Index:

I

• Ideal gas:
• law, 2.2.1-9
• velocity of sound in, 2.2.1-9
• Ilexan, heat transfer medium, 5.5.15-50
• Illingworth, A., 4.7.1-1/4.7.10-1
• Imbedded fins, 2.4.9-4
• Immersed bodies:
• combined free and forced convection around, 2.5.9-1/2.5.9-6
• creeping flow regime (assisting convection), 2.5.9-3
• opposing convection, 2.5.9-4
• slightly inertial regime (assisting convection), 2.5.9-3/2.5.9-4
• thin boundary layer regime (assisting convection), 2.5.9-1/2.5.9-3
• transverse flow, 2.5.9-4/2.5.9-6
• turbulent regime (assisting convection), 2.5.9-4
• free convective heat transfer to, 2.5.7-1/2.5.7-31
• generalized solutions for, 2.5.7-25/2.5.7-28
• horizontal cylinders, 2.5.7-20/2.5.7-23
• inclined and horizontal surfaces, 2.5.7-13/2.5.7-19
• open-ended channels, 2.5.7-19/2.5.7-20
• other shapes, 2.5.7-25
• spheres, 2.5.7-24/2.5.7-25
• vertical cones, 2.5.7-24
• vertical and inclined cylinders, 2.5.7-23/2.5.7-24
• vertical plates, 2.5.7-2/2.5.7-13
• single-phase flow over, 2.2.3-1/2.2.3-9
• circular cylinder, 2.2.3-3/2.2.3-6
• flow regimes in, 2.2.3-1/2.2.3-2
• forces exerted on, in, 2.2.3-2/2.2.3-3
• noncircular cylinders, 2.2.3-7/2.2.3-8
• single-phase forced convective heat transfer to: flat plates, 2.5.2-1/2.5.2-5
• single bodies, 2.5.2-5/2.5.2-13
• Immersed tubes, in fluidized beds, heat transfer to, 2.8.4-6/2.8.4-7
• Immersion exchangers, 4.4.4-2/4.4.4-3
• Immersion heaters, 4.4.4-2/4.4.4-3
• Immiscible liquids, condensation of vapors producing 2.6.4-1/2.6.4-16
• approximate general method for, 2.6.4-3/2.6.4-7
• azeotropic condensation, 2.6.4-7
• binary mixtures, 2.6.4-5/2.6.4-7
• calculation of cooling (condensation) curve for, 2.6.4-3/2.6.4-5
• dry wall desuperheating, 2.6.4-6/2.6.4-7
• multicomponent mixtures, 2.6.4-5/2.6.4-7
• description, 2.6.1-1, 2.6.4-1/2.6.4-2
• film method for, 2.6.4-8/2.6.4-13
• azeotropic condensation, 2.6.4-9
• binary mixtures, 2.6.4-8/2.6.4-9
• multicomponent mixtures, 2.6.4-10/2.6.4-13
• Imperfectly diffuse surfaces:
• definition, 2.9.4-1
• radiative heat transfer between specular surfaces and, 2.9.4-1/2.9.4-11
• Impingement damage in heat exchangers, 4.5.3-1
• Impingement plate:
• in condensers, 3.4.3-5
• construction features, 4.2.5-7/4.2.5-8
• effect on inlet pressure drop in shell-and-tube heat exchangers, 2.2.7-4/2.2.7-5
• (See also Impingement protection)
• Impingement protection, in shell-and-tube heat exchangers, 3.3.5-10/3.3.5-11
• with condensation, 3.4.3-5
• Impinging jets:
• average coefficients in, 2.5.6-3/2.5.6-4
• single-phase heat transfer in, 2.5.6-1/2.5.6-11
• local coefficients in, 2.5.6-2/2.5.6-3
• Implicit equations, solution of 2.4.7-19/2.4.7-25
• successive over-under relaxation (SOR), 2.4.7-19/2.4.7-22
• Gauss-Seidel method, 2.4.7-21/2.4.7-22
• alternating direction method (ADR) 2.4.7-22/2.4.7-23
• Stone's strongly implicit method, 2.4.7-23/2.4.7-25
• Inclined cylinders (see Inclined pipes; Cylinders)
• Inclined enclosures, free convective heat transfer in, 2.5.8-17/2.5.8-20
• large aspect ratios, 2.5.8-17/2.5.8-19
• moderate aspect ratios, 2.5.8-20
• Inclined flow, effect of on heat transfer to cylinders, 2.5.2-7
• Inclined pipes:
• flow regimes in gas-liquid flow in, 2.3.2-4/2.3.2-5
• free convection heat transfer on outside, 2.5.7-23/2.5.7-24
• heat transfer in boiling in, 2.7.4-8
• pneumatic conveying (solid/gas flow) in, 2.3.3-2
• (See also Pipes, circular)
• Inclined plates (see Inclined surfaces; Flat plates)
• Inclined surfaces, 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
• Inclined tubes (see Pipes, circular; Pipes, noncircular; Inclined Pipes; Cylinders)
• Incondensables (see Noncondensables)
• Inconel, spectral characteristics of reflectance from oxidized surface of, 2.9.2-15
• Incremental collapse, as failure mode in heat exchanger, 4.1.1-3/4.1.1-5
• Inert gases
• effect on condensation, 2.1.6-3/2.1.6-4
• formation in heat pipe heat exchangers, 3.10.8-7
• Injection:
• effect on laminar flow over flat plate, 2.2.1-27
• effect in transition flow over flat plate, 2.2.1-28/2.2.1-29
• effect in turbulent flow over flat plate, 2.2.1-35
• use in augmentation of heat transfer, 2.5.11-3/2.5.11-9
• Inlet effects in shell-and-tube heat exchangers, 3.3.6-9/3.3.6-10
• In-life flow, bundles of tubes (see Tube banks)
• In-line tube banks:
• correlations for heat transfer in, 2.5.3-1/2.5.3-30
• finned tubes, 2.5.3-21/2.5.3-30
• plain tubes, 2.5.3-1/2.5.3-20
• drag coefficients for tubes in, 2.2.4-4
• pressure drop in with finned tubes, 2.2.4-14
• pressure drop in with plain tubes, 2.2.4-7/2.2.4-8
• correction factors for small number of tube rows, 2.2.4-10
• effect of yawing on, 2.2.4-12
• Inorganic compounds, solutions of, as heat transfer media, 5.5.15-2/5.5.15-5
• Inorganic substances:
• liquid physical properties, 5.5.10-74/5.5.10-78
• saturation properties, 5.5.1-155/5.5.1-165
• superheated vapor properties, 5.5.11-155/5.5.11-166
• transport properties at elevated pressures, 5.5.14-41/5.5.14-45
• Inspection (see Testing and inspection)
• Instability, parallel channel, in condensers, 3.4.5-3
• Insulation and external protection of heat exchangers, 4.15.1-1/4.15.6-2
• acoustic insulation, 4.15.3-1/4.15.3-2
• cold insulation, 4.15.2-5/4.15.2-6
• application, 4.15.2-6/4.15.-7
• materials for, 4.15.2-5/4.15.2-6
• corrosion protection under, 4.15.5-6
• insulation thickness determination, 4.15.1-1/4.15.1-2
• hot insulation, 4.15.2-2/4.15.2-5
• application, 4.15.2-3/4.15.2-5
• materials for, 4.15.2-2/4.15.2-3
• paintings and coatings, 4.15.5-1/4.15.5-6
• passive fire protection, 4.15.6-1/4.15.6-2
• personnel protection by, 4.15.4-1
• Insulators, thermal conductivity of, 5.4.3-1/5.4.3-2
• Integral condensation:
• calculation of condensation curves for, 2.6.3-3/2.6.3-5
• description, 3.4.4-2, 2.6.3-1/2.6.3-3
• Integral finned tubes:
• as augmentation device in condensation, 2.6.6-9, 2.6.6-12, 2.6.6-15/2.6.6-17
• as augmentation device in natural convection, 2.5.11-3
• description of, 2.4.9-4
• use in shell-and-tube heat exchangers, 4.2.5-3
• Interaction coefficients in heat exchangers, 1.1.2-1/1.1.2-2
• Interaction parameters for binary systems, tables, 5.5.4-8/5.5.4-9
• Interfacial friction, in three-phase (liquid-liquid-gas) stratified flows, 2.3.6-4/2.3.6-5
• Interfacial effects, in single phase heat transfer in microchannels, 2.13.3-13/2.13.3-14
• Interfacial resistance, in condensation, 2.6.2-15
• Interfacial roughness, relationships for, in annular gas-liquid flow, 2.3.2-20/2.3.2-21
• Interfacial shear stress, effect on filmwise condensation, on vertical surface, 2.6.2-5/2.6.2-7
• Interfacial tension (see Surface tension)
• Intergrannular corrosion, of
• stainless steels, 4.5.6-12/4.5.6-13
• Intermating troughs, as corrugation design in plate heat exchangers, 3.7.1-4/3.7.1-5
• Intermittent flows:
• gas liquid, in horizontal and inclined flows, 2.3.2-2/2.3.2-5
• in boiling in horizontal tubes, 2.7.4-1/2.7.4-3
• plug flow, in vertical pipes, 2.3.2-19
• slug flow, in horizontal pipes, 2.3.2-24/2.3.2-25
• Internal energy (see Specific internal energy)
• Internal heat sources, temperature distribution in bodies with, 2.4.2-3
• Internal heat transfer coefficient, use in transient conduction calculations, 2.4.3-7/2.4.3-8
• Internal reboilers (in distillation columns), characteristics advantages and disadvantages of, 3.6.1-3/3.6.1-4
• Internally finned tubes, heat transfer and pressure drop in, 2.5.11-5/2.5.11-6
• International codes for pressure vessels, 4.3.1-4/4.3.1-6
• CEN code, 4.3.1-5
• ISO code, 4.3.1-4
• International Standards Organization (see ISO)
• International System of Units (SI), xxiixxxiii
• amount of substance, xxv
• base units, xxiv
• conversion factors, xxviixxix
• derived units, xxiiixxxi
• multiples and submultiples, xxxiii
• temperature units, xxvxxvi
• Interpenetrating continua (as representation of heat exchangers):
• partial differential equations for, 1.2.6-1/1.2.6-7
• porosity in, 1.2.6-2
• Intertube velocity, in tube banks, 2.2.4-3
• Inviscid flow, compressible, with heat addition, 2.2.2-13/2.2.2-14
• Iodine:
• liquid properties, 5.5.10-170
• saturation properties, 5.5.1-171
• superheated vapor properties, 5.5.11-172
• Iodobenzene:
• liquid properties, 5.5.10-136
• saturation properties, 5.5.1-136
• superheated vapor properties, 5.5.11-133
• Iodoethane:
• liquid properties, 5.5.10-124
• saturation properties, 5.5.1-124
• superheated vapor properties, 5.5.11-123
• Iodomethane:
• liquid properties, 5.5.10-113
• saturation properties, 5.5.1-114
• superheated vapor properties, 5.5.11-113
• Irvine, T. F., Jr., 2.4.6-1/2.4.6-6
• ISO codes for mechanical design of heat exchangers, 4.3.1-4
• Isobutane:
• liquid properties, 5.5.10-15
• saturation properties, 5.5.1-19
• superheated gaseous physical properties, 5.5.11-15
• thermodynamic properties, 5.5.2-6
• transport properties at elevated pressure, 5.5.14-13
• Isobutanol:
• liquid properties, 5.5.10-66
• saturation properties, 5.5.1-68
• superheated vapor properties, 5.5.11-66
• Isobutene (see 2-Methylpropene)
• Isobutylamine:
• liquid properties, 5.5.10-143
• saturation properties, 5.5.1-143
• superheated vapor properties, 5.5.11-142
• Isobutylformate:
• liquid properties, 5.5.10-76
• saturation properties, 5.5.1-77
• superheated vapor properties, 5.5.11-76
• Isobutyric acid:
• liquid properties, 5.5.10-96
• saturation properties, 5.5.1-96
• superheated vapor properties, 5.5.11-96
• Isodurene (see 1,2,3,5-Tetramethylbenzene)
• Isooctane (see 2,2,4-Trimethylpentane)
• Isoparaffins:
• liquid properties, 5.5.10-15/5.5.10-19
• saturation properties, 5.5.1-19/5.5.1-23
• superheated vapor properties, 5.5.11-15/5.5.11-19
• transport properties at elevated pressure, 5.5.14-13/5.5.14-14
• Isopentane:
• liquid properties, 5.5.10-15
• saturation properties, 5.5.1-19
• superheated vapor properties, 5.5.11-15
• Isopentanol:
• liquid properties, 5.5.10-67
• saturation properties, 5.5.1-69
• superheated vapor properties, 5.5.11-67
• Isoprene, see 2 Methylbutadiene
• Isopropanol:
• liquid properties, 5.5.10-66
• saturation properties, 5.5.1-68
• superheated gaseous: physical properties, 5.5.11-66
• thermodynamic properties, 5.5.2-2
• transport properties of gases at elevated pressure, 5.5.14-17
• Isopropylacetate:
• liquid properties, 5.5.10-78
• superheated vapor properties, 5.5.11-78
• Isopropylalcohol (see Isopropanol)
• Isopropylamine:
• liquid properties, 5.5.10-142
• saturation properties, 5.5.1-142
• superheated vapor properties, 5.5.11-141
• Isopropylbenzene:
• liquid properties, 5.5.10-49
• saturation properties, 5.5.1-52
• superheated vapor properties, 5.5.11-49
• Isopropylchloride (see 2-Chloropropane)
• Isopropylcyclohexane:
• liquid properties, 5.5.10-45
• saturation properties, 5.5.1-48
• superheated vapor properties, 5.5.11-45
• Isothermal flow, compressible, in ducts, 2.2.2-13
• Isothermal gas, radiation heat transfer to walls from, 2.9.6-1/2.9.6-9
• Isotropic materials, elastic properties, 5.4.5-3/5.4.5-4
• Isotropic scattering, 2.9.5-2
• Italy, guide to national practice for heat exchanger mechanical design, 4.3.5-7