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

A 5-cm-external-diameter, 10-m-long hot-water pipe at \(80^{\circ} \mathrm{C}\) is losing heat to the surrounding air at \(5^{\circ} \mathrm{C}\) by natural convection with a heat transfer coefficient of \(25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Determine the rate of heat loss from the pipe by natural convection. Answer: \(2945 \mathrm{~W}\)

Short Answer

Expert verified
Answer: The rate of heat loss from the pipe by natural convection is approximately 2945 W.

Step by step solution

01

Calculate the surface area of the pipe

The pipe is of cylindrical shape, so its surface area can be calculated using the formula \(A=2 \pi r L\), where \(r\) is the radius and \(L\) is the length of the pipe. Since the diameter is given, we can find the radius by dividing the diameter by two. So \(r = \frac{5}{2} \mathrm{~cm} = 0.025 \mathrm{~m}\). Now we can find the surface area of the pipe: \(A=2 \pi (0.025 \mathrm{~m})(10 \mathrm{~m}) \approx 1.571 \mathrm{~m}^2\).
02

Find the temperature difference

The temperature difference between the pipe and the surrounding air can be found by subtracting the surrounding air temperature (\(T_\mathrm{air}=5^{\circ} \mathrm{C}\)) from the pipe temperature (\(T_\mathrm{pipe}=80^{\circ} \mathrm{C}\)). So, the temperature difference is \(ΔT = T_\mathrm{pipe} - T_\mathrm{air} = 80^{\circ} \mathrm{C} - 5^{\circ} \mathrm{C} = 75 \mathrm{~K}\).
03

Calculate the rate of heat loss

Now we can use the formula for heat transfer by natural convection, which is \(q=h \cdot A \cdot ΔT\), where \(q\) represents the rate of heat loss, \(h\) is the heat transfer coefficient, \(A\) is the surface area of the pipe, and \(ΔT\) is the temperature difference. Plugging in the given and calculated values, we get: \(q = (25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}) \cdot (1.571 \mathrm{~m}^2) \cdot (75 \mathrm{~K}) \approx 2945 \mathrm{~W}\). The rate of heat loss from the pipe by natural convection is approximately \(2945 \mathrm{~W}\).

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!

Key Concepts

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

Natural Convection
Natural convection is a process where heat is transferred without any external aid, such as fans or pumps. This happens because of the movement caused by differences in temperature and density within the fluid surrounding the object. In the case of the hot-water pipe, the warm surface of the pipe heats the air nearby. As the air warms up, it becomes less dense and rises. Cooler, denser air then moves in to take its place. This cycle of rising warm air and falling cool air leads to natural convection currents.
The efficiency of heat transfer by natural convection depends on the surface area involved, the temperature difference between the surface and the surrounding fluid, and a property specific to the condition known as the heat transfer coefficient.
Heat Loss Calculation
Calculating heat loss involves determining how much heat escapes from an object into its surroundings. For objects like pipes, heat loss is primarily driven by the temperature difference between the pipe and its environment, as well as the medium through which the heat is lost. In natural convection, the formula used is:
  • \[ q = h \times A \times \Delta T \]
where:
  • \( q \) is the rate of heat loss in watts (W),
  • \( h \) is the heat transfer coefficient in watts per square meter per kelvin (\( \mathrm{W} / \mathrm{m}^{2} \, \mathrm{K} \)),
  • \( A \) is the surface area in square meters (\( \mathrm{m}^2 \)),
  • \( \Delta T \) is the temperature difference in kelvin (K).
Understanding this formula helps in assessing the energy efficiency of piping systems and making necessary improvements to reduce energy costs.
Surface Area of Pipe
The surface area of a pipe significantly affects how much heat it can transfer to its surroundings. To find the surface area of a cylindrical pipe, the following formula is used:
  • \[ A = 2 \pi r L \]
where \( r \) is the radius of the pipe and \( L \) is the length. Converting the diameter to radius is essential: given a diameter of 5 cm, the radius is half of that, or 2.5 cm (which is 0.025 meters for calculations).
The calculated surface area for a 10-meter-long pipe with this radius is approximately 1.571 square meters. A larger surface area allows for greater heat loss, making this a crucial value in heat transfer calculations.
Temperature Difference
A key driver in the rate of heat transfer by natural convection is the temperature difference between the object and its surroundings. The formula:
  • \[ \Delta T = T_{\text{pipe}} - T_{\text{air}} \]
naturally arises from subtracting the temperature of the surrounding air from that of the pipe. In this scenario, the hot-water pipe is at \( 80^{\circ} \mathrm{C} \), and the external air is at \( 5^{\circ} \mathrm{C} \).
This difference of 75 Kelvin drives the convective heat transfer process. A greater temperature difference typically increases the rate of heat loss, as the energy moves more quickly from the warmer area to the cooler area to establish equilibrium.

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

Two surfaces, one highly polished and the other heavily oxidized, are found to be emitting the same amount of energy per unit area. The highly polished surface has an emissivity of \(0.1\) at \(1070^{\circ} \mathrm{C}\), while the emissivity of the heavily oxidized surface is \(0.78\). Determine the temperature of the heavily oxidized surface.

A cylindrical resistor element on a circuit board dissipates \(1.2 \mathrm{~W}\) of power. The resistor is \(2 \mathrm{~cm}\) long, and has a diameter of \(0.4 \mathrm{~cm}\). Assuming heat to be transferred uniformly from all surfaces, determine \((a)\) the amount of heat this resistor dissipates during a 24-hour period, \((b)\) the heat flux, and \((c)\) the fraction of heat dissipated from the top and bottom surfaces.

It is well-known that at the same outdoor air temperature a person is cooled at a faster rate under windy conditions than under calm conditions due to the higher convection heat transfer coefficients associated with windy air. The phrase wind chill is used to relate the rate of heat loss from people under windy conditions to an equivalent air temperature for calm conditions (considered to be a wind or walking speed of \(3 \mathrm{mph}\) or \(5 \mathrm{~km} / \mathrm{h})\). The hypothetical wind chill temperature (WCT), called the wind chill temperature index (WCTI), is an equivalent air temperature equal to the air temperature needed to produce the same cooling effect under calm conditions. A 2003 report on wind chill temperature by the U.S. National Weather Service gives the WCTI in metric units as WCTI \(\left({ }^{\circ} \mathrm{C}\right)=13.12+0.6215 T-11.37 V^{0.16}+0.3965 T V^{0.16}\) where \(T\) is the air temperature in \({ }^{\circ} \mathrm{C}\) and \(V\) the wind speed in \(\mathrm{km} / \mathrm{h}\) at \(10 \mathrm{~m}\) elevation. Show that this relation can be expressed in English units as WCTI \(\left({ }^{\circ} \mathrm{F}\right)=35.74+0.6215 T-35.75 V^{0.16}+0.4275 T V^{0.16}\) where \(T\) is the air temperature in \({ }^{\circ} \mathrm{F}\) and \(V\) the wind speed in \(\mathrm{mph}\) at \(33 \mathrm{ft}\) elevation. Also, prepare a table for WCTI for air temperatures ranging from 10 to \(-60^{\circ} \mathrm{C}\) and wind speeds ranging from 10 to \(80 \mathrm{~km} / \mathrm{h}\). Comment on the magnitude of the cooling effect of the wind and the danger of frostbite.

A 25 -cm-diameter black ball at \(130^{\circ} \mathrm{C}\) is suspended in air, and is losing heat to the surrounding air at \(25^{\circ} \mathrm{C}\) by convection with a heat transfer coefficient of \(12 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), and by radiation to the surrounding surfaces at \(15^{\circ} \mathrm{C}\). The total rate of heat transfer from the black ball is (a) \(217 \mathrm{~W}\) (b) \(247 \mathrm{~W}\) (c) \(251 \mathrm{~W}\) (d) \(465 \mathrm{~W}\) (e) \(2365 \mathrm{~W}\)

Air at \(20^{\circ} \mathrm{C}\) with a convection heat transfer coefficient of \(20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) blows over a pond. The surface temperature of the pond is at \(40^{\circ} \mathrm{C}\). Determine the heat flux between the surface of the pond and the air.

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