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Explain how the maximum possible heat transfer rate \(\dot{Q}_{\max }\) in a heat exchanger can be determined when the mass flow rates, specific heats, and inlet temperatures of the two fluids are specified. Does the value of \(\dot{Q}_{\max }\) depend on the type of the heat exchanger?

Short Answer

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Based on the given information, determine the maximum possible heat transfer rate (\(\dot{Q}_{\max}\)) in a heat exchanger. 1. \(\dot{m}_{1}\) = mass flow rate of fluid 1 (kg/s) 2. \(\dot{m}_{2}\) = mass flow rate of fluid 2 (kg/s) 3. \(C_{p1}\) = specific heat of fluid 1 (J/kg·K) 4. \(C_{p2}\) = specific heat of fluid 2 (J/kg·K) 5. \(T_{1,in}\) = inlet temperature of fluid 1 (°C or K) 6. \(T_{2,in}\) = inlet temperature of fluid 2 (°C or K) Answer: To determine the maximum possible heat transfer rate (\(\dot{Q}_{\max}\)), follow the steps below: 1. Identify the minimum and maximum mass flow rates, denoted as \(\dot{m}_{min}\) and \(\dot{m}_{max}\). 2. Calculate the heat capacity rates for both fluids using the specific heats and mass flow rates: \(C_{1}=\dot{m}_{1} \cdot C_{p1}\) and \(C_{2}=\dot{m}_{2} \cdot C_{p2}\). 3. Determine the minimum and maximum heat capacity rates, denoted as \(C_{min}\) and \(C_{max}\). 4. Calculate the maximum possible temperature difference: \(\Delta T_{max}=\left|T_{1,in}-T_{2,in}\right|\) 5. Calculate the maximum possible heat transfer rate: \(\dot{Q}_{max}=C_{min} \cdot \Delta T_{max}\) The result will be the maximum possible heat transfer rate (\(\dot{Q}_{\max}\)) in the heat exchanger, independent of the type of heat exchanger used.

Step by step solution

01

Identify the minimum and maximum mass flow rates

Based on the mass flow rates of both fluids (\(\dot{m}_{1}\) and \(\dot{m}_{2}\)), we need to identify the fluids with the minimum and maximum mass flow rates. Let's denote them as \(\dot{m}_{min}\) and \(\dot{m}_{max}\).
02

Calculate the heat capacity rates

Using the specific heats (\(C_{p1}\) and \(C_{p2}\)) and mass flow rates for both fluids, we can calculate the heat capacity rates for each fluid: $$C_{1}=\dot{m}_{1} \cdot C_{p1}$$ $$C_{2}=\dot{m}_{2} \cdot C_{p2}$$
03

Determine the minimum and maximum heat capacity rates

Based on the calculated heat capacity rates, we need to determine the fluids with the minimum and maximum heat capacity rates. Let's denote them as \(C_{min}\) and \(C_{max}\).
04

Calculate the maximum possible temperature difference

The maximum possible temperature difference between the two fluids can be determined by comparing their inlet temperatures. If \(T_{1,in}\) and \(T_{2,in}\) denote the inlet temperatures of fluids 1 and 2, respectively, the maximum possible temperature difference (\(\Delta T_{max}\)) can be calculated as: $$\Delta T_{\max }=\left|T_{1, \mathrm{in}}-T_{2, \mathrm{in}}\right|$$
05

Calculate the maximum possible heat transfer rate

Now that we have all the necessary information, we can calculate the maximum possible heat transfer rate (\(\dot{Q}_{\max}\)) using the following formula: $$\dot{Q}_{\max }=C_{\min } \cdot \Delta T_{\max }$$ This calculation is independent of the type of heat exchanger used, as it only takes into consideration the maximum energy transfer between the two fluids based on their properties and inlet temperatures.

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Most popular questions from this chapter

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?

Write an essay on the static and dynamic types of regenerative heat exchangers, and compile information about the manufacturers of such heat exchangers. Choose a few models by different manufacturers and compare their costs and performance.

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) \(0.805 \mathrm{~m}^{2}\)

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: \((a) 11.4 \mathrm{~m}^{2}\)

What are the common causes of fouling in a heat exchanger? How does fouling affect heat transfer and pressure drop?

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