Index:

A

• Absorbing media, interaction phenomena in, 2.9.8-7/2.9.8-9
• Absorption of thermal radiation:
• in gases, 2.9.5-1/2.9.5-12
• gas mixtures, 2.9.5-11/2.9.5-12
• measurement, 2.9.5-2/2.9.5-4
• molecular, 2.9.5-8/2.9.5-11
• in solids, 2.9.2-2/2.9.2-3
• characteristics, 2.9.2-1/2.9.2-2
• measurement, 2.9.2-3
• Absorption coefficient, 2.9.5-2
• Absorption spectra in gases, 2.9.5-4/2.9.5-8
• Absorptivity:
• of particles, 2.9.5-1
• of surfaces: definition, 2.9.2-1
• measurement of, 2.9.2-3
• Acentric factor:
• definition, 5.1.1-4
• Poling et al correlation for, 5.1.1-4/5.1.1-5
• Acetaldehyde:
• liquid properties, 5.5.10-85
• saturation properties, 5.5.1-86
• superheated vapor properties, 5.5.11-85
• Acetic acid:
• liquid properties, 5.5.10-94
• saturation properties, 5.5.1-95
• superheated vapor properties, 5.5.11-94
• Acetic anhydride:
• liquid properties, 5.5.10-99
• saturation properties, 5.5.1-100
• superheated vapor properties, 5.5.11-99
• Acetone:
• liquid properties, 5.5.10-90
• saturation properties, 5.5.1-90
• superheated vapor properties, 5.5.11-43
• transport properties of gas at elevated pressure, 5.5.14-90
• Acetonitrile:
• liquid properties, 5.5.10-149
• saturation properties, 5.5.1-149
• superheated vapor properties, 5.5.11-148
• Acetophenone:
• liquid properties, 5.5.10-99
• saturation properties, 5.5.1-93
• superheated vapor properties, 5.5.11-93
• Acetylene:
• liquid properties, 5.5.10-37
• saturation properties, 5.5.1-40
• superheated vapor properties, 5.5.11-37
• transport properties at elevated pressures, 5.5.14-19
• Acetylenes
• liquid properties of, 5.5.10-37/5.5.10-38
• saturation properties, 5.5.1-40/5.5.1-41
• superheated vapour properties, 5.5.11-37/5.5.11-38
• Ackerman correction factor in condensation, 2.6.3-9
• Acoustic insulation, of heat exchangers, 4.15.3-1/4.15.3-2
• Acoustic methods, for fouling mitigation, 3.17.8-3/3.17.8-4
• Acoustic vibration of heat exchangers, 4.6.4-3/4.6.4-4
• Acrolein:
• liquid properties, 5.5.10-87
• saturation properties, 5.5.1-88
• superheated vapor properties, 5.5.11-87
• Acrylic acid:
• liquid properties, 5.5.10-46
• saturation properties, 5.5.1-98
• superheated vapor properties, 5.5.11-97
• Active systems for augmentation of heat transfer:
• definition, 2.5.11-3
• in forced convection, 2.5.11-4/2.5.11-9
• in free convection, 2.5.11-8/2.5.11-9
• Additives:
• effect on friction factor, 2.2.2-8
• use in heat transfer augmentation, 2.5.11-2, 2.7.9-4
• Adiabatic flows, compressible, in duct, 2.2.2-14
• Admiralty brass, 4.5.7-3
• Advanced models for furnaces, 3.11.7-1/3.11.7-5
• Agitated beds, heat transfer to, 2.8.3-1/2.8.3-7
• Agitated vessels, 3.14.1-1
• approximate overall heat transfer coefficients in, 2.1.2-5
• equipment used in, 3.14.2-1/3.14.2-4
• gas sparging, 3.14.2-1/3.14.2-2
• mechanical agitators, 3.14.2-1
• vessel internals, 3.14.2-2/3.14.2-4
• fouling in, 3.17.7-8
• heat exchanger, description of, 3.1.2-5/3.1.2-6
• heat transfer correlations for, 3.14.3-1/3.14.3-8
• with anchors and helical ribbons, 3.14.3-1/3.14.3-4
• with nonproximity agitators, 3.14.3-1/3.14.3-3
• scraped-wall pipe and related equipment, 3.14.3-4/3.14.3-6
• Ahmad scaling method for critical heat flux in flow boiling of nonaqueous fluids, 2.7.3-36
• Air:
• as a coolant, 3.8.1-1
• liquid properties, 5.5.10-160
• properties of dry and saturated, 3.12.2-4/3.12.2-5
• saturated liquid/vapor properties, 5.5.1-159
• superheated gaseous:
• physical properties, 5.5.11-159
• thermodynamic properties, 5.5.2-22
• transport properties at elevated pressure, 5.5.14-41
• Air-activated gravity conveyor, 2.3.3-2
• Air-cooled heat exchangers:
• comparison of air and water as coolants, 3.8.1-1
• cooling air supply: by fans, 3.8.7-1/3.8.7-4
• by natural draft, 3.8.8-1
• costing, 4.8.3-1/4.8.3-3
• custom built, 3.8.2-1/3.8.2-2
• description, 3.1.2-4/3.1.2-5
• finned tube bundles for, 3.8.4-1/3.8.4-2
• finned tube systems for, 3.8.3-1/3.8.3-3
• fouling in, 3.17.7-7/3.17.7-8
• mechanical design, 4.4.1-1/4.4.1-7
• for cold climates and viscous fluid, 4.4.1-7
• components, 4.4.1-2/4.4.1-6
• nomenclature for, 4.4.1-2
• structural design factors, 4.4.1-6/4.4.1-7
• operation of, practical aspects, 3.18.3-1/3.18.3-8
• air distribution, 3.18.3-3/3.18.3-4
• air-side corrosion, 3.18.3-2/3.18.3-3
• control of, 3.18.3-7/3.18.3-8
• fan noise, 3.18.3-4/3.18.3-6
• flowrate measurement, 3.18.3-6/3.18.3-7
• hydraulic problems, 3.18.3-7
• problems with fans and drives, 3.18.3-4
• process flow distribution, 3.18.3-3
• special features, 3.8.9-1/3.8.9-7
• sound emission from, 3.8.9-1/3.8.9-2
• specification of, 4.9.2-1/4.9.2-4
• thermal rating, 3.8.5-1/3.8.5-6
• tubeside flow arrangements, 3.8.6-1
• Air preheaters, fouling in, 3.17.7-1/3.17.7-12
• Albedo for single scatter in radiation, 2.9.7-2
• Alcohols:
• liquid properties, 5.5.10-61/5.5.10-72
• saturation properties, 5.5.1-64/5.5.1-73
• superheated vapor properties, 5.5.11-61/5.5.11-72
• transport properties at elevated pressures, 5.5.14-22/5.5.14-26
• Aldehydes:
• liquid physical properties, 5.5.10-85/5.5.10-89
• saturation properties, 5.5.1-86/5.5.1-90
• superheated vapor properties, 5.5.11-85/5.5.11-89
• Aldred, D. L., 4.11.2-1/4.11.2-6
• Allene, see Propadiene
• Allyl alcohol:
• liquid properties, 5.5.10-69
• saturation properties, 5.5.1-70
• superheated vapor properties, 5.5.11-69
• Allyl chloride (3-chloropropane)
• liquid properties, 5.5.10-133
• saturation properties, 5.5.1-133
• superheated vapor properties, 5.5.11-132
• Alternating direction (ADR) method, for solution of implicit finite difference equations, 2.4.7-22/2.4.7-23
• program for, 2.4.7-34/2.4.7-36
• Aluminum, spectral characteristics of anodized surfaces, 2.9.2-16
• Aluminum alloys, thermal and mechanical properties, 5.5.12-11
• Aluminium brass, 4.5.7-3
• Ambrose-Walton corresponding states method, for vapour pressure, 5.1.2-3/5.1.2-4
• Amides:
• liquid properties, 5.5.10-151
• superheated vapor properties, 5.5.11-150
• Amines:
• liquid physical properties, 5.5.10-138/5.5.10-149
• saturation properties, 5.5.1-138/5.5.1-148
• superheated vapor physical properties, 5.5.11-137/5.5.11-148
• Ammonia:
• liquid properties, 5.5.10-161
• saturation properties, 5.5.1-160
• superheated gaseous: physical properties, 5.5.11-160
• thermodynamic properties, 5.5.2-22
• transport properties of gas at elevated pressure, 5.5.14-42
• use in Ocean Thermal Energy Conversion systems (OTEC), 3.22.3-13/3.22.3-14
• Ammonia plant, waste heat boilers for, 3.16.1-2
• Amyl acetate, see Pentyl acetate
• tert-Amyl alcohol:
• liquid properties, 5.5.10-68
• saturation properties, 5.5.1-70
• superheated vapor properties, 5.5.11-68
• Amyl chloride (see Chloropentane)
• AMTD (see Arithmetic mean temperature difference)
• Analogy between heat and mass and momentum transfer, 1.2.3-6/1.2.3-7, 2.1.5-1/2.1.5-4
• Analytic solutions for heat exchangers, 1.3.1-1/1.3.2-1
• Analytical solution of groups, for calculation of thermodynamic
• properties of nonhydrocarbons, 5.2.2-3/5.2.2-9
• tables of constants for, 5.5.4-1/5.5.4-6
• Anchor agitators:
• description, 3.14.2-1/3.14.2-2
• heat transfer with, 3.14.3-3/3.14.3-4
• Andrade equation for variation of viscosity with temperature, 5.1.4-3
• Anelasticity, 5.4.5-5
• Angled tubes, use in increasing flooding rate in reflux condensation, 2.6.2-8/2.6.2-9
• Aniline:
• liquid properties, 5.5.10-146
• saturation properties, 5.5.1-146
• superheated vapor properties, 5.5.11-145
• Anisotropy of elastic properties, 5.4.5-4/5.4.5-5
• Annular dispersed flow (see Annular flow)
• Annular distributor in shell-and-tube heat exchangers, 3.3.5-11
• Annular ducts:
• critical heat flux in flow in, 2.7.3-28/2.7.3-33
• forced convective heat transfer in single phase flow: laminar
• flow, 2.5.1-13/2.5.1-14
• with liquid metals, 2.5.13-1/2.5.13-2
• turbulent heat transfer in, 2.5.1-14, 2.5.1-18
• free convective heat transfer in closed-end: horizontal, 2.5.8-14/2.5.8-16
• vertical (heated on vertical curved surfaces), 2.4.8-13/2.5.8-14
• heat transfer to liquid metals in, 2.5.13-2/2.5.13-3
• single phase flow and pressure drop in, 2.2.2-8/2.2.2-10
• laminar flow, 2.2.2-8/2.2.2-9
• turbulent flow, 2.2.2-9/2.2.2-10
• Annular (radial) fins, efficiency, 2.4.4-9/2.4.9-13, 2.5.3-19/2.5.3-20
• Annular flow (gas-liquid):
• critical heat flux in, 2.7.3-22/2.7.3-30
• hydrodynamics in horizontal tubes, 2.3.2-25/2.3.2-26
• hydrodynamics in vertical tubes, 2.3.2-19/2.3.2-21
• deposition and entrainment correlations, 2.3.2-21
• interfacial roughness relationship, 2.3.2-20
• triangular relationship for, 2.3.2-10
• in boiling in horizontal tubes, 2.7.4-3/2.7.4-4
• regimes of occurrence of: in horizontal flow, 2.3.2-3/2.3.2-4
• in inclined tubes, 2.3.2-4/2.3.2-5
• in systems with phase change, 2.3.2-6/2.3.2-7
• Annular flow (liquid-liquid), 2.3.5-10/2.3.5-14
• pressure drop and holdup in, 2.3.5-11/2.3.5-14
• Annular flow (liquid-liquid-gas), 2.3.6-3
• Annuli (see Annular ducts)
• Anti-foulants, 3.17.8-7/3.17.8-8
• Antoine equation, for vapour pressure, 5.1.3-1
• Aqueous solutions, as heat transfer media, 5.5.15-14/5.5.15-23
• of inorganic compounds, 5.5.15-14/5.5.15-17
• of organic compounds, 5.5.15-18/5.5.15-28
• Arc welding of tubes into tube sheets:
• on inner face, 4.2.6-10
• on outer face, 4.2.6-8
• Archimedes number, 2.2.1-11
• Area, conversion of units, xxxii, xlv-lvi
• conversion chart for, l
• Area of tube outside surface in shell-and-tube heat exchangers:
• charts for, 3.1.4-6, 3.3.10-5
• Argon:
• liquid properties, 5.5.10-166
• saturated properties, 5.5.1-166
• superheated gaseous: physical properties, 5.5.11-167
• thermodynamic properties, 5.5.2-27
• transport properties at elevated pressure, 5.5.14-47
• Arithmetic mean temperature difference, definition, 3.1.4-2
• Armstrong, Robert C., 2.2.8-1/2.2.8-16, 2.5.12-1/2.5.12-19
• Aromatics:
• liquid properties, 5.5.10-47/5.5.10-60
• saturation properties, 5.5.1-59/5.5.1-63
• superheated vapor properties, 5.5.11-47/5.5.11-60
• transport properties at elevated pressure, 5.5.14-20/5.5.14-21
• Asbestos-free calendered gaskets, 4.12.2-1
• ASME VIII code, for mechanical design of shell-and-tube heat exchangers:
• description, 4.3.1-3
• ASOG (see Analytical solution of groups)
• Assisted convection:
• around immersed bodies, 2.5.9-1/2.5.9-4
• in vertical channels, 2.5.9-2/2.5.9-6
• Asymmetric loading, in heat exchangers, 4.1.2-2/4.1.2-9
• Attachment, of fouling layers, 3.17.7-9
• Attemperators, for waste heat boilers, 3.16.2-12/3.16.2-13
• Augmentation of heat transfer, 2.5.11-1/2.5.11-12, 2.6.6-1/2.6.6-4, 2.7.9-1/2.7.9-5
• active systems for: definition, 2.5.11-3
• in forced convection, 2.5.11-8/2.5.11-9
• in free convection, 2.5.11-4
• entropy generation in, 1.8.2-5/1.8.2-7
• in boiling, 2.7.9-1/2.7.9-5
• pool boiling, 2.7.9-1/2.7.9-2
• within tubes, 2.7.9-3/2.7.9-4
• compound systems for, 2.5.11-9
• in condensation, 2.6.6-1/2.6.6-32
• axial wire attachments for, 2.6.6-9
• basic approaches, 2.6.6-2
• coiled tubes for, 2.6.6-23
• electric fields in, 2.6.6-13
• fluted tubes for, 2.6.6-6/2.6.6-9
• Gregoric surfaces in, 2.6.6-4
• in dropwise condensation, 2.6.6-5
• in plate type heat exchangers, 2.6.6-23
• integral (low fin) tubes for, 2.6.6-9/2.6.6-12, 2.6.6-15/2.2.6-17
• internally finned tubes for, 2.6.6-17, 2.6.6-24
• micro-fin tubes for, 2.6.6-18/2.6.6-20, 2.6.6-25
• non-wetting surfaces for, 2.6.6-5/2.6.6-6
• roughness effects in, 2.6.6-6, 2.6.6-22, 2.6.6-25
• surface tension effects in, 2.6.6-3/2.6.6-8
• twisted tape inserts for, 2.6.6-21, 2.6.6-25
• wire-wrapped tubes for, 2.6.6-9
• in kettle reboilers, 3.6.2-6
• passive systems for: definition, 2.5.11-1/2.5.11-3
• in forced convection, 2.5.11-4/2.5.11-8
• in free convection, 2.5.11-3
• performance evaluation criteria for, 2.5.11-9/2.5.11-10
• in shell-and-tube heat exchangers using low finned tubes, 3.3.11-2/3.3.11-3
• Austenitic stainless steels, 4.5.6-2/4.5.6-5
• as materials of construction, 4.5.2-4
• Average phase velocity in multiphase flows, 2.3.1-4
• Avogadro number, xxxiii
• Axial flow reboilers, 3.6.2-8/3.6.2-12
• Axial wire attachments, for augmentation of condensation, 2.6.6-9
• Azeotropes, condensation of, 2.6.4-7, 2.6.4-9