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Classify heat exchangers according to flow type and explain the characteristics of each type.

Short Answer

Expert verified
Answer: The three main types of flow arrangements in heat exchangers are parallel flow, counterflow, and crossflow. Parallel flow involves both the hot and cold fluids flowing in the same direction, leading to a simpler design but with less efficiency due to decreasing temperature differences along the exchanger. Counterflow features fluids entering at opposite ends and flowing in opposite directions, resulting in a higher temperature difference and increased heat transfer efficiency compared to parallel flow. Crossflow occurs when the hot and cold fluids flow perpendicular to each other, offering versatility and the ability to handle different flow rates and temperature differentials. It can be further divided into un-mixed and mixed crossflow, depending on whether the fluids flow in separate channels or mix due to turbulence or heat transfer media movement.

Step by step solution

01

Understand Heat Exchangers

A heat exchanger is a device designed to transfer heat between two or more fluids without mixing them. These fluids can be gases, liquids, or a combination of both. Heat exchangers are widely used in various industries such as power generation, chemical processing, and HVAC (Heating, Ventilation, and Air Conditioning).
02

Identify the Types of Flow Arrangements

Heat exchangers can be classified based on the flow arrangement of the two fluids. There are three main types of flow arrangements: 1. Parallel flow 2. Counterflow 3. Crossflow
03

Describe Parallel Flow

In a parallel flow heat exchanger, both the hot and cold fluids enter the exchanger at the same side, flow in the same direction, and exit at the same end. This arrangement is simpler and less efficient than other flow configurations because the temperature difference between the fluids decreases along the length of the exchanger. Consequently, the heat transfer rate also decreases, causing less energy to be exchanged between the two fluids.
04

Explain Counterflow

Counterflow heat exchangers have fluids entering at opposite ends and flowing in opposite directions. This arrangement maintains a higher temperature difference along the length of the exchanger, resulting in a more efficient heat transfer relative to parallel flow. Counterflow heat exchangers are more compact and can achieve higher temperature changes, making them more suitable for applications requiring significant heat transfer.
05

Illustrate Crossflow

In crossflow heat exchangers, the hot and cold fluids flow perpendicular to each other. This configuration can be further divided into two subtypes: un-mixed and mixed crossflow. In un-mixed crossflow, the fluids flow in separate channels maintaining consistent flow rates, whereas, in mixed crossflow, the fluids can mix due to turbulence or the movement of heat transfer media. Crossflow heat exchangers are widely used in various applications such as air conditioning, automotive, and industrial processes due to their versatility and ability to handle different flow rates and temperature differentials.
06

Conclusion

To sum up, heat exchangers can be classified based on their flow arrangement into parallel flow, counterflow, and crossflow. Parallel flow exchangers are simple but less efficient, while counterflow exchangers provide higher efficiency and temperature changes. Crossflow exchangers offer versatility and can handle different flow rates and temperature differentials. Each type of heat exchanger has its characteristics and suitable applications, making them essential components in numerous industries.

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Parallel Flow Heat Exchanger
When learning about parallel flow heat exchangers, it's important to envision two streams moving side-by-side in the same direction through the device. Since both the hot and cold fluids enter and exit the exchanger from the same direction, the initial temperature gradient (the driving force behind heat transfer) is quite high but diminishes as the fluids approach the exit. This reduction in temperature difference along the heat exchanger means that the efficiency of heat transfer isn't at its maximum potential.

Furthermore, due to this decrement in temperature difference, parallel flow heat exchangers tend to require a longer length to achieve the necessary heat transfer, impacting the overall size and cost. They are, however, easier to construct and may be used in systems where the desired temperature change is low or space constraints are not a pressing concern.
Counterflow Heat Exchanger
Moving on to counterflow heat exchangers, these devices are viewed as the more efficient cousins to parallel flow counterparts. In this configuration, the two fluids move in opposite directions, creating a consistently high temperature gradient along the length of the exchanger. This sustained thermal driving force leads to enhanced heat transfer efficiency, allowing the exchanger to be more compact for the same heat transfer duty.

Moreover, since the coldest part of the cold fluid meets the hottest part of the hot fluid, the possibility for the fluids to reach a closer temperature approach is greater, which is particularly useful for processes requiring substantial thermal energy recovery. Counterflow heat exchangers are ideal for cases where space is limited or when maximum heat transfer is necessary within a minimal volume.
Crossflow Heat Exchanger
Discussing the crossflow heat exchangers will illustrate a system where fluid flows intersect perpendicularly. This unique feature makes crossflow designs popular in scenarios where the heat transfer surfaces need to be exposed openly to the fluid streams, as in the radiator of a car or an air handling unit. These exchangers can be constructed to allow mixing (where the fluids can intermingle and create turbulence) or to prevent it (keeping fluids in separate channels).

In un-mixed crossflow, the effectiveness can be optimized by using fins or plates to maintain high surface area contact, whereas in mixed crossflow, the increased turbulence can itself enhance the heat transfer rates. This versatile configuration can deal with a wide variety of flow rates and thermal conditions, making it suitable for a diverse range of industrial applications.
Heat Transfer Efficiency
Lastly, when discussing heat transfer efficiency, it is a measure of how well a heat exchanger performs its function of moving thermal energy from one fluid to another. The efficiency is influenced by several factors, such as the flow arrangement, the properties of the fluids involved, the temperature difference, and the heat transfer surface area. For example, counterflow arrangements are inherently more efficient than parallel flow arrangements due to the higher and more consistent temperature difference.

An efficient heat exchanger will transfer the maximum amount of heat with a minimal loss in energy. High efficiency is desirable as it can lead to cost savings by reducing energy consumption, operation costs, and may also decrease the exchanger size needed for a particular duty. Engineers strive to design heat exchangers that optimize efficiency for their specific application, considering the right balance of size, cost, and performance.

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Most popular questions from this chapter

Oil in an engine is being cooled by air in a crossflow heat exchanger, where both fluids are unmixed. Oil \(\left(c_{p h}=\right.\) \(2047 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K})\) 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 \(53 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) 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.

Cold water \(\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) leading to a shower enters a thin-walled double-pipe counter-flow 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 \(950 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), determine the rate of heat transfer and the heat transfer surface area of the heat exchanger using the \(\varepsilon-\mathrm{NTU}\) method.

The condenser of a room air conditioner is designed to reject heat at a rate of \(15,000 \mathrm{~kJ} / \mathrm{h}\) from refrigerant-134a as the refrigerant is condensed at a temperature of \(40^{\circ} \mathrm{C}\). Air \(\left(c_{p}=1005 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) flows across the finned condenser coils, entering at \(25^{\circ} \mathrm{C}\) and leaving at \(35^{\circ} \mathrm{C}\). If the overall heat transfer coefficient based on the refrigerant side is \(150 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), determine the heat transfer area on the refrigerant side.

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 4 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 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 tubes 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 NTU method, determine \((a)\) effectiveness of the heat exchanger, \((b)\) length of the tube, and \((c)\) rate of steam condensation.

Under what conditions can a counter-flow heat exchanger have an effectiveness of one? What would your answer be for a parallel-flow heat exchanger?

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