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Wadekar, V
Wagner equation, for vapour pressure,
Wake, Coles law of the,
Wall layer transmissivity,
Wall temperature:
Wallis correlations:
Wallis criterion, for transition from stratified to annular flow, applications in condensation,
Walz' method, for laminar boundary layers,
Waste heat boilers,
Waste water, fouling by,
Water:
Watertube boiler,
Wavelengths, of blackbody radiation,
Waves, interfacial, effect on film condensation on vertical surface,
Wavy fins, in plate fin exchangers,
Webb, D R
Webb, R L
Weber, M,
Weber number,
Weil, C J
Welded channel head, in shell-and tube heat exchanger,
Welded fins:
Welded plate exchangers:
Welding:
Welds:
Wentz and Thodos equation, for fixed-bed pressure drop,
Wet-bulb temperature,
Wettability, of surface, effect on pool boiling,
Whalley and Hewitt correlations:
White-Metzner model, for non-Newtonian fluid,
Wicks, for heat pipes:
Wilday, A J
Wildsmith, G,
Wills-Johnson flow stream analysis method for segmentally baffled shell-and-tube heat exchangers,
Wilson, D I
Window zone, in shell-and-tube heat exchangers:
Winter, H H,
Wire matrix inserts, in heat exchangers,
Wirth, K E,
Wispy annular flow, regions of occurrence of,
Work (in exergy analysis)
Working fluid, selection of for heat pipe,
Index
HEDH
A
B
C
D
E
F
G
H
I
J
K
L
M
N
O
P
Q
R
S
T
U
V
W
Wadekar, V
Wagner equation, for vapour pressure,
Wake, Coles law of the,
Wall layer transmissivity,
Wall temperature:
Wallis correlations:
Wallis criterion, for transition from stratified to annular flow, applications in condensation,
Walz' method, for laminar boundary layers,
Waste heat boilers,
Waste water, fouling by,
Water:
Watertube boiler,
Wavelengths, of blackbody radiation,
Waves, interfacial, effect on film condensation on vertical surface,
Wavy fins, in plate fin exchangers,
Webb, D R
Webb, R L
Weber, M,
Weber number,
Weil, C J
Welded channel head, in shell-and tube heat exchanger,
Welded fins:
Welded plate exchangers:
Welding:
Welds:
Wentz and Thodos equation, for fixed-bed pressure drop,
Wet-bulb temperature,
Wettability, of surface, effect on pool boiling,
Whalley and Hewitt correlations:
White-Metzner model, for non-Newtonian fluid,
Wicks, for heat pipes:
Wilday, A J
Wildsmith, G,
Wills-Johnson flow stream analysis method for segmentally baffled shell-and-tube heat exchangers,
Wilson, D I
Window zone, in shell-and-tube heat exchangers:
Winter, H H,
Wire matrix inserts, in heat exchangers,
Wirth, K E,
Wispy annular flow, regions of occurrence of,
Work (in exergy analysis)
Working fluid, selection of for heat pipe,
X
Y
Z
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Nonisothermal Gas Radiation
DOI 10.1615/hedhme.a.000210
2.9 HEAT TRANSFER BY RADIATION
2.9.7 Nonisothermal gas radiation
D. K. Edwards
A. Solution of the equation of transfer
Recall that Equation 208.6 for the change of intensity along slant path increment ds,
\[\label{eq1} \dfrac{dI}{ds}=-k_aI+k_aI_b\qquad(k_s=0) \tag{1}\]
had a solution for the homogeneous isothermal gas given by Equation 209.3,
\[\label{eq2} I=I_0e^{-k_as}+I_b(T_g)(1-e^{-k_as})\qquad(I_b=\mbox{const}) \tag{2}\]
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