Under what conditions can the overall heat transfer coefficient of a heat exchanger be determined from \(U=\) \(\left(1 / h_{i}+1 / h_{o}\right)^{-1} ?\)

Short Answer

Expert verified
Answer: The formula can be used when the heat exchanger is simple, operating at steady-state, has fully developed flow in both inside and outside regions, has heat transfer due to convection only, and is free of additional factors such as fouling or temperature-dependent fluid properties.

Step by step solution

01

Recap on heat transfer coefficients

A heat transfer coefficient is a parameter that quantifies the rate of heat transfer across a surface due to a temperature difference across that surface. The heat transfer coefficient represents the convective heat transfer between the fluid and the surface. There are two heat transfer coefficients in the given formula: \(h_{i}\) (the inside surface) and \(h_{o}\) (the outside surface).
02

Discuss what affects the overall heat transfer coefficient

The overall heat transfer coefficient (U) is dependent on several factors, such as the type of heat exchanger, fluid properties and flow rates, surface conditions, and the presence of any additional resistances (like thermal resistance due to fouling or wall conduction). The provided formula assumes that all these factors are incorporated in the heat transfer coefficients.
03

Identify when the provided formula can be utilized

The formula \(U=\) \(\left(1 / h_{i}+1 / h_{o}\right)^{-1}\) can be used to determine the overall heat transfer coefficient (U) of a heat exchanger under the following conditions: - The heat exchanger is simple and has no additional complexities or features that would affect the overall heat transfer. - The flow is steady-state and fully developed in both the inside and outside regions. - Heat transfer is only due to convection, and other modes of heat transfer (e.g., radiation and conduction) can be neglected. - There is no significant fouling present in the heat exchanger that would affect the overall heat transfer coefficient. - Fluid properties are not significantly affected by temperature or local conditions. In summary, the formula can be used to determine the overall heat transfer coefficient for a heat exchanger, provided that the heat exchanger is relatively simple, operating at steady-state, and free of additional factors such as fouling or temperature-dependent fluid properties.

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Most popular questions from this chapter

Can the temperature of the cold fluid rise above the inlet temperature of the hot fluid at any location in a heat exchanger? Explain.

Consider a shell-and-tube water-to-water heat exchanger with identical mass flow rates for both the hotand cold-water streams. Now the mass flow rate of the cold water is reduced by half. Will the effectiveness of this heat exchanger increase, decrease, or remain the same as a result of this modification? Explain. Assume the overall heat transfer coefficient and the inlet temperatures remain the same.

Consider an oil-to-oil double-pipe heat exchanger whose flow arrangement is not known. The temperature measurements indicate that the cold oil enters at \(20^{\circ} \mathrm{C}\) and leaves at \(55^{\circ} \mathrm{C}\), while the hot oil enters at \(80^{\circ} \mathrm{C}\) and leaves at \(45^{\circ} \mathrm{C}\). Do you think this is a parallel-flow or counter-flow heat exchanger? Why? Assuming the mass flow rates of both fluids to be identical, determine the effectiveness of this heat exchanger.

In a parallel-flow heat exchanger, the NTU is calculated to be \(2.5\). The lowest possible effectiveness for this heat exchanger is (a) \(10 \%\) (b) \(27 \%\) (c) \(41 \%\) (d) \(50 \%\) (e) \(92 \%\)

A shell-and-tube heat exchanger with 2-shell passes and 4-tube passes is used for cooling oil \(\left(c_{p}=2.0 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\) from \(125^{\circ} \mathrm{C}\) to \(55^{\circ} \mathrm{C}\). The coolant is water, which enters the shell side at \(25^{\circ} \mathrm{C}\) and leaves at \(46^{\circ} \mathrm{C}\). The overall heat transfer coefficient is \(900 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). For an oil flow rate of \(10 \mathrm{~kg} / \mathrm{s}\), calculate the cooling water flow rate and the heat transfer area.

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