In the heat transfer relation \(\dot{Q}=U A_{s} F \Delta T_{\mathrm{lm}}\) for a heat exchanger, what is the quantity \(F\) called? What does it represent? Can \(F\) be greater than one?

Short Answer

Expert verified
Answer: The quantity F in the heat transfer relation for a heat exchanger is called the "correction factor." It represents the ratio of the actual heat transfer rate to the heat transfer rate under ideal conditions (perfect counterflow or parallel flow). F cannot be greater than one, as it would indicate that the heat exchanger operates more efficiently than the ideal case, which is not possible.

Step by step solution

01

Understand the heat transfer relation

The heat transfer relation for a heat exchanger is given by the equation: \(\dot{Q}=U A_{s} F \Delta T_{\mathrm{lm}}\) In this equation, \(\dot{Q}\) = Rate of heat transfer \(U\) = Overall heat transfer coefficient \(A_s\) = Surface area of the heat exchanger \(F\) = Correction factor for the heat exchanger \(\Delta T_{\mathrm{lm}}\) = Logarithmic mean temperature difference
02

Define the correction factor (F)

The quantity \(F\) is called the "correction factor" for the heat exchanger. It is used to account for the deviation from ideal counterflow or parallel flow conditions, caused by the actual temperature profiles in complex heat exchangers with multi-passes or cross-flow arrangements.
03

Explain the role of F and its possible values

The correction factor \(F\) represents the ratio of the actual heat transfer rate to the heat transfer rate under ideal conditions (perfect counterflow or parallel flow). It is used to modify the heat transfer equation to account for non-ideal conditions that may occur in real heat exchangers. As for the possible values of \(F\), it can vary between 0 and 1. If \(F = 1\), it indicates that the heat exchanger operates under ideal or perfect counterflow conditions with no deviation in temperature profile. On the other hand, if \(F = 0\), it means that there is virtually no heat transfer taking place. In practice, for most heat exchangers, the value of \(F\) typically lies between 0.7 and 0.9. It is important to note that \(F\) cannot be greater than 1, as it would indicate that the heat exchanger operates more efficiently than the ideal case, which is not possible.

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Most popular questions from this chapter

In a one-shell and eight-tube pass heat exchanger, the temperature of water flowing at rate of \(50,000 \mathrm{lbm} / \mathrm{h}\) is raised from \(70^{\circ} \mathrm{F}\) to \(150^{\circ} \mathrm{F}\). Hot air \(\left(c_{p}=0.25 \mathrm{Btu} / \mathrm{lbm} \cdot{ }^{\circ} \mathrm{F}\right)\) that flows on the tube side enters the heat exchanger at \(600^{\circ} \mathrm{F}\) and exits at \(300^{\circ} \mathrm{F}\). If the convection heat transfer coefficient on the outer surface of the tubes is \(30 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}\), determine the surface area of the heat exchanger using both LMTD and \(\varepsilon-\mathrm{NTU}\) methods. Account for the possible fouling resistance of \(0.0015\) and \(0.001 \mathrm{~h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F} /\) Btu on water and air side, respectively.

Reconsider Prob. 11-131. Using EES (or other) software, plot the number of tube passes as a function of water velocity as it varies from \(1 \mathrm{~m} / \mathrm{s}\) to \(8 \mathrm{~m} / \mathrm{s}\), and discuss the results.

A cross-flow 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.

Under what conditions can a counter-flow heat exchanger have an effectiveness of one? What would your answer be for a parallel-flow heat exchanger?

A test is conducted to determine the overall heat transfer coefficient in a shell-and-tube oil-to-water heat exchanger that has 24 tubes of internal diameter \(1.2 \mathrm{~cm}\) and length \(2 \mathrm{~m}\) in a single shell. Cold water \(\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters the tubes at \(20^{\circ} \mathrm{C}\) at a rate of \(3 \mathrm{~kg} / \mathrm{s}\) and leaves at \(55^{\circ} \mathrm{C}\). Oil \(\left(c_{p}=2150 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) flows through the shell and is cooled from \(120^{\circ} \mathrm{C}\) to \(45^{\circ} \mathrm{C}\). Determine the overall heat transfer coefficient \(U_{i}\) of this heat exchanger based on the inner surface area of the tubes.

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