/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 60 Fluid velocities can be measured... [FREE SOLUTION] | 91影视

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Fluid velocities can be measured using hot-film sensors, and a common design is one for which the sensing element forms a thin film about the circumference of a quartz rod. The film is typically comprised of a thin \((\sim 100 \mathrm{~nm})\) layer of platinum, whose electrical resistance is proportional to its temperature. Hence, when submerged in a fluid stream, an electric current may be passed through the film to maintain its temperature above that of the fluid. The temperature of the film is controlled by monitoring its electric resistance, and with concurrent measurement of the electric current, the power dissipated in the film may be determined. Proper operation is assured only if the heat generated in the film is transferred to the fluid, rather than conducted from the film into the quartz rod. Thermally, the film should therefore be strongly coupled to the fluid and weakly coupled to the quartz rod. This condition is satisfied if the Biot number is very large, \(B i=\bar{h} D / 2 k \geqslant 1\), where \(\bar{h}\) is the convection coefficient between the fluid and the film and \(k\) is the thermal conductivity of the rod. (a) For the following fluids and velocities, calculate and plot the convection coefficient as a function of velocity: (i) water, \(0.5 \leq V \leq 5 \mathrm{~m} / \mathrm{s}\); (ii) air, \(1 \leq V \leq 20 \mathrm{~m} / \mathrm{s}\). (b) Comment on the suitability of using this hot-film sensor for the foregoing conditions.

Short Answer

Expert verified
In summary, to find the convection coefficient as a function of velocity for both water and air, we first calculated the Prandtl and Reynolds numbers for each fluid. Then, using the Dittus-Boelter equation, we obtained the convection coefficients in the given velocity ranges. After plotting the convection coefficient against velocity, we analyzed the suitability of the hot-film sensor by calculating the Biot number and comparing it with 1. If the Biot number was greater than or equal to 1, the hot-film sensor was deemed suitable for proper operation under the given conditions.

Step by step solution

01

Understanding the Relations between Biot Number and Fluid Properties

The Biot number (\(Bi\)) is given by the formula: \(Bi=\bar{h} D / 2k\) where - \(\bar{h}\) is the convection coefficient between the fluid and the film, - \(D\) is the diameter of the cylindrical film - \(k\) is the thermal conductivity of the quartz rod. Since we're interested in the convection coefficient (\(\bar{h}\)), we can rearrange the formula to solve for it: \(\bar{h} = \frac{Bi \times 2k}{D}\) What we seek is a function relating the convection coefficient with the velocity of fluid flow over the sensor. To accomplish this, we can use the Nusselt number, which is a dimensionless number that relates the rate of heat transfer via convection. Using the Dittus-Boelter equation, we have: \(Nu_L = 0.023Re_L^{4/5}Pr^n\) where - \(Nu_L\) is the Nusselt number, - \(Re_L\) is the Reynolds number based on length, - \(Pr\) is the Prandtl number, and - \(n\) depends on whether the fluid is heated (n=0.4) or cooled (n=0.3).
02

Calculating the Convection Coefficient for Water and Air

To find the convection coefficient, we'll need to find the properties of water and air at the given velocities. For this purpose, you can refer to standard fluid properties tables or online resources such as engineeringtoolbox.com or NIST WebBook. (a) For water: At room temperature (25潞C), water properties are roughly: - Density (蟻): 997.05 kg/m鲁 - Specific heat (cp): 4181.3 J/kg路K - Dynamic viscosity (渭): 0.893 mPa路s - Thermal conductivity (k_water): 0.606 W/m路K We can now calculate the corresponding Prandtl number (Pr) and Reynolds number (Re_index) for water: \( Pr = \frac{cp \times 渭}{k_{water}}\) For the given range of velocities, \(0.5 \leq V \leq 5\,\text{m}/\text{s}\), the Reynolds number can be calculated: \(Re = \frac{蟻V}{渭}\) Using these values and the Dittus-Boelter equation, we can obtain the convection coefficient in the given range for water,. Similar calculations shall be done for air: (b) For air: At room temperature, air properties are roughly: - Density (蟻): 1.184 kg/m鲁 - Specific heat (cp): 1006 J/kg路K - Dynamic viscosity (渭): 1.81 x 10^(鈭5) Pa路s - Thermal conductivity (k_air): 0.025 W/m路K We can follow the same procedure as for water to calculate the corresponding Prandtl number, Reynolds number, and convection coefficient in the given range (\(1 \leq V \leq 20\,\text{m}/\text{s}\)) for air.
03

Plotting the Convection Coefficient as a Function of Velocity

Now, we can plot the convection coefficient as a function of velocity for both water and air using a graphing software or spreadsheet. Label the x-axis as "Velocity (m/s)" and the y-axis as "Convection Coefficient (W/m虏路K)".
04

Analyzing the Suitability of the Hot-film Sensor

To determine if the hot-film sensor is suitable for the given conditions, we need to check if the Biot number is significantly larger than 1 for both water and air in the respective velocity ranges. Calculate the Biot number using the calculated convection coefficients, the given diameter, D, and the quartz rod's thermal conductivity, k (assuming a typical value, e.g., k=1.3 W/m路K). Compare the Biot number values with 1, if \(Bi \geq 1\), proper operation is ensured and the thermal coupling conditions are satisfied. Comment on the suitability based on these results. Following these steps, you should be able to calculate and plot the convection coefficient as a function of velocity for water and air, and make a statement about the suitability of the hot-film sensor for the given conditions.

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Key Concepts

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

Convection Coefficient
The convection coefficient, often symbolized by \( \bar{h} \), plays a critical role in understanding heat transfer between a solid surface and adjacent fluid. It quantifies the rate at which heat is transferred by convection, which is the heat exchange due to the bulk movement of molecules within fluids such as gases and liquids.

Calculating the convection coefficient is essential when dealing with systems where heat is dissipated into moving fluids, such as in the case of hot-film sensors used to measure fluid velocities. These sensors operate effectively only if there's good thermal coupling with the fluid, meaning a high convection coefficient is preferable for swift heat dissipation.

In practical applications, such as cooling systems in electronic devices or the design of heat exchangers, the value of \( \bar{h} \) is crucial to ensure sufficient cooling and efficient design. The higher the convection coefficient, the more efficient the system is at transferring heat.
Biot Number
The Biot Number (Bi) is a dimensionless quantity used in heat transfer calculations, representing the ratio of heat conduction within an object to the heat convection across its boundary with a fluid. A low Biot Number indicates that the object is thermally 'small', meaning temperature gradients within the object are negligible compared to the difference across its boundary. Conversely, a high Biot Number suggests temperature gradients within the object must be considered due to significant internal thermal resistance.

In the context of hot-film sensors, the Biot Number can dictate the thermal performance and reliability of the sensor. A high Biot Number implies that the heat transfer from the film to the fluid is efficient, thus assuring accurate measurements of fluid flow velocity. If the Biot Number is significantly greater than 1, as suggested in the exercise, it indicates that the sensor is thermally well-coupled with the fluid, facilitating effective operation.
Hot-film Sensors
Hot-film sensors are sophisticated devices used for the precise measurement of fluid flow velocities. These consist of a thin layer of conductive material, like platinum, applied on a non-conductive substrate, such as quartz. By monitoring the electrical resistance of the film, that changes with temperature, the sensor can determine velocity based on the heat dissipated by the film to the surrounding fluid.

Their operation hinges on the convective heat transfer from the film to the fluid; thus, understanding and ensuring optimized thermal coupling through parameters like the Biot Number are pivotal. This coupling allows hot-film sensors to maintain accurate performance across various fluid flow conditions. The sensor's reliability is highly dependent on its thermal designs, such as the thermal conductivity of the film and the substrate, the fluid properties, and the flow velocity.
Nusselt Number
The Nusselt Number (Nu) is another dimensionless quantity in heat transfer that describes the ratio of convective to conductive heat transfer across a boundary. It is used in correlating heat transfer data so that it can be used for various scales, geometries, and fluid flow conditions. A higher Nusselt Number indicates more efficient convective heat transfer.

The Nusselt Number is related to the convection coefficient \( \bar{h} \) and can be calculated using empirical correlations such as the Dittus-Boelter equation, which relates the Nusselt Number to the Reynolds and Prandtl numbers. The Nusselt Number helps in determining \( \bar{h} \) and thus is essential in the design and analysis of heat transfer equipment, including hot-film sensors which are the focus of the original exercise. In practice, knowing the Nusselt Number assists engineers in predicting the thermal performance of systems and in scaling up from laboratory models to full-scale operations.

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Most popular questions from this chapter

A circular pipe of 25 -mm outside diameter is placed in an airstream at \(25^{\circ} \mathrm{C}\) and 1 -atm pressure. The air moves in cross flow over the pipe at \(15 \mathrm{~m} / \mathrm{s}\), while the outer surface of the pipe is maintained at \(100^{\circ} \mathrm{C}\). What is the drag force exerted on the pipe per unit length? What is the rate of heat transfer from the pipe per unit length?

Air at \(27^{\circ} \mathrm{C}\) with a free stream velocity of \(10 \mathrm{~m} / \mathrm{s}\) is used to cool electronic devices mounted on a printed circuit board. Each device, \(4 \mathrm{~mm} \times 4 \mathrm{~mm}\), dissipates \(40 \mathrm{~mW}\), which is removed from the top surface. A turbulator is located at the leading edge of the board, causing the boundary layer to be turbulent. (a) Estimate the surface temperature of the fourth device located \(15 \mathrm{~mm}\) from the leading edge of the board. (b) Generate a plot of the surface temperature of the first four devices as a function of the free stream velocity for \(5 \leq u_{s} \leq 15 \mathrm{~m} / \mathrm{s}\). (c) What is the minimum free stream velocity if the surface temperature of the hottest device is not to exceed \(80^{\circ} \mathrm{C}\) ?

In the production of sheet metals or plastics, it is customary to cool the material before it leaves the production process for storage or shipment to the customer. Typically, the process is continuous, with a sheet of thickness \(\delta\) and width \(W\) cooled as it transits the distance \(L\) between two rollers at a velocity \(V\). In this problem, we consider cooling of an aluminum alloy (2024-T6) by an airstream moving at a velocity \(u_{\infty}\) in counter flow over the top surface of the sheet. A turbulence promoter is used to provide turbulent boundary layer development over the entire surface. (a) By applying conservation of energy to a differential control surface of length \(d x\), which either moves with the sheet or is stationary and through which the sheet passes, derive a differential equation that governs the temperature distribution along the sheet. Because of the low emissivity of the aluminum, radiation effects may be neglected. Express your result in terms of the velocity, thickness, and properties of the sheet \(\left(V, \delta, \rho, c_{p}\right)\), the local convection coefficient \(h_{x}\) associated with the counter flow, and the air temperature. For a known temperature of the sheet \(\left(T_{i}\right)\) at the onset of cooling and a negligible effect of the sheet velocity on boundary layer development, solve the equation to obtain an expression for the outlet temperature \(T_{a}\). (b) For \(\delta=2 \mathrm{~mm}, V=0.10 \mathrm{~m} / \mathrm{s}, L=5 \mathrm{~m}, W=1 \mathrm{~m}\), \(u_{\infty}=20 \mathrm{~m} / \mathrm{s}, T_{\infty}=20^{\circ} \mathrm{C}\), and \(T_{i}=300^{\circ} \mathrm{C}\), what is the outlet temperature \(T_{a}\) ?

Explain under what conditions the total rate of heat transfer from an isothermal flat plate of dimensions \(L \times 2 L\) would be the same, independent of whether parallel flow over the plate is directed along the side of length \(L\) or \(2 L\). With a critical Reynolds number of \(5 \times 10^{5}\), for what values of \(R e_{L}\) would the total heat transfer be independent of orientation?

Consider the packed bed of aluminum spheres described in Problem \(5.12\) under conditions for which the bed is charged by hot air with an inlet velocity of \(V=1 \mathrm{~m} / \mathrm{s}\) and temperature of \(T_{g, i}=300^{\circ} \mathrm{C}\), but for which the convection coefficient is not prescribed. If the porosity of the bed is \(\varepsilon=0.40\) and the initial temperature of the spheres is \(T_{i}=25^{\circ} \mathrm{C}\), how long does it take a sphere near the inlet of the bed to accumulate \(90 \%\) of its maximum possible energy?

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