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Hagen-Poiseuille law
Hagen-Rubens relation, between electrical and optical constants,
Hall Taylor, N S,
Halogenated hydrocarbons:
Handley and Heggs equation for fixed bed pressure drop,
Hankinson and Thomson method, for liquid density:
Hardening (precipative) of stainless steels,
Hardwick, R,
Harris, D,
Hausen equation for developing laminar flow,
Hays, G F
Headers in shell-and-tube heat exchangers,
Heads, in heat exchangers:
Heat and mass transfer:
Heat exchanger design, introduction,
Heat exchangers:
condensers,
corrosion and other damage,
costing,
definitions and quantitative relationships,
description of,
design,
double pipe,
effectiveness of:
entropy generation in,
F-correction method for
F-factor charts for,
fouling of,
gas-liquid pressure drop in,
heat pipe,
mechanical design: air-cooled,
networks of, pinch analysis method for,
numerical solution methods for: with calculation of flow pattern,
plate fin,
plate, thermal design of,
P-NTU method for
practical aspects of operation,
pressure drop in headers, nozzles, and turnarounds,
representation as interpenetrating continua,
safety of
shell-and-tube (single phase), thermal design of
suction line exchangers in refrigeration,
twisted tube,
with dimpled surfaces,
with tube inserts,
Θ-method for
Θ-method chart for,
Heat of vaporisation (see Enthalpy of vaporisation), of pure substances
Heat pipes:
Heat pumping, relation to heat exchanger network design,
Heat storage (see Regenerators and thermal energy storage) entropy generation in,
Heat transfer:
Heat transfer coefficient:
Heat transfer media,
Heat transfer salt,
Heat transfer regimes:
Heat of vaporization,
Heated cavity reflectometer,
Heating media, for reboilers,
Heavy water, physical properties of,
Heggs, P J,
Helical coils of circular cross section:
Helical coils of rectangular cross section,
Helical inserts, for enhancement of heat transfer in boiling,
Helium:
Helmholtz reciprocity principle, in radiative heat transfer,
Henry, J A R,
Henry-Fauske model, for critical two-phase flow,
Henry's law, for partial pressure,
Heptadecane:
Heptadecene:
Heptane:
1-Heptanol:
1-Heptene:
Herman, K W,
Hermes, C L L,
Heterogeneous conveyance in horizontal pipes,
Heterogeneous nucleation in boiling,
Hewitt, G F
Hexachloroethane (Refrigerant 116):
Hexacyclopentane, superheated vapor properties,
Hexadecane:
Hexadecene:
1,5-Hexadiene:
Hexagonal cells, in free convection,
Hexamethylbenzene:
Hexane:
Hexanoic acid:
1-Hexanol:
1-Hexene:
Hexylbenzene:
Hexylcyclohexane:
Hexylcyclopentane,
Hicks equation, for fixed-bed pressure drop,
High pressure closures, ASME VIII code guidance for,
High-chrome steels, thermal and mechanical properties,
High-finned tubes, correlations for single-phase heat transfer in flow over,
Hills, P D
Hohlraum cavity,
Holdup, in liquid-liquid flow,
Holland, guide to national practice for mechanical design of heat exchangers,
Homogeneous condensation (fog formation),
Homogeneous model:
Homogeneous nucleation:
Honeycombs:
Hopkins, D,
Horizontal condensers:
Horizontal cylinders:
Horizontal layers, of fluid, free convection heat transfer in,
Horizontal pipes:
Horizontal shell-side evaporator,
Horizontal surfaces:
Horizontal thermosiphon reboilers:
Horizontal tube-side evaporator,
Horizontal tubes:
Hottel's rule, in absorption of radiation by gases,
Hsu criterion, for onset of nucleate boiling,
Hybrid cooling towers,
Hydraulic conveyance:
Hydraulic expansion, of tubes into tube sheets in shell-and-tube heat exchangers,
Hydraulic turbine, lost work in,
Hydraulic resistance, in flow of supercritical fluids,
Hydraulically smooth surface,
Hydrazine:
Hydrocarbons:
Hydrodynamic entrance length, in single-phase flow in ducts,
Hydrogen:
Hydrogen bromide:
Hydrogen chloride:
Hydrogen cyanide:
Hydrogen fluoride:
Hydrogen iodide:
Hydrogen peroxide:
Hydrogen sulfide:
Hydrostatic testing of shell-and-tube heat exchangers,
Hysteresis:
Index
HEDH
A
B
C
D
E
F
G
H
Hagen-Poiseuille law
Hagen-Rubens relation, between electrical and optical constants,
Hall Taylor, N S,
Halogenated hydrocarbons:
Handley and Heggs equation for fixed bed pressure drop,
Hankinson and Thomson method, for liquid density:
Hardening (precipative) of stainless steels,
Hardwick, R,
Harris, D,
Hausen equation for developing laminar flow,
Hays, G F
Headers in shell-and-tube heat exchangers,
Heads, in heat exchangers:
Heat and mass transfer:
Heat exchanger design, introduction,
Heat exchangers:
I
J
K
L
M
N
O
P
Q
R
S
T
U
V
W
X
Y
Z
condensers,
corrosion and other damage,
costing,
definitions and quantitative relationships,
description of,
design,
double pipe,
effectiveness of:
entropy generation in,
F-correction method for
F-factor charts for,
fouling of,
gas-liquid pressure drop in,
heat pipe,
mechanical design: air-cooled,
networks of, pinch analysis method for,
numerical solution methods for: with calculation of flow pattern,
plate fin,
plate, thermal design of,
P-NTU method for
practical aspects of operation,
pressure drop in headers, nozzles, and turnarounds,
representation as interpenetrating continua,
safety of
shell-and-tube (single phase), thermal design of
suction line exchangers in refrigeration,
twisted tube,
with dimpled surfaces,
with tube inserts,
Θ-method for
Θ-method chart for,
Heat of vaporisation (see Enthalpy of vaporisation), of pure substances
Heat pipes:
Heat pumping, relation to heat exchanger network design,
Heat storage (see Regenerators and thermal energy storage) entropy generation in,
Heat transfer:
Heat transfer coefficient:
Heat transfer media,
Heat transfer salt,
Heat transfer regimes:
Heat of vaporization,
Heated cavity reflectometer,
Heating media, for reboilers,
Heavy water, physical properties of,
Heggs, P J,
Helical coils of circular cross section:
Helical coils of rectangular cross section,
Helical inserts, for enhancement of heat transfer in boiling,
Helium:
Helmholtz reciprocity principle, in radiative heat transfer,
Henry, J A R,
Henry-Fauske model, for critical two-phase flow,
Henry's law, for partial pressure,
Heptadecane:
Heptadecene:
Heptane:
1-Heptanol:
1-Heptene:
Herman, K W,
Hermes, C L L,
Heterogeneous conveyance in horizontal pipes,
Heterogeneous nucleation in boiling,
Hewitt, G F
Hexachloroethane (Refrigerant 116):
Hexacyclopentane, superheated vapor properties,
Hexadecane:
Hexadecene:
1,5-Hexadiene:
Hexagonal cells, in free convection,
Hexamethylbenzene:
Hexane:
Hexanoic acid:
1-Hexanol:
1-Hexene:
Hexylbenzene:
Hexylcyclohexane:
Hexylcyclopentane,
Hicks equation, for fixed-bed pressure drop,
High pressure closures, ASME VIII code guidance for,
High-chrome steels, thermal and mechanical properties,
High-finned tubes, correlations for single-phase heat transfer in flow over,
Hills, P D
Hohlraum cavity,
Holdup, in liquid-liquid flow,
Holland, guide to national practice for mechanical design of heat exchangers,
Homogeneous condensation (fog formation),
Homogeneous model:
Homogeneous nucleation:
Honeycombs:
Hopkins, D,
Horizontal condensers:
Horizontal cylinders:
Horizontal layers, of fluid, free convection heat transfer in,
Horizontal pipes:
Horizontal shell-side evaporator,
Horizontal surfaces:
Horizontal thermosiphon reboilers:
Horizontal tube-side evaporator,
Horizontal tubes:
Hottel's rule, in absorption of radiation by gases,
Hsu criterion, for onset of nucleate boiling,
Hybrid cooling towers,
Hydraulic conveyance:
Hydraulic expansion, of tubes into tube sheets in shell-and-tube heat exchangers,
Hydraulic turbine, lost work in,
Hydraulic resistance, in flow of supercritical fluids,
Hydraulically smooth surface,
Hydrazine:
Hydrocarbons:
Hydrodynamic entrance length, in single-phase flow in ducts,
Hydrogen:
Hydrogen bromide:
Hydrogen chloride:
Hydrogen cyanide:
Hydrogen fluoride:
Hydrogen iodide:
Hydrogen peroxide:
Hydrogen sulfide:
Hydrostatic testing of shell-and-tube heat exchangers,
Hysteresis:
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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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