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A pipe is used for transporting boiling water in which the inner surface is at \(100^{\circ} \mathrm{C}\). The pipe is situated in surroundings where the ambient temperature is \(10^{\circ} \mathrm{C}\) and the convection heat transfer coefficient is \(70 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The wall thickness of the pipe is \(3 \mathrm{~mm}\) and its inner diameter is \(30 \mathrm{~mm}\). The pipe wall has a variable thermal conductivity given as \(k(T)=k_{0}(1+\beta T)\), where \(k_{0}=1.23 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \beta=0.002 \mathrm{~K}^{-1}\), and \(T\) is in \(\mathrm{K}\). For safety reasons and to prevent thermal burn to workers, the outer surface temperature of the pipe should be kept below \(50^{\circ} \mathrm{C}\). Determine whether the outer surface temperature of the pipe is at a safe temperature so as to avoid thermal burn.

Short Answer

Expert verified
Answer: Yes, the outer surface temperature is approximately 47.6°C, which is below the safety limit of 50°C, making it safe for workers.

Step by step solution

01

Calculate the average pipe wall conductivity (k)

We are given the variable thermal conductivity formula: \(k(T)=k_{0}(1+\beta T)\) with \(k_{0}=1.23\,\mathrm{W}/(\mathrm{m}\cdot\mathrm{K})\), \(\beta=0.002\,\mathrm{K}^{-1}\), and \(T\) in \(\mathrm{K}\). We first have to estimate the average temperature between the inner surface \((100^{\circ}\mathrm{C})\) and the outer surface \((50^{\circ}\mathrm{C})\), so \(T_\text{avg}=\frac{100 + 50}{2}=75^{\circ}\mathrm{C}\). In Kelvin, we have \(T_\text{avg} = 75 + 273.15 = 348.15\,\mathrm{K}\). Now, we can calculate the average pipe wall conductivity: \(k = k_{0}(1 + \beta T_\text{avg}) = 1.23(1 + 0.002\cdot 348.15) = 1.23(1+0.6963) \approx 2.08\,\mathrm{W}/(\mathrm{m}\cdot\mathrm{K})\)
02

Compute the heat transfer per unit length (Q')

Now we can find the conduction heat transfer per unit length \((Q')\) using the conduction formula \(Q' = \frac{-k\cdot A(T_\text{in}-T_\text{out})}{L}\) and knowing \(A = \pi d_i\) (circumference of the inner pipe). We have: \(d_i = 0.03\,\mathrm{m}\) (inner diameter) \(L = 0.003\,\mathrm{m}\) (pipe wall thickness) Given the ambient temperature \((T_\text{amb} = 10^{\circ}\mathrm{C})\) and the inner surface temperature \((T_\text{in} = 100^{\circ}\mathrm{C})\): \(Q' = \frac{-2.08\pi d_i(100 - 10)}{0.003} \approx -1792.3\,\mathrm{W}/\mathrm{m}\)
03

Calculate the outer surface temperature (T_out)

Now we can find the outer surface temperature \((T_\text{out})\) using the convection formula \(Q'=hA(T_\text{out}-T_\text{amb})\) and \(A = \pi d_o\) (circumference of the outer pipe): \(h = 70\,\mathrm{W}/(\mathrm{m}^2\cdot\mathrm{K})\) (convection heat transfer coefficient) \(d_o = d_i + 2L = 0.03 + 2\cdot 0.003 = 0.036\,\mathrm{m}\) (outer diameter) Solving for \(T_\text{out}\), we have: \(-1792.3\,\mathrm{W}/\mathrm{m} = 70(\pi d_o)(T_\text{out} - 10)\) \(T_\text{out} = \frac{-1792.3\,\mathrm{W}/\mathrm{m}}{70(\pi d_o)} + 10 \approx 47.6^{\circ}\mathrm{C}\) Since the outer surface temperature is \(47.6^{\circ}\mathrm{C}\), which is below the safety limit of \(50^{\circ}\mathrm{C}\), the pipe is safe and prevents thermal burn to workers.

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Key Concepts

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

Understanding Convection Heat Transfer
Convection heat transfer is a mechanism of heat transfer where thermal energy is carried away by the movement of a fluid, which could be a liquid or a gas. This is particularly important in the context of the exercise we're discussing, where hot water is transported through a pipe and the ambient air is at a much lower temperature.

In our scenario, the heat from the boiling water within the pipe transfers to the pipe's inner surface and from there to the outer surface, eventually dissipating into the surrounding air. This transition from hotter to cooler regions occurs due to the difference in temperature—driving a heat flow from the pipe to the ambient environment.

To quantify this process, we use the 'convection heat transfer coefficient,' denoted as 'h' in the exercise. This coefficient reflects how effective a fluid is at transporting heat. The higher the value of 'h', the more efficient the convection process, meaning more heat will be transferred for a given surface area and temperature difference.
Heat Transfer in Pipes
Heat transfer in pipes is a complex process affected by the material's thermal conductivity, the fluid inside, and the environmental conditions.

Thermal conductivity, 'k', is a property that indicates how well a material can conduct heat. In the given exercise, the thermal conductivity varies with temperature, adding a layer of complexity when calculating the amount of heat loss through the pipe's walls. An accurate prediction of heat transfer is crucial for ensuring that the pipe's temperature remains within safe operating limits.

The students must understand how to calculate the correct average thermal conductivity for the wall's material knowing that it changes with temperature. By doing so, we can determine whether the pipe's outer surface temperature is within a safe range. This involves mathematical computation to estimate the average temperature across the pipe's thickness and then using the specific conductivity formula provided.
Safety in Thermal Systems
Safety is paramount when designing and operating thermal systems. The exercise highlights a typical safety concern—preventing burns from surfaces that are too hot to touch.

Here, the safety threshold for the pipe's outer surface temperature has been set at no more than 50 degrees Celsius. There are many ways to manage and mitigate these safety concerns, including insulation, material selection with specific thermal properties, and sometimes regulating the operating temperatures of the fluid inside the systems.

When solving thermal problems, students must be aware of excluding unrealistic results or conditions that might compromise safety. Exercises like these help to reinforce the practical application of heat transfer principles in designing safe thermal system components, such as pipes in this case, that are both efficient and avoid hazards like thermal burns in the workplace.

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Most popular questions from this chapter

A flat-plate solar collector is used to heat water by having water flow through tubes attached at the back of the thin solar absorber plate. The absorber plate has an emissivity and an absorptivity of \(0.9\). The top surface \((x=0)\) temperature of the absorber is \(T_{0}=35^{\circ} \mathrm{C}\), and solar radiation is incident on the absorber at \(500 \mathrm{~W} / \mathrm{m}^{2}\) with a surrounding temperature of \(0^{\circ} \mathrm{C}\). Convection heat transfer coefficient at the absorber surface is \(5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), while the ambient temperature is \(25^{\circ} \mathrm{C}\). Show that the variation of temperature in the absorber plate can be expressed as \(T(x)=-\left(\dot{q}_{0} / k\right) x+T_{0}\), and determine net heat flux \(\dot{q}_{0}\) absorbed by the solar collector.

A spherical container of inner radius \(r_{1}=2 \mathrm{~m}\), outer radius \(r_{2}=2.1 \mathrm{~m}\), and thermal conductivity \(k=30 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) is filled with iced water at \(0^{\circ} \mathrm{C}\). The container is gaining heat by convection from the surrounding air at \(T_{\infty}=25^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(h=18 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Assuming the inner surface temperature of the container to be \(0^{\circ} \mathrm{C},(a)\) express the differential equation and the boundary conditions for steady one- dimensional heat conduction through the container, \((b)\) obtain a relation for the variation of temperature in the container by solving the differential equation, and \((c)\) evaluate the rate of heat gain to the iced water.

Consider a large plate of thickness \(L\) and thermal conductivity \(k\) in which heat is generated uniformly at a rate of \(\dot{e}_{\text {gen. }}\) One side of the plate is insulated while the other side is exposed to an environment at \(T_{\infty}\) with a heat transfer coefficient of \(h\). \((a)\) Express the differential equation and the boundary conditions for steady one-dimensional heat conduction through the plate, \((b)\) determine the variation of temperature in the plate, and \((c)\) obtain relations for the temperatures on both surfaces and the maximum temperature rise in the plate in terms of given parameters.

The heat conduction equation in a medium is given in its simplest form as $$ \frac{1}{r} \frac{d}{d r}\left(r k \frac{d T}{d r}\right)+\dot{e}_{\text {gen }}=0 $$ Select the wrong statement below. (a) The medium is of cylindrical shape. (b) The thermal conductivity of the medium is constant. (c) Heat transfer through the medium is steady. (d) There is heat generation within the medium. (e) Heat conduction through the medium is one-dimensional.

The conduction equation boundary condition for an adiabatic surface with direction \(n\) being normal to the surface is (a) \(T=0\) (b) \(d T / d n=0\) (c) \(d^{2} T / d n^{2}=0\) (d) \(d^{3} T / d n^{3}=0\) (e) \(-k d T / d n=1\)

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