Index:

D

• Damage, sources of heat exchangers, 4.5.3-1/4.5.3-7, 4.6.1-1/4.6.1-2
• Damkohler number:
• definition, 2.2.1-13
• modified form for compressible flows with heat transfer, 2.2.2-13
• Damping:
• capacity, anelasticity, and, 5.4.5-5
• of flow-induced vibration, 4.6.2-4
• Darcy model, for flow in porous media, 2.11.1-3
• Davis and Anderson criterion, for onset of nucleate boiling, 2.7.3-7
• Deaerators, for waste heat boilers, 3.16.2-2
• Decal, heat transfer medium, 5.5.15-45
• Decane:
• liquid properties, 5.5.10-9
• saturation properties, 5.5.1-13
• superheated vapor properties, 5.5.11-9
• transport properties at elevated pressures, 5.5.14-12
• 1-Decanol:
• liquid properties, 5.5.10-65
• superheated vapor properties, 5.5.11-65
• 1-Decene:
• liquid properties, 5.5.10-23
• saturation properties, 5.5.1-27
• superheated vapour properties, 5.5.11-23
• Degradation temperature, of polymers, 2.5.12-1
• "Del" operator (see Differential vector operators)
• Delaware method, for shell-side heat transfer and pressure drop, (see Bell-Delaware method)
• Demisters, wire mesh, for multistage flash evaporators, 3.22.2-23/3.22.2-30
• design parameters, 3.22.2-25/3.22.2-26
• materials for, 3.22.2-24/3.22.2-25
• models and correlations for, 3.22.2-29/3.22.2-30
• performance of, 3.22.2-26/3.22.2-29
• Dener, Y.M., 4.15.5-1/4.15.6-2
• Dengler and Addoms correlation, for forced convective heat transfer in two-phase flow, 2.7.3-13
• Density:
• conversion of units for, xxix, xlv-lvi
• definition, 2.2.1-1
• fluid with constant, 2.2.1-10
• fluid with small variations of, 2.2.1-9/2.2.1-10
• of fluid mixtures, 5.2.1-1/5.2.1-8
• gases, 5.2.1-1/5.2.1-3
• liquids, 5.2.1-3/5.2.1-7
• of heat transfer media, 5.5.15-1/5.5.15-42
• of heavy water, 5.5.9-1
• of liquid water, 5.5.3-1/5.5.3-21
• of liquids below their boiling point, 5.5.10-1/5.5.10-175
• of multicomponent liquid mixtures, 5.2.3-1/5.2.3-2
• of pure fluids, 5.1.2-1/5.1.2-23
• gases, 5.1.2-1/5.1.2-9
• liquids, 5.1.2-9/5.1.2-22
• of saturated liquids and vapors, 5.5.1-1/5.5.1-178
• of seawater, 5.5.13-7/5.5.13-8
• of solids, 5.4.1-1/5.4.1-2
• aluminum alloys, 5.5.12-11
• carbon and low-alloy steels, 5.5.12-31
• cast iron, 5.5.12-12
• copper and copper alloys, 5.5.12-10
• graphite and carbon, 5.4.1-1
• high chrome steels, 5.5.12-7/5.5.12-8
• metal alloys, 5.4.1-1
• nickel and nickel alloys, 5.5.12-8/5.5.12-9
• organics, 5.4.1-2
• refractories, 5.4.1-1/5.4.1-2
• titanium, 5.5.12-12
• zirconium, 5.5.12-12
• of superheated fluids, 5.5.2-1/5.5.2-36
• of superheated gases, 5.5.11-1/5.5.11-174
• relation with viscosity for gases, 2.2.1-11
• Deposition of droplets in annular flow, 2.3.2-21, 2.7.3-24
• Deposition in fouling, 3.17.3-1/3.17.3-3
• deposit strength, 3.17.3-4
• deposition probability, 3.17.3-3
• Desalination plants:
• flash evaporation systems for, 3.22.1-1/3.22.2-54
• fouling in, 3.17.6-26
• in Ocean Thermal Energy Conversion (OTEC) systems, 3.22.3-17
• Design of heat exchangers, introduction, 3.1.1-1/3.1.4-9
• Design procedures, for segmentally baffled heat exchangers, 3.3.10-1/3.3.10-8
• Desuperheaters for use in association with evaporators, 3.5.4-4
• Developing flow in ducts:
• single-phase flow and pressure drop in, 2.2.2-10/2.2.2-12
• hydrodynamic entrance region in, 2.2.2-10/2.2.2-12
• various forms and effects on, 2.2.2-11
• Dew-poin corrosion, 3.17.6-25
• Diathermanous fluid, 2.9.1-1
• 1,1-Dibromoethane:
• liquid properties, 5.5.10-124
• saturation properties, 5.5.1-124
• superheated vapor properties, 5.5.11-123
• Dibromomethane:
• liquid properties, 5.5.10-112
• saturation properties, 5.5.1-113
• superheated vapor properties, 5.5.11-112
• 1,2-Dibromotetrafluoroethane (Refrigerant 114B2):
• liquid properties, 5.5.10-126
• saturation properties, 5.5.1-126
• superheated vapor properties, 5.5.11-125
• Dibutylamine:
• liquid properties, 5.5.10-144
• saturation properties, 5.5.1-144
• superheated vapor properties, 5.5.11-143
• Dibutyl ether:
• liquid properties, 5.5.10-104
• saturation properties, 5.5.1-104
• superheated vapor properties, 5.5.11-103
• Dichloroacetic acid:
• liquid properties, 5.5.10-99
• saturation properties, 5.5.1-99
• superheated vapor properties, 5.5.11-99
• o-Dichlorobenzene:
• liquid properties, 5.5.10-137
• saturation properties, 5.5.1-137
• superheated vapor properties, 5.5.11-136
• Dichlorodifluoromethane (see Refrigerant 12)
• critical heat flux table for flow of in vertical tube, 2.7.3-29
• liquid properties, 5.5.10-116
• saturation properties, 5.5.1-117
• superheated gaseous: physical properties, 5.5.11-116
• thermodynamic properties, 5.5.2-18
• transport properties at elevated pressure, 5.5.14-30
• 1,1-Dichloroethane (Refrigerant 150a):
• liquid properties, 5.5.10-120
• saturation properties, 5.5.1-121
• superheated vapor properties, 5.5.11-120
• 1,2-Dichloroethane (Refrigerant 150):
• liquid properties, 5.5.10-121
• saturation properties, 5.5.1-121
• superheated vapor properties, 5.5.11-120
• 1,1-Dichloroethylene:
• liquid properties, 5.5.10-130
• saturation properties, 5.5.1-130
• superheated vapor properties, 5.5.11-129
• cis-1,2-Dichloroethylene:
• liquid properties, 5.5.10-131
• saturation properties, 5.5.1-131
• superheated vapor properties, 5.5.11-130
• trans-1,2-Dichloroethylene:
• liquid properties, 5.5.10-131
• saturation properties, 5.5.1-131
• superheated vapor properties, 5.5.11-130
• Dichlorofluoromethane (see Refrigerant 21)
• critical heat flux table for flow of in vertical tube, 2.7.3-29
• liquid properties, 5.5.10-116
• saturation properties, 5.5.1-117
• superheated gaseous: physical properties, 5.5.11-116
• thermodynamic properties, 5.5.2-18
• transport properties at elevated pressure, 5.5.14-30
• Dichloromethane (Refrigerant 30):
• liquid properties, 5.5.10-110
• saturation properties, 5.5.1-111
• superheated vapor properties, 5.5.11-110
• 1,2-Dichlorotetrafluoroethane (Refrigerant 114)
• liquid properties, 5.5.10-126
• saturation properties, 5.5.1-126
• superheated vapor properties, 5.5.11-125
• thermal conductivity at elevated pressures, 5.5.14-36
• 1,2,3-Dichlorotrifluoroethane (Refrigerant 123)
• transport properties at elevated pressures, 5.5.14-39
• Dielectric constant, of water, 5.5.3-30
• Diethylamine:
• liquid properties, 5.5.10-140
• superheated vapor properties, 5.5.11-64
• superheated vapor properties, 5.5.11-139
• n,n-Diethylaniline:
• liquid properties, 5.5.10-148
• saturation properties, 5.5.1-148
• superheated vapor properties, 5.5.11-147
• Diethylene glycol:
• liquid properties, 5.5.10-70
• saturation properties, 5.5.1-71
• superheated vapor properties, 5.5.11-70
• Diethyl ether:
• liquid properties, 5.5.10-101
• saturation properties, 5.5.1-101
• superheated vapor properties, 5.5.11-101
• transport properties at elevated pressure, 5.5.14-28
• Diethyl ketone:
• liquid properties, 5.5.10-92
• saturation properties, 5.5.1-92
• superheated vapor properties, 5.5.11-91
• Diethylsulfide:
• liquid properties, 5.5.10-155
• saturation properties, 5.5.1-154
• superheated vapor properties, 5.5.11-154
• Differential condensation:
• calculation of condensation curves, 2.6.3-5
• description, 3.4.4-2, 2.6.3-3/2.6.3-5
• Differential formulations for nonisothermal gas radiation, 2.9.7-5/2.9.7-8
• embedding, 2.9.7-7/2.9.7-8
• multiflex methods, 2.9.7-6/2.9.7-7
• radiation diffusion, 2.9.7-5/2.9.7-6
• Differential resistance term in heat exchanger design, 3.3.9-2
• Differential vector operators in heat conduction, 2.4.1-2
• Diffraction models for radiative heat transfer from surfaces, 2.9.4-7/2.9.4-8
• Diffuse surfaces, radiative heat transfer between, 2.9.3-1/2.9.3-17
• Diffuse wall passages, radiative heat transfer in, 2.9.3-13/2.9.3-16
• Diffusers, single-phase flow and pressure drop in, 2.2.2-18/2.2.2-21
• effect of inlet conditions, 2.2.2-20
• with free discharge, 2.2.2-19/2.2.2-20
• methods of improving performance in, 2.2.2-20/2.2.2-21
• performance, 2.2.2-20/2.2.2-21
• Diffusion, in multi-component condensation, 2.6.4-8/2.6.4-13
• n,n-Diffusion coefficients:
• in gases, 5.2.5-3/5.2.5-4
• in liquids, 5.2.5-1/5.2.5-3
• 1,1-Difluoroethane (Refrigerant 152a):
• liquid properties, 5.5.10-118
• saturation properties, 5.5.1-118
• superheated vapor properties, 5.5.11-117
• transport properties at elevated pressure, 5.1.14-37
• Difluoromethane (Refrigerant 32):
• liquid properties, 5.5.10-108
• saturation properties, 5.5.1-109
• superheated vapor properties, 5.5.11-108
• Diiodomethane:
• liquid properties, 5.5.10-114
• saturation properties, 5.5.1-114
• superheated vapor properties, 5.5.11-113
• Diisobutylamine:
• liquid properties, 5.5.10-143
• Diisopropylamine:
• liquid properties, 5.5.10-143
• saturation properties, 5.5.1-142
• superheated vapor properties, 5.5.11-141
• Diisopropylether:
• liquid properties, 5.5.10-49
• saturation properties, 5.5.1-104
• Dimensional analysis:
• pi theorem for, 2.2.1-12/2.2.1-15
• and theory of similarity, 2.2.1-15
• Dimensionless groups:
• equivalent groups in heat and mass transfer, 2.1.5-2
• in free convective heat transfer to immersed bodies, 2.5.7-2/2.5.7-3
• in forced convection in ducts, 2.5.1-2
• in regenerator performance calculation, 3.15.6-1/3.15.6-3
• table of, 2.2.1-13
• Dimensionless numbers (see Dimensionless groups)
• Dimensionless temperature difference, ?, 1.5.1-4/1.5.1-5
• Dimensionless time (see Fourier number)
• Dimethylacetylene:
• liquid properties, 5.5.10-38
• saturation properties, 5.5.1-41
• superheated vapor properties, 5.5.11-38
• Dimethylamine:
• liquid properties, 5.5.10-139
• saturation properties, 5.5.1-139
• superheated vapor properties, 5.5.11-138
• Dimethylaniline:
• liquid properties, 5.5.10-147
• saturation properties, 5.5.1-147
• superheated vapor properties, 5.5.11-146
• 2,2-Dimethylbutane:
• liquid properties, 5.5.10-18
• saturation properties, 5.5.1-22
• superheated vapor properties, 5.5.11-18
• 2,3-Dimethylbutane:
• liquid properties, 5.5.10-18
• saturation properties, 5.5.1-22
• superheated vapor properties, 5.5.11-18
• 1,1-Dimethylcyclopentane:
• liquid properties, 5.5.10-41
• saturation properties, 5.5.1-44
• superheated vapor properties, 5.5.11-100
• Dimethylether:
• liquid properties, 5.5.10-100
• saturation properties, 5.5.1-101
• superheated vapor properties, 5.5.11-48
• Dimethylketone:
• liquid properties, 5.5.10-90
• superheated liquid properties, 5.5.11-44
• 2,2-Dimethylpropane (neopentane):
• liquid properties, 5.5.10-17
• saturation properties, 5.5.1-21
• superheated vapor properties, 5.5.11-17
• Dimethylsulfide:
• liquid properties, 5.5.10-155
• saturation properties, 5.5.1-154
• superheated vapor properties, 5.5.11-154
• 1,4-Dioxane:
• liquid properties, 5.5.10-107
• saturation properties, 5.5.1-108
• superheated vapor properties, 5.5.11-107
• Diphenyl:
• liquid physical properties, 5.5.11-29
• saturation properties, 5.5.1-60
• superheated vapor properties, 5.5.11-57
• Diphenylamine:
• liquid properties, 5.5.10-144
• saturation properties, 5.5.1-144
• superheated vapor properties, 5.5.11-143
• Diphenylether:
• liquid properties, 5.5.10-104
• saturation properties, 5.5.1-105
• superheated vapor properties, 5.5.11-104
• Diphenylmethane:
• liquid properties, 5.5.10-57
• saturation properties, 5.5.1-60
• superheated vapor properties, 5.5.11-57
• Dipropyl ether:
• liquid properties, 5.5.10-103
• saturation properties, 5.5.1-103
• superheated vapor properties, 5.5.11-103
• Diisopropyl ether:
• liquid properties, 5.5.10-103
• saturation properties, 5.5.1-104
• Dipropyl ketone:
• liquid properties, 5.5.10-92
• saturation properties, 5.5.1-93
• superheated vapor properties, 5.5.11-92
• Direct-contact condensers, 3.20.1-1/3.20.4-5
• bubble-type, 3.20.1-3, 3.20.4-1/3.20.4-5
• effect of incondensable vapors in, 3.20.4-2
• Florschuetz and Chao equation for bubble collapse in, 3.20.4-1
• Jacobs and Major model for condensation of vapour forming immiscible liquids in, 3.20.4-2
• use as vapor suppression systems, 3.20.4-4
• Wittke and Chao model for collapse of moving bubble in, 3.20.4-1
• drop-type, 3.20.2-1/3.20.2-9
• barometric condenser, 3.20.1-2
• condensation on jets and sheets in, 3.20.2-3/3.20.2-8
• energy balances for, 3.20.2-1/3.20.2-3
• Jacobs and Cook equation for drop growth in, 3.20.2-2
• Lekic and Ford equation for drop velocity in, 3.20.1-1
• solid-curtain condenser, 3.20.1-2
• spray condenser, 3.20.1-2
• Westinghouse jet condenser, 3.20.1-3
• film-type, 3.20.1-3, 3.20.3-1/3.20.3-5
• condensation on a film flowing down a plate, 3.20.3-1/3.20.3-3
• condensation on a film flowing over sphere, 3.20.3-3/3.20.3-4
• effect of noncondensables in, 3.20.3-3/3.20.3-4
• packed-bed condenser, 3.20.1-3
• volumetric heat transfer coefficients in packed bed condensers, 3.20.3-3
• introduction to, 3.20.1-1/3.20.1-4
• mechanical construction of, 4.4.6-6/4.4.6-7
• Direct-contact cooling, 4.4.4-8
• Direct-contact evaporation, 4.4.4-7
• Direct contact heat exchangers, 3.1.2-9, 3.19.1-1/3.19.5-2
• baffle tray columns, 3.19.5-2
• drop behaviour 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
• one dimensional models for, 3.19.3-1/3.19.3-4
• types of direct contact heat exchangers, 3.19.1-1/3.19.1-5
• columns, 3.19.1-2
• disk and doughnut baffled columns, 3.19.1-2
• mechanically agitated, 3.19.1-4
• packed bed, 3.19.1-3
• sieve tray column, 3.19.1-3
• spray columns, 3.19.1-2
• turbulent pipe contactor, 3.19.1-4
• with drops and bubbles, 3.19.2-1/3.19.2-4
• drop and bubble formation, 3.19.2-1/3.19.2-4
• Direct contact heat transfer, 2.10.1-1/2.10.3-16
• between parallel continuous streams, 2.10.2-1/2.10.2-7
• disperse media (drops, particles and bubbles) 2.10.2-4/2.10.2-6
• falling films, 2.10.2-1/2.10.2-3
• sheets and jets, 2.10.2-3/2.10.2-4
• with phase change, 2.10.3-1/2.10.3-16
• condensation, 2.10.3-4/2.10.3-12
• evaporation and boiling, 2.10.3-1/2.10.3-4
• in solidification, 2.10.3-12
• Direct numerical simulation, of turbulence, 2.2.1-19
• Dirichlet boundary condition, finite difference method, 2.4.7-2/2.4.7-3
• Dirt (see Fouling)
• Dished heads:
• EN13445 code for
• under external pressure, 4.3.3-7
• under internal pressure, 4.3.3-5/4.3.3-6
• PD5500 code for
• under external pressure, 4.3.2-7
• under internal pressure, 4.3.2-5/4.3.2-6
• Discretization in numerical analysis:
• for cases where flow patterns must be calculated, 1.4.2-1
• in design of heat exchangers with prescribed flow patterns, 1.4.1-1/1.4.1-6
• effect of fineness, 1.4.1-5/1.4.1-6
• subdivision of space, 1.4.1-1/1.4.1-2
• subdivision of time, 1.4.1-2/1.4.1-3
• Disk-and-doughnut baffles columns, for direct contact heat transer, 3.19.1-2, 3.19.5-2
• Disk-and-doughnut baffled heat exchangers, 3.3.11-2
• Disk turbine agitator, 3.14.2-1/3.14.2-2
• heat transfer in vessel agitated by, 3.14.3-1
• Disks, free convective heat transfer from inclined, 2.5.7-25
• Dispersants, for fouling control, 3.17.8-7
• Dispersed bubble flow (see Bubble flow)
• Dispersed flow (liquid-liquid), 2.3.5-14/2.3.5-24
• drop size in, 2.3.5-22/2.3.5-24
• homogeneous model for, 2.3.5-15/2.3.5-16
• in vertical tubes, 2.3.5-22/2.3.5-24
• phase inversion in, 2.3.5-19/2.3.5-20
• viscosity of emulsions in, 2.3.5-16/2.3.5-19
• Dissipation of turbulent energy, 2.2.1-20
• Distillation:
• closed distillation process, 2.1.7-8
• lost work in, 1.9.5-8/1.9.5-10
• Distribution:
• annular, in shell-and-tube heat exchangers, 3.3.5-11
• design in fluidized beds, 2.2.6-12/2.2.6-13
• in plate heat exchangers, 3.7.2-2
• Dittus-Boelter equation, for single-phase forced convective heat transfer, 2.7.3-6
• Dividing flow, loss coefficients in, 2.2.2-21
• DNB (departure from nucleate boiling) (see Critical heat flux)
• DNS (see Direct numerical simulation)
• Dodecane:
• liquid physical properties, 5.5.10-10
• saturated physical properties, 5.5.1-14
• superheated vapor properties, 5.5.11-10
• 1-Dodecene:
• liquid properties, 5.5.10-24
• saturation properties, 5.5.1-28
• superheated vapor properties, 5.5.11-24
• Donohue method, for shell-side heat transfer in shell-and-tube heat exchangers, 3.3.2-2
• Double-pipe heat exchangers:
• approximate overall heat transfer coefficients, 2.1.2-3
• construction and operational characteristics, 3.2.1-1/3.2.1-5
• longitudinal finned tubes for, 3.2.1-1/3.2.1-3
• design data for, 3.2.1-4
• fin efficiency in, 3.2.2-6
• heat transfer coefficients in, 3.2.2-1/3.2.1-3
• mean temperature difference in, 3.2.3-1/3.2.3-3
• mechanical design, 4.4.4-1/4.4.4-2
• overall heat transfer coefficient in, 3.2.3-1
• pressure drop in, 3.2.2-4
• Double segmental baffled heat exchangers, 3.3.11-2
• Double-tube type of waste heat boilers, 3.16.2-5
• Downward facing surfaces, free convective heat transfer from, 2.5.7-13/2.5.7-15
• Downward flow in vertical tubes, flow patterns in gas/liquid, 2.3.2-2
• Dowtherm A:
• liquid properties, 5.5.10-78
• Dowtherm J:
• liquid properties, 5.5.10-78
• Dowtherms, as heat transfer media, 5.5.15-45/5.5.15-48
• Drag coefficient:
• for circular cylinder, 2.2.3-5
• definition, 2.2.3-2
• for sphere, 2.2.3-3
• on tube in tube bank, 2.2.4-3/2.2.4-5
• Drag force:
• on immersed bodies, 2.2.3-2/2.2.3-3
• on tube in tube bank, 2.2.4-3/2.2.4-5
• Drag reduction, 2.2.8-14
• effect on heat transfer, 2.5.12-16
• Drainage, of condensate, 3.18.4-1/3.18.4-2
• Drift flux model for two-phase flows, 2.3.1-7/2.3.1-9
• Drop-type direct-contact condensers, 3.20.2-1/3.20.2-9
• barometric condenser, 3.20.1-2
• condensation on drops and sheets in, 3.20.2-3/3.20.2-8
• energy balances for, 3.20.2-1/3.20.2-3
• Jacobs and Cook equation for drop growth in, 3.20.2-2
• Lekic and Ford equation for drop velocity in, 3.20.1-1
• solid-curtain condenser, 3.20.1-2
• spray condenser, 3.20.1-8
• Westinghouse jet condenser, 3.20.1-3
• Droplets:
• condensation on, 2.10.2-1/2.10.2-7
• deposition and entrainment of, in annular flow, 2.3.2-21
• formation of, 3.19.2-1/3.19.2-4
• in direct contact heat transfer, 2.10.2-4/2.10.2-6
• nucleation of in supersaturated vapors, 2.6.7-1/2.6.7-2
• on solid surfaces, molecular dynamics simulation of, 2.13.7-16/2.13.7-19
• size in liquid-liquid dispersed flow, 2.3.5-22/2.3.5-24
• use in augmentation of heat transfer, 2.5.11-8
• Dropwise condensation, 2.6.5-1/2.6.5-11, 2.6.6-5
• condensation of steam in, 2.6.5-4/2.6.5-8
• effect of non-condensing gas on, 2.6.5-2
• introduction, 2.1.7-6, 2.6.1-1, 2.6.5-1
• mechanisms of, 2.6.5-2/2.6.5-4
• of organic fluids, 2.6.5-8/2.6.5-9
• promotors for, 2.6.5-1/2.6.5-2
• Dry cooling towers, 3.8.2-1/3.8.2-2, 3.8.8-1, 3.12.5-1/3.12.5-2
• Dry-wall convection, in evaporation (see Postdryout heat transfer)
• Dry wall desuperheating (in condensation), 2.6.4-6/2.6.4-7
• Dryers:
• classification and selection, 3.13.2-1/3.13.2-4
• introduction, 3.13.1-1/3.13.1-2
• layout and performance data, 3.13.3-1/3.13.3-5
• description of drying process in the Mollier chart, 3.13.3-4/3.13.3-5
• energy and mass balances, 3.13.3-1/3.13.3-2
• Mollier chart, 3.13.3-1
• wet bulb temperature in, 3.13.3-2/3.13.3-4
• practical design, 3.13.7-1/3.13.7-3
• band dryers, 3.13.7-1/3.13.7-2
• fluid bed dryers, 3.13.7-2
• pneumatical conveying dryers, 3.13.7-2
• rotary dryers, 3.13.7-2
• spray dryers, 3.13.7-2/3.13.7-3
• prediction of drying rates in, 3.13.4-1/3.13.4-5
• prediction of residence time in: with nonprescribed material flow, 3.13.6-1
• with prescribed material flow, 3.13.5-1/3.15.5-5
• as type of heat exchange equipment, 1.1.5-3
• Drying, combined heat and mass transfer in, 2.1.6-1/2.1.6-2
• Drying loft, 3.13.2-3
• Drying plant (see Dryers)
• Drying rates, prediction of, 3.13.4-1/3.13.4-5
• Dryout:
• introduction, 2.7.3-2
• as mechanism for critical heat flux: of liquid film, 2.7.3-26/2.7.3-33
• under a vapor clot, 2.7.3-27
• (See also Critical heat flux)
• Ductile fracture as failure mode of heat exchanger, 4.1.1-3
• Ducts, single-phase fluid flow and pressure drop in, 2.2.2-1/2.2.2-28
• circular pipes, fully developed flow, 2.2.2-1/2.2.2-10
• compressible flow in, 2.2.2-12/2.2.2-15
• curved ducts, 2.2.2-15/2.2.2-18
• developing flow in, 2.2.2-10/2.2.2-12
• entropy generation in, 1.8.2-1/1.8.2-7
• losses in piping components in, 2.2.2-15/2.2.2-21
• noncircular ducts, fully developed flow, 2.2.2-8/2.2.2-10
• radiation/convection interaction phenomena in, 2.9.8-14/2.9.8-16
• unsteady flow in, 2.2.2-15
• Duplex stainless steels, 4.5.6-5/4.5.6-7
• Durand correlation for heterogeneous conveyance in solid/liquid flow, 2.3.4-6
• Durene, see 1,2,45-Tetramethylbenzene
• Dynamic viscosity (see Viscosity)
• Dynamically stable foam, 2.12.1-1
• Dyphyl, heat transfer media, 5.5.15-44/5.5.15-45