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A counterflow heat exchanger is stated to have an overall heat transfer coefficient based on outside tube area of $50 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F}$ when operating at design and clean conditions. After a period of use, scale buildup in the heat exchanger gives a fouling factor of $0.002 \mathrm{~h} \cdot \mathrm{ft}^{2},{ }^{\circ} \mathrm{F} /\( Btu. Determine \)(a)$ the overall heat transfer coefficient of the heat exchanger and \((b)\) the percentage change in the overall heat transfer coefficient due to the scale buildup.

Short Answer

Expert verified
Answer: The overall heat transfer coefficient with the fouling factor is 48.54 Btu/h·ft²·°F, and the percentage change in the overall heat transfer coefficient due to the scale buildup is -2.92%.

Step by step solution

01

Given values.

The given values are \(U_{clean} = 50 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^2 \cdot{ }^{\circ} \mathrm{F}\) and fouling factor \(R_f = 0.002 \mathrm{~h} \cdot \mathrm{ft}^2,{ }^{\circ} \mathrm{F} /\) Btu.
02

Calculate the overall heat transfer coefficient with the fouling factor.

First, we need to calculate the overall heat transfer coefficient with the fouling factor using the formula: $$\frac{1}{U_{fouled}} = \frac{1}{U_{clean}} + R_f$$ Plugging in the values, we get: $$\frac{1}{U_{fouled}} = \frac{1}{50 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^2 \cdot{ }^{\circ} \mathrm{F}} + 0.002 \mathrm{~h} \cdot \mathrm{ft}^2,{ }^{\circ} \mathrm{F} / \mathrm{Btu}$$ Solving for \(U_{fouled}\), we get: $$U_{fouled} = \frac{1}{\frac{1}{50} + 0.002} = 48.54 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^2 \cdot{ }^{\circ} \mathrm{F}$$
03

Calculate the percentage change in the overall heat transfer coefficient.

Now, we need to calculate the percentage change in the overall heat transfer coefficient using the formula: $$\% \text{ Change} = \frac{U_{fouled} - U_{clean}}{U_{clean}} \times 100$$ Plugging in the values, we get: $$\% \text{ Change} = \frac{48.54 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^2 \cdot{ }^{\circ} \mathrm{F} - 50 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^2 \cdot{ }^{\circ} \mathrm{F}}{50 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^2 \cdot{ }^{\circ} \mathrm{F}} \times 100$$ $$\% \text{ Change} = -2.92 \%$$ The overall heat transfer coefficient with the fouling factor is \(48.54 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^2 \cdot{ }^{\circ} \mathrm{F}\), and the percentage change in the overall heat transfer coefficient due to the scale buildup is \(-2.92 \%\).

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Most popular questions from this chapter

A double-pipe parallel-flow heat exchanger is used to heat cold tap water with hot water. Hot water $\left(c_{p}=4.25 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( enters the tube at \)85^{\circ} \mathrm{C}$ at a rate of \(1.4 \mathrm{~kg} / \mathrm{s}\) and leaves at \(50^{\circ} \mathrm{C}\). The heat exchanger is not well insulated, and it is estimated that 3 percent of the heat given up by the hot fluid is lost from the heat exchanger. If the overall heat transfer coefficient and the surface area of the heat exchanger are \(1150 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and $4 \mathrm{~m}^{2}$, respectively, determine the rate of heat transfer to the cold water and the log mean temperature difference for this heat exchanger.

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