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A crossflow heat exchanger with both fluids unmixed has an overall heat transfer coefficient of \(200 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), and a heat transfer surface area of \(400 \mathrm{~m}^{2}\). The hot fluid has a heat capacity of \(40,000 \mathrm{~W} / \mathrm{K}\), while the cold fluid has a heat capacity of \(80,000 \mathrm{~W} / \mathrm{K}\). If the inlet temperatures of both hot and cold fluids are \(80^{\circ} \mathrm{C}\) and $20^{\circ} \mathrm{C}\(, respectively, determine \)(a)$ the exit temperature of the hot fluid and \((b)\) the rate of heat transfer in the heat exchanger.

Short Answer

Expert verified
Answer: The exit temperature of the hot fluid is approximately 31.1°C, and the rate of heat transfer in the heat exchanger is approximately 1,956,000 W.

Step by step solution

01

Calculate the heat capacity rates of hot and cold fluids

First, calculate the heat capacity rates (C) of the hot and cold fluids using the following formula: \(C=\dot{m} \times C_{p}\) For the hot fluid, we have: \(C_{h} = 40,000 \frac{\mathrm{W}}{\mathrm{K}}\) And for the cold fluid, we have: \(C_{c} = 80,000 \frac{\mathrm{W}}{\mathrm{K}}\)
02

Determine the minimum heat capacity rate (Cmin)

In order to use the effectiveness-NTU method, we need to find the minimum heat capacity rate (Cmin) which is the smaller of C_h and C_c: \(C_{\min }=\min \left(C_{h}, C_{c}\right)\) Here, \(C_h = 40,000 W/K\) and \(C_c = 80,000 W/K\). So, the minimum heat capacity rate is: \(C_{\min }=C_{h}=40,000 \frac{\mathrm{W}}{\mathrm{K}}\)
03

Calculate the NTU (Number of Transfer Units) of the heat exchanger

Next, we calculate the NTU (Number of Transfer Units) by using the overall heat transfer coefficient (U), heat transfer surface area (A), and Cmin from step 2: \(NTU=\frac{UA}{C_{\min }}\) Plug in the given values: \(NTU=\frac{200 \frac{\mathrm{W}}{\mathrm{m}^{2} \mathrm{K}} \times 400 \mathrm{m}^{2}}{40,000 \frac{\mathrm{W}}{\mathrm{K}}} = 2\)
04

Determine the effectiveness of the heat exchanger

In crossflow heat exchangers with both fluids unmixed, the effectiveness (ε) can be determined using the following approximate formula: \(\epsilon \approx 1-e ^{-NTU}\) Plug in the value of NTU from step 3: \(\epsilon \approx 1-e ^{-2} \approx 0.865\)
05

Calculate the exit temperature of the hot fluid

Using the effectiveness calculated in step 4, we can find the exit temperature (T_h_out) of the hot fluid using the following formula: \(T_{h_{out}}=T_{h_{in}}-\epsilon \Delta T_{in}\) Here, \(T_{h_{in}}\) is the inlet temperature of the hot fluid (80°C) and \(\Delta T_{in}\) is the temperature difference between the hot and cold fluids at the inlet (80°C - 20°C = 60°C). Plug in the values: \(T_{h_{out}}=80^{\circ} \mathrm{C}-0.865 \times 60^{\circ} \mathrm{C} \approx 31.1^{\circ} \mathrm{C}\) The exit temperature of the hot fluid is approximately 31.1°C.
06

Calculate the rate of heat transfer in the heat exchanger

The rate of heat transfer (Q) can be determined by using the minimum heat capacity rate (Cmin) and the temperature difference of the hot fluid: \(Q=C_{\min }\left(T_{h_{in}}-T_{h_{out}}\right)\) Plug in the values: \(Q=40,000 \frac{\mathrm{W}}{\mathrm{K}}\left(80^{\circ} \mathrm{C}-31.1^{\circ} \mathrm{C}\right) \approx 1,956,000 \mathrm{~W}\) The rate of heat transfer in the heat exchanger is approximately 1,956,000 W. In conclusion, the exit temperature of the hot fluid is approximately 31.1°C, and the rate of heat transfer in the heat exchanger is approximately 1,956,000 W.

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Most popular questions from this chapter

By taking the limit as \(\Delta T_{2} \rightarrow \Delta T_{1}\), show that when \(\Delta T_{1}=\Delta T_{2}\) for a heat exchanger, the \(\Delta T_{\mathrm{lm}}\) relation reduces to \(\Delta T_{\mathrm{lm}}=\Delta T_{1}=\Delta T_{2}\).

A double-pipe parallel-flow heat exchanger is used to heat cold tap water with hot water. Hot water $\left(c_{p}=4.25 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( enters the tube at \)85^{\circ} \mathrm{C}$ at a rate of \(1.4 \mathrm{~kg} / \mathrm{s}\) and leaves at \(50^{\circ} \mathrm{C}\). The heat exchanger is not well insulated, and it is estimated that 3 percent of the heat given up by the hot fluid is lost from the heat exchanger. If the overall heat transfer coefficient and the surface area of the heat exchanger are \(1150 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and $4 \mathrm{~m}^{2}$, respectively, determine the rate of heat transfer to the cold water and the log mean temperature difference for this heat exchanger.

In a parallel-flow, liquid-to-liquid heat exchanger, the inlet and outlet temperatures of the hot fluid are \(150^{\circ} \mathrm{C}\) and $90^{\circ} \mathrm{C}\( while those of the cold fluid are \)30^{\circ} \mathrm{C}$ and \(70^{\circ} \mathrm{C}\), respectively. For the same overall heat transfer coefficient, the percentage decrease in the surface area of the heat exchanger if counterflow arrangement is used is (a) \(3.9 \%\) (b) \(9.7 \%\) (c) \(14.5 \%\) (d) \(19.7 \%\) (e) \(24.6 \%\)

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?

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