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In a particular application involving fluid flow at a rate \(\dot{m}\) through a circular tube of length \(L\) and diameter \(D\), the surface heat flux is known to have a sinusoidal variation with \(x\), which is of the form \(q_{s}^{\prime \prime}(x)=q_{s, m}^{\prime \prime} \sin (\pi x / L)\). The maximum flux, \(q_{s, m}^{n}\), is a known constant, and the fluid enters the tube at a known temperature, \(T_{m, i}\) Assuming the convection coefficient to be constant, how do the mean temperature of the fluid and the surface temperature vary with \(x\) ?

Short Answer

Expert verified
The short answer to the question is as follows: By using the convective heat transfer correlation, \(q_s^{\prime \prime}(x) = h (T_s(x) - T_m(x))\), and substituting the given surface heat flux function, \(q_{s, m}^{\prime \prime} \sin (\pi x / L) = h (T_s(x) - T_m(x))\), we can integrate both sides of this equation with respect to \(x\). By applying the given boundary conditions, such as the fluid's initial mean temperature \(T_{m, i}\), we can find the functions \(T_m(x)\) and \(T_s(x)\), which describe how the mean temperature of the fluid and the surface temperature vary with \(x\).

Step by step solution

01

Convective heat transfer correlation.

In order to find the relationship between the fluid's mean temperature and the surface temperature, we can use the convective heat transfer correlation: \(q_s^{\prime \prime}(x) = h \cdot (T_s(x) - T_m(x))\), Where \(q_s^{\prime \prime}(x)\) is the surface heat flux, \(h\) is the convection coefficient, \(T_s(x)\) is the surface temperature, and \(T_m(x)\) is the mean temperature of the fluid.
02

Express the surface heat flux given in the problem.

We are given the surface heat flux function in the problem: \(q_s^{\prime \prime}(x) = q_{s, m}^{\prime \prime} \sin (\pi x / L)\).
03

Substitute the surface heat flux expression in the convective heat transfer equation.

By substituting the given surface heat flux in the convective heat transfer correlation, we get: \(q_{s, m}^{\prime \prime} \sin (\pi x / L) = h (T_s(x) - T_m(x))\).
04

Integrate to find the mean temperature of the fluid and the surface temperature variation with x.

In order to find the mean temperature of the fluid \((T_m(x))\) and the surface temperature \((T_s(x))\), we need to integrate the previous equation with respect to \(x\). Integrating the left-hand side: \(\int q_{s, m}^{\prime \prime} \sin (\pi x / L) dx = q_{s, m}^{\prime \prime} \int \sin(\pi x / L) dx\). Integrating the right-hand side: \(h \int (T_s(x) - T_m(x)) dx\). By integrating and applying the given boundary conditions (such as the fluid's initial mean temperature \(T_{m, i}\)), we can find the functions \(T_m(x)\) and \(T_s(x)\), which describe how the mean temperature of the fluid and the surface temperature vary with \(x\).

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Key Concepts

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

Mean Temperature Variation
To understand how the mean temperature of the fluid varies as it moves along the tube, consider the concept of convective heat transfer. This process occurs when heat is transferred between a solid surface and a fluid in motion. The mean temperature, denoted as \(T_m(x)\), reflects the average temperature of the fluid across the tube's cross-section at any given point \(x\).

In this scenario, the mean temperature changes because of the varying surface heat flux, which supplies heat to the fluid. This transfer of heat is influenced by the convection coefficient \(h\), determining the rate at which the fluid's temperature changes. Initially, the fluid enters the tube with a known mean temperature \(T_{m, i}\), and as it travels, the mean temperature gradually increases or decreases determined by the heat flux and convection dynamics. Therefore, by integrating the heat transfer equation, you can determine a function for \(T_m(x)\) that describes its dependency on the position within the tube.
Surface Heat Flux
The surface heat flux \(q_s^{\prime \prime}(x)\) is a critical parameter that influences how heat is exchanged between the tube's surface and the fluid. It is defined as the rate of heat transfer per unit area through the surface. In this situation, it is characterized by a sinusoidal distribution dependent on the distance \(x\) along the tube.

By understanding this variation, one can predict areas where the fluid gains or loses heat more intensely, guiding engineers to design more efficient heat exchangers or cooling systems. The surface heat flux in this problem is given by \(q_{s, m}^{\prime \prime} \sin(\pi x / L)\), where \(q_{s, m}^{\prime \prime}\) is the maximum heat flux. This expression shows a periodic variation, illustrating portions of high and low heat exchange as the fluid traverses the tube.
Sinusoidal Heat Flux Distribution
The sinusoidal heat flux distribution describes how the heat flux varies along the length of the tube in a wave-like pattern. Mathematically, it is represented by the function \(q_s^{\prime \prime}(x) = q_{s, m}^{\prime \prime} \sin(\pi x / L)\). This type of variation is often encountered in applications where the heat input is cyclic, like in oscillating thermal processes.

The sinusoidal pattern allows for prediction of the heat transfer intensity at each point \(x\). When the sine function reaches its peak, the surface heat flux is at its maximum, \(q_{s, m}^{\prime \prime}\), indicating a high rate of heat transfer. Conversely, at the zeros of the sine function, the flux drops to zero, indicating no heat transfer at those points.

This knowledge is fundamental in designing heating or cooling processes that require precise control of heat distribution over a component or a pipe.
Convection Coefficient
The convection coefficient \(h\) is a pivotal factor in the realm of heat transfer, representing the efficiency of heat transfer between the solid surface and the fluid in motion. Numeric values of \(h\) depend on several factors, such as the fluid's velocity, viscosity, and thermal properties, as well as the geometric characteristics of the surface.

In the exercise, \(h\) is considered constant, simplifying calculations and allowing direct integration of heat transfer equations to find temperature distributions. Along with the surface heat flux and temperature difference between the surface and the fluid, the convection coefficient directly influences the rate of heat transfer. Higher values of \(h\) suggest a more efficient heat transfer process, which may be desired in applications demanding rapid thermal response.
  • Enhances heat transfer process efficiency.
  • Determines the rate of temperature change in fluid.
  • Depends on fluid motion and surface characteristics.
Understanding the convection coefficient's role is essential in optimizing designs of systems where heat exchange is critical, like in heating, ventilation, and air conditioning systems, as well as in industrial applications.

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Most popular questions from this chapter

A flat-plate solar collector is used to heat atmospheric air flowing through a rectangular channel. The bottom surface of the channel is well insulated, while the top surface is subjected to a uniform heat flux \(q_{o}^{\prime \prime}\), which is due to the net effect of solar radiation absorption and heat exchange between the absorber and cover plates. (a) Beginning with an appropriate differential control volume, obtain an equation that could be used to determine the mean air temperature \(T_{m}(x)\) as a function of distance along the channel. Solve this equation to obtain an expression for the mean temperature of the air leaving the collector. (b) With air inlet conditions of \(\dot{m}=0.1 \mathrm{~kg} / \mathrm{s}\) and \(T_{m, i}=40^{\circ} \mathrm{C}\), what is the air outlet temperature if \(L=3 \mathrm{~m}, w=1 \mathrm{~m}\), and \(q_{o}^{\prime \prime}=700 \mathrm{~W} / \mathrm{m}^{2}\) ? The specific heat of air is \(c_{p}=1008 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\).

A cold plate is an active cooling device that is attached to a heat-generating system in order to dissipate the heat while maintaining the system at an acceptable temperature. It is typically fabricated from a material of high thermal conductivity, \(k_{\text {cp, }}\), within which channels are machined and a coolant is passed. Consider a copper cold plate of height \(H\) and width \(W\) on a side, within which water passes through square channels of width \(w=h\). The transverse spacing between channels \(\delta\) is twice the spacing between the sidewall of an outer channel and the sidewall of the cold plate. Consider conditions for which equivalent heat-generating systems are attached to the top and bottom of the cold plate, maintaining the corresponding surfaces at the same temperature \(T_{s}\). The mean velocity and inlet temperature of the coolant are \(u_{m}\) and \(T_{m i}\), respectively. (a) Assuming fully developed turbulent flow throughout each channel, obtain a system of equations that may be used to evaluate the total rate of heat transfer to the cold plate, \(q\), and the outlet temperature of the water, \(T_{m, o}\), in terms of the specified parameters. (b) Consider a cold plate of width \(W=100 \mathrm{~mm}\) and height \(H=10 \mathrm{~mm}\), with 10 square channels of width \(w=6 \mathrm{~mm}\) and a spacing of \(\delta=4 \mathrm{~mm}\) between channels. Water enters the channels at a temperature of \(T_{m, i}=300 \mathrm{~K}\) and a velocity of \(u_{m}=2 \mathrm{~m} / \mathrm{s}\). If the top and bottom cold plate surfaces are at \(T_{s}=360 \mathrm{~K}\), what is the outlet water temperature and the total rate of heat transfer to the cold plate? The thermal conductivity of the copper is \(400 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), while average properties of the water may be taken to be \(\rho=984 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=4184 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}, \mu=489 \times\) \(10^{-6} \mathrm{~N} \cdot \mathrm{s} / \mathrm{m}^{2}, k=0.65 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), and \(P r=3.15\). Is this a good cold plate design? How could its performance be improved?

8.106 Consider the pharmaceutical product of Problem 8.27. Prior to finalizing the manufacturing process, test trials are performed to experimentally determine the dependence of the shelf life of the drug as a function of the sterilization temperature. Hence, the sterilization temperature must be carefully controlled in the trials. To promote good mixing of the pharmaceutical and, in turn, relatively uniform outlet temperatures across the exit tube area, experiments are performed using a device that is constructed of two interwoven coiled tubes, each of 10 -mm diameter. The thin-walled tubing is welded to a solid high thermal conductivity rod of diameter \(D_{r}=40 \mathrm{~mm}\). One tube carries the pharmaceutical product at a mean velocity of \(u_{p}=0.1 \mathrm{~m} / \mathrm{s}\) and inlet temperature of \(25^{\circ} \mathrm{C}\), while the second tube carries pressurized liquid water at \(u_{w}=0.12 \mathrm{~m} / \mathrm{s}\) with an inlet temperature of \(127^{\circ} \mathrm{C}\). The tubes do not contact each other but are each welded to the solid metal rod, with each tube making 20 turns around the rod. The exterior of the apparatus is well insulated. (a) Determine the outlet temperature of the pharmaceutical product. Evaluate the liquid water properties at \(380 \mathrm{~K}\). (b) Investigate the sensitivity of the pharmaceutical's outlet temperature to the velocity of the pressurized water over the range \(0.10

Water flowing at \(2 \mathrm{~kg} / \mathrm{s}\) through a \(40-\mathrm{mm}\)-diameter tube is to be heated from 25 to \(75^{\circ} \mathrm{C}\) by maintaining the tube surface temperature at \(100^{\circ} \mathrm{C}\). (a) What is the required tube length for these conditions? (b) To design a water heating system, we wish to consider using tube diameters in the range from 30 to \(50 \mathrm{~mm}\). What are the required tube lengths for water flow rates of 1,2 , and \(3 \mathrm{~kg} / \mathrm{s}\) ? Represent this design information graphically. (c) Plot the pressure gradient as a function of tube diameter for the three flow rates. Assume the tube wall is smooth.

Consider pressurized liquid water flowing at \(\dot{m}=0.1 \mathrm{~kg} / \mathrm{s}\) in a circular tube of diameter \(D=0.1 \mathrm{~m}\) and length \(L=6 \mathrm{~m}\). (a) If the water enters at \(T_{m, i}=500 \mathrm{~K}\) and the surface temperature of the tube is \(T_{s}=510 \mathrm{~K}\), determine the water outlet temperature \(T_{\text {m,o. }}\). (b) If the water enters at \(T_{m, i}=300 \mathrm{~K}\) and the surface temperature of the tube is \(T_{s}=310 \mathrm{~K}\), determine the water outlet temperature \(T_{\text {m, } \sigma}\). (c) If the water enters at \(T_{m, i}=300 \mathrm{~K}\) and the surface temperature of the tube is \(T_{s}=647 \mathrm{~K}\), discuss whether the flow is laminar or turbulent.

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