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There are two heat exchangers that can meet the heat transfer requirements of a facility. One is smaller and cheaper but requires a larger pump, while the other is larger and more expensive but has a smaller pressure drop and thus requires a smaller pump. Both heat exchangers have the same life expectancy and meet all other requirements. Explain which heat exchanger you would choose and under what conditions. 11-138C A heat exchanger is to be selected to cool a hot liquid chemical at a specified rate to a specified temperature. Explain the steps involved in the selection process.

Short Answer

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Answer: The choice between the smaller, cheaper heat exchanger and the larger, more expensive one depends on factors such as initial cost, space availability, energy efficiency, and system requirements. The smaller, cheaper heat exchanger may be preferred if initial cost is a major concern, space is limited, and the operating cost difference between the pumps is not significant. The larger, more expensive heat exchanger may be chosen if long-term operation costs outbalance the initial investment, space is not a constraint, and better efficiency is prioritized. The steps in selecting a heat exchanger involve defining application requirements, determining the type and material of construction, calculating the heat transfer area, selecting a heat exchanger model, performing an economic analysis, and finally purchasing and installing the chosen heat exchanger.

Step by step solution

01

Heat exchanger comparison

In this scenario, we have two heat exchangers to choose from. The first heat exchanger is smaller, cheaper, but requires a larger pump, while the second one is larger, more expensive, but needs a smaller pump due to its smaller pressure drop. To decide which heat exchanger to choose, various factors need to be considered. These factors include: - Total cost of ownership (initial cost, operation cost, maintenance cost) - Space availability at the facility - Energy efficiency - Any specific requirements of the facility or system
02

Conditions for selection

Depending on the case, one may prefer the smaller and cheaper heat exchanger if: - Initial cost is a major concern - Space available at the facility is limited - The operating cost difference between the larger and smaller pump is not significant On the other hand, the larger and more expensive heat exchanger may be chosen if: - Long term operation costs (such as energy consumption) outbalance the initial investment - Space is not a constraint - Better efficiency is prioritized due to environmental or system requirements
03

Steps in heat exchanger selection

When selecting a heat exchanger for cooling a hot liquid chemical, the following steps should be followed: 1. Define the application requirements: Determine the specific cooling duty, required temperature change, flow rates, operating pressures, and any chemical compatibility or safety concerns. 2. Determine the type and material of construction: Based on the application requirements, select the most suitable type of heat exchanger (plate, shell and tube, spiral, etc.) and the material of construction (copper, aluminum, stainless steel, etc.) 3. Calculate the heat transfer area: Based on the selected heat exchanger type and material, calculate the required heat transfer surface area using the heat transfer rate, temperature difference, and an estimated heat transfer coefficient. 4. Select a heat exchanger model: Based on the calculated heat transfer area and the specific requirements of the system, select the most appropriate heat exchanger model that satisfies all the requirements. 5. Perform economic analysis: Assess and compare the total costs of ownership (including initial cost, operation cost, and maintenance cost) of the available options and select the heat exchanger with the most favorable balance between performance and cost. 6. Procure and install the selected heat exchanger: Finally, purchase the chosen heat exchanger and install it in the facility according to the proper integration and safety guidelines.

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Most popular questions from this chapter

Water \(\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters the \(2.5\)-cm-internaldiameter tube of a double-pipe counterflow heat exchanger at \(20^{\circ} \mathrm{C}\) at a rate of $2.2 \mathrm{~kg} / \mathrm{s}\(. Water is heated by steam condensing at \)120^{\circ} \mathrm{C}\left(h_{f g}=2203 \mathrm{~kJ} / \mathrm{kg}\right)$ in the shell. If the overall heat transfer coefficient of the heat exchanger is $700 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, determine the length of the tube required in order to heat the water to \(80^{\circ} \mathrm{C}\) using \((a)\) the LMTD method and \((b)\) the \(\varepsilon-\mathrm{NTU}\) method.

Steam is to be condensed on the shell side of a twoshell-passes and eight- tube-passes condenser, with 20 tubes in each pass. Cooling water enters the tubes at a rate of \(2 \mathrm{~kg} / \mathrm{s}\). If the heat transfer area is \(14 \mathrm{~m}^{2}\) and the overall heat transfer coefficient is $1800 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, the effectiveness of this condenser is (a) \(0.70\) (b) \(0.80\) (c) \(0.90\) (d) \(0.95\) (e) \(1.0\)

Ethanol is vaporized at $78^{\circ} \mathrm{C}\left(h_{f \mathrm{~g}}=846 \mathrm{~kJ} / \mathrm{kg}\right)$ in a double-pipe parallel-flow heat exchanger at a rate of \(0.04 \mathrm{~kg} / \mathrm{s}\) by hot oil \(\left(c_{p}=2200 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) that enters at \(115^{\circ} \mathrm{C}\). If the heat transfer surface area and the overall heat transfer coefficients are \(6.2 \mathrm{~m}^{2}\) and $320 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, respectively, determine the outlet temperature and the mass flow rate of oil using \((a)\) the LMTD method and \((b)\) the \(\varepsilon-\mathrm{NTU}\) method.

Consider a double-pipe counterflow heat exchanger. In order to enhance heat transfer, the length of the heat exchanger is now doubled. Do you think its effectiveness will also double?

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 12 times the inner surface area, the overall heat transfer coefficient of this heat exchanger based on the inner surface area is (a) \(760 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (b) \(832 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (c) \(947 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (d) \(1075 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (e) \(1210 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\)

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