How does a cross-flow heat exchanger differ from a counter-flow one? What is the difference between mixed and unmixed fluids in cross-flow?

Short Answer

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Question: Explain the difference between cross-flow and counter-flow heat exchangers and discuss the difference between mixed and unmixed fluids in cross-flow heat exchangers. Answer: Cross-flow heat exchangers have fluid streams flowing perpendicular to each other, leading to a more localized heat transfer, whereas counter-flow heat exchangers have fluid streams flowing parallel but in opposite directions, resulting in heat transfer along the entire length. This makes counter-flow heat exchangers typically more efficient than cross-flow heat exchangers. In cross-flow heat exchangers, mixed fluids result in a higher heat transfer rate due to increased turbulence and larger contact area between the fluids, while unmixed fluids have lower heat transfer rates but prevent contamination, making them ideal for applications where the fluids must remain separate.

Step by step solution

01

Definition of Cross-Flow Heat Exchanger

A cross-flow heat exchanger is a type of heat exchanger where the two fluid streams flow perpendicular to each other. The heat transfer occurs between these two fluid streams as they come into contact with each other without direct mixing.
02

Definition of Counter-Flow Heat Exchanger

A counter-flow heat exchanger is a type of heat exchanger where two fluid streams flow parallel to each other but in opposite directions. The heat transfer in this configuration occurs along the length of the heat exchanger as the temperature difference between the hot and cold fluids decreases gradually along the heat exchanger.
03

Comparing Cross-Flow and Counter-Flow Heat Exchangers

While cross-flow heat exchangers have fluids moving perpendicular to each other, counter-flow heat exchangers have fluids moving parallel but in opposite directions. The heat transfer process in cross-flow heat exchangers is more localized, whereas in counter-flow heat exchangers, the heat transfer occurs along the entire length. Cross-flow heat exchangers are typically more compact and have lower heat transfer rates compared to counter-flow heat exchangers, which have higher heat transfer rates and are generally more efficient in heat recovery.
04

Definition of Mixed and Unmixed Fluids in Cross-Flow

In a cross-flow heat exchanger, there are two configurations concerning the fluid streams: mixed and unmixed. 1. Mixed: In this configuration, the streams in the heat exchanger are allowed to mix with each other. This mixing can enhance the heat transfer process due to increased turbulence and a larger contact area between the two fluids. 2. Unmixed: In the unmixed configuration, the two streams in the exchanger are not allowed to mix. Heat exchange occurs only through the solid surface separating the two fluids (such as a plate). The heat transfer rate is primarily determined by the surface area and the thermal properties of the solid material.
05

Difference between Mixed and Unmixed Fluids in Cross-Flow

Mixed fluids in cross-flow heat exchangers provide a higher heat transfer rate due to the increased turbulence and larger contact area between the fluids. On the other hand, in unmixed configuration, the heat transfer is solely dependent on the surface area and thermal properties of the solid material separating the fluids. Unmixed fluids have lower heat transfer rates compared to mixed fluids, but they also prevent contamination and cross-contamination, making them ideal for applications where the fluids must remain separate.

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Key Concepts

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

Cross-Flow Heat Exchanger
Understanding how a cross-flow heat exchanger functions is crucial in various industries where thermal energy needs to be transferred between two fluids. Within this device, the two fluids move at right angles to each other, hence the term 'cross-flow'. Imagine one fluid passing through tubes while the other moves around these tubes; this creates a perpendicular flow pattern that facilitates heat transfer. This design is quite prevalent in automotive radiators and HVAC systems due to its compact nature.

However, despite its widespread use, cross-flow heat exchangers typically do not provide as high heat transfer rates as some other types. This is partly because the heat exchange occurs in a more localized area, where the fluids are in close proximity.

One significant advantage is their ability to handle cross-contamination between fluids, making cross-flow models very suitable for situations where maintaining fluid integrity is important. Furthermore, these exchangers can operate effectively even when there is a temperature discrepancy between the incoming fluids.
Counter-Flow Heat Exchanger
A counter-flow heat exchanger presents a different approach to thermal energy transfer. Fluids flow in parallel paths but in opposing directions, establishing a continuous temperature gradient along the length of the exchanger. Such a design is revered for its efficiency; because the coldest part of one fluid comes into contact with the coldest part of the second fluid, an overall greater temperature difference is maintained. This results in very effective heat transfer.

Consider an example where hot water is used to warm up cold oil. As the hot water moves down the length of the exchanger, it continuously encounters slightly cooler oil, transferring its heat. By the time the hot water reaches the end of the exchanger, it has cooled significantly, having given up its heat along the way. This configuration can achieve near-total energy transfer, making it ideal for processes that require maximal thermal recovery, such as certain chemical processing applications or energy generation systems.
Mixed vs Unmixed Fluids
When delving into the details of cross-flow heat exchangers, the concepts of mixed and unmixed fluids become significant. Mixed fluid configurations allow the two streams to intermingle, increasing turbulence and heat transfer. Such mixing can occur in a variety of ways, often by using fins or other disruption methods to create a more dynamic flow.

Mixed Fluids

The increased contact area and turbulent flow patterns significantly boost the heat transfer efficiency. This configuration is particularly beneficial when rapid temperature changes are required and when fluid properties allow for safe mixing without concerns of corrosion or contamination.

Unmixed Fluids

On the other hand, the unmixed setup confines each fluid within its own stream, preventing direct contact. Here, heat transfer relies on the surface area and material properties of the separation surface. Although the heat transfer rate might be lower compared to a mixed scenario, this configuration is essential in applications where fluid purity is crucial, such as in pharmaceutical or food processing industries.
Heat Transfer Efficiency
Heat transfer efficiency is the benchmark for evaluating the performance of different heat exchanger designs. It’s determined by how proficiently a heat exchanger can transfer thermal energy from the hot to the cold fluid without unnecessary energy losses.

Factors that influence efficiency include the temperature difference between the fluids, the surface area available for heat transfer, and the thermal conductivity of the exchange materials. Configurations like counter-flow are noted for their higher efficiency because they maintain a large temperature gradient throughout the exchanger's length. Mixed fluids in cross-flow exchangers can also enhance efficiency by fostering turbulence and greater surface contact.

Engineers aim to design heat exchangers that extract the maximum amount of useful energy while minimizing the product's size, cost, and the risk of fluid contamination. By balancing these priorities, they can produce an efficient thermal management system suitable for the intended application, whether for environmental control, industrial processing, or energy conservation.

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Most popular questions from this chapter

Consider a water-to-water counter-flow heat exchanger with these specifications. Hot water enters at \(95^{\circ} \mathrm{C}\) while cold water enters at \(20^{\circ} \mathrm{C}\). The exit temperature of hot water is \(15^{\circ} \mathrm{C}\) greater than that of cold water, and the mass flow rate of hot water is 50 percent greater than that of cold water. The product of heat transfer surface area and the overall heat transfer coefficient is \(1400 \mathrm{~W} / \mathrm{K}\). Taking the specific heat of both cold and hot water to be \(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\), determine (a) the outlet temperature of the cold water, \((b)\) the effectiveness of the heat exchanger, \((c)\) the mass flow rate of the cold water, and \((d)\) the heat transfer rate.

A shell-and-tube heat exchanger is to be designed to cool down the petroleum- based organic vapor available at a flow rate of \(5 \mathrm{~kg} / \mathrm{s}\) and at a saturation temperature of \(75^{\circ} \mathrm{C}\). The cold water \(\left(c_{p}=4187 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) used for its condensation is supplied at a rate of \(25 \mathrm{~kg} / \mathrm{s}\) and a temperature of \(15^{\circ} \mathrm{C}\). The cold water flows through copper tubes with an outside diameter of \(20 \mathrm{~mm}\), a thickness of \(2 \mathrm{~mm}\), and a length of \(5 \mathrm{~m}\). The overall heat transfer coefficient is assumed to be \(550 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and the latent heat of vaporization of the organic vapor may be taken to be \(580 \mathrm{~kJ} / \mathrm{kg}\). Assuming negligible thermal resistance due to pipe wall thickness, determine the number of tubes required.

Consider a heat exchanger that has an NTU of 4 . Someone proposes to double the size of the heat exchanger and thus double the NTU to 8 in order to increase the effectiveness of the heat exchanger and thus save energy. Would you support this proposal?

Water \(\left(c_{p}=1.0 \mathrm{Btu} / \mathrm{lbm} \cdot{ }^{\circ} \mathrm{F}\right)\) is to be heated by solarheated hot air \(\left(c_{p}=0.24 \mathrm{Btu} / \mathrm{lbm} \cdot{ }^{\circ} \mathrm{F}\right)\) in a double- pipe counterflow heat exchanger. Air enters the heat exchanger at \(190^{\circ} \mathrm{F}\) at a rate of \(0.7 \mathrm{lbm} / \mathrm{s}\) and leaves at \(135^{\circ} \mathrm{F}\). Water enters at \(70^{\circ} \mathrm{F}\) at a rate of \(0.35 \mathrm{lbm} / \mathrm{s}\). The overall heat transfer coefficient based on the inner side of the tube is given to be \(20 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F}\). Determine the length of the tube required for a tube internal diameter of \(0.5 \mathrm{in}\).

A 1 -shell and 2-tube type heat exchanger has an overall heat transfer coefficient of \(300 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F}\). The shell side fluid has a heat capacity rate of \(20,000 \mathrm{Btu} / \mathrm{h} \cdot{ }^{\circ} \mathrm{F}\), while the tube side fluid has a heat capacity rate of \(40,000 \mathrm{Btu} / \mathrm{h} \cdot{ }^{\circ} \mathrm{F}\). The inlet temperatures on the shell side and tube side are \(200^{\circ} \mathrm{F}\) and \(90^{\circ} \mathrm{F}\), respectively. If the total heat transfer area is \(100 \mathrm{ft}^{2}\), determine \((a)\) the heat transfer effectiveness and \((b)\) the actual heat transfer rate in the heat exchanger.

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