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Heat Exchanger Design Handbook - Online

Links to:
HEDH 2002
HEDU

Index:

A B C D E F G H I J K L M N O P Q R S T U V W X Y Z

O

  • Oberbeck-Boussinesq approximation, for natural convection in porous media, 2.11.5-1
  • Oblate spheroids, free convective heat transfer from, 2.5.7-25
  • Ocean Thermal Energy Conversion (OTEC), 3.22.3-1/3.22.3-20
    • closed cycle OTEC, 3.22.3-3/3.22.3-5
    • condensers for, 3.22.3-12/3.22.3-15
    • evaporators, for, 3.22.3-12/3.22.3-15
    • flash evaporation systems in, 3.22.3-9/3.22.3-12
      • orifice/weir flashing, 3.22.3-11/3.22.3-12
      • spray flashing, 3.22.3-10/3.22.3-11
    • hybrid cycle OTEC, 3.22.3-7/3.22.3-8
    • in water desalination, 3.22.3-17
    • open cycle OTEC, 3.22.3-5/3.22.3-6
    • working fluids for, 3.22.3-8/3.22.3-9
  • Octadecane:
    • liquid properties, 5.5.10-13
    • saturation properties, 5.5.1-17
    • superheated vapor properties, 5.5.11-13
    • transport properties of gases at elevated pressure, 5.5.14-19
  • Octadecene:
    • liquid properties, 5.5.10-27
    • saturation properties, 5.5.1-31
    • superheated vapor properties, 5.5.11-27
  • Octane:
    • liquid properties, 5.5.10-8
    • saturation properties, 5.5.1-12
    • superheated vapor properties, 5.5.11-8
    • transport properties at elevated pressures, 5.5.14-10
  • 1-Octanol:
    • liquid properties, 5.5.10-64
    • saturation properties, 5.5.1-67
    • superheated vapor properties, 5.5.11-64
  • 1-Octene:
    • liquid properties, 5.5.10-22
    • saturation properties, 5.5.1-26
    • superheated vapor properties, 5.5.11-22
  • Octafluorocyclobutane (Refrigerant C318)
    • liquid properties, 5.5.10-134
    • thermodynamic properties of, 5.5.2-20
    • saturation properties, 5.5.1-134
    • superheated vapor properteis, 5.5.11-133
    • thermal conductivity at elevated pressures, 5.5.14-40
  • OEST, heat transfer medium, 5.5.15-54
  • Ohm (SI unit), xxviii
  • Oldroyd eight constant model, for non-Newtonian fluid, 2.2.8-9
  • Olefins:
    • liquid properties, 5.5.10-19/5.5.10-36
    • saturated properties, 5.5.1-23/5.5.1-39
    • superheated vapor properties, 5.5.11-19/5.5.11-36
    • transport properties at elevated pressure, 5.5.14-15/5.5.14-19
  • Olex, heat transfer medium, 5.5.15-45
  • ONB (onset of nucleate boiling):
    • in pool boiling, 2.7.2-2/2.7.2-3
    • in subcooled boiling in vertical tubes, 2.7.3-6/2.7.3-8
  • Once-through cooling towers, 3.12.1-4
  • Once-through multistage flash evaporators, (MSF-OT)
    • processes in, 3.22.2-5
    • mathematical models for, 3.22.2-40/3.22.2-50
  • One-equation models, for turbulent boundary layers, 2.2.1-18
  • Open-circuit cooling towers, 3.12.1-4
  • Openings, mechanical design aspects, 4.1.8-1/4.1.8-2
  • Operational envelope of a heat pipe, 3.10.4-1
  • Operational problems:
    • of condensers, 3.4.5-1/3.4.5-3
    • of heat exchangers, 3.18.1-1/3.18.6-3
  • Opposed convection:
    • around immersed bodies, 2.5.9-11
    • in vertical tubes, 2.5.10-6
  • Optimization methods, for heat exchanger design, 3.3.4-2
  • Organic compounds, aqueous solutions of, as heat transfer media, 5.5.15-7/5.5.15-11
  • Organic solids, density, 5.4.1-2
  • Organic sulfur compounds:
    • liquid properties, 5.5.10-154/5.5.10-156
    • superheated vapor properties, 5.5.11-153/5.5.11-155
  • Organic vapours, dropwise condensation of, 2.6.5-8/2.6.5-9
  • Orifices:
    • loss coefficients in, 2.2.2-21
    • two-phase gas liquid flow, 2.3.2-17/2.3.2-18
  • Orifice baffles, in tube bundles with longitudinal flow, 3.3.12-6
    • design considerations for, 3.3.12-13/3.3.12-15
    • heat transfer with, 3.3.12-10/3.3.12-12
    • pressure drop with, 3.3.12-7/3.3.12-10
  • O-ring seal, hollow metal, 4.14.8-1
  • OTEC, (see Ocean Thermal Energy Conversion)
  • OTL (see Outer tube limit)
  • Outer tube limit, in shell-and-tube heat exchangers, 4.2.5-9
  • Outlet effects, in shell-and-tube heat exchangers, 3.3.6-9/3.3.6-10
  • Overall heat transfer coefficient, 2.1.2-1
    • in air-cooled heat exchangers, 3.8.5-1/3.8.5-5
    • approximate values: in shell-and-tube heat exchangers, 3.1.4-4/3.1.4-5
      • in liquid metal heat exchangers, 2.5.13-3
      • in various heat exchangers, 2.1.2-3/2.1.2-4
  • Overall power hypothesis, for critical heat flux in flow boiling, 2.7.3-24
  • Overcapacity, in condensers, 3.4.5-1/3.4.5-2
  • Oxygen:
    • liquid properties, 5.5.10-168
    • saturation properties, 5.5.1-169
    • superheated gaseous: physical properties, 5.5.11-170
      • thermodynamic properties, 5.5.2-33
      • transport properties at elevated pressure, 5.5.14-53