ch 8 radiation - university of technology, iraq...other names for the radiation shape factor are...

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1 Ch – 8- Thermal radiation Heat Transfer 8-1 INTRODUCTION We now wish to consider the third mode of heat transfer—thermal radiation. Thermal radiation is that electromagnetic radiation emitted by a body as a result of its temperature. 8-2 PHYSICAL MECHANISM There are many types of electromagnetic radiation; thermal radiation is only one. Regardless of the type of radiation, we say that it is propagated at the speed of light, 3x10 8 m/s. The speed is equal to the product of the wavelength and frequency of the radiation, C=λν C: speed of light, λ: wavelength, ν:frequency. A portion of the electromagnetic spectrum is shown is the fig. 8-1 Thermal radiation lies in the range from about 0.1 to 100μm, while the visible- light portion of the spectrum is very narrow, extending from about 0.35 to 0.75 μ m.

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Page 1: ch 8 radiation - University of Technology, Iraq...Other names for the radiation shape factor are view factor, angle factor, and configuration factor. The total energy leaving surface

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Ch – 8- Thermal radiation Heat Transfer

8-1 INTRODUCTION

We now wish to consider the third mode of heat transfer—thermal radiation. Thermal radiation is that electromagnetic radiation emitted by a body as a result of its temperature. 8-2 PHYSICAL MECHANISM There are many types of electromagnetic radiation; thermal radiation is only one. Regardless of the type of radiation, we say that it is propagated at the speed of light, 3x108 m/s. The speed is equal to the product of the wavelength and frequency of the radiation, C=λν C: speed of light, λ: wavelength, ν:frequency. A portion of the electromagnetic spectrum is shown is the fig. 8-1

Thermal radiation lies in the range from about 0.1 to 100μm, while the visible-light portion of the spectrum is very narrow, extending from about 0.35 to 0.75 μm.

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The total energy emitted is proportional to absolute temperature to the fourth power: Eb =σT 4 [8-3] Equation (8-3) is called the Stefan-Boltzmann law, Eb is the energy radiated per unit time and per unit area by the ideal radiator, and σ is the Stefan-Boltzmann constant, which has the value σ =5.669×10−8 W/m2 ・K4 [0.1714×10−8 Btu/h ・ ft2 ・ ◦R4]

where Eb is in watts per square meter and T is in degrees Kelvin.

The blackbody radiation: The subscript b denotes that this is the radiation from a blackbody. We call this blackbody radiation because materials which obey this law appear black to the eye; they appear black because they do not reflect any radiation. Thus a blackbody is also considered as one which absorbs all radiation incident upon it. Eb is called the emissive power of a blackbody. 8-3 RADIATION PROPERTIES When radiant energy strikes a material surface, part of the radiation is reflected, part is absorbed, and part is transmitted, as shown in Fig. 8-2.

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ρ +α +τ =1.

We define the reflectivity ρ as the fraction reflected, the absorptivity α as the fraction absorbed, and the transmissivity τ as the fraction transmitted. Most solid bodies do not transmit thermal radiation, so that the transmissivity may be taken as zero. Then ρ+α=1

- Specular surface: the angle of incidence is equal to the angle of reflection. Fig. 8-3a.

- Diffuse surface: an incident beam is distributed uniformly in all directions after

reflection. Fig 8-3b.

The relation between the emissive power of a body and the material properties:

Assume that a perfectly black enclosure is available, i.e., one which absorbs all the incident radiation falling upon it, as shown in Fig. 8-4.

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This enclosure will also emit radiation according to T4 law Let the radiant flux arriving at some area in the enclosure be qi W/m2.. Now suppose that a body is placed inside the enclosure and allowed to come into temperature equilibrium with it. At equilibrium the energy absorbed by the body must be equal to the energy emitted; otherwise there would be an energy flow into or out of the body which would raise or lower its temperature. At equilibrium we may write EA = qi Aα [8-5] If we now replace the body in the enclosure with a blackbody of the same size and shape and allow it to come to equilibrium with the enclosure at the same temperature, EbA=qiA(1) [8-6] since the absorptivity of a blackbody is unity. If Equation (8-5) is divided by Equation (8-6), E/Eb =α And we find that the ratio of the emissive power of a body to the emissive power of a blackbody at the same temperature is equal to the absorptivity of the body. This ratio is defined as the emissivity ε of the body, ε =E/Eb ⇒ε =α which is called Kirchhoff’s identity.

The Gray body A gray body is defined such that the monochromatic emissivity ελ of the bodyis independent of wavelength. The monochromatic emissivity is defined as the ratio

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of the monochromatic emissive power of the body to the monochromatic emissive power of a blackbody at the same wavelength and temperature. Thus

The total emissivity of the body may be related to the monochromatic emissivity by noting that

[8-9]

where Ebλ is the emissive power of a blackbody per unit wavelength

A plot of Ebλ as a function of temperature and wavelength is given in Fig. 8-5a. Figure 8-5 (a) Blackbody emissive power as a function of wavelength and temperature; (b) comparison of emissive power of ideal blackbodies and gray bodies with that of a real surface.

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The maximum point in the radiation curves are related by Wien’s displacement law, λmaxT = 2897.6μm⋅K Why the material appears much brighter at higher temperature? Fig 8-5a, b.

Figure 8-5b indicates the relative radiation spectra from a blackbody at 3000◦F and a corresponding ideal gray body with emissivity equal to 0.6.Also shown is a curve indicating an approximate behavior for a real surface, which may differ considerably from that of either an ideal blackbody or an ideal gray body. For analysis purposes surfaces are usually considered as gray bodies, with emissivities taken as the integrated average value.

We are frequently interested in the amount of energy radiated from a blackbody in a certain specified wavelength range. The fraction of the total energy radiated between 0 and λ is given by

[8-14]

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Now, for any specified temperature, the integrals in Equation (8-14) may be expressed in terms of the single variable λT . The ratio in Equation (8-14) is tabulated in Table 8-1, along with the ratio Ebλ/T5.

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If the radiant energy emitted between wavelengths λ1 and λ2 is desired, then

[8-16]

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8-4 RADIATION SHAPE FACTOR

We wish to obtain a general expression for the energy exchange between these surfaces when they are maintained at different temperatures. The problem becomes essentially one of determining the amount of energy which leaves one surface and reaches the other. To solve this problem the radiation shape factors are defined as F1-2 = fraction of energy leaving surface 1 which reaches surface 2 F2-1 = fraction of energy leaving surface 2 which reaches surface 1 Fm-n = fraction of energy leaving surface m which reaches surface n Other names for the radiation shape factor are view factor, angle factor, and configuration factor. The total energy leaving surface 1 and arriving at surface 2 is

Eb1A1F12 And the energy leaving surface 2 and arriving at surface 1 is Eb2A2F21 Since the surfaces are black, all the incident radiation will be absorbed, and the net energy exchange is Eb1A1F12 - Eb2A2F21 = Q1-2 IF both surfaces are at the same temperature, there can be no net heat exchange, that is, Q1-2 = 0. Also, for T1=T2 Eb1=Eb2 So that A1F12 = A2F21 The net heat exchange is therefore Q1-2 = A1 F12 (Eb1 - Eb2) = A2 F21 (Eb1 - Eb2)

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The above equation is known as a reciprocity relation, and it applies in a general way for any two surfaces m and n: Am Fmn = An Fnm It also holds for other surfaces as long as diffuse radiation is involved.

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8-5 RELATIONS BETWEEN SHAPE FACTORS

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Suppose we wish to determine the shape factor F1−3 for the surfaces

in Figure 8-20 in terms of known shape factors for perpendicular rectangles with a common edge. We may write F1−2,3 =F1−2 +F1−3

in accordance with Equation (8-25). Both F1−2,3 and F1−2 may be determined from

Figure 8-14, so that F1−3 is easily calculated when the dimensions are known.

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Now consider the somewhat more complicated situation shown in Figure 8-21.An expression for the shape factor F1−4 is desired in terms of known shape factors for perpendicular rectangles with a common edge.We write A1,2 F1,2−3,4 = A1F1−3,4 + A2F2−3,4 [a]

in accordance with Equation (8-25). Both F1,2−3,4 and F2−3,4 can be obtained from

Figure 8-14, and F1−3,4 may be expressed A1F1−3,4 = A1F1−3 + A1F1−4 [b] Also A1,2 F1,2−3 = A1F1−3 + A2F2−3 [c]

Solving forA1F1−3 from (c), inserting this in (b), and then inserting the resultant expression For A1F1−3,4 in (a) gives

A1,2 F1,2−3,4 = A1,2 F1,2−3 −A2F2−3 + A1F1−4 +A2F2−3,4 [d] Notice that all shape factors except F1−4 may be determined from Figure 8-14. Thus F1−4 = 1/A1 (A1,2 F1,2−3,4 + A2F2−3 − A1,2 F1,2−3 − A2F2−3,4) [8-28]

In the foregoing discussion the tacit assumption has been made that the various bodies do not see themselves, that is, F11 =F22 =F33 =0 ・ ・ ・

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Exercise: Homework

Consider the view factor F14 for surfaces surfaces are perpendicular but do not share a common edge.

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for surfaces 1 and 4 of the following geometry. These but do not share a common edge.

the following geometry. These

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8-6 HEAT EXCHANGE BETWEEN NONBLACKBODIES When radiation energy strikes nonblack bodies, part of the energy will be reflected back to another heat transfer surface. In order to analyes the energy emits by nonblack bodies, two terms may be defined :

G= irradiation = total radiation incident upon a surface per unit time and per unit area J = radiosity = total radiation that leaves a surface per unit time and per unit area

Figure 8-24 (a) Surface energy balance for opaque material; (b) element representing “surface resistance” in the radiation-network method. As shown in Figure 8-24, the radiosity is the sum of the energy emitted and the energy reflected when no energy is transmitted, or J =εEb +ρG Since the transmissivity is assumed to be zero, the reflectivity may be expressed as ρ=1−α=1−ε so that J =εEb +(1−ε)G

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The net energy leaving the surface is the difference between the radiosity and the irradiation: q/A =J −G=εEb +(1− ε)G−G Solving for G in terms of J

Or q = potential difference / internal thermal resistance( surface resistance)

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