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A thermocouple with a spherical junction diameter of \(0.5 \mathrm{~mm}\) is used for measuring the temperature of hot airflow in a circular duct. The convection heat transfer coefficient of the airflow can be related with the diameter \((D)\) of the spherical junction and the average airflow velocity \((V)\) as \(h=2.2(V / D)^{0.5}\), where \(D, h\), and \(V\) are in $\mathrm{m}, \mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}\(, and \)\mathrm{m} / \mathrm{s}$, respectively. The properties of the thermocouple junction are $k=35 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(, \)\rho=8500 \mathrm{~kg} / \mathrm{m}^{3}\(, and \)c_{p}=320 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$. Determine the minimum airflow velocity that the thermocouple can use, if the maximum response time of the thermocouple to register 99 percent of the initial temperature difference is \(5 \mathrm{~s}\).

Short Answer

Expert verified
Answer: The minimum airflow velocity is approximately 4.295 m/s.

Step by step solution

01

Write down the response time formula

According to the first-order thermocouple system, the response time formula can be expressed as: $$ t=\frac{\tau}{Bi}= \frac{\rho V_{s} c_{p}}{3h} $$ where \(t\) is the response time, \(\tau\) is the time constant, \(V_s\) is the volume of the sphere, \(h\) is the convection heat transfer coefficient, and \(Bi\) is the Biot number.
02

Calculate the Biot number

The formula for the Biot number is given by: $$ Bi = \frac{hL_c}{k} $$ In this case, the characteristic length (\(L_c\)) for a sphere is \(L_c = \frac{D}{3}\) with \(D\) being the diameter of the sphere. Substitute \(L_c = \frac{D}{3}\) and \(h=2.2(V / D)^{0.5}\) into the Biot number formula: $$ Bi = \frac{2.2(V / D)^{0.5} D}{3k} $$
03

Substitute the given values into the response time formula

We are given the maximum response time as \(t=5\,\mathrm{s}\), so we can substitute into the response time formula: $$ 5 = \frac{\rho V_{s} c_{p}}{3 \cdot 2.2(V / D)^{0.5} D} $$ Now, {we need to find the volume of the sphere} using \(V_{s} = \frac{4}{3}\pi r^{3}\), where \(r = \frac{D}{2}\) and \(D=0.5\,\mathrm{mm}\). The diameter of the sphere given in the problem is in millimeters, so we need to convert it to meters for consistency with the other units. $$ D = 0.5\,\mathrm{mm} \times \frac{1\,\mathrm{m}}{1000\,\mathrm{mm}} = 5 \times 10^{-4}\, \mathrm{m} $$ Thus, compute the volume of the sphere: $$ V_{s} = \frac{4}{3}\pi\left(\frac{5 \times 10^{-4}}{2}\right)^{3} = 6.54\times 10^{-11}\, \mathrm{m^3} $$ Plug \(V_{s}\), \(\rho\), \(c_p\), and \(D\) into the response time formula: $$ 5 = \frac{8500\cdot 6.54\times 10^{-11}\cdot 320}{3 \cdot 2.2(V / (5 \times 10^{-4}))^{0.5}(5\times 10^{-4})} $$
04

Solve for the airflow velocity

Now, we can solve for the minimum airflow velocity \(V\): $$ V = \frac{8500\cdot 6.54\times 10^{-11}\cdot 320}{3 \cdot 2.2(5) \cdot (5\times 10^{-4})^{0.5}} $$ $$ V \approx 4.295\,\mathrm{m/s} $$ Hence, the minimum airflow velocity that the thermocouple can use to register 99% of the initial temperature difference in 5 seconds is approximately \(4.295\,\mathrm{m/s}\).

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Most popular questions from this chapter

What is an infinitely long cylinder? When is it proper to treat an actual cylinder as being infinitely long, and when is it not? For example, is it proper to use this model when finding the temperatures near the bottom or top surfaces of a cylinder? Explain.

Lumped system analysis of transient heat conduction situations is valid when the Biot number is (a) very small (b) approximately one (c) very large (d) any real number (e) cannot say unless the Fourier number is also known

Hailstones are formed in high-altitude clouds at \(253 \mathrm{~K}\). Consider a hailstone with diameter of \(20 \mathrm{~mm}\) that is falling through air at \(15^{\circ} \mathrm{C}\) with convection heat transfer coefficient of $163 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Assuming the hailstone can be modeled as a sphere and has properties of ice at \(253 \mathrm{~K}\), determine how long it takes to reach melting point at the surface of the falling hailstone. Solve this problem using the analytical one-term approximation method.

A semi-infinite aluminum cylinder $(k=237 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(, \)\alpha=9.71 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}$ ) of diameter \(D=15 \mathrm{~cm}\) is initially at a uniform temperature of \(T_{i}=115^{\circ} \mathrm{C}\). The cylinder is now placed in water at \(10^{\circ} \mathrm{C}\), where heat transfer takes place by convection with a heat transfer coefficient of $h=140 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. Determine the temperature at the center of the cylinder \)5 \mathrm{~cm}$ from the end surface 8 min after the start of cooling. Solve this problem using the analytical one-term approximation method.

A 30 -cm-long cylindrical aluminum block $\left(\rho=2702 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=0.896 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}, k=236 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\right.\(, and \)\left.\alpha=9.75 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\right), 15 \mathrm{~cm}$ in diameter, is initially at a uniform temperature of \(20^{\circ} \mathrm{C}\). The block is to be heated in a furnace at \(1200^{\circ} \mathrm{C}\) until its center temperature rises to \(300^{\circ} \mathrm{C}\). If the heat transfer coefficient on all surfaces of the block is $80 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, determine how long the block should be kept in the furnace. Also, determine the amount of heat transfer from the aluminum block if it is allowed to cool in the room until its temperature drops to $20^{\circ} \mathrm{C}$ throughout. Solve this problem using the analytical one-term approximation method.

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