/*! 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 59 A \(0.20\)-m-diameter, thin-wall... [FREE SOLUTION] | 91Ó°ÊÓ

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A \(0.20\)-m-diameter, thin-walled steel pipe is used to transport saturated steam at a pressure of 20 bars in a room for which the air temperature is \(25^{\circ} \mathrm{C}\) and the convection heat transfer coefficient at the outer surface of the pipe is \(20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). (a) What is the heat loss per unit length from the bare pipe (no insulation)? Estimate the heat loss per unit length if a 50 -mm-thick layer of insulation (magnesia, \(85 \%\) is added. The steel and magnesia may each be assumed to have an emissivity of \(0.8\), and the steam-side convection resistance may be neglected. (b) The costs associated with generating the steam and installing the insulation are known to be \(\$ 4 / 10^{9} \mathrm{~J}\) and \(\$ 100 / \mathrm{m}\) of pipe length, respectively. If the steam line is to operate \(7500 \mathrm{~h} / \mathrm{yr}\), how many years are needed to pay back the initial investment in insulation?

Short Answer

Expert verified
The heat loss per unit length without insulation is approximately \(23568 \mathrm{~W/m}\), and with insulation, it is approximately \(7253 \mathrm{~W/m}\). The payback period for the insulation investment is approximately 5.37 years.

Step by step solution

01

Determine the heat loss per unit length without insulation

Using the formula for heat loss per unit length by convection, we have: \[q'=h \cdot \pi \cdot D \cdot \Delta T\] Where, \(q'\) is the heat loss per unit length, and \(\Delta T = T_{s} - T_{r}\). But first, we need to find the temperature of the steam, \(T_{s}\), at the given pressure (20 bars). For this, we can use the steam table to look up the saturation temperature: 1 bar = 100000 Pa, therefore 20 bars = 2000000 Pa. Looking up in the steam table, we find that the saturation temperature at 2000000 Pa is around \(212 ^\circ \mathrm{C}\). Now we can proceed with the calculation. \[\Delta T = 212 - 25 = 187 \mathrm{~K}\] \[q' = 20 \cdot \pi \cdot 0.20 \cdot 187 = 23568 \mathrm{~W/m}\] The heat loss per unit length without insulation is approximately \(23568 \mathrm{~W/m}\).
02

Determine the heat loss per unit length with insulation

To calculate the heat loss per unit length with insulation, we need to find the overall heat transfer coefficient (including convection, conduction, and radiation). We can use the following equation: \[\frac{1}{U_{total}} = \frac{1}{h} + \frac{1}{h_{r}} + \frac{t}{k}\] Where, \(U_{total}\) is the overall heat transfer coefficient, \(h_{r}\) is the radiation heat transfer coefficient, and \(k\) is the thermal conductivity of the insulation material. According to the given information, we can assume that the steam-side convection resistance is negligible. The emissivity of the steel and magnesia is \(0.8\). We can use the following equation to calculate the radiation heat transfer coefficient: \[h_{r} = \epsilon \cdot \sigma \cdot \frac{(T_{s}+273)^{4} - (T_{r}+273)^{4}}{(T_{s}-T_{r})}\] Where, \(\sigma = 5.67 \times 10^{-8}\) is the Stefan-Boltzmann constant. Plugging in the values, we get \(h_{r}\approx 19.928 \mathrm{~W/m^{2} \cdot K}\). Now, we need to find the thermal conductivity of the insulation material (magnesia). The given information states that it is \(85\%\) magnesia. Looking up the thermal conductivity of \(85 \% \) magnesia, we find \(k \approx 0.045 \mathrm{~W/m \cdot K}\). Now we can find the overall heat transfer coefficient: \[\frac{1}{U_{total}} = \frac{1}{20} + \frac{1}{19.928} + \frac{0.05}{0.045}\] \[U_{total} \approx 6.07989 \mathrm{~W/m^{2} \cdot K}\] Lastly, we can find the heat loss per unit length with insulation: \[q'_{insulation} = U_{total} \cdot \pi \cdot D \cdot \Delta T \approx 6.07989 \cdot \pi \cdot 0.20 \cdot 187 = 7253 \mathrm{~W/m}\] The heat loss per unit length with insulation is approximately \(7253 \mathrm{~W/m}\).
03

Estimate the payback period for the insulation

Let's calculate the energy cost without insulation per year and the energy cost with insulation per year: Energy cost without insulation per year (\(C_{no\_insulation}\)): \[\frac{23568 \mathrm{~W/m}}{10^{9} \mathrm{~J}} \times 7500 \mathrm{~h/yr} \times 3600 \mathrm{~s/h} \times \$4 = \$2523.9744/m\] Energy cost with insulation per year (\(C_{insulation}\)): \[\frac{7253 \mathrm{~W/m}}{10^{9} \mathrm{~J}} \times 7500 \mathrm{~h/yr} \times 3600 \mathrm{~s/h} \times \$4 = \$774.6888/m\] Now, let's find the initial insulation investment cost: \[\$100/m\] Now, we can find the payback years: \[\textrm{Payback years} = \frac{\textrm{Initial investment cost}}{\textrm{Energy cost saved per year}} = \frac{100}{2523.9744 - 774.6888}\] \[\textrm{Payback years} \approx 5.37\] The payback period for the insulation investment is approximately 5.37 years.

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Key Concepts

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

Convection Heat Transfer
Convection heat transfer refers to the process by which heat is transferred through the motion of fluids, such as liquids or gases. In the context of our problem, we are concerned with air surrounding a hot steel pipe. The heat from the pipe is transferred to the air, causing it to warm and rise.Convection heat transfer is calculated using the convection heat transfer coefficient (denoted as \(h\)). This coefficient represents how effectively heat is transferred from the pipe to the surrounding air. In the given scenario, the convection heat transfer coefficient is \(20 \, \mathrm{W/m^2 \cdot K}\). The higher the coefficient, the more efficient the heat transfer by convection.
  • The formula to calculate heat loss per unit length from a surface by convection is: \[q' = h \cdot \pi \cdot D \cdot \Delta T\]where \(q'\) is the heat loss per unit length, \(D\) is the diameter of the pipe, and \(\Delta T\) is the temperature difference between the pipe surface and the air.
  • In our exercise, the pipe's convection heat loss, where the air temperature is \(25^\circ \mathrm{C}\), helps us understand how effective the pipe is in transferring heat to its surroundings.
Understanding convection is essential as it helps evaluate energy efficiency and design considerations for systems involving fluids.
Thermal Conductivity
Thermal conductivity is a property of materials that indicates their ability to conduct heat. It is a crucial factor when considering insulation materials. A lower thermal conductivity means that a material is better at preventing heat transfer, thus providing better insulation.In this exercise, we looked at a magnesia layer being added to insulate the steel pipe. The thermal conductivity of the magnesia, considering its composition is 85%, is approximately \(0.045 \, \mathrm{W/m \cdot K}\).
  • Thermal conductivity \(k\) is used in the formula for the overall heat transfer coefficient:\[ \frac{1}{U_{total}} = \frac{1}{h} + \frac{1}{h_{r}} + \frac{t}{k} \]where \(t\) is the thickness of the insulation.
  • The lower the thermal conductivity, the higher the overall insulation efficiency, reducing heat loss and making the system more energy-efficient.
Evaluating thermal conductivity helps in choosing the right material for energy conservation and system design, thereby saving costs on heating or cooling over time.
Insulation Efficiency
Insulation efficiency revolves around how well an insulation material can reduce heat loss. It directly correlates with the ability of the material to maintain desired temperatures inside pipes or buildings, reducing the need for external heating or cooling resources.In this problem, the addition of a 50-mm-thick magnesia layer demonstrates its capability to provide a significant reduction in heat loss, from \(23568 \, \mathrm{W/m}\) without insulation to \(7253 \, \mathrm{W/m}\) with insulation.
  • Insulation efficiency can be gauged by the reduction in heat transfer coefficient \(U_{total}\):\[ U_{total} = \frac{1}{\left(\frac{1}{h} + \frac{1}{h_{r}} + \frac{t}{k}\right)} \]
  • Efficient insulation plays a critical role in industrial applications where energy costs and sustainability are concerns.
Well-insulated systems contribute to energy conservation and cost savings, thereby increasing the system's overall efficiency and reducing the environmental impact.
Radiation Heat Transfer
Radiation heat transfer is the transfer of heat energy through electromagnetic waves without needing a medium like air or water. This form of heat transfer can occur in a vacuum.In the exercise, the emissivity of the steel pipe and insulation (both at 0.8) is crucial for determining the pipe's radiation heat transfer coefficient, denoted as \(h_r\).
  • The radiation heat transfer coefficient \(h_r\) is given by the formula:\[ h_r = \varepsilon \cdot \sigma \cdot \frac{(T_s+273)^4 - (T_r+273)^4}{(T_s-T_r)} \]where \(\varepsilon\) is emissivity, and \(\sigma = 5.67 \times 10^{-8} \, \mathrm{W/m^2 \cdot K^4}\) is the Stefan-Boltzmann constant.
  • The calculated \(h_r\) lets us understand the amount of heat transfer resisted by radiation.
Understanding radiation heat transfer is vital for evaluating the system's cooling or heating requirements. It affects how much energy is lost or conserved, influencing the overall efficiency and cost management of thermal systems.

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Most popular questions from this chapter

An uninsulated, thin-walled pipe of \(100-\mathrm{mm}\) diameter is used to transport water to equipment that operates outdoors and uses the water as a coolant. During particularly harsh winter conditions, the pipe wall achieves a temperature of \(-15^{\circ} \mathrm{C}\) and a cylindrical layer of ice forms on the inner surface of the wall. If the mean water temperature is \(3^{\circ} \mathrm{C}\) and a convection coefficient of \(2000 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) is maintained at the inner surface of the ice, which is at \(0^{\circ} \mathrm{C}\), what is the thickness of the ice layer?

The wall of a spherical tank of \(1-m\) diameter contains an exothermic chemical reaction and is at \(200^{\circ} \mathrm{C}\) when the ambient air temperature is \(25^{\circ} \mathrm{C}\). What thickness of urethane foam is required to reduce the exterior temperature to \(40^{\circ} \mathrm{C}\), assuming the convection coefficient is \(20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) for both situations? What is the percentage reduction in heat rate achieved by using the insulation?

An experimental arrangement for measuring the thermal conductivity of solid materials involves the use of two long rods that are equivalent in every respect, except that one is fabricated from a standard material of known thermal conductivity \(k_{\mathrm{A}}\) while the other is fabricated from the material whose thermal conductivity \(k_{\mathrm{B}}\) is desired. Both rods are attached at one end to a heat source of fixed temperature \(T_{b}\), are exposed to a fluid of temperature \(T_{\infty}\), and are instrumented with thermocouples to measure the temperature at a fixed distance \(x_{1}\) from the heat source. If the standard material is aluminum, with \(k_{\mathrm{A}}=200 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), and measurements reveal values of \(T_{\mathrm{A}}=75^{\circ} \mathrm{C}\) and \(T_{\mathrm{B}}=60^{\circ} \mathrm{C}\) at \(x_{1}\) for \(T_{b}=100^{\circ} \mathrm{C}\) and \(T_{\infty}=25^{\circ} \mathrm{C}\), what is the thermal conductivity \(k_{\mathrm{B}}\) of the test material?

One method that is used to grow nanowires (nanotubes with solid cores) is to initially deposit a small droplet of a liquid catalyst onto a flat surface. The surface and catalyst are heated and simultaneously exposed to a higher- temperature, low-pressure gas that contains a mixture of chemical species from which the nanowire is to be formed. The catalytic liquid slowly absorbs the species from the gas through its top surface and converts these to a solid material that is deposited onto the underlying liquid-solid interface, resulting in construction of the nanowire. The liquid catalyst remains suspended at the tip of the nanowire. Consider the growth of a 15 -nm-diameter silicon carbide nanowire onto a silicon carbide surface. The surface is maintained at a temperature of \(T_{s}=2400 \mathrm{~K}\), and the particular liquid catalyst that is used must be maintained in the range \(2400 \mathrm{~K} \leq T_{c} \leq 3000 \mathrm{~K}\) to perform its function. Determine the maximum length of a nanowire that may be grown for conditions characterized by \(h=10^{5} \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and \(T_{\infty}=8000 \mathrm{~K}\). Assume properties of the nanowire are the same as for bulk silicon carbide.

A thin metallic wire of thermal conductivity \(k\), diameter \(D\), and length \(2 L\) is annealed by passing an electrical current through the wire to induce a uniform volumetric heat generation \(\dot{q}\). The ambient air around the wire is at a temperature \(T_{\infty}\), while the ends of the wire at \(x=\pm L\) are also maintained at \(T_{\infty}\). Heat transfer from the wire to the air is characterized by the convection coefficient \(h\). Obtain expressions for the following: (a) The steady-state temperature distribution \(T(x)\) along the wire, (b) The maximum wire temperature. (c) The average wire temperature.

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