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A single-pass crossflow heat exchanger uses hot air (mixed) to heat water (unmixed), flowing with a mass flow rate of \(3 \mathrm{~kg} / \mathrm{s}\), from \(30^{\circ} \mathrm{C}\) to \(80^{\circ} \mathrm{C}\). The hot air enters and exits the heat exchanger at \(220^{\circ} \mathrm{C}\) and $100^{\circ} \mathrm{C}\(, respectively. If the overall heat transfer coefficient is \)200 \mathrm{~W} / \mathrm{m}^{2}, \mathrm{~K}$, determine the required surface area.

Short Answer

Expert verified
Answer: The required surface area of the single-pass crossflow heat exchanger is approximately 30.69 m².

Step by step solution

01

Calculate the heat capacity rate of the water

First, let's calculate the heat capacity rate of the water. The specific heat capacity of water is approximately \(4.18 \mathrm{~kJ/kg·K}\). The heat capacity rate can be calculated using the formula \(\dot{C} = m\dot{c}_p\), where \(\dot{C}\) is the heat capacity rate, \(m\) is the mass flow rate, and \(\dot{c}_p\) is the specific heat capacity. The heat capacity rate for the water is: \(\dot{C}_w = m\dot{c}_{p,w} = (3 \mathrm{~kg/s}) (4.18 \mathrm{~kJ/kg·K}) = 12.54 \mathrm{~kJ/s·K}\)
02

Calculate the heat transfer rate

The heat transfer rate can be calculated using the heat capacity rate and the temperature difference of the water before and after the heat exchanger: \(\dot{Q} = \dot{C}_w (\Delta T_w) = 12.54 \mathrm{~kJ/s·K} (80^{\circ} \mathrm{C} - 30^{\circ} \mathrm{C}) = 12.54 \times 50 \mathrm{~kJ/s} = 627 \mathrm{~kW}\)
03

Calculate the required temperature difference

To calculate the required surface area, we need to know the Log Mean Temperature Difference (LMTD) for the heat exchanger. The LMTD can be calculated as follows: \(\mathrm{LMTD} = \dfrac{\Delta T_1 - \Delta T_2}{\ln \frac{\Delta T_1}{\Delta T_2}}\) Where: \(\Delta T_1 = T_{h,i} - T_{c,o} = 220^{\circ} \mathrm{C} - 80^{\circ} \mathrm{C} = 140^{\circ} \mathrm{C}\) \(\Delta T_2 = T_{h,o} - T_{c,i} = 100^{\circ} \mathrm{C} - 30^{\circ} \mathrm{C} = 70^{\circ} \mathrm{C}\) \(\mathrm{LMTD} = \dfrac{140^{\circ} \mathrm{C} -70^{\circ} \mathrm{C}}{\ln \frac {140^{\circ} \mathrm{C}}{70^{\circ} \mathrm{C}}} = 102.2^{\circ} \mathrm{C}\)
04

Calculate the required surface area

Now, we will use the overall heat transfer coefficient and the LMTD to calculate the required surface area for the heat exchanger using the formula: \(A = \dfrac{\dot{Q}}{U \times \mathrm{LMTD}}\) Where \(A\) is the required surface area, \(\dot{Q}\) is the heat transfer rate, \(U\) is the overall heat transfer coefficient, and LMTD is the log mean temperature difference. \(A = \dfrac{627 \times 10^{3} \mathrm{~W}}{200 \mathrm{~W/m^2·K} \times 102.2^{\circ} \mathrm{C}} = 30.69 \mathrm{~m}^2\) So, the required surface area of the single-pass crossflow heat exchanger is approximately \(30.69 \mathrm{~m}^2\).

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Most popular questions from this chapter

Cold water $\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)$ leading to a shower enters a thin-walled double-pipe counterflow heat exchanger at \(15^{\circ} \mathrm{C}\) at a rate of $0.25 \mathrm{~kg} / \mathrm{s}\( and is heated to \)45^{\circ} \mathrm{C}$ by hot water \(\left(c_{p}=4190 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) that enters at \(100^{\circ} \mathrm{C}\) at a rate of $3 \mathrm{~kg} / \mathrm{s}\(. If the overall heat transfer coefficient is \)950 \mathrm{~W} / \mathrm{m}^{2}\(. \)\mathrm{K}$, determine the rate of heat transfer and the heat transfer surface area of the heat exchanger using the \(\varepsilon-\mathrm{NTU}\) method. Answers: \(31.35 \mathrm{~kW}\), $0.482 \mathrm{~m}^{2}$

Consider a heat exchanger in which both fluids have the same specific heats but different mass flow rates. Which fluid will experience a larger temperature change: the one with the lower or higher mass flow rate?

Consider a closed-loop heat exchanger that carries exit water $\left(c_{p}=1 \mathrm{Btu} / \mathrm{lbm} \cdot{ }^{\circ} \mathrm{F}\right.$ and \(\left.\rho=62.4 \mathrm{lbm} / \mathrm{ft}^{3}\right)\) of a condenser side initially at \(100^{\circ} \mathrm{F}\). The water flows through a 500 -ft-long stainless steel pipe of 1 in inner diameter immersed in a large lake. The temperature of lake water surrounding the heat exchanger is $45^{\circ} \mathrm{F}$. The overall heat transfer coefficient of the heat exchanger is estimated to be $250 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}$. What is the exit temperature of the water from the immersed heat exchanger if it flows through the pipe at an average velocity of \(9 \mathrm{ft} / \mathrm{s}\) ? Use the \(\varepsilon-N T U\) method for analysis.

Water is boiled at \(150^{\circ} \mathrm{C}\) in a boiler by hot exhaust gases $\left(c_{p}=1.05 \mathrm{~kJ} / \mathrm{kg}^{\circ}{ }^{\circ} \mathrm{C}\right)\( that enter the boiler at \)540^{\circ} \mathrm{C}$ at a rate of \(0.4 \mathrm{~kg} / \mathrm{s}\) and leave at \(200^{\circ} \mathrm{C}\). The surface area of the heat exchanger is \(0.64 \mathrm{~m}^{2}\). The overall heat transfer coefficient of this heat exchanger is\(\mathrm{kg} / \mathrm{s}\) with cold water $\left(c_{p}=4.18 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( that enters the heat exchanger at \)20^{\circ} \mathrm{C}$ at a rate of \(0.6 \mathrm{~kg} / \mathrm{s}\). If the overall heat transfer coefficient is \(800 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), the heat transfer area of the heat exchanger is (a) \(0.745 \mathrm{~m}^{2}\) (b) \(0.760 \mathrm{~m}^{2}\) (c) \(0.775 \mathrm{~m}^{2}\) (d) \(0.790 \mathrm{~m}^{2}\) (e) \(0.805 \mathrm{~m}^{2}\)

Oil in an engine is being cooled by air in a crossflow heat exchanger, where both fluids are unmixed. Oil $\left(c_{p l}=2047 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( flowing with a flow rate of \)0.026 \mathrm{~kg} / \mathrm{s}\( enters the tube side at \)75^{\circ} \mathrm{C}$, while air \(\left(c_{p c}=1007 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters the shell side at \(30^{\circ} \mathrm{C}\) with a flow rate of $0.21 \mathrm{~kg} / \mathrm{s}$. The overall heat transfer coefficient of the heat exchanger is \(53 \mathrm{~W} / \mathrm{m}^{2}, \mathrm{~K}\), and the total surface area is \(1 \mathrm{~m}^{2}\). If the correction factor is \(F=0.96\), determine the outlet temperatures of the oil and air.

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