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A B C D E F G H I J K L M N O P Q R S T U V W X Y Z
G-type shells in shell-and-tube heat exchangers:
Gaddis, E S,
Galerkin method, for heat conduction finite-element calculations,
Galileo number,
Gas-liquid flows:
Gas-liquid-solid interfaces, fouling at,
Gas-solid interfaces, fouling at,
Gas tungsten arc welding,
Gaseous fuels, properties of,
Gases:
Gaskets:
Gauss-Seidel method, for solution of implicit equations,
Geometric optics models for radiative heat transfer from surfaces,
geothermal brines, fouling of heat exchangers by,
Germany, Federal Republic of, mechanical design of heat exchangers in:
Gersten, K,
Girth flanges, in shell-and-tube heat exchangers,
Glass production, furnaces and kilns for,
Glycerol (glycerine):
Gn (heat generation number),
Gnielinski, V
Gnielinski correlation, for heat transfer in tube banks,
Gomez-Thodas method, for vapour pressure,
Goodness factor, as a basis for comparison of plate fin heat exchanger surfaces,
Goody narrow band model for gas radiation properties,
Gorenflo correlation, for nucleate boiling,
Gowenlock, R,
Graetz number:
Granular products, moving, heat transfer to,
Graphite, density of,
Grashof number
Gravitational acceleration, effect in pool boiling,
Gravity conveyor:
Gregorig effect in enhancement of condensation,
Grid baffles:
Grid selection, for finite difference method,
Griffin, J M,
Groeneveld correlation for postdryout heat transfer,
Groeneveld and Delorme correlation for postdryout heat transfer,
Gross plastic deformation
Group contribution parameters tables,
Guerrieri and Talty correlations for forced convective heat transfer in two-phase flow,
Gungor and Winterton correlation, for forced convective boiling,
Gylys, J,
Index
HEDH
A
B
C
D
E
F
G
G-type shells in shell-and-tube heat exchangers:
Gaddis, E S,
Galerkin method, for heat conduction finite-element calculations,
Galileo number,
Gas-liquid flows:
Gas-liquid-solid interfaces, fouling at,
Gas-solid interfaces, fouling at,
Gas tungsten arc welding,
Gaseous fuels, properties of,
Gases:
Gaskets:
Gauss-Seidel method, for solution of implicit equations,
Geometric optics models for radiative heat transfer from surfaces,
geothermal brines, fouling of heat exchangers by,
Germany, Federal Republic of, mechanical design of heat exchangers in:
Gersten, K,
Girth flanges, in shell-and-tube heat exchangers,
Glass production, furnaces and kilns for,
Glycerol (glycerine):
Gn (heat generation number),
Gnielinski, V
Gnielinski correlation, for heat transfer in tube banks,
Gomez-Thodas method, for vapour pressure,
Goodness factor, as a basis for comparison of plate fin heat exchanger surfaces,
Goody narrow band model for gas radiation properties,
Gorenflo correlation, for nucleate boiling,
Gowenlock, R,
Graetz number:
Granular products, moving, heat transfer to,
Graphite, density of,
Grashof number
Gravitational acceleration, effect in pool boiling,
Gravity conveyor:
Gregorig effect in enhancement of condensation,
Grid baffles:
Grid selection, for finite difference method,
Griffin, J M,
Groeneveld correlation for postdryout heat transfer,
Groeneveld and Delorme correlation for postdryout heat transfer,
Gross plastic deformation
Group contribution parameters tables,
Guerrieri and Talty correlations for forced convective heat transfer in two-phase flow,
Gungor and Winterton correlation, for forced convective boiling,
Gylys, J,
H
I
J
K
L
M
N
O
P
Q
R
S
T
U
V
W
X
Y
Z
G
G-type shells in shell-and-tube heat exchangers:
temperature difference correction factor (F) and ?-NTU chart for,
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F and θ charts for shell-and-tube exchangers
DOI 10.1615/hedhme.a.000106
1.5 MEAN TEMPERATURE DIFFERENCE
1.5.2 F and θ charts for shell-and-tube exchangers
J. Taborek
In this Section are presented sets of equations and graphs for simple heat exchanger configurations and for a set of shell-and-tube exchangers defined using the nomenclature of the TEMA Handbook. Descriptive material, comments on proper usage and limiting points are also included with each specific configuration. The topics covered are:
A. | Counter Flow | Figure 1 |
B. | Co-current Flow | Figure 2 |
C. | TEMA E shell-and-tube | |
flow arrangements | ||
E-shell, 1-2N | Figure 3 | |
E-shell, 2 in series | Figure 4 | |
E-shell, 3 in series | Figure 5 | |
E-shell, 4 in series | Figure 6 | |
E-shell, 5 in series | Figure 7 | |
E-shell, 6 in series | Figure 8 | |
D. | E-shell, 3 tube passes | Figure 9 |
E. | J-shell, one tube pass | Figure 10 |
2N tube passes | Figure 11 | |
F. | G-shell, 2N tube passes | Figure 12 |
G. | F-shell, partition thermal leakage | Figure 13 |
The reader should refer to Section 105 for a description of the terms involved.
A. Countercurrent flow (Figure 1)
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