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What are the common causes of fouling in a heat exchanger? How does fouling affect heat transfer and pressure drop?

Short Answer

Expert verified
Answer: The common causes of fouling in a heat exchanger include particulate fouling, chemical fouling, biological fouling, and corrosion fouling. Fouling affects heat transfer by increasing the thermal resistance, lowering the heat transfer coefficient, and reducing the heat exchanger's efficiency. Additionally, fouling increases the pressure drop, leading to higher fluid friction losses and additional energy consumption for pumping.

Step by step solution

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1. Introduction to Heat Exchangers and Fouling

A heat exchanger is a device that transfers heat between two fluids with different temperatures without mixing them. Fouling is the accumulation of unwanted materials on the surfaces of the heat exchanger, which affects its performance and efficiency.
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2. Common Causes of Fouling

Various factors contribute to the fouling of heat exchangers. Some of the common causes are: a. Particulate fouling: It occurs due to the deposition of suspended particles present in the fluid. These particles can be in the form of dirt, scale, or rust. b. Chemical fouling: It results from the precipitation of dissolved solids in the fluid, such as salts, which form scale layers on the heat transfer surfaces. c. Biological fouling: It is caused by the colonization and growth of microorganisms, like algae or bacteria, on the heat transfer surfaces. d. Corrosion fouling: It happens when the heat exchanger materials undergo a chemical reaction with the surrounding fluids, forming corrosion products that deposit on the surfaces.
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3. Impact of Fouling on Heat Transfer

Fouling in a heat exchanger has a significant effect on heat transfer, as it reduces the overall heat transfer coefficient. The presence of fouling layers increases the thermal resistance between the fluids, resulting in decreased heat transfer efficiency. The thick layers act as a barrier, impeding the flow of heat from the hotter fluid to the cooler one. Consequently, this may lead to a higher temperature difference required to achieve the desired heat transfer and may cause the heat exchanger to operate at a lower effectiveness.
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4. Impact of Fouling on Pressure Drop

Fouling also has an impact on the pressure drop across the heat exchanger. The accumulated layers obstruct the flow of fluids, reducing the effective flow area within the heat exchanger. This forces the fluid to flow through narrower channels and increases the frictional losses in the system. As a result, the pressure drop across the heat exchanger becomes higher, leading to an additional energy consumption in pumping the fluids. In severe cases, fouling can lead to complete blockage of the flow channels, rendering the heat exchanger ineffective.
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5. Conclusion

In summary, fouling in heat exchangers is caused by various factors, including particulate, chemical, biological, and corrosion fouling. Fouling affects heat transfer by increasing the thermal resistance, lowering the heat transfer coefficient, and reducing the heat exchanger's efficiency. Moreover, it increases the pressure drop, leading to higher fluid friction losses and additional energy consumption for pumping. Regular maintenance, including cleaning and inspection, is crucial in mitigating fouling and optimizing the performance of heat exchangers.

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Most popular questions from this chapter

Consider a closed-loop heat exchanger that carries exit water $\left(c_{p}=1 \mathrm{Btu} / \mathrm{lbm} \cdot{ }^{\circ} \mathrm{F}\right.$ and \(\left.\rho=62.4 \mathrm{lbm} / \mathrm{ft}^{3}\right)\) of a condenser side initially at \(100^{\circ} \mathrm{F}\). The water flows through a 500 -ft-long stainless steel pipe of 1 in inner diameter immersed in a large lake. The temperature of lake water surrounding the heat exchanger is $45^{\circ} \mathrm{F}$. The overall heat transfer coefficient of the heat exchanger is estimated to be $250 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}$. What is the exit temperature of the water from the immersed heat exchanger if it flows through the pipe at an average velocity of \(9 \mathrm{ft} / \mathrm{s}\) ? Use the \(\varepsilon-N T U\) method for analysis.

In a parallel-flow, water-to-water heat exchanger, the hot water enters at \(75^{\circ} \mathrm{C}\) at a rate of \(1.2 \mathrm{~kg} / \mathrm{s}\) and cold water enters at \(20^{\circ} \mathrm{C}\) at a rate of $0.9 \mathrm{~kg} / \mathrm{s}$. The overall heat transfer coefficient and the surface area for this heat exchanger are \(750 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and \(6.4 \mathrm{~m}^{2}\), respectively. The specific heat for both the hot and cold fluids may be taken to be $4.18 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}$. For the same overall heat transfer coefficient and the surface area, the increase in the effectiveness of this heat exchanger if counterflow arrangement is used is (a) \(0.09\) (b) \(0.11\) (c) \(0.14\) (d) \(0.17\) (e) \(0.19\)

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) \(1210 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\)

In a textile manufacturing plant, the waste dyeing water $\left(c_{p}=4295 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( at \)80^{\circ} \mathrm{C}$ is to be used to preheat fresh water $\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( at \)10^{\circ} \mathrm{C}$ at the same flow rate in a double-pipe counterflow heat exchanger. The heat transfer surface area of the heat exchanger is \(1.65 \mathrm{~m}^{2}\), and the overall heat transfer coefficient is $625 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. If the rate of heat transfer in the heat exchanger is \)35 \mathrm{~kW}$, determine the outlet temperature and the mass flow rate of each fluid stream.

The National Sanitation Foundation (NSF) standard for commercial warewashing equipment (ANSL/NSF 3) requires that the final rinse water temperature be between 82 and \(90^{\circ} \mathrm{C}\). A shell-and-tube heat exchanger is to heat \(0.5 \mathrm{~kg} / \mathrm{s}\) of water $\left(c_{p}=4200 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( from 48 to \)86^{\circ} \mathrm{C}$ by geothermal brine flowing through a single shell pass. The heated water is then fed into commercial warewashing equipment. The geothermal brine enters and exits the heat exchanger at 98 and \(90^{\circ} \mathrm{C}\), respectively. The water flows through four thin-walled tubes, each with a diameter of $25 \mathrm{~mm}$, with all four tubes making the same number of passes through the shell. The tube length per pass for each tube is \(5 \mathrm{~m}\). The corresponding convection heat transfer coefficients on the outer and inner tube surfaces are 1050 and $2700 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, respectively. The estimated fouling factor caused by the accumulation of deposit from the geothermal brine is $0.0002 \mathrm{~m}^{2} . \mathrm{K} / \mathrm{W}$. Determine the number of passes required for the tubes inside the shell to heat the water to \(86^{\circ} \mathrm{C}\), within the temperature range required by the ANIS/NSF 3 standard.

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