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

Short Answer

Expert verified
Answer: No, the temperature of the cold fluid cannot rise above the inlet temperature of the hot fluid in a heat exchanger due to the principle of energy conservation and the temperature relationships in the heat exchanger.

Step by step solution

01

Heat Exchanger Principle

In a heat exchanger, two fluids are separated by a solid wall, where one fluid transfers heat energy to the other fluid without any direct contact or mixing between the two fluids. The cold fluid gains thermal energy from the hot fluid, causing its temperature to rise while the hot fluid's temperature decreases.
02

Conservation of Energy

The principle of energy conservation states that energy cannot be created or destroyed, only converted from one form to another. In a heat exchanger, the total energy input equals the total energy output. This means that the thermal energy lost by the hot fluid must be equal to the thermal energy gained by the cold fluid.
03

Temperature Relationships

In a heat exchanger, the hot fluid's inlet temperature (T_{hi}) must always be higher than the cold fluid's inlet temperature (T_{ci}) for heat transfer to occur. As the fluids flow through the exchanger, heat is transferred from the hot fluid to the cold fluid, causing the hot fluid's exit temperature (T_{ho}) to be lower than its inlet temperature, and the cold fluid's exit temperature (T_{co}) to be higher than its inlet temperature. We have the following relationships: 1. T_{hi} > T_{ci} 2. T_{ho} < T_{hi} 3. T_{co} > T_{ci}
04

Cold Fluid's Temperature Rising Above Hot Fluid's Inlet Temperature

Based on the principle of energy conservation and temperature relationships in the heat exchanger, the cold fluid's exit temperature cannot rise above the hot fluid's inlet temperature. This is because the hot fluid will always lose thermal energy to the cold fluid, hence its exit temperature will always be lower than the inlet temperature. Therefore, T_{co} can never be greater than T_{hi}. In conclusion, the temperature of the cold fluid cannot rise above the inlet temperature of the hot fluid at any location in a heat exchanger.

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Most popular questions from this chapter

By taking the limit as \(\Delta T_{2} \rightarrow \Delta T_{1}\), show that when \(\Delta T_{1}=\Delta T_{2}\) for a heat exchanger, the \(\Delta T_{\mathrm{lm}}\) relation reduces to \(\Delta T_{\mathrm{lm}}=\Delta T_{1}=\Delta T_{2}\).

In a parallel-flow, liquid-to-liquid heat exchanger, the inlet and outlet temperatures of the hot fluid are \(150^{\circ} \mathrm{C}\) and $90^{\circ} \mathrm{C}\( while those of the cold fluid are \)30^{\circ} \mathrm{C}$ and \(70^{\circ} \mathrm{C}\), respectively. For the same overall heat transfer coefficient, the percentage decrease in the surface area of the heat exchanger if counterflow arrangement is used is (a) \(3.9 \%\) (b) \(9.7 \%\) (c) \(14.5 \%\) (d) \(19.7 \%\) (e) \(24.6 \%\)

A performance test is being conducted on a doublepipe counterflow 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 for a long time, it is suspected that fouling might have developed inside the heat exchanger that could affect 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?

A shell-and-tube heat exchanger with two shell passes and 12 tube passes is used to heat water $\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( in the tubes from \)20^{\circ} \mathrm{C}\( to \)70^{\circ} \mathrm{C}\( at a rate of \)4.5 \mathrm{~kg} / \mathrm{s}$. Heat is supplied by hot oil \(\left(c_{p}=2300 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) that enters the shell side at \(170^{\circ} \mathrm{C}\) at a rate of $10 \mathrm{~kg} / \mathrm{s}$. For a tube-side overall heat transfer coefficient of \(350 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), determine the heat transfer surface area on the tube side. Answer: \(25.7 \mathrm{~m}^{2}\)

The cardiovascular countercurrent heat exchanger has an overall heat transfer coefficient of \(100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Arterial blood enters at \(37^{\circ} \mathrm{C}\) and exits at \(27^{\circ} \mathrm{C}\). Venous blood enters at \(25^{\circ} \mathrm{C}\) and exits at $34^{\circ} \mathrm{C}$. Determine the mass flow rates of the arterial blood and venous blood in \(\mathrm{g} / \mathrm{s}\) if the specific heat of both arterial and venous blood is constant and equal to $3475 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\(, and the surface area of the heat transfer to occur is \)0.15 \mathrm{~cm}^{2}$.

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