Heat Exchanger Design Handbook - Online

Description TOC Index Editorial Board

Links to:
HEDH 2002
HEDU

Subscriptions Policy

Purchase Options

Enter

Index:

H

Hagen-Poiseuille law, 2.1.1-2, 2.2.2-1, 2.2.2-3
Hagen-Rubens relation, between electrical and optical constants, 2.9.2-10
Halogenated hydrocarbons:

liquid physical properties, 5.5.10-108/5.5.10-138

saturation properties, 5.5.1-108/5.5.1-138

superheated vapor properties, 5.5.11-107/5.5.11-137

transport properties at elevated pressures, 5.5.14-29/5.5.14-40

Hampson coils (see Helical coils)
Handley and Heggs equation for fixed bed pressure drop, 2.2.5-3
Hankinson and Thomson method, for liquid density:

for liquid mixtures, 5.2.1-3/5.2.1-4

for pure liquids, 5.1.2-9/5.1.2-21

Hardening (precipative) of stainless steels, 4.5.6-6
Hardwick, R., 4.5.5-1/4.5.5-6
Harris, D., 4.3.6-1/4.3.6-30
Hausen equation for developing laminar flow, 2.5.1-2
Hausen method for regenerators, 3.15.5-1/3.15.5-2
Hays, G. F., 3.17.1-1/3.17.1-2, 3.17.4-1/3.17.4-3, 3.17.6-11/3.17.6-27, 3.17.7-1/3.17.7-2, 3.17.7-18, 3.17.8-5/3.17.8-6
Headers in shell-and-tube heat exchangers, 2.2.7-1/2.2.7-2

inlet distribution header, 2.2.7-5/2.2.7-6

outlet combining headers, 2.2.7-6/2.2.7-7

tube entry/exit pressure loss, 2.2.7-7/2.2.7-8

Heads, in heat exchangers:

constructional features of affecting mechanical design, 4.2.6-1/4.2.6-2

mechanical design of, 4.1.8-1

types of, in shell-and-tube exchangers, 4.2.4-1/4.2.4-2

bolted channel, 4.2.4-1

bolted cone, 4.2.4-2

bonnett-type, 4.2.4-1/4.2.4-2

high-pressure, 4.2.4-2/4.2.4-3

welded channel, 4.2.4-1

Heat and mass transfer:

combined, 2.1.6-1/2.1.6-4

in condensation, 2.1.6-2/2.1.6-4

in cooling towers, 3.12.2-1/3.12.2-3

in drying, 2.1.6-1/2.1.6-2

in heat exchangers, 1.1.2-1, 1.2.2-3/1.2.2-4

in single-phase free convection, 2.5.7-12/2.5.7-13

relations between, 1.2.3-6/1.2.3-7

state of the art, 2.1.7-1/2.1.7-8

Heat capacity (see Specific heat capacity)
Heat conduction (see Conduction, heat)
Heat exchanger design, introduction, 3.1.1-1/3.1.4-9

approximate sizing of shell-and-tube heat exchangers, 3.1.4-1/3.1.4-9

basic design equation, 3.1.4-1

estimation of heat load, 3.1.4-1/3.1.4-2

estimation of mean temperature difference, 3.1.4-2/3.1.4-3

estimation of overall heat transfer coefficient, 3.1.4-3/3.1.4-6

estimation of surface area, 3.1.4-6/3.1.4-7

example, 3.1.4-7/3.1.4-9

for liquid metals, 2.5.13-7/2.5.13-9

fundamental concepts, 3.1.1-1/3.1.1-4

basic design equation, 3.1.1-3

heat transfer coefficients, 3.1.1-1/3.1.1-3

mean temperature difference, 3.1.1-3/3.1.1-4

logic of the design process, 3.1.3-1/3.1.3-4

criteria for successful design, 3.1.3-1/3.1.3-2

relationship among selection rating and design, 3.1.3-2/3.1.3-3

simplified example of design modification algorithm for computer, 3.1.3-3/3.1.3-4

types of heat exchangers and their applications, 3.1.2-1/3.1.2-9

air-cooled, 3.1.2-6/3.1.2-7

direct contact, 3.1.2-9

double-pipe, 3.1.2-1/3.1.2-2

mechanically aided, 3.1.2-7/3.1.2-9

multiple hairpin, 3.1.2-2

plate fin or matrix, 3.1.2-6

plate, 3.1.2-4/3.1.2-6

printed circuit, 3.1.2-7/3.1.2-8

shell-and-tube, 3.1.2-2/3.1.2-3

Heat exchangers:

agitated vessels, 3.14.1-1/3.14.3-8

air-cooled, thermal design, 3.8.1-1/3.8.9-4

checks at design stage, 3.18.2-1/3.18.2-5

condensers, 3.4.1-1/3.4.9-5

corrosion and other damage, 4.5.3-1/4.5.3-7

costing, 4.8.1-1/4.8.4-2

air-cooled, 4.8.3-1/4.8.3-3

plate, 4.8.4-1/4.8.4-2

shell-and-tube, 4.8.2-1/4.8.2-5

definitions and quantitative relationships, 1.2.0-1/1.2.6-7

balance equations for equipment, 1.2.4-1/1.2.4-7

differential equations for streams in, 1.2.5-1/1.2.5-3

flux relationships, 1.2.2-1/1.2.2-4

partial differential equations for interpenetrating continua in, 1.2.6-1/1.2.6-7

thermodynamic concepts, 1.2.1-1/1.2.1-3

transfer coefficient dependences, 1.2.3-1/1.2.3-7

description of, 1.1.0-1/1.1.6-1

equipment forms, 1.1.5-1/1.1.5-3

interactions between streams in, 1.1.2-1/1.1.2-2

interfaces between streams in, 1.1.4-1/1.1.4-2

temperature change patterns, 1.1.3-1/1.1.3-2

types of flow configuration, 1.1.1-1/1.1.1-4

unsteady operation, 1.1.6-1

design, 3.1.1-1/3.1.4-9

checks at design stage, 3.18.2-1/3.18.2-5

of, with titanium and titanium alloys, 4.5.9-8/4.5.9-13

direct contact, 3.19.1-1/3.19.5-2

baffle tray columns, 3.19.5-2

drop behavior in, 3.19.1-4/3.19.1-5

sieve tray columns, 3.19.1-3, 3.19.4-1/3.19.4-3

spray columns, 3.19.1-2, 3.19.3-1/3.19.3-4

types of, 3.19.1-1/3.19.1-5

with drops and bubbles, 3.19.2-1/3.19.2-4

double pipe, 3.2.1-1/3.2.3-3

approximate overall heat transfer coefficients, 2.1.3-3

fin efficiency in, 3.2.2-6

heat transfer coefficients in, 3.2.2-1/3.2.2-3, 3.2.3-1

mean temperature difference in, 3.2.3-1/3.2.3-3

mechanical design, 4.4.4-1/4.4.4-2

pressure drop in, 3.2.2-4

effectiveness of:

definition, 1.2.4-3, 2.1.2-2

cell method for, 1.6.1-1/1.6.12-1

entropy generation in, 1.8.1-1/1.8.4-7

F-correction method for, 1.2.4-4, 1.3.1-2/1.3.1-4

F-factor charts for, 1.5.2-3/1.5.3-16

finite element methods in mechanical design of, 4.1.9-1/4.1.9-8

fouling of, 3.17.1-1/3.17.8-23

design for, 3.17.6-1/3.17.6-33

gas-liquid pressure drop in, 2.3.2-12/2.3.2-13

heat pipe, 3.10.8-1/3.10.8-11

capillary type, 3.10.8-1/3.10.8-2

inert gas formation in, 3.10.8-7

thermal design, 3.10.8-3/3.10.8-6

thermosyphon type, 3.10.8/3.10.8-2

working fluids, 3.10.8-3

liquid metal heat transfer in, 2.5.13-8/2.5.13-4

materials of construction, 4.5.2-1/4.5.2-6

thermal and mechanical properties of, 5.5.12-1/5.5.12-13

mechanical design: air-cooled, 4.4.1-1/4.4.1-7

basic principles, 4.1.1-1/4.1.8-3

block-type, 4.4.4-4

direct contact, 4.4.4-6/4.4.4-8

double-pipe, 3.2.5-1/3.2.5-2, 4.4.4-1/4.4.4-2

example of design, 4.3.6-1/4.3.6-23

heat pipes, 4.4.4-9/4.4.4-11

helical (Hampson) coils, 4.4.4-8/4.4.4-9

jacketed heaters, 4.4.4-3/4.4.4-4

plate fin heat exchangers, 4.4.3-1/4.4.3-9

plate heat exchangers, 4.4.2-1/4.4.2-5

scraped surface, 4.4.4-5/4.4.4-6

shell-and-tube (codes), 4.3.1-1/4.3.5-1

shell-and-tube (construction), 4.2.1-1/4.2.6-13

spiral plate, 4.4.4-5

tubular and panel immersion, 4.4.4-2/4.4.4-3

networks of, pinch analysis method for, 1.7.14/1.7.6-1

numerical solution methods for: with calculation of flow pattern, 1.4.2-1/1.4.2-4

with prescribed flow patterns, 1.4.1-1/1.4.1-6

plate fin, 3.9.1-1/3.9.13-4

plate, thermal design of, 3.7.1-1/3.7.4-7

porous medium model for, 2.11.4-1/2.11.4-3

P-NTU method for, 1.2.4-4/1.2.4-5, 1.3.1-2

practical aspects of operation, 3.18.1-1/3.18.6-3

air cooled heat exchangers, 3.18.3-1/3.18.3-8

checks at design stage, 3.18.2-1/3.18.2-5

condensers, 3.18.4-1/3.18.4-3

cooling towers, 3.18.6-1/3.18.6-3

vaporizers, 3.18.5-1/3.18.5-4

pressure drop in headers, nozzles, and turnarounds, 2.2.7-1

representation as interpenetrating continua, 1.2.6-1/1.2.6-7

safety of, 4.17.1-1/4.17.1-4, 4.17.2-1/4.17.2-15

selection for safe operation, 4.17.1-2/4.17.1-3

shell-and-tube (single phase), thermal design of, 3.3.1-1/3.3.11-5, 3.3.13-1/3.3.13-10

film coefficients, approximate, in, 4.8.3-3

overall coefficients in, 4.8.3-3

safety of, 4.17.1-2/4.17.1-3, 4.17.2-1/4.17.2-15

tubeside rupture and subsequent relief, 4.17.2-1/4.17.2-15

?-method for, 1.2.4-5, 1.3.1-2/1.3.1-4

?-method chart for, 1.5.2-1/1.5.3-16

Heat flux, conversion of units for, xxx
Heat generation number (Gn), 2.3.12-6
Heat losses, in regenerators, 3.15.2-1/3.15.2-3
Heat of vaporisation (see Enthalpy of vaporisation), of pure substances, 5.5.1-1/5.5.1-178, 5.5.10-1/5.5.10-175
Heat pipes:

axial heat transfer and operational envelope for, 3.10.4-1

characteristics of wicks for, 3.10.6-1/3.10.6-2

circulation and axial heat transfer in, 3.10.2-1/3.10.2-3

introduction to, 3.10.1-1/3.10.1-2, 2.13.8-1/2.13.8-2

mechanical design of exchangers using, 4.4.4-9/4.4.4-11

micro heat pipes, 2.13.8-1/2.13.8-26

applications of, 2.13.8-22/2.13.8-24

experimental studies of, 2.13.8-4/2.13.8-14

mathematical modelling, 2.13.8-14/2.13.8-22

pulsating type, 2.13.8-2/2.13.8-4

selection of working fluid for, 3.10.5-1/3.10.5-2

start-up and control of, 3.10.7-1/3.10.7-2

temperature distribution and radial heat flux in, 3.10.3-1/3.10.3-2

Heat pipe heat exchangers, 3.10.8-1/3.10.8-11

capillary type, 3.10.8-1/3.10.8-2

inert gas formation in, 3.10.8-7

thermal design, 3.10.8-3/3.10.8-6

thermosyphon type, 3.10.8-1/3.10.8-2

working fluids, 3.10.8-3

Heat pumping, relation to heat exchanger network design, 1.7.5-5
Heat storage (see Regenerators and thermal energy storage) entropy generation in, 1.8.3-4/1.8.3-8
Heat storage heat exchangers, 3.15.0-3
Heat transfer:

analogy with mass transfer, 2.1.5-1/2.1.5-4

augmentation of (see Augmentation of heat transfer)

in cooling towers, 3.12.2-1/3.12.2-2

enhancement of (see Augmentation of heat transfer)

in fluidized beds, fluid-to-particle, 2.5.5-2/2.5.5-6

in microchannels, 2.13.1-1/2.13.8-26

boiling/evaporation, 2.13.4-1/2.13.4-27

condensation, 2.13.6-1/2.13.6-30

single-phase, 2.13.2-1/2.13.2-20

in nonuniform systems, 2.1.4-1/2.1.4-4

in packed beds, 2.1.4-3/2.1.4-4

in shell-and-tube heat exchangers, 2.1.4-1/2.1.4-3

in regenerators, 3.15.3-1/3.15.3-2

in porous media, 2.11.1-1/2.11.7-4

fundamentals of, 2.11.1-1/2.11.1-7

heat conduction, 2.11.2-1/2.11.1-2

forced convective, 2.11.2-1/2.11.2-6

heat exchangers, treatment as porous media, 2.11.4-1/2.11.4-3

natural convection, external flow, 2.11.5-1/2.11.5-8

natural convection, internal flow, 2.11.6-1/2.11.6-9

combined effects in, 2.11.1-1/2.11.1-4

lost work in, 1.9.5-1/1.9.5-5

single-phase convective (see Convective heat transfer, single phase)

in transition flow over flat plate, 2.2.1-25

in tubes: Colburn j factor (laminar and turbulent), 2.1.3-7

correlations for, 2.5.1-1/2.5.1-21

Nusselt numbers for (laminar and turbulent), 2.1.3-6

by radiation (see Radiative heat transfer)

Heat transfer coefficient:

average and overall values for, discussion, 1.2.4-2/1.2.4-3

conversion of units for, xxxi, xlv-lvi

in agitated vessels, 3.14.3-1/3.14.3-8

in air-cooled heat exchangers, 3.8.5-1/3.8.5-6

in bed-to-wall heat transfer in fluidized beds, 2.8.4-1/2.8.4-7

in boiling in a vertical tube, 2.7.3-1/2.7.3-50

variation with quality of, 2.7.3-3/2.7.3-6

in boiling in horizontal tubes, bends, and coils, 2.7.4-1/2.7.4-12

in boiling in microchannels, 2.13.4-1/2.13.4-27

flow boiling, 2.13.4-6/2.13.4-13

models for, 2.13.4-13/2.13.4-14

in boiling of binary and multicomponent mixtures: forced convective, 2.7.8-1/2.7.8-10

pool boiling, 2.7.7-1/2.7.7-7

in boiling on outside of single tubes and tube banks 2.7.5-1/2.7.5-7

in combined free and forced convection: in channels, 2.5.10-1/2.5.10-10

over immersed bodies, 2.5.9-1/2.5.9-6

in condensation, 2.6.1-2

in double-pipe exchangers, 3.2.2-1/3.2.2-3, 3.2.3-1

in evaporators, 3.5.7-1/3.5.7-6

in fixed beds: between wall and bed, stagnant (no flow)

conditions, 2.8.1-5/2.8.1-13

particle-to-fluid, 2.5.4-1

in flow over tube banks, 2.5.3-1/2.5.3-30

in fluidized beds, particle-to-fluid heat transfer, 2.5.5-1/2.5.5-6

in free convection: in layers and enclosures, 2.5.8-1/2.5.8-25

over immersed bodies, 2.5.7-1/2.5.7-31

in ideal tube banks, 3.3.12-2/3.3.12-4

in longitudinal flow in tube banks, 3.3.12-2/3.3.12/17

in microchannels, 2.13.6-1/2.13.6-30

in tube banks with grid baffles, 3.3.12-4/3.3.12-17

individual, definition, 1.2.2-1/1.2.2-2, 2.1.2-6

typical values, 2.1.2-6

internal, use in transient conduction calculations, 2.4.3-7/2.4.3-8

in moving, agitated, and vibrated beds of particles, 2.8.3-3/2.8.3-7

in non-Newtonian flows, 2.5.12-1/2.5.12-16

in plate fin exchangers, 3.9.4-1/3.9.6-2

in plate heat exchangers, 3.7.3-1/3.7.3-4

in pool boiling, 2.7.2-1/2.7.2-24

in reboilers, 3.6.2-1/3.6.2-12

in shell-and-tube exchangers, approximate values for, 4.8.1-3

in single-phase flow in ducts, 2.5.1-1/2.5.1-21

definition of heat transfer coefficient, 2.5.1-1/2.5.1-2

dimensionless numbers for, 2.5.1-2

in smooth straight tubes, laminar flow, 2.5.1-2/2.5.1-6

in smooth straight tubes, turbulent flow, 2.5.1-6/2.5.1-8

in parallel plates, laminar flow, 2.5.1-9/2.5.1-13

in parallel plates, turbulent flow, 2.5.1-13

in concentric annular ducts, laminar flow, 2.5.1-13/2.5.1-14

in concentric annular ducts, turbulent flow, 2.5.1-14/2.5.1-18

in single-phase flow in microchannels, 2.13.3-1/2.13.3-17

in circular microchannels (micropipes), 2.13.3-2/2.13.3-8

in non-circular microchannels, 2.13.2-8

interfacial effects in, 2.13.3-12/2.13.3-14

laminar, 2.13.8-8/2.13.8-11

theoretical analyses for, 2.13.3-12/2.13.3-13

turbulent, 2.13.8-11/2.13.8-12

local, definition, 2.5.1-1

mean, along duct, 2.5.1-1

numerical calculation of, 1.4.3-3/1.4.3-4

on the shell side in shell-and-tube heat exchangers, 3.3.1-1/3.3.11-5, 3.3.13-1/3.3.13-10

overall definition, 1.2.2-1/1.2.2-2, 2.1.2-1, 3.1.1-1

in various heat exchangers, 2.1.2-3/2.1.2-4

volumetric, 1.1.2-2

with liquid metals, 2.5.13-1/2.5.13-10

Heat transfer media, 5.5.15-1/5.5.15-68

aqueous solutions of inorganic compounds, 5.5.15-14/5.5.15-17

aqueous solutions of organic compounds, 5.5.15-18/5.5.15-23

heat transfer salt, 5.5.15-67/5.5.15-68

mineral oils, 5.5.15-28/5.5.15-39

polyglycols, 5.5.15-24/5.5.15-27

refrigerants, 5.5.15-12/5.5.15-13

silicone oils and fluorinated organic compounds, 5.5.15-62/5.5.15-67

synthetic media, 5.5.15-44/5.5.15-61

CALFLO, 5.5.15-54/5.5.15-55

Decal, 5.5.15-45

Dowtherm, 5.5.15-45/5.5.15-48

Dyphyl, 5.5.15-44/5.5.15-45

Fincotherm, 5.5.15-48

Ilexan, 5.5.15-50

Marlotherm, 5.5.15-48/5.5.15-50

Mediatherm, 5.5.15-51

mixtures of, 5.5.15-56/5.5.15-61

OEST, 5.5.15-54

Olex, 5.5.15-45

Renotherm, 5.5.15-48

Santotherm, 5.5.15-51/5.5.15-54

Thermocal, 5.5.15-50/5.5.15-51

Thermofluid S, 5.5.15-44

Ucotherm, 5.5.15-48

Heat transfer salt, 5.5.15-67/5.5.15-68
Heat transfer regimes:

in boiling in a vertical tube, 2.7.3-2

in free and forced single-phase convection, 2.5.10-2

Heat of vaporization, 5.1.3-4/5.1.3-7

of commonly used fluids, 5.5.1-1/5.5.1-178

Heated cavity reflectometer, 2.9.2-7
Heating media, for reboilers, 3.6.2-10
Heavy water, physical properties of, 5.5.9-1/5.5.9-4
Heggs, P. J., 2.2.5-1/2.2.5-7
Helical coils:

in agitated vessels, 3.14.2-2/3.14.2-3

heat transfer to, 3.14.3-1/3.14.3-2

augmentation of condensation heat transfer using, 2.6.6-23

augmentation of boiling heat transfer using, 2.7.9-4

convective boiling in, 2.7.4-9/2.7.4-10

cooler, approximate overall heat transfer coefficients in, 2.1.2-4

dryout in evaporative heat transfer in, 2.7.4-9/2.7.4-10

Hampson-type for heat exchangers, 4.4.4-8/4.4.4-9

heat transfer to liquid metals flowing over, 2.5.13-5/2.5.13-7

single-phase flow and pressure drop in, 2.2.2-15/2.2.2-18, 2.5.11-6/2.5.11-7

single-phase heat transfer in, 2.5.14-1/2.5.14-4

critical Reynolds number, 2.5.14-2

laminar flow, 2.5.14-2

transition region, 2.5.14-3

turbulent flow, 2.5.14-2/2.5.14-3

Helical inserts, for enhancement of heat transfer in boiling, 2.7.9-3
Helical ribbon agitator:

description, 3.14.2-1/3.14.2-2

heat transfer with, 3.14.3-3/3.14.3-4

Helium:

saturation properties, 5.5.1-166

superheated gaseous: physical properties, 5.5.11-166

thermodynamic properties, 5.5.2-26

transport properties at elevated pressure, 5.5.14-46

Helmholtz reciprocity principle, in radiative heat transfer, 2.9.2-6
Hemimelitene, see 1,2,3 Trimethylbenze
Henry (SI unit), xxviii
Henry, J. A. R., 2.2.7-1/2.2.7-11
Henry-Fauske model, for critical two-phase flow, 2.3.2-28/2.3.2-29
Henry's law, for partial pressure, 2.7.6-1
Heptadecane:

liquid properties, 5.5.10-13

saturation properties, 5.5.1-17

superheated vapor properties, 5.5.11-13

Heptadecene:

liquid properties, 5.5.10-27

saturation properties, 5.5.1-31

superheated vapor properties, 5.5.11-27

Heptane:

liquid properties, 5.5.10-8

saturated properties, 5.5.1-12

superheated vapor properties, 5.5.11-8

transport properties of gases at elevated pressure, 5.5.2-9

1-Heptanol:

liquid physical properties, 5.5.10-64

saturation properties, 5.5.1-67

superheated vapor properties, 5.5.11-64

1-Heptene:

liquid properties, 5.5.10-22

saturation properties, 5.5.1-26

superheated vapor properties, 5.5.11-22

transport properties of gases at elevated pressure, 5.5.14-18

Herman, K. W., 3.17.6-20/3.17.6-22
Hertz (SI unit), xxvii
Heterogeneous conveyance in horizontal pipes, 2.3.4-3/2.3.4-6
Heterogeneous nucleation in boiling, 2.7.1-3/2.7.1-5
Hewitt, G. F., 2.3.1-1/2.3.2-33, 2.7.3-1/2.7.3-50, 2.7.4-1/2.7.8-14, 3.3.13-1/3.3.13-10, 4.8.1-1/4.8.1-10
Hexachloroethane (Refrigerant 116):

liquid properties, 5.5.10-123

superheated vapor properties, 5.5.11-119

Hexacyclopentane, superheated vapor properties, 5.5.11-22
Hexadecane:

liquid physical properties, 5.5.10-12

saturation properties, 5.5.1-16

superheated vapor properties, 5.5.11-12

Hexadecene:

liquid properties, 5.5.10-26

saturation properties, 5.5.1-30

superheated vapor properties, 5.5.11-26

1,5-Hexadiene:

liquid properties, 5.5.10-36

saturation properties, 5.5.1-39

superheated vapor properties, 5.5.11-36

Hexafluoroethane (see Refrigerant 116)
Hexagonal cells, in free convection, 2.5.8-2
Hexamethylbenzene:

liquid properties, 5.5.10-56

saturation properties, 5.5.1-59

superheated vapor properties, 5.5.11-56

Hexane:

liquid properties, 5.5.10-7

saturated properties, 5.5.1-11

superheated vapor properties, 5.5.11-7

transport properties of gases at elevated pressure, 5.5.14-8

Hexanoic acid:

liquid properties, 5.5.10-97

saturation properties, 5.5.1-97

superheated vapor properties, 5.5.11-97

1-Hexanol:

liquid physical properties, 5.5.10-63

saturation properties, 5.5.1-66

superheated vapor properties, 5.5.11-63

1-Hexene:

liquid properties, 5.5.10-21

saturated properties, 5.5.1-25

superheated vapor properties, 5.5.11-21

transport properties of gases at elevated pressure, 5.5.14-17

Hexylbenzene:

liquid properties, 5.5.10-51

saturation properties, 5.5.1-54

superheated vapor properties, 5.5.11-51

Hexylcyclohexane:

liquid properties, 5.5.10-24

Hexylcyclopentane, 5.5.10-22
Hicks equation, for fixed-bed pressure drop, 2.2.5-3
High-chrome steels, thermal and mechanical properties, 5.5.12-7/5.5.12-8
High-finned tubes, correlations for single-phase heat transfer in flow over, 2.5.3-11/2.5.3-12
Hills, P. D., 3.5.1-1/3.5.8-4, 3.18.6-1/3.18.6-8
Hinchley, P., 3.16.1-1/3.16.4-2
Hohlraum cavity, 2.9.1-3
Holdup, in liquid-liquid flow, 2.3.5-1/2.3.5-40
Holland, guide to national practice for mechanical design of heat exchangers, 4.3.5-5
Homogeneous condensation (fog formation), 2.6.1-1

effects, 2.6.7-3

nuclei formation, 2.6.7-1/2.6.7-2

supersaturation, 2.6.7-1/2.6.7-3

Homogeneous model:

conservation equations for, in multiphase flows, 2.3.1-4/2.3.1-7

in gas-liquid flows: conservation equations, 2.3.2-8

critical flow estimation by, 2.3.2-28

frictional pressure drop correlations based on, 2.3.2-10

pressure drop in singularities calculated by, 2.3.2-15/2.3.2-18

in liquid-liquid flow, 2.3.5-15/2.3.5-16

in liquid-liquid gas flow, 2.3.6-8/2.3.6-9

in solid-liquid flow, 2.3.4-2/2.3.4-3

Homogeneous nucleation:

of droplets in supersaturated vapor, 2.6.7-1/2.6.7-2

of vapor bubbles in liquids, 2.7.1-3/2.7.1-4

table of values of temperature for various substances, 2.7.1-4

Honeycombs:

free convective heat transfer in, 2.5.8-20/2.5.8-23

loss coefficients in, 2.2.2-21

Hopkins, D., 4.5.8-1/4.5.8-19
Horizontal condensers:

baffles in, 3.4.3-4

bundle layout in, 3.4.3-6

crossflow (X-shell) type, 3.4.3-5/3.4.3-6

impingement devices in, 3.4.3-5

in-tube, 3.4.3-3

outside turbulent, 3.4.3-3/3.4.3-6

subcooling in, 3.4.3-5

turbine exhaust, 3.4.3-3/3.4.3-8

Horizontal cylinders:

free convective heat transfer inside, 2.5.8-14

(See also Cylinders; Horizontal tubes)

Horizontal layers, of fluid, free convection heat transfer in, 2.5.8-1/2.5.8-3
Horizontal pipes:

hydraulic conveyance in, 2.3.4-1/2.3.4-6

pneumatic conveyance in, 2.3.3-1/2.3.3-2

(See alsoPipes, circular; Horizontal tubes)
Horizontal plates (see Horizontal surfaces; Flat plates)
Horizontal shell-side evaporator, 3.5.2-1
Horizontal surfaces:

combined free and forced convection in transverse flow over, 2.5.9-4/2.5.9-6

free convective heat transfer from, 2.5.7-13/2.5.7-18

downward-facing surfaces, 2.5.7-13/2.5.7-15

upward-facing surfaces, 2.5.7-15/2.5.7-18

pool boiling from, 2.7.2-1/2.7.2-24

Horizontal thermosiphon reboilers:

calculation procedures for, 3.6.5-2/3.6.5-3

characteristics, advantages, and disadvantages of, 3.6.1-4/3.6.1-5

thermal design, 2.7.5-8/2.7.5-9, 3.6.2-1/3.6.2-7

convection effects, 3.6.2-3/3.6.2-4

critical heat flux and film boiling, 3.6.2-5/3.6.2-7

effective mean temperature difference, 3.6.2-5

finned tubes in, 3.6.2-8

flow distribution and hydraulics of, 3.6.2-8

mixture effects, 3.6.2-4/3.6.2-5

single tube nucleate boiling, 3.6.2-1/3.6.2-3

vapor liquid disengagement in, 3.6.2-7/3.6.2-8

Horizontal tube-side evaporator, 3.5.2-7/3.5.2-8
Horizontal tubes:

boiling outside with crossflow, 2.7.5-1/2.7.5-4

combined free and forced convection in, 2.5.10-7/2.5.10-11

with uniform heat flux, 2.5.10-7/2.5.10-11

with uniform wall temperature, 2.5.10-7

combined free and forced convective heat transfer from outside, 2.5.9-1/2.5.9-6

condensation on inside, 2.6.2-12/2.6.2-15, 3.4.6-1/3.4.6-2

annular flow, 2.6.2-15

flow regimes, 2.6.2-12/2.6.2-14, 3.4.6-2

stratifying flow, 2.6.2-13/2.6.2-14, 3.4.6-2

condensation on outside of, 2.6.2-8/2.6.2-12, 3.4.6-3

in bundles, 2.6.2-9/2.6.2-11

effect of vapor shear, single tube, 2.6.2-8/2.6.2-9

laminar flow, single tube, 2.6.2-9

convective boiling in, 2.7.4-1/2.7.4-8

critical heat flux in, 2.7.4-7/2.7.4-8

flow patterns in, 2.7.4-1/2.7.4-4

heat transfer coefficients in, 2.7.4-4/2.7.4-5

flow regimes in gas-liquid flow in, 2.3.2-2/2.3.2-4

flow regimes in liquid-liquid flow in:

description, 2.3.5-1/2.3.3-7

transition of, 2.3.5-20/2.3.5-29

free convective heat transfer from outside of, 2.5.7-20/2.5.7-23

heat transfer to, in fluidized beds, 2.8.4-6/2.8.4-7

hydrodynamics of various two-phase flow regimes in, 2.3.2-23/2.3.2-26

annular flow, 2.3.2-25/2.3.2-26

slug flow, 2.3.2-24/2.3.2-25

stratified flow, 2.3.2-23/2.3.2-24

pool boiling from, 2.7.2-1/2.7.2-24

types of waste heat boilers, 3.16.2-3

(See also Horizontal pipes; Pipes, circular)

Hot insulation, of heat exchangers, 4.15.2-2/4.15.2-5
Hottel's rule, in absorption of radiation by gases, 2.9.5-7
Hsu criterion, for onset of nucleate boiling, 2.7.2-2
Hybrid cooling towers, 3.12.1-3
Hydraulic conveyance:

homogeneous and pseudohomogeneous, 2.3.4-2/2.3.4-3

in horizontal tubes: flow regimes in, 2.3.4-1/2.3.4-2

heterogeneous conveyance in, 2.3.4-3/2.3.4-6

Hydraulic expansion, of tubes into tube sheets in shell-and-tube heat exchangers, 4.11.2-1/4.11.2-6

comparison with roller expansion, 4.11.2-1/4.11.2-3

equipment for, 4.11.2-3/4.11.2-4

limitations of, 4.11.2-5/4.11.2-6

Hydraulic turbine, lost work in, 1.9.5-8
Hydraulically smooth surface, 2.2.2-1
Hydrazine:

liquid properties, 5.5.10-162

saturation properties, 5.5.1-161

superheated vapor properties, 5.5.11-162

Hydrocarbons:

fouling in streams of, 3.17.6-1/3.17.6-6

thermodynamic properties, 5.2.2-1/5.2.2-9

Hydrodynamic entrance length, in single-phase flow in ducts, 2.2.2-10/2.2.2-11
Hydrogen:

adsorption of, in carbon nanotubes, 2.13.7-20

liquid properties, 5.5.10-167

saturation properties, 5.5.1-168

superheated gaseous: physical properties, 5.5.11-169

thermodynamic properties, 5.5.2-31

transport properties at elevated pressure, 5.5.14-51

Hydrogen bromide:

liquid properties, 5.5.10-158

saturation properties, 5.5.1-157

superheated vapor properties, 5.5.11-157

Hydrogen chloride:

liquid properties, 5.5.10-157

saturation properties, 5.5.1-156

superheated vapor properties, 5.5.11-156

Hydrogen cyanide:

liquid properties, 5.5.10-159

saturation properties, 5.5.1-158

superheated vapor properties, 5.5.11-158

Hydrogen fluoride:

liquid properties, 5.5.10-157

saturation properties, 5.5.1-156

superheated vapor properties, 5.5.11-156

Hydrogen iodide:

liquid properties, 5.5.10-158

saturation properties, 5.5.1-157

superheated vapor properties, 5.5.11-157

Hydrogen peroxide:

liquid properties, 5.5.10-160

saturation properties, 5.5.1-159

superheated vapor properties, 5.5.11-159

Hydrogen sulfide:

liquid properties, 5.5.10-159

saturation properties, 5.5.1-158

superheated gaseous: physical properties, 5.5.11-158

thermodynamic properties, 5.5.2-21

Hydrostatic testing of shell-and-tube heat exchangers, 4.2.6-11/4.2.6-13
Hysteresis:

in boiling curve, 2.7.2-8

reduction of, using porous surfaces, 2.7.9-3

Menu

Heat Exchanger Design Handbook - Online

Index:

H