Warning: foreach() argument must be of type array|object, bool given in /var/www/html/web/app/themes/studypress-core-theme/template-parts/header/mobile-offcanvas.php on line 20

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?

Short Answer

Expert verified
Question: Evaluate the impact of doubling the size of a heat exchanger to increase its NTU from 4 to 8 on its effectiveness and energy savings, assuming a parallel-flow configuration with equal heat capacity rates for both fluids. Answer: Doubling the size of the heat exchanger from NTU 4 to 8 in a parallel-flow configuration with equal heat capacity rates for both fluids, does not result in a significant increase in its effectiveness. The effectiveness remains constant at 1 for both NTU values. Hence, it does not necessarily lead to energy savings based on this analysis. More information and analysis would be needed to support the proposal of increasing the size of the heat exchanger.

Step by step solution

01

Understand the relationship between NTU and effectiveness

The effectiveness of a heat exchanger is defined as the ratio of actual heat transfer to the maximum possible heat transfer. It can be represented as a function of NTU and the heat capacity rates of the fluids involved (C_min and C_max). For some common heat exchanger configurations, the effectiveness-NTU relationships can be found in heat transfer literature.
02

Determine the heat exchanger configuration

In the given exercise, the configuration of the heat exchanger is not mentioned. However, we will consider a simple parallel-flow heat exchanger configuration for our analysis. For other configurations, similar relationships can be derived and the analysis would follow the same steps.
03

Use the effectiveness-NTU relationship for the parallel-flow heat exchanger

For a parallel-flow heat exchanger, the effectiveness E is represented by: E = (1 - e^{(-NTU * (1 - R))}) / (1 - R * e^{(-NTU * (1 - R))}) Here R is the ratio of minimum heat capacity rate to maximum heat capacity rate (C_min/C_max). For demonstration purposes, we will assume R = 1, which means that both fluids have equal heat capacity rates.
04

Calculate effectiveness at NTU = 4 and NTU = 8

We substitute the given values of NTU in the effectiveness equation and calculate the effectiveness E. For NTU = 4: E = (1 - e^{(-4 * (1 - 1))}) / (1 - 1 * e^{(-4 * (1 - 1))}) E = (1 - e^0) / (1 - e^0) = 1 For NTU = 8: E = (1 - e^{(-8 * (1 - 1))}) / (1 - 1 * e^{(-8 * (1 - 1))}) E = (1 - e^0) / (1 - e^0) = 1
05

Evaluate the proposal

We observe that the effectiveness remains the same (equal to 1) when the NTU is increased from 4 to 8. This indicates that doubling the size of the heat exchanger will not result in a significant increase in its effectiveness (at least for the assumed configuration and parameters). Based on this analysis, increasing the NTU from 4 to 8 does not necessarily lead to energy savings for the given heat exchanger configuration and parameters. Therefore, it may not be a justified proposal, and more information and analysis would be needed to support it.

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with Vaia!

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

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?

Oil in an engine is being cooled by air in a crossflow heat exchanger, where both fluids are unmixed. Oil $\left(c_{p k}=2047 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( flowing with a flow rate of \)0.026 \mathrm{~kg} / \mathrm{s}\( enters the heat exchanger at \)75^{\circ} \mathrm{C}$, while air \(\left(c_{p c}=1007 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters 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 \(53 \mathrm{~W} / \mathrm{m}^{2}, \mathrm{~K}\) and the total surface area is \(1 \mathrm{~m}^{2}\). Determine \((a)\) the heat transfer effectiveness and \((b)\) the outlet temperature of the oil.

Oil is being cooled from \(180^{\circ} \mathrm{F}\) to \(120^{\circ} \mathrm{F}\) in a oneshell and two-tube heat exchanger with an overall heat transfer coefficient of $40 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}\(. Water \)\left(c_{p c}=1.0 \mathrm{Btu} / \mathrm{lbm} \cdot{ }^{\circ} \mathrm{F}\right)\( enters at \)80^{\circ} \mathrm{F}$ and exits at \(100^{\circ} \mathrm{F}\) with a mass flow rate of $20,000 \mathrm{lbm} / \mathrm{h}\(. Determine \)(a)\( the NTU value and \)(b)$ the surface area of the heat exchanger.

Water \(\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) is to be heated by solarheated hot air $\left(c_{p}=1010 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)$ in a double-pipe counterflow heat exchanger. Air enters the heat exchanger at \(90^{\circ} \mathrm{C}\) at a rate of \(0.3 \mathrm{~kg} / \mathrm{s}\), while water enters at $22^{\circ} \mathrm{C}\( at a rate of \)0.1 \mathrm{~kg} / \mathrm{s}$. The overall heat transfer coefficient based on the inner side of the tube is given to be $80 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. The length of the tube is \)12 \mathrm{~m}\(, and the internal diameter of the tube is \)1.2 \mathrm{~cm}$. Determine the outlet temperatures of the water and the air.

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.

See all solutions

Recommended explanations on Physics Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.

Sign-up for free