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The water main in the cities must be placed at sufficient depth below the earth's surface to avoid freezing during extended periods of subfreezing temperatures. Determine the minimum depth at which the water main must be placed at a location where the soil is initially at \(15^{\circ} \mathrm{C}\) and the earth's surface temperature under the worst conditions is expected to remain at \(-10^{\circ} \mathrm{C}\) for a period of 75 days. Take the properties of soil at that location to be \(k=0.7 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and \(\alpha=1.4 \times\) \(10^{-5} \mathrm{~m}^{2} / \mathrm{s}\). Answer: \(7.05 \mathrm{~m}\)

Short Answer

Expert verified
Answer: The minimum depth at which the water main must be placed is 7.05 meters.

Step by step solution

01

Understand the given data

We are given the following information: - Initial soil temperature: \(T_i = 15°C\) - Surface temperature: \(T_s = -10°C\) - Duration of subfreezing temperatures: \(t = 75\) days - Soil thermal conductivity: \(k = 0.7 \frac{W}{m \cdot K}\) - Soil thermal diffusivity: \(\alpha = 1.4 \times 10^{-5} \frac{m^2}{s}\) We need to find the critical depth \(x\) where the temperature drops to 0°C after 75 days.
02

Convert the time from days to seconds

To work with the given values of thermal diffusivity (\(\alpha\)), convert the time from days to seconds. \(t = 75 \text{ days} \times 24 \frac{\text{hours}}{\text{day}} \times 60 \frac{\text{minutes}}{\text{hour}} \times 60 \frac{\text{seconds}}{\text{minute}} = 6480000 \text{ seconds}\)
03

Use the 1D unsteady heat conduction equation to find temperature distribution in the soil

The temperature distribution in a semi-infinite medium is given by the following equation: $$T(x,t) = T_s + (T_i - T_s) \text{erfc} \left(\frac{x}{2 \sqrt{\alpha t}}\right)$$ Where \(T(x,t)\) is the temperature at a depth \(x\) and time \(t\), and \(\text{erfc}\) is the complementary error function. We need to find the critical depth where \(T(x, t) = 0°C\). Set \(T(x, t) = 0\) and solve for \(x\).
04

Solve for the critical depth

\(0 = -10 + (15 - (-10)) \text{ \text{erfc} }\left(\frac{x}{2 \sqrt{1.4 \times 10^{-5} \cdot 6480000}}\right)\) Simplify the expression: %% $$ (20) \text{ \text{erfc} }\left(\frac{x}{2 \sqrt{1.4 \times 10^{-5} \cdot 6480000}}\right) = 10 $$ %% So, the complementary error function value is: $$\text{erfc} \left(\frac{x}{2 \sqrt{1.4 \times 10^{-5} \cdot 6480000}}\right) = 0.5$$ Now, we need to find the inverse of the erfc function: $$\frac{x}{2 \sqrt{1.4 \times 10^{-5} \cdot 6480000}} = \text{erfc}^{-1}(0.5)$$ Using a calculator or software that has an inverse erfc function, we find: $$\text{erfc}^{-1}(0.5) = 0.4769$$ Now we solve for \(x\): %% x = 2 \sqrt{1.4 \times 10^{-5} \cdot 6480000} \times 0.4769 $$ Calculate the value of \(x\): \(x = 2 \times \sqrt{1.4 \times 10^{-5} \times 6480000} \times 0.4769 = 7.05 \text{ meters}\) So, the minimum depth at which the water main must be placed at the location is 7.05 meters.

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Key Concepts

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

Heat Transfer Fundamentals
Heat transfer is a discipline of thermal engineering that concerns the generation, use, conversion, and exchange of thermal energy between physical systems. Fundamental modes of heat transfer include conduction, convection, and radiation. Heat conduction, or thermal conduction, is the transfer of heat from one part of a body to another with which it is in contact, without appreciable movement of the body as a whole.

In the exercise regarding the prevention of water pipes from freezing, we're focusing on the concept of unsteady heat conduction, which occurs when the temperature distribution within a material changes over time. The temperature change at a specific point within the material depends on the thermal properties of the material and the conditions at the boundaries. The exercise requires us to apply knowledge of unsteady heat conduction to determine how deep water pipes need to be buried to avoid freezing.
Thermal Conductivity
Thermal conductivity is a property of materials that indicates their ability to conduct heat. It is denoted by the symbol \(k\) and typically measured in watts per meter per kelvin (\(W/m \times K\)). A high thermal conductivity means that the material can transfer heat effectively, while a low thermal conductivity indicates poor heat transfer ability.

In the textbook exercise, we use the soil's thermal conductivity value to calculate how heat would move through the soil over time. The depth of the water main is directly influenced by the soil's ability to transfer heat to or from the pipe. A factor to consider is that different materials will have different thermal conductivity values, therefore changing the value of \(k\) could affect the required depth of the water pipes to resist freezing temperatures.
Temperature Distribution
Temperature distribution refers to how temperature varies within a material. When considering unsteady heat conduction, temperature distribution changes with both location and time. An understanding of temperature distribution within a material is critical to solving a wide array of thermal problems.

In the exercise we are focusing on, we explore temperature distribution within soil over a period of 75 days where the surface temperature is maintained at a constant \(-10^\circ C\). To calculate the distribution, we apply the 1D unsteady heat conduction equation which includes the thermal diffusivity of the soil (\(\alpha\)) and the initial and boundary temperatures. The calculated temperature distribution helps to determine the minimum depth for the water main to prevent it from reaching the freezing point. It's important to realize that the temperature distribution is not uniform across the soil depth; it changes with the specific soil properties and environmental conditions.

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Most popular questions from this chapter

When water, as in a pond or lake, is heated by warm air above it, it remains stable, does not move, and forms a warm layer of water on top of a cold layer. Consider a deep lake \(\left(k=0.6 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, c_{p}=4.179 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\) that is initially at a uniform temperature of \(2^{\circ} \mathrm{C}\) and has its surface temperature suddenly increased to \(20^{\circ} \mathrm{C}\) by a spring weather front. The temperature of the water \(1 \mathrm{~m}\) below the surface 400 hours after this change is (a) \(2.1^{\circ} \mathrm{C}\) (b) \(4.2^{\circ} \mathrm{C}\) (c) \(6.3^{\circ} \mathrm{C}\) (d) \(8.4^{\circ} \mathrm{C}\) (e) \(10.2^{\circ} \mathrm{C}\)

In a production facility, 3-cm-thick large brass plates \(\left(k=110 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \rho=8530 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=380 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right.\), and \(\left.\alpha=33.9 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\right)\) that are initially at a uniform temperature of \(25^{\circ} \mathrm{C}\) are heated by passing them through oven maintained at \(700^{\circ} \mathrm{C}\). The plates remain in the oven for a period of \(10 \mathrm{~min}\). Taking the convection heat transfer coefficient to be \(h=80 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), determine the surface temperature of the plates when they come out of the oven. Solve this problem using analytical one-term approximation method (not the Heisler charts). Can this problem be solved using lumped system analysis? Justify your answer.

Conduct the following experiment at home to determine the combined convection and radiation heat transfer coefficient at the surface of an apple exposed to the room air. You will need two thermometers and a clock. First, weigh the apple and measure its diameter. You can measure its volume by placing it in a large measuring cup halfway filled with water, and measuring the change in volume when it is completely immersed in the water. Refrigerate the apple overnight so that it is at a uniform temperature in the morning and measure the air temperature in the kitchen. Then take the apple out and stick one of the thermometers to its middle and the other just under the skin. Record both temperatures every \(5 \mathrm{~min}\) for an hour. Using these two temperatures, calculate the heat transfer coefficient for each interval and take their average. The result is the combined convection and radiation heat transfer coefficient for this heat transfer process. Using your experimental data, also calculate the thermal conductivity and thermal diffusivity of the apple and compare them to the values given above.

Layers of 23 -cm-thick meat slabs \((k=0.47 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and \(\left.\alpha=0.13 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\right)\) initially at a uniform temperature of \(7^{\circ} \mathrm{C}\) are to be frozen by refrigerated air at \(-30^{\circ} \mathrm{C}\) flowing at a velocity of \(1.4 \mathrm{~m} / \mathrm{s}\). The average heat transfer coefficient between the meat and the air is \(20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Assuming the size of the meat slabs to be large relative to their thickness, determine how long it will take for the center temperature of the slabs to drop to \(-18^{\circ} \mathrm{C}\). Also, determine the surface temperature of the meat slab at that time.

A long 35-cm-diameter cylindrical shaft made of stainless steel \(304\left(k=14.9 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \rho=7900 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=477 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right.\), and \(\alpha=3.95 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\) ) comes out of an oven at a uniform temperature of \(400^{\circ} \mathrm{C}\). The shaft is then allowed to cool slowly in a chamber at \(150^{\circ} \mathrm{C}\) with an average convection heat transfer coefficient of \(h=60 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Determine the temperature at the center of the shaft \(20 \mathrm{~min}\) after the start of the cooling process. Also, determine the heat transfer per unit length of the shaft during this time period. Solve this problem using analytical one-term approximation method (not the Heisler charts).

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