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Consider a heat exchanger that has an NTU of \(0.1\). Someone proposes to triple the size of the heat exchanger and thus triple the NTU to \(0.3\) in order to increase the effectiveness of the heat exchanger and thus save energy. Would you support this proposal?

Short Answer

Expert verified
Answer: Tripling the size of the heat exchanger to triple the NTU value to 0.3 does result in increased effectiveness of the heat exchanger. However, the energy savings observed may not be significant due to diminishing returns and the practical implications such as increased costs and space requirements.

Step by step solution

01

Understand the NTU Method

The NTU (Number of Transfer Units) is a dimensionless parameter that indicates the size and performance of a heat exchanger. It is the ratio of the actual heat transfer rate to the maximum possible heat transfer rate. The effectiveness of a heat exchanger can be calculated using the following equation: Effectiveness, \(\epsilon = \frac{Q_{actual}}{Q_{max}}\) Where: \(\epsilon\) = Effectiveness \(Q_{actual}\) = Actual heat transfer rate (W) \(Q_{max}\) = Maximum heat transfer rate (W) Using the NTU method, the effectiveness of the heat exchanger is related to the NTU value and the heat capacity rate ratio \(C_{min}/C_{max}\). Generally, an increase in the heat exchanger's size (and consequently the NTU value) results in an increase in effectiveness.
02

Evaluating the proposal - Tripling the NTU value

To evaluate the proposal of tripling the NTU, consider the initial NTU value of \(0.1\). With the proposal, the NTU value will be tripled to \(0.3\). The effectiveness would depend on the type of heat exchanger and the heat capacity ratio. For the sake of simplicity, let's assume a simple counterflow heat exchanger. The effectiveness formula for such a heat exchanger is given by: \(\epsilon = \frac{1 - e^{-(NTU)(1+C_r)(1-e^{-NTU(1-C_r)})}}{(1 + C_r)(1-e^{-NTU(1-C_r)})}\) Where: \(C_r\) = heat capacity rate ratio = \(C_{min}/C_{max}\) \(NTU\) = Number of Transfer Units Now, we do not know the \(C_r\) for our current scenario. To truly evaluate the effectiveness of the proposed idea, we must consider the relationship between NTU and effectiveness while keeping \(C_r\) constant.
03

Illustrate the relationship between NTU and effectiveness

One way to illustrate this relationship is to create a graph of effectiveness versus NTU while keeping the \(C_r\) constant. When you create such a graph, you would observe that the effectiveness increases with increasing NTU value. However, it is also important to note that the effectiveness has a diminishing return as the NTU value gets larger, and the curve will asymptotically approach \(100\%\) (complete energy transfer) without reaching it.
04

Conclusion - Evaluating the proposal

Although increasing the size of the heat exchanger can result in higher effectiveness, it is essential to consider the practical implications of tripling the size of the heat exchanger. A larger heat exchanger may result in higher capital costs, increased maintenance requirements, and potentially a larger footprint. In conclusion, while increasing NTU does increase the effectiveness of the heat exchanger, the effectiveness gain per NTU decreases when NTU is increased. Therefore, tripling the size of the heat exchanger to triple the NTU to \(0.3\) may save some energy but may not be worth the investment considering the diminishing returns and the practical implications such as costs and space requirements.

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Key Concepts

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

Heat Exchanger Effectiveness
Heat exchanger effectiveness is an integral concept in understanding how well a heat exchanger is performing its task of transferring heat from one fluid to another. It is defined as the ratio of the actual heat transfer rate to the maximum possible heat transfer rate within the heat exchanger.

In simple terms, it is a measure of how close the heat exchanger comes to reaching its maximum potential. The effectiveness, represented by the symbol \( \epsilon \), can be described by the equation:\
\[ \epsilon = \frac{Q_{actual}}{Q_{max}} \]
where \( Q_{actual} \) is the actual rate of heat transferred and \( Q_{max} \) is the theoretical maximum rate of heat transfer if the exiting fluid temperature were to reach the entering temperature of the hot/cold stream.

In practice, this parameter helps in deciding whether a heat exchanger is efficient enough for a particular application or whether modifications, such as increasing the size to raise the NTU, are warranted.
Heat Transfer Rate
The heat transfer rate in a heat exchanger ties directly into its effectiveness. It represents the quantity of heat transferred between the two fluids inside the heat exchanger per unit time, typically measured in watts (W). The actual heat transfer rate, \( Q_{actual} \), can be affected by several factors including the size of the heat exchanger, the materials used, the flow arrangement, and the temperature gradient.

Engineers aim to maximize this rate to improve the heat exchanger's performance while considering the constraints of the system. For example, by enlarging the surface area through which the heat is transferred, they can increase the heat transfer rate up to a point dictated by the laws of diminishing returns relative to size and cost.
Heat Capacity Rate Ratio
Understanding the heat capacity rate ratio, often symbolized as \( C_r \) and defined as the ratio \( C_{min}/C_{max} \), where \( C_{min} \) and \( C_{max} \) are the minimum and maximum heat capacity rates of the fluids involved, is essential when analyzing or designing heat exchangers.

This ratio impacts how the heat exchanger's effectiveness will respond to changes in the NTU. It's an indication of the relative capacity of one fluid to hold heat compared to the other fluid. When this ratio is balanced, the heat exchanger can work more effectively, and adjustments to the NTU can be more predictable in their impact on effectiveness.
Diminishing Returns in Heat Exchanger Performance
The concept of diminishing returns in the context of heat exchanger performance refers to the observation that after a certain point, increasing the size of the heat exchanger and hence the NTU yields progressively smaller improvements in effectiveness.

As illustrated in the step-by-step solution, making the heat exchanger three times larger to triple the NTU from \(0.1\) to \(0.3\) will increase effectiveness, but not linearly. The effectiveness curve will asymptotically approach 100% as NTU is increased, but never actually reach it, indicating that there's a practical limit to the benefits gained from just enlarging the heat exchanger. Beyond a specific NTU value, the cost, space, and added complexity may outweigh the marginal gains in effectiveness, which is crucial to consider when proposing such upgrades.

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Most popular questions from this chapter

For a specified fluid pair, inlet temperatures, and mass flow rates, what kind of heat exchanger will have the highest effectiveness: double-pipe parallel- flow, double-pipe counterflow, cross-flow, or multipass shell-and-tube heat exchanger?

Saturated liquid benzene flowing at a rate of \(5 \mathrm{~kg} / \mathrm{s}\) is to be cooled from \(75^{\circ} \mathrm{C}\) to \(45^{\circ} \mathrm{C}\) by using a source of cold water \(\left(c_{p}=4187 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) flowing at \(3.5 \mathrm{~kg} / \mathrm{s}\) and \(15^{\circ} \mathrm{C}\) through a \(20-\mathrm{mm}-\) diameter tube of negligible wall thickness. The overall heat transfer coefficient of the heat exchanger is estimated to be \(750 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). If the specific heat of the liquid benzene is \(1839 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\) and assuming that the capacity ratio and effectiveness remain the same, determine the heat exchanger surface area for the following four heat exchangers: \((a)\) parallel flow, \((b)\) counter flow, \((c)\) shelland-tube heat exchanger with 2 -shell passes and 40-tube passes, and \((d)\) cross-flow heat exchanger with one fluid mixed (liquid benzene) and other fluid unmixed (water).

Hot water coming from the engine is to be cooled by ambient air in a car radiator. The aluminum tubes in which the water flows have a diameter of \(4 \mathrm{~cm}\) and negligible thickness. Fins are attached on the outer surface of the tubes in order to increase the heat transfer surface area on the air side. The heat transfer coefficients on the inner and outer surfaces are 2000 and \(150 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), respectively. If the effective surface area on the finned side is 10 times the inner surface area, the overall heat transfer coefficient of this heat exchanger based on the inner surface area is (a) \(150 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (b) \(857 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (c) \(1075 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (d) \(2000 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (e) \(2150 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\)

What does the effectiveness of a heat exchanger represent? Can effectiveness be greater than one? On what factors does the effectiveness of a heat exchanger depend?

A performance test is being conducted on a double pipe counter flow 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 over a long period of time it is suspected that the fouling might have developed inside the heat exchanger that might have affected 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?

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