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Consider a 1.2-m-high and 2-m-wide double-pane window consisting of two 3 -mm- thick layers of glass (k= 0.78 W/mK ) separated by a 12mm-wide stagnant air space (k=0.026 W/mK). Determine the steady rate of heat transfer through this double-pane window and the temperature of its inner surface for a day during which the room is maintained at 24C while the temperature of the outdoors is 5C. Take the convection heat transfer coefficients on the inner and outer surfaces of the window to be h1=10 W/m2K and h2= 25 W/m2K, and disregard any heat transfer by radiation.

Short Answer

Expert verified
Answer: The steady rate of heat transfer through the double-pane window is approximately 358.73 W, and the temperature of its inner surface is approximately 9.0C.

Step by step solution

01

Calculate thermal resistances

First, we need to calculate the thermal resistances for convection and conduction across the window system. These thermal resistances are R1 for convection on inner glass surface, R2 for conduction in the inner glass layer, R3 for conduction in the air space, R4 for conduction in the outer glass layer, and R5 for convection on outer glass surface. We can calculate the convection and conduction resistances using the following equations: Rconv=1hA Rcond=LkA where h is the convection heat transfer coefficient, k is the thermal conductivity, A is the area, and L is the thickness.
02

Determine the total thermal resistance

Next, we will find the total thermal resistance by adding all the thermal resistances in the window system. Rtotal=R1+R2+R3+R4+R5
03

Calculate the steady rate of heat transfer

Now, we can calculate the steady rate of heat transfer (Q) by using the following equation: Q=TinToutRtotal where Tin is the temperature inside the room and Tout is the temperature outside.
04

Determine the temperature of the inner surface

Finally, we can find the temperature of the inner surface (T1) using the following equation: T1=TinQR1 Now, let's calculate the values.
05

(Calculations)

The area of the double-pane window is 1.2 m * 2 m = 2.4 m². All the resistances are in series. Thus, they will all have the same area, A = 2.4 m². R1=1h1A=1(10Wm2K)(2.4m2)=0.04167 K/W R2=LkA=0.003m(0.78Wm K)(2.4m2)=0.00161 K/W R3=LkA=0.012m(0.026Wm K)(2.4m2)=0.01923 K/W R4=LkA=0.003m(0.78Wm K)(2.4m2)=0.00161 K/W R5=1h2A=1(25Wm2K)(2.4m2)=0.01667 K/W
06

(Calculations)

Now, let's determine the total thermal resistance. Rtotal=R1+R2+R3+R4+R5=0.04167+0.00161+0.01923+0.00161+0.01667=0.08079 K/W
07

(Calculations)

We can now calculate the steady rate of heat transfer (Q). Q=TinToutRtotal=24°C(5°C)0.08079 K/W=358.73 W
08

(Calculations)

Finally, let's find the temperature of the inner surface (T1). T1=TinQR1=24°C(358.73 W)(0.04167 K/W)=9.05°C9.0C. The steady rate of heat transfer through the double-pane window is approximately 358.73 W, and the temperature of its inner surface is approximately 9.0C.

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Key Concepts

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

Thermal Resistance
Thermal resistance is a measure of how well an object resists the flow of heat. Imagine it as insulation in a house; the more insulation, the harder it is for heat to flow through the walls. Similarly, in a material, thermal resistance determines how difficult it is for heat to transfer from one side to another.
In thermal systems, we often treat thermal resistance like electrical resistance in circuits. It's calculated using specific formulas depending on the type of heat transfer involved. If it's conduction, we use the formula:
  • Rcond=LkA
Here, Rcond is thermal resistance due to conduction, L is the thickness, k is the thermal conductivity, and A is the area.
For convection, we use:
  • Rconv=1hA
Where h is the heat transfer coefficient, unique to the nature of the surface and fluid in contact. In the exercise, these resistances collectively form a sort of barrier to heat transfer across the window.
Conduction
Conduction is the process where heat energy is transmitted through a material. This happens when two areas of a material are at different temperatures. Heat flows from the warmer area to the cooler area. Think about touching a hot stove. The heat moves from the stove to your hand, that's conduction at work.
  • Materials with high thermal conductivity, like metals, transfer heat easily.
  • Materials with low thermal conductivity, like wood and foam, are effective insulators.
For our window example, the heat mainly conducts through glass layers and the air space. The resistances, R2 and R4, pertain to the glass, while R3 relates to the air space. Each material's thickness and thermal conductivity factor into calculating these resistances. The low thermal conductivity value of air highlights it as a poor conductor, which means it serves as a good insulator in this case.
Convection
Convection is the transfer of heat by the movement of a fluid, either a liquid or a gas. If you boil water, you'll notice the warm water rising to the top while cooler water sinks. That's convection. It happens naturally, as in that boiling pot, or it can be forced, like with fans or pumps.In windows, convection occurs at the boundary where the glass meets the air, both inside and out. The heat transfer coefficient h determines how quickly heat is transferred between the glass and the moving air. In the exercise, values h1 and h2 dictate the speed of heat transfer on the inside and outside window surfaces, respectively. The convection resistances R1 and R5 are calculated taking these coefficients into account. These resistances tell us how well the surfaces resist the transfer of heat due to the fluid flow.
Heat Transfer Coefficient
The heat transfer coefficient, denoted as h, is an essential parameter in any calculation involving convection heat transfer. It measures the ability of a fluid to carry heat away from a surface it touches. A higher coefficient means the fluid is good at removing or adding heat.
  • This coefficient depends on the nature of the flow (like turbulent or laminar) and the physical properties of the fluid.
  • In the exercise, h1=10 W/m2K is used for the inside window surface (often less agitated indoor air), while h2=25 W/m2K fits the often windier outdoor surface.
By including these coefficients in their calculations, engineers ensure heat transfer efficiency is appropriately modeled in real-world scenarios. The heat transfer coefficients combine with surface areas to give the resistances R1 and R5, showing how effective convection is at transferring heat through the window.

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Most popular questions from this chapter

A pipe is insulated to reduce the heat loss from it. However, measurements indicate that the rate of heat loss has increased instead of decreasing. Can the measurements be right?

A 4-mm-diameter and 10-cm-long aluminum fin (k=237 W/mK) is attached to a surface. If the heat transfer coefficient is 12 W/m2K, determine the percent error in the rate of heat transfer from the fin when the infinitely long fin assumption is used instead of the adiabatic fin tip assumption.

A 1-m-inner-diameter liquid-oxygen storage tank at a hospital keeps the liquid oxygen at 90 K. The tank consists of a 0.5cm-thick aluminum ( k=170 W/mK) shell whose exterior is covered with a 10 -cm-thick layer of insulation (k= 0.02 W/mK). The insulation is exposed to the ambient air at 20C and the heat transfer coefficient on the exterior side of the insulation is 5 W/m2K. The temperature of the exterior surface of the insulation is (a) 13C (b) 9C (c) 2C (d) 3C (e) 12C

A hot surface at 80C in air at 20C is to be cooled by attaching 10 -cm-long and 1 -cm-diameter cylindrical fins. The combined heat transfer coefficient is 30 W/m2K, and heat transfer from the fin tip is negligible. If the fin efficiency is 0.75, the rate of heat loss from 100 fins is (a) 325 W (b) 707 W (c) 566 W (d) 424 W (e) 754 W

Steam at 320C flows in a stainless steel pipe (k= 15 W/mK ) whose inner and outer diameters are 5 cm and 5.5 cm, respectively. The pipe is covered with 3cm-thick glass wool insulation (k=0.038 W/mK). Heat is lost to the surroundings at 5C by natural convection and radiation, with a combined natural convection and radiation heat transfer coefficient of 15 W/m2K. Taking the heat transfer coefficient inside the pipe to be 80 W/m2K, determine the rate of heat loss from the steam per unit length of the pipe. Also determine the temperature drops across the pipe shell and the insulation.

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