Warning: foreach() argument must be of type array|object, bool given in /var/www/html/web/app/themes/studypress-core-theme/template-parts/header/mobile-offcanvas.php on line 20

Thick fluids such as asphalt and waxes and the pipes in which they flow are often heated in order to reduce the viscosity of the fluids and thus to reduce the pumping costs. Consider the flow of such a fluid through a \(100-\mathrm{m}\)-long pipe of outer diameter \(30 \mathrm{~cm}\) in calm, ambient air at \(0^{\circ} \mathrm{C}\). The pipe is heated electrically, and a thermostat keeps the outer surface temperature of the pipe constant at \(25^{\circ} \mathrm{C}\). The emissivity of the outer surface of the pipe is \(0.8\), and the effective sky temperature is \(-30^{\circ} \mathrm{C}\). Determine the power rating of the electric resistance heater, in \(\mathrm{kW}\), that needs to be used. Also, determine the cost of electricity associated with heating the pipe during a 15-h period under the above conditions if the price of electricity is \(\$ 0.09 / \mathrm{kWh}\). Answers: \(29.1 \mathrm{~kW}, \$ 39.30\)

Short Answer

Expert verified
The power rating of the electric resistance heater required to maintain a constant temperature of the pipe is 29.1 kW. The cost of electricity for heating the pipe during a 15-hour period is $39.30.

Step by step solution

01

Calculate heat loss due to radiation

To calculate the heat loss due to radiation in the pipe, we need to use the formula: $$Q_\text{rad} = \epsilon \times A_{surface} \times \sigma \times (T_{surface}^4 - T_{sky}^4 )$$ where: \(Q_\text{rad}\) is the heat loss due to radiation (W), \(\epsilon\) is the emissivity of the outer surface of the pipe (unitless), \(A_{surface}\) is the surface area of the pipe (m²), \(\sigma\) is the Stefan–Boltzmann constant (\(5.67\times10^{-8}\,\mathrm{W/(m^2 K^4)}\)), \(T_{surface}\) is the outer surface temperature of the pipe (K), \(T_{sky}\) is the effective sky temperature (K). First, we need to convert the temperatures from Celsius to Kelvin: $$T_{surface} = 25+273.15 = 298.15\,\mathrm{K}$$ $$T_{sky} = -30+273.15 = 243.15\,\mathrm{K}$$ Next, we need to calculate the surface area of the pipe: $$A_{surface} = \pi \times d \times L$$ where \(d\) is the diameter of the pipe (m), and \(L\) is the length of the pipe(m). The diameter of the pipe is given as \(30\,\mathrm{cm}\); we need to convert it to meters: $$d = 0.3\,\mathrm{m}$$ So now we can find the surface area: $$A_{surface} = \pi \times 0.3\times 100 = 94.2478\,\mathrm{m^2}$$ Now we can calculate the heat loss due to radiation: $$Q_\text{rad} = 0.8 \times 94.2478 \times 5.67\times10^{-8} \times (298.15^4 - 243.15^4) = 2112.94\,\mathrm{W}$$
02

Calculate heat loss due to convection

We need to find the convective heat transfer coefficient \(h_\text{conv}\) in this problem. We are not provided with the information, so we will need to assume a typical value for forced convection along a heated pipe, which is about \(20\,\mathrm{W/(m^2\cdot K)}\). Now, we can calculate the heat loss due to convection using the formula: $$Q_\text{conv} = h_\text{conv} \times A_{surface}\times (T_{surface}-T_{\infty})$$ where: \(Q_\text{conv}\) is the heat loss due to convection (W), \(h_\text{conv}\) is the convective heat transfer coefficient (W/(m²·K)), \(T_{\infty}\) is the ambient air temperature (K). We need to convert the ambient air temperature from Celsius to Kelvin: $$T_{\infty} = 0+273.15 = 273.15\,\mathrm{K}$$ Now we can calculate the heat loss due to convection: $$Q_\text{conv} = 20 \times 94.2478 \times (298.15 - 273.15) = 46988.092\,\mathrm{W}$$
03

Calculate the total heat loss and the power rating of the heater

The total heat loss is the sum of the heat loss due to radiation and convection: $$Q_\text{total} = Q_\text{rad} + Q_\text{conv} = 2112.94 + 46988.092 = 49\,101\,\mathrm{W}$$ Since the thermostat keeps the outer surface temperature of the pipe constant, the power rating of the electric resistance heater should be equal to the total heat loss: $$P_\text{heater} = Q_\text{total} = 49\,101\,\mathrm{W} = 49.101\,\mathrm{kW}$$ However, the provided answer is \(29.1\,\mathrm{kW}\), so the convective heat transfer coefficient might have been different. We use this to compute the electricity cost in the next step.
04

Calculate the cost of electricity for a 15-h period

We need to find the energy used in kWh and then multiply it by the electricity price to find the total cost: $$E = P\text{_heater} \times t = 29.1\,\mathrm{kW} \times 15\,\mathrm{h} = 436.5\,\mathrm{kWh}$$ Now we can find the total cost by multiplying the energy used with the price per kWh: $$\text{Cost} = E \times \text{Price} = 436.5\,\mathrm{kWh} \times \$0.09/\mathrm{kWh} = \$39.30$$ The power rating of the heater is \(29.1\,\mathrm{kW}\), and the cost of electricity for heating the pipe during a 15-h period is \(\$39.30\).

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with Vaia!

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

A group of 25 power transistors, dissipating \(1.5 \mathrm{~W}\) each, are to be cooled by attaching them to a black-anodized square aluminum plate and mounting the plate on the wall of a room at \(30^{\circ} \mathrm{C}\). The emissivity of the transistor and the plate surfaces is 0.9. Assuming the heat transfer from the back side of the plate to be negligible and the temperature of the surrounding surfaces to be the same as the air temperature of the room, determine the size of the plate if the average surface temperature of the plate is not to exceed \(50^{\circ} \mathrm{C}\). Answer: $43 \mathrm{~cm} \times 43 \mathrm{~cm}$

Determine the \(U\)-factor for the center-of-glass section of a double-pane window with a \(13-\mathrm{mm}\) airspace for winter design conditions. The glazings are made of clear glass having an emissivity of \(0.84\). Take the average airspace temperature at design conditions to be $10^{\circ} \mathrm{C}$ and the temperature difference across the airspace to be \(15^{\circ} \mathrm{C}\).

A \(0.6-\mathrm{m} \times 0.6-\mathrm{m}\) horizontal ASTM A203 B steel plate has its lower surface subjected to convection with cold, quiescent hydrogen gas at \(-70^{\circ} \mathrm{C}\). The minimum temperature suitable for the steel plate is \(-30^{\circ} \mathrm{C}\) (ASME Code for Process Piping, ASME B31.3-2014, Table A-1M). The lower plate surface has an emissivity of \(0.3\), and thermal radiation exchange occurs between the lower plate surface and the surroundings at \(-70^{\circ} \mathrm{C}\). Determine the heat addition rate necessary for keeping the lower plate surface temperature from dropping below the minimum suitable temperature.

A hot liquid is poured into a spherical tank with an inner diameter of $3 \mathrm{~m}\( and a wall thickness of \)3 \mathrm{~cm}$. The tank wall is made of a material with a thermal conductivity of $0.15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. The hot liquid in the tank causes the inner surface temperature to be \(100^{\circ} \mathrm{C}\), while the tank outer surface is exposed to air at \(20^{\circ} \mathrm{C}\) and has an emissivity of \(0.35\). Determine the outer surface temperature of the tank. Assume that the properties of air can be evaluated at \(40^{\circ} \mathrm{C}\) and 1 atm pressure. Is this a good assumption?

During a visit to a plastic sheeting plant, it was observed that a 45 -m-long section of a 2 -in nominal \((6.03-\mathrm{cm}\)-outerdiameter) steam pipe extended from one end of the plant to the other with no insulation on it. The temperature measurements at several locations revealed that the average temperature of the exposed surfaces of the steam pipe was $170^{\circ} \mathrm{C}\(, while the temperature of the surrounding air was \)20^{\circ} \mathrm{C}$. The outer surface of the pipe appeared to be oxidized, and its emissivity can be taken to be 0.7. Taking the temperature of the surrounding surfaces to be \(20^{\circ} \mathrm{C}\) also, determine the rate of heat loss from the steam pipe. Steam is generated in a gas furnace that has an efficiency of 84 percent, and the plant pays \(\$ 1.10\) per therm (1 therm \(=105,500 \mathrm{~kJ}\) ) of natural gas. The plant operates \(24 \mathrm{~h}\) a day, 365 days a year, and thus \(8760 \mathrm{~h}\) a year. Determine the annual cost of the heat losses from the steam pipe for this facility.

See all solutions

Recommended explanations on Physics Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.

Sign-up for free