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In flow across tube banks, how does the heat transfer coefficient vary with the row number in the flow direction? How does it vary with in the transverse direction for a given row number?

Short Answer

Expert verified
Answer: In flow across tube banks, the heat transfer coefficient decreases with increasing row number in the flow direction due to flow disturbance and stabilization created by upstream tubes. However, it remains relatively constant in the transverse direction for a given row number due to the constant crossflow effect and uniform flow distribution.

Step by step solution

01

Understand the Tube Bank Setup and Objectives

In the case of flow across tube banks, tubes are arranged in a series of rows perpendicular to the flow direction. Flow direction is the direction along which the fluid flows around the tubes while transverse direction is perpendicular to the flow direction. The main objective is to determine the variation of heat transfer coefficient with respect to row number in both flow and transverse direction.
02

Identify Heat Transfer Coefficient Variation Factors

The heat transfer coefficient involves the convective heat transfer between the fluid flowing across the tubes and the surface of the tubes in the heat exchanger. Some factors influencing the heat transfer coefficient in tube banks include tube diameter, flow velocity, tube arrangement, fluid properties, and row number. Among these factors, the analysis focuses on the row number in the flow direction and the transverse direction for a given row number.
03

Analyze Heat Transfer Coefficient Dependence on Row Number in Flow Direction

Due to the developing flow across tubes in series, the heat transfer coefficients in tube banks often decrease with increasing row numbers. The reason behind this is the flow disturbance created by upstream tubes affecting downstream tubes. As we go downstream in the flow direction, the flow patterns around the tubes start to stabilize, which in turn, reduces turbulence, and the heat transfer coefficients subsequently decrease.
04

Examine Heat Transfer Coefficient Dependence on Row Number in Transverse Direction

For a given row number, the heat transfer coefficient does not significantly vary in the transverse direction. This is because the tube arrangement generates a constant crossflow effect on the tubes across the same row, allowing almost uniform flow distribution and turbulence. Thus, the heat transfer coefficient remains relatively constant in the transverse direction. In summary, the heat transfer coefficient decreases with increasing row number in the flow direction while remaining relatively constant in the transverse direction for a given row number in flow across tube banks.

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Convective Heat Transfer
Understanding convective heat transfer is like getting to know a critical messenger in the energy world. It's a type of heat transport that occurs when a fluid—such as air or water—moves across a surface, carrying energy with it. Imagine you're cooking soup; the heat from the stove warms the pot, which then warms the soup through conduction. But, it's the motion of the soup as you stir that represents convective heat transfer, evenly distributing the warmth.

Within a heat exchanger, the heat transfer coefficient is a quantitative measure of convective heat transfer. It's affected by factors like the fluid's velocity, its properties (like viscosity and thermal conductivity), the surface geometry, and the temperature difference between the surface and the fluid. In the case of a fluid flowing across a tube bank, the heat transfer coefficient is crucial for predicting how well the heat exchanger will perform, determining how quickly energy is exchanged between the fluid and the tubes.
Flow Across Tube Banks
Picturing flow across tube banks can be visualized by considering cars flowing through a crowded parking lot. The tubes are like a series of cars parked in rows, and the fluid is like the wind weaving through them. In this setup, the fluid encounters a sequence of obstacles—our 'parked cars'—affecting how it moves.

The flow starts laminar (smooth) but can quickly become turbulent as it wraps around each tube, forming vortices and wake regions. This interaction between fluid particles generates enhanced mixing, contributing to the convective heat transfer coefficient's nature. The setup in tube banks can be in-line or staggered, which influences the flow patterns and, consequently, the heat transfer rates. The examination of how these flows behave requires a detailed understanding of fluid dynamics principles and heat transfer mechanisms.
Turbulence and Heat Transfer
Diving into the relationship between turbulence and heat transfer is akin to stirring that pot of soup more vigorously. As the fluid flow becomes more chaotic and turbulent, it leads to a larger transfer of heat. Turbulence enhances the mixing of the fluid particles, and as a result, areas of higher and lower temperature begin to blend more effectively.

In the context of tube banks, turbulence plays a critical role. Fluid hitting the first row of tubes generates a lot of disturbances, creating a high heat transfer coefficient. However, as the fluid progresses to subsequent rows, the turbulence initially produced diminishes, leading to a drop in the heat transfer coefficient. This is a delicate dance between flow dynamics and energy transfer, and engineers carefully consider these aspects while designing efficient heat exchangers.
Thermal Performance of Heat Exchangers
The thermal performance of heat exchangers encapsulates their effectiveness in transferring heat from one fluid to another. This performance hinges on several criteria, such as the heat transfer coefficient and the geometry of the heat exchange surface. Tube banks are the battleground where fluid mechanics and thermal dynamics come together to decide the fate of a heat exchanger's efficiency.

The design of the tube bank—its layout and surface characteristics—can significantly alter the thermal performance. An optimized design minimizes energy loss and maximizes transfer efficiency. The challenge is finding the right balance between the heat transfer enhancement due to turbulence and the pressure drop that too much turbulence can create. Engineers use various configurations and surface treatments to guide the flow for improved thermal performance, while also keeping an eye on the economic and practical constraints of heat exchanger design.

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Most popular questions from this chapter

Combustion air in a manufacturing facility is to be preheated before entering a furnace by hot water at \(90^{\circ} \mathrm{C}\) flowing through the tubes of a tube bank located in a duct. Air enters the duct at \(15^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\) with a mean velocity of \(3.8 \mathrm{~m} / \mathrm{s}\), and flows over the tubes in normal direction. The outer diameter of the tubes is \(2.1 \mathrm{~cm}\), and the tubes are arranged in-line with longitudinal and transverse pitches of \(S_{L}=S_{T}=5 \mathrm{~cm}\). There are eight rows in the flow direction with eight tubes in each row. Determine the rate of heat transfer per unit length of the tubes, and the pressure drop across the tube bank. Evaluate the air properties at an assumed mean temperature of \(20^{\circ} \mathrm{C}\) and 1 atm. Is this a good assumption?

On average, superinsulated homes use just 15 percent of the fuel required to heat the same size conventional home built before the energy crisis in the 1970 s. Write an essay on superinsulated homes, and identify the features that make them so energy efficient as well as the problems associated with them. Do you think superinsulated homes will be economically attractive in your area?

Air at \(25^{\circ} \mathrm{C}\) flows over a 5 -cm-diameter, \(1.7\)-m-long pipe with a velocity of \(4 \mathrm{~m} / \mathrm{s}\). A refrigerant at \(-15^{\circ} \mathrm{C}\) flows inside the pipe and the surface temperature of the pipe is essentially the same as the refrigerant temperature inside. Air properties at the average temperature are \(k=0.0240 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \operatorname{Pr}=0.735\), \(\nu=1.382 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\). The rate of heat transfer to the pipe is (a) \(343 \mathrm{~W}\) (b) \(419 \mathrm{~W}\) (c) \(485 \mathrm{~W}\) (d) \(547 \mathrm{~W}\) (e) \(610 \mathrm{~W}\)

Air \((k=0.028 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \operatorname{Pr}=0.7)\) at \(50^{\circ} \mathrm{C}\) flows along a 1 -m-long flat plate whose temperature is maintained at \(20^{\circ} \mathrm{C}\) with a velocity such that the Reynolds number at the end of the plate is 10,000 . The heat transfer per unit width between the plate and air is (a) \(20 \mathrm{~W} / \mathrm{m}\) (b) \(30 \mathrm{~W} / \mathrm{m}\) (c) \(40 \mathrm{~W} / \mathrm{m}\) (d) \(50 \mathrm{~W} / \mathrm{m}\) (e) \(60 \mathrm{~W} / \mathrm{m}\)

Hydrogen gas at \(1 \mathrm{~atm}\) is flowing in parallel over the upper and lower surfaces of a 3-m-long flat plate at a velocity of \(2.5 \mathrm{~m} / \mathrm{s}\). The gas temperature is \(120^{\circ} \mathrm{C}\) and the surface temperature of the plate is maintained at \(30^{\circ} \mathrm{C}\). Using the EES (or other) software, investigate the local convection heat transfer coefficient and the local total convection heat flux along the plate. By varying the location along the plate for \(0.2 \leq x \leq 3 \mathrm{~m}\), plot the local convection heat transfer coefficient and the local total convection heat flux as functions of \(x\). Assume flow is laminar but make sure to verify this assumption. 7-31 Carbon dioxide and hydrogen as ideal gases at \(1 \mathrm{~atm}\) and \(-20^{\circ} \mathrm{C}\) flow in parallel over a flat plate. The flow velocity of each gas is \(1 \mathrm{~m} / \mathrm{s}\) and the surface temperature of the 3 -m-long plate is maintained at \(20^{\circ} \mathrm{C}\). Using the EES (or other) software, evaluate the local Reynolds number, the local Nusselt number, and the local convection heat transfer coefficient along the plate for each gas. By varying the location along the plate for \(0.2 \leq x \leq 3 \mathrm{~m}\), plot the local Reynolds number, the local Nusselt number, and the local convection heat transfer coefficient for each gas as functions of \(x\). Discuss which gas has higher local Nusselt number and which gas has higher convection heat transfer coefficient along the plate. Assume flow is laminar but make sure to verify this assumption.

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