) \(19^{\circ} \mathrm{C}\) (d) \(22^{\circ} \mathrm{C}\) (e) \(25^{\circ} \mathrm{C}\)

Water \(\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) is to be heated by solarheated hot air $\left(c_{p}=1010 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)$ in a double-pipe counterflow heat exchanger. Air enters the heat exchanger at \(90^{\circ} \mathrm{C}\) at a rate of \(0.3 \mathrm{~kg} / \mathrm{s}\), while water enters at $22^{\circ} \mathrm{C}\( at a rate of \)0.1 \mathrm{~kg} / \mathrm{s}$. The overall heat transfer coefficient based on the inner side of the tube is given to be $80 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. The length of the tube is \)12 \mathrm{~m}\(, and the internal diameter of the tube is \)1.2 \mathrm{~cm}$. Determine the outlet temperatures of the water and the air.

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