Fundamental Radiation Concepts
Electromagnetic Radiation Spectrum
- Thermal radiation: Emission of electromagnetic waves from a surface due to its temperature
- Wavelength range: Thermal radiation occurs primarily in the range of 0.1 to 100 μm
- Speed of light: \(c = 2.998 \times 10^8\) m/s (in vacuum)
Wavelength-Frequency Relationship
\[ \lambda = \frac{c}{\nu} \]
Where:- \(\lambda\) = wavelength (m or μm)
- \(c\) = speed of light = \(2.998 \times 10^8\) m/s
- \(\nu\) = frequency (Hz or s-1)
Photon Energy
\[ E = h\nu = \frac{hc}{\lambda} \]
Where:- \(E\) = photon energy (J)
- \(h\) = Planck's constant = \(6.626 \times 10^{-34}\) J·s
- \(\nu\) = frequency (Hz)
- \(c\) = speed of light (m/s)
- \(\lambda\) = wavelength (m)
Blackbody Radiation
Blackbody Definition
- A blackbody is an ideal surface that absorbs all incident radiation regardless of wavelength and direction
- A blackbody also emits the maximum possible radiation at any given temperature
- No real surface is a perfect blackbody, but it serves as an idealization
Planck's Law
\[ E_{b\lambda}(T) = \frac{C_1}{\lambda^5 \left[e^{C_2/\lambda T} - 1\right]} \]
Where:- \(E_{b\lambda}\) = spectral (monochromatic) emissive power of a blackbody (W/m2·μm or W/m3)
- \(T\) = absolute temperature (K)
- \(\lambda\) = wavelength (μm or m)
- \(C_1\) = first radiation constant = \(3.742 \times 10^8\) W·μm4/m2 = \(2\pi hc^2\)
- \(C_2\) = second radiation constant = \(1.439 \times 10^4\) μm·K = \(hc/k\)
- \(k\) = Boltzmann constant = \(1.381 \times 10^{-23}\) J/K
Wien's Displacement Law
\[ \lambda_{max} T = C_3 \]
Where:- \(\lambda_{max}\) = wavelength at which maximum spectral emissive power occurs (μm)
- \(T\) = absolute temperature (K)
- \(C_3\) = Wien's displacement constant = 2898 μm·K
Note: As temperature increases, the peak wavelength shifts to shorter wavelengths (higher frequencies).
Stefan-Boltzmann Law
\[ E_b = \sigma T^4 \]
Where:- \(E_b\) = total (integrated over all wavelengths) emissive power of a blackbody (W/m2)
- \(\sigma\) = Stefan-Boltzmann constant = \(5.670 \times 10^{-8}\) W/(m2·K4)
- \(T\) = absolute temperature (K)
Alternative form: \[ E_b = \int_0^\infty E_{b\lambda} \, d\lambda = \sigma T^4 \]
Blackbody Radiation Intensity
\[ I_b = \frac{E_b}{\pi} = \frac{\sigma T^4}{\pi} \]
Where:- \(I_b\) = blackbody intensity (W/m2·sr)
- \(E_b\) = blackbody emissive power (W/m2)
Note: The factor π arises because blackbody emission is diffuse (Lambertian).
Real Surface Radiation Properties
Emissivity
Total hemispherical emissivity: \[ \varepsilon = \frac{E}{E_b} = \frac{E}{\sigma T^4} \]
Where:- \(\varepsilon\) = total hemispherical emissivity (dimensionless, 0 ≤ ε ≤ 1)
- \(E\) = total emissive power of the real surface (W/m2)
- \(E_b\) = blackbody emissive power at the same temperature (W/m2)
Spectral emissivity: \[ \varepsilon_\lambda = \frac{E_\lambda}{E_{b\lambda}} \]
Where:- \(\varepsilon_\lambda\) = spectral (monochromatic) emissivity
- \(E_\lambda\) = spectral emissive power of the real surface
- \(E_{b\lambda}\) = spectral emissive power of a blackbody
Absorptivity
Total hemispherical absorptivity: \[ \alpha = \frac{G_{abs}}{G} \]
Where:- \(\alpha\) = total hemispherical absorptivity (dimensionless, 0 ≤ α ≤ 1)
- \(G_{abs}\) = absorbed radiation (W/m2)
- \(G\) = incident radiation (irradiation) (W/m2)
Spectral absorptivity: \[ \alpha_\lambda = \frac{G_{\lambda,abs}}{G_\lambda} \]
Reflectivity
\[ \rho = \frac{G_{ref}}{G} \]
Where:- \(\rho\) = total hemispherical reflectivity (dimensionless, 0 ≤ ρ ≤ 1)
- \(G_{ref}\) = reflected radiation (W/m2)
- \(G\) = incident radiation (W/m2)
Transmissivity
\[ \tau = \frac{G_{tr}}{G} \]
Where:- \(\tau\) = total hemispherical transmissivity (dimensionless, 0 ≤ τ ≤ 1)
- \(G_{tr}\) = transmitted radiation (W/m2)
- \(G\) = incident radiation (W/m2)
Conservation of Incident Radiation
\[ \alpha + \rho + \tau = 1 \]
For opaque surfaces (τ = 0): \[ \alpha + \rho = 1 \]
Kirchhoff's Law
For surfaces in thermal equilibrium: \[ \varepsilon = \alpha \]
Spectral form: \[ \varepsilon_\lambda = \alpha_\lambda \]
Important conditions:- Valid when the surface temperature equals the temperature of the incident radiation source
- For diffuse, gray surfaces at different temperatures, often approximated as ε = α
Gray Surface Assumption
- A gray surface has spectral properties independent of wavelength: \(\varepsilon_\lambda = \varepsilon = \text{constant}\)
- Similarly: \(\alpha_\lambda = \alpha = \text{constant}\)
- Simplifies radiation calculations significantly
Diffuse Surface Assumption
- A diffuse surface has radiation properties independent of direction
- Emitted and reflected radiation intensity is uniform in all directions
- Follows Lambert's cosine law
Radiation Heat Transfer Between Surfaces
Radiation Emitted by a Real Surface
\[ q_{emit} = \varepsilon A \sigma T^4 \]
Where:- \(q_{emit}\) = total radiation emitted by the surface (W)
- \(\varepsilon\) = emissivity of the surface
- \(A\) = surface area (m2)
- \(\sigma\) = Stefan-Boltzmann constant = \(5.670 \times 10^{-8}\) W/(m2·K4)
- \(T\) = absolute temperature of the surface (K)
Net Radiation Heat Transfer
For a single surface exchanging radiation with surroundings: \[ q_{net} = \varepsilon A \sigma (T^4 - T_{surr}^4) \]
Where:- \(q_{net}\) = net radiation heat transfer from the surface (W)
- \(T\) = surface temperature (K)
- \(T_{surr}\) = temperature of surroundings (K)
Assumption: Surroundings act as a blackbody and completely enclose the surface.
Radiation Between Two Infinite Parallel Plates
\[ q = \frac{\sigma A (T_1^4 - T_2^4)}{\frac{1}{\varepsilon_1} + \frac{1}{\varepsilon_2} - 1} \]
Where:- \(q\) = heat transfer rate (W)
- \(A\) = area of either plate (m2)
- \(T_1, T_2\) = absolute temperatures of plates 1 and 2 (K)
- \(\varepsilon_1, \varepsilon_2\) = emissivities of plates 1 and 2
Radiation Between Two Concentric Cylinders or Spheres
For concentric cylinders (per unit length): \[ q = \frac{\sigma (2\pi r_1) (T_1^4 - T_2^4)}{\frac{1}{\varepsilon_1} + \frac{r_1}{r_2}\left(\frac{1}{\varepsilon_2} - 1\right)} \]
For concentric spheres: \[ q = \frac{\sigma (4\pi r_1^2) (T_1^4 - T_2^4)}{\frac{1}{\varepsilon_1} + \frac{r_1^2}{r_2^2}\left(\frac{1}{\varepsilon_2} - 1\right)} \]
Where:- \(r_1\) = radius of inner surface (m)
- \(r_2\) = radius of outer surface (m)
- \(T_1, T_2\) = absolute temperatures of inner and outer surfaces (K)
- \(\varepsilon_1, \varepsilon_2\) = emissivities of inner and outer surfaces
Special case: If inner surface is small compared to outer surface (\(r_1 \ll r_2\)): \[ q \approx \varepsilon_1 A_1 \sigma (T_1^4 - T_2^4) \]
View Factors (Configuration Factors)
View Factor Definition
- The view factor \(F_{ij}\) is the fraction of radiation leaving surface i that is directly intercepted by surface j
- Also called shape factor or configuration factor
- Purely geometric quantity; independent of surface properties and temperatures
View Factor Properties
Reciprocity relation: \[ A_i F_{ij} = A_j F_{ji} \]
Where:- \(A_i, A_j\) = areas of surfaces i and j (m2)
- \(F_{ij}\) = view factor from surface i to surface j
- \(F_{ji}\) = view factor from surface j to surface i
Summation rule (enclosure): \[ \sum_{j=1}^{N} F_{ij} = 1 \]
- For an enclosure with N surfaces, all radiation leaving surface i must be intercepted by the N surfaces (including itself)
For flat or convex surfaces: \[ F_{ii} = 0 \]
- A flat or convex surface cannot see itself
- For concave surfaces, \(F_{ii} > 0\)
Common View Factor Relations
Two parallel, identical rectangles or disks:- Use charts or tables from NCEES PE Reference Handbook or standard references
Perpendicular rectangles with common edge:- Use charts or tables from standard references
Sphere inside a cube or cylinder:- Use reciprocity and summation rules with known geometric relations
View Factor Algebra
Subdivision of surfaces: \[ F_{i(j,k)} = F_{ij} + F_{ik} \]
Where:- Surface composed of j and k can be analyzed using subdivision
Example application: \[ A_i F_{i(j+k)} = A_i F_{ij} + A_i F_{ik} \]
Radiation Heat Transfer in Enclosures
Radiosity
\[ J = \varepsilon E_b + \rho G \]
Where:- \(J\) = radiosity, total radiation leaving a surface per unit area (W/m2)
- \(\varepsilon\) = emissivity
- \(E_b = \sigma T^4\) = blackbody emissive power (W/m2)
- \(\rho\) = reflectivity
- \(G\) = irradiation, incident radiation per unit area (W/m2)
For gray, diffuse surfaces with ρ = 1 - ε: \[ J = \varepsilon \sigma T^4 + (1 - \varepsilon) G \]
Net Radiation Leaving a Surface
\[ q_i = A_i (J_i - G_i) \]
Alternative form: \[ q_i = \frac{E_{bi} - J_i}{\frac{1-\varepsilon_i}{\varepsilon_i A_i}} \]
Where:- \(q_i\) = net radiation heat transfer from surface i (W)
- \(A_i\) = area of surface i (m2)
- \(E_{bi} = \sigma T_i^4\) = blackbody emissive power of surface i
- \(J_i\) = radiosity of surface i
- \(\varepsilon_i\) = emissivity of surface i
Note: The term \(\frac{1-\varepsilon_i}{\varepsilon_i A_i}\) is the
surface resistance.
Radiation Exchange Between Surfaces
\[ q_{ij} = A_i F_{ij} (J_i - J_j) \]
Where:- \(q_{ij}\) = radiation heat transfer from surface i to surface j (W)
- \(F_{ij}\) = view factor from surface i to surface j
Alternative form using space resistance: \[ q_{ij} = \frac{J_i - J_j}{\frac{1}{A_i F_{ij}}} \]
Note: The term \(\frac{1}{A_i F_{ij}}\) is the
space resistance or
geometric resistance.
Two-Surface Enclosure
\[ q_{12} = \frac{\sigma (T_1^4 - T_2^4)}{\frac{1-\varepsilon_1}{\varepsilon_1 A_1} + \frac{1}{A_1 F_{12}} + \frac{1-\varepsilon_2}{\varepsilon_2 A_2}} \]
Where:- \(q_{12}\) = net radiation from surface 1 to surface 2 (W)
- \(T_1, T_2\) = absolute temperatures (K)
- \(\varepsilon_1, \varepsilon_2\) = emissivities
- \(A_1, A_2\) = surface areas (m2)
- \(F_{12}\) = view factor from surface 1 to surface 2
Special cases: Large (infinite) parallel plates: \(A_1 = A_2 = A\), \(F_{12} = 1\) \[ q = \frac{A \sigma (T_1^4 - T_2^4)}{\frac{1}{\varepsilon_1} + \frac{1}{\varepsilon_2} - 1} \]
Small object in large enclosure: \(A_1 \ll A_2\), \(F_{12} = 1\) \[ q = \varepsilon_1 A_1 \sigma (T_1^4 - T_2^4) \]
Three-Surface Enclosure
For an enclosure with three gray, diffuse surfaces, the net heat transfer from each surface is: \[ q_1 = \frac{E_{b1} - J_1}{\frac{1-\varepsilon_1}{\varepsilon_1 A_1}} \] \[ q_2 = \frac{E_{b2} - J_2}{\frac{1-\varepsilon_2}{\varepsilon_2 A_2}} \] \[ q_3 = \frac{E_{b3} - J_3}{\frac{1-\varepsilon_3}{\varepsilon_3 A_3}} \]
Conservation of energy for the enclosure: \[ q_1 + q_2 + q_3 = 0 \]
Radiation exchange between surfaces: \[ q_{12} = \frac{J_1 - J_2}{\frac{1}{A_1 F_{12}}} \] \[ q_{13} = \frac{J_1 - J_3}{\frac{1}{A_1 F_{13}}} \] \[ q_{23} = \frac{J_2 - J_3}{\frac{1}{A_2 F_{23}}} \]
For surface 1: \[ q_1 = q_{12} + q_{13} \]
Solution method:- Solve system of equations for radiosities \(J_1, J_2, J_3\)
- Calculate heat transfer rates using radiosity values
- Network analogy: surface resistances in series with space resistances
Reradiating (Adiabatic) Surface
For a surface that is perfectly insulated (adiabatic): \[ q_i = 0 \] \[ J_i = E_{bi} \]
- The reradiating surface absorbs and re-emits all incident radiation
- Its radiosity equals its blackbody emissive power
- Temperature adjusts to satisfy energy balance
Radiation Shields
Single Radiation Shield Between Parallel Plates
\[ q = \frac{\sigma (T_1^4 - T_2^4)}{\frac{1}{\varepsilon_1} + \frac{1}{\varepsilon_2} - 1 + \frac{1}{\varepsilon_{s1}} + \frac{1}{\varepsilon_{s2}} - 1} \]
Where:- \(q\) = heat transfer per unit area (W/m2)
- \(T_1, T_2\) = temperatures of the two plates (K)
- \(\varepsilon_1, \varepsilon_2\) = emissivities of the two plates
- \(\varepsilon_{s1}, \varepsilon_{s2}\) = emissivities of the two sides of the shield
If shield has identical emissivities on both sides (\(\varepsilon_{s1} = \varepsilon_{s2} = \varepsilon_s\)): \[ q = \frac{\sigma (T_1^4 - T_2^4)}{\frac{1}{\varepsilon_1} + \frac{1}{\varepsilon_2} - 1 + \frac{2}{\varepsilon_s} - 1} \]
Reduction in heat transfer:- With one shield, heat transfer is approximately halved compared to no shield (for similar emissivities)
- Multiple shields provide further reduction
Multiple Radiation Shields
For N shields between two parallel plates: \[ q = \frac{\sigma (T_1^4 - T_2^4)}{\frac{1}{\varepsilon_1} + \frac{1}{\varepsilon_2} - 1 + N\left(\frac{2}{\varepsilon_s} - 1\right)} \]
Where:- \(N\) = number of shields
- \(\varepsilon_s\) = emissivity of each shield (assuming all shields identical)
Radiation Combined with Convection
Total Heat Transfer
\[ q_{total} = q_{conv} + q_{rad} \] \[ q_{total} = hA(T_s - T_\infty) + \varepsilon A \sigma (T_s^4 - T_{surr}^4) \]
Where:- \(q_{total}\) = total heat transfer (W)
- \(q_{conv}\) = convection heat transfer (W)
- \(q_{rad}\) = radiation heat transfer (W)
- \(h\) = convection heat transfer coefficient (W/m2·K)
- \(A\) = surface area (m2)
- \(T_s\) = surface temperature (K)
- \(T_\infty\) = ambient fluid temperature (K)
- \(T_{surr}\) = temperature of surroundings for radiation (K)
Radiation Heat Transfer Coefficient
Linearized radiation heat transfer: \[ q_{rad} = h_r A (T_s - T_{surr}) \]
Where the radiation heat transfer coefficient is: \[ h_r = \varepsilon \sigma (T_s + T_{surr})(T_s^2 + T_{surr}^2) \]
Alternative form: \[ h_r = \varepsilon \sigma (T_s^2 + T_{surr}^2)(T_s + T_{surr}) \]
Approximate form for small temperature differences: \[ h_r \approx 4 \varepsilon \sigma T_{avg}^3 \]
Where:- \(T_{avg} = \frac{T_s + T_{surr}}{2}\)
Combined Heat Transfer Coefficient
\[ q_{total} = (h + h_r) A (T_s - T_\infty) \]
Where:- \(h + h_r\) = combined (total) heat transfer coefficient
Assumption: \(T_{surr} \approx T_\infty\) for this simplification to be valid.
Gas Radiation
Gas Emissivity and Absorptivity
- Participating media: Gases like CO2, H2O, CO, SO2, and hydrocarbons absorb and emit radiation
- Nonparticipating media: Monoatomic and most diatomic gases (O2, N2, H2, air) are transparent to thermal radiation
- Gas radiation is a volumetric phenomenon, not a surface phenomenon
- Gas emissivity depends on temperature, partial pressure, and path length (beam length)
Gas Radiation Heat Transfer
Emission from a gas volume to a surface: \[ q = \varepsilon_g A \sigma T_g^4 \]
Where:- \(\varepsilon_g\) = gas emissivity (function of \(T_g\), \(p_a L\))
- \(A\) = surface area (m2)
- \(T_g\) = gas temperature (K)
- \(p_a\) = partial pressure of absorbing gas (atm)
- \(L\) = mean beam length (m)
Absorption by a gas from a surface: \[ q = \alpha_g A \sigma T_s^4 \]
Where:- \(\alpha_g\) = gas absorptivity (function of \(T_s\), \(p_a L\))
- \(T_s\) = surface temperature (K)
Net radiation exchange between gas and surface: \[ q = A \sigma (\varepsilon_g T_g^4 - \alpha_g T_s^4) \]
Mean Beam Length
- The mean beam length \(L\) is a characteristic dimension of the gas volume
- Accounts for the average path length of radiation through the gas
Common geometries:- Sphere of diameter D: \(L = 0.65D\)
- Infinite cylinder of diameter D: \(L = 0.95D\)
- Semi-infinite cylinder of diameter D radiating to base: \(L = 0.65D\)
- Cube of side L radiating to a face: \(L = 0.66L\)
- Rectangular parallelepiped: Use charts or approximation formulas
General approximation: \[ L = 3.6 \frac{V}{A} \]
Where:- \(V\) = gas volume (m3)
- \(A\) = surface area enclosing the gas (m2)
Solar Radiation
Solar Constant
\[ G_{sc} = 1367 \text{ W/m}^2 \]
- Solar constant is the solar radiation incident on a surface normal to the sun's rays at the outer edge of Earth's atmosphere
- Average distance between Earth and Sun
Solar Radiation Components
Total solar radiation on a surface: \[ G_{total} = G_{beam} + G_{diffuse} + G_{reflected} \]
Where:- \(G_{beam}\) = direct (beam) radiation from the sun
- \(G_{diffuse}\) = diffuse radiation from the sky
- \(G_{reflected}\) = radiation reflected from surrounding surfaces
Solar Radiation on a Surface
\[ G = G_{beam} \cos\theta + G_{diffuse} \]
Where:- \(G\) = total solar irradiation on the surface (W/m2)
- \(\theta\) = angle of incidence (angle between sun's rays and normal to surface)
Solar Absorptivity and Emissivity
- Solar absorptivity \(\alpha_s\): fraction of incident solar radiation absorbed
- Infrared emissivity \(\varepsilon\): emissivity for thermal radiation at surface temperature
- For many surfaces: \(\alpha_s \neq \varepsilon\) (non-gray behavior)
- Selective surfaces: High \(\alpha_s\), low \(\varepsilon\) (e.g., solar collectors)
Heat Balance on a Solar-Irradiated Surface
\[ \alpha_s G A = \varepsilon A \sigma (T_s^4 - T_{surr}^4) + hA(T_s - T_\infty) \]
Where:- \(\alpha_s\) = solar absorptivity
- \(G\) = solar irradiation (W/m2)
- \(\varepsilon\) = infrared emissivity
- \(T_s\) = surface temperature (K)
- \(T_{surr}\) = surrounding temperature for radiation (K)
- \(h\) = convection heat transfer coefficient (W/m2·K)
- \(T_\infty\) = ambient air temperature (K)
Radiation Error in Temperature Measurement
Thermocouple Radiation Error
Energy balance on a thermocouple in a gas flow: \[ h(T_g - T_{tc}) = \varepsilon \sigma (T_{tc}^4 - T_{surr}^4) \]
Where:- \(T_g\) = true gas temperature (K)
- \(T_{tc}\) = measured thermocouple temperature (K)
- \(T_{surr}\) = temperature of surrounding surfaces (K)
- \(h\) = convection heat transfer coefficient between gas and thermocouple (W/m2·K)
- \(\varepsilon\) = emissivity of thermocouple
Radiation error: \[ T_g - T_{tc} = \frac{\varepsilon \sigma (T_{tc}^4 - T_{surr}^4)}{h} \]
To minimize error:- Increase gas velocity (increases \(h\))
- Use radiation shield around thermocouple
- Use low-emissivity thermocouple
Effective Sky Temperature
Sky Radiation Model
For surfaces exposed to clear sky: \[ q_{rad,sky} = \varepsilon A \sigma (T_s^4 - T_{sky}^4) \]
Where:- \(T_{sky}\) = effective sky temperature (K)
- Sky is modeled as a blackbody at temperature \(T_{sky}\)
Empirical correlation for clear sky: \[ T_{sky} \approx 0.0552 \, T_{air}^{1.5} \]
Where:- \(T_{air}\) = ambient air temperature (K)
- \(T_{sky}\) is typically 10-30 K below \(T_{air}\) for clear skies
Alternative approximation: \[ T_{sky} = T_{air} - 6 \text{ K (clear sky)} \]
Important Constants and Properties
Physical Constants
- Stefan-Boltzmann constant: \(\sigma = 5.670 \times 10^{-8}\) W/(m2·K4)
- Planck's constant: \(h = 6.626 \times 10^{-34}\) J·s
- Boltzmann constant: \(k = 1.381 \times 10^{-23}\) J/K
- Speed of light: \(c = 2.998 \times 10^8\) m/s
- Wien's displacement constant: \(C_3 = 2898\) μm·K
- First radiation constant: \(C_1 = 3.742 \times 10^8\) W·μm4/m2
- Second radiation constant: \(C_2 = 1.439 \times 10^4\) μm·K
- Solar constant: \(G_{sc} = 1367\) W/m2
Typical Emissivity Values
- Polished metals: 0.02-0.10
- Oxidized metals: 0.4-0.8
- Black paint: 0.95-0.98
- White paint: 0.85-0.95
- Concrete, brick: 0.85-0.95
- Wood: 0.80-0.90
- Glass: 0.90-0.95
- Water: 0.95-0.96
- Human skin: 0.95
Note: Actual values depend on surface condition, temperature, and wavelength. Consult tables for specific applications.