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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

G

  • G-type shells in shell-and-tube heat exchangers:
    • description, 3.3.4-3
    • temperature difference correction factor (F) and ?-NTU chart for, 1.5.2-16
  • Gaddis, E. S., 1.6.1-1/1.6.12-1
  • Galerkin method, for heat conduction finite-element calculations, 2.4.8-11/2.4.8-17
  • Galileo number, 2.2.1-11
    • in bubble rise in liquids, 2.3.2-19
  • Gap number, in thermal contact resistance, 2.4.6-3
  • Gas constant, xxxiii
  • Gas heater, approximate overall heat transfer coefficients in, 2.1.2-3
  • Gas-liquid flows:
    • applications of one-dimensional equations, 2.3.2-7/2.3.2-18
      • conservation equations, 2.3.2-8/2.3.2-9
      • correlation for void fraction, 2.3.2-13/2.3.2-15
      • frictional pressure drop in straight channels, 2.3.2-9/2.3.2-12
      • pressure changes across singularities, 2.3.2-15/2.3.2-18
      • pressure drop in heat exchangers, 2.3.2-12/2.3.2-13
    • critical two-phase flow, 2.3.2-26/2.3.2-29
    • flow patterns in, 2.3.2-1/2.3.2-7
      • horizontal tubes, 2.3.2-2/2.3.2-4
      • shell-and-tube heat exchangers, 2.3.2-5/2.3.2-6
      • in systems with phase change, 2.3.2-6/2.3.2-7
      • inclined tubes, 2.3.2-4/2.3.2-5
      • vertical tubes, 2.3.2-1/2.3.2-2
    • hydrodynamics of specific flow regimes (horizontal), 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
    • hydrodynamics of specific flow regimes (vertical), 2.3.2-18/2.3.2-23
      • annular flow, 2.3.2-19/2.3.2-21
      • bubble flow, 2.3.2-18/2.3.2-19
      • countercurrent flow and flooding, 2.3.2-21/2.3.2-23
      • plug-slug flow, 2.3.2-19
    • in microchannels, 2.13.5-1/2.13.5-20
      • flow patterns in, 2.13.5-5/2.13.5-12
      • in boiling in, 2.13.4-4/2.13.4-6
      • in condensation in, 2.13.6-5/2.13.6-19
      • phase inlet configuration for studies of, 2.13.5-2/2.13.5-4
      • pressure drop in, 2.13.5-14/2.13.5-17
      • void fraction in, 2.13.5-12/2.13.5-14
    • in plate heat exchangers, 3.7.3-5
  • Gas-liquid-liquid flows, see Liquid-liquid-gas flows
  • Gas-liquid-solid interfaces, fouling at, 3.17.2-14
  • Gas-solid flow (see Solid-gas flow)
  • Gas-solid interfaces, fouling at, 3.17.2-1/3.17.2-2
  • Gas sparging, for agitation of vessels:
    • description, 3.14.2-1/3.14.2-2
    • heat transfer with, 3.14.3-3
  • Gas tungsten arc welding, 4.11.3-1/4.11.3-5
  • Gaseous fuels, properties of, 3.11.3-2
  • Gases:
    • as constituent of multiphase flows, 2.3.1-2
    • density of pure, 5.1.2-1/5.1.2-9
      • corresponding states principle for, 5.1.2-1/5.1.2-7
      • virial equation for, 5.1.2-7/5.1.2-9
    • diffusion coefficients in, 5.2.5-3/5.2.5-4
    • emissivity of, 2.9.5-1/2.9.5-13
      • table of, 5.5.5-1/5.5.5-4
    • emissivity of combustion product mixtures of, 3.11.3-4, 5.5.5-3/5.5.5-4
    • isothermal, radiative heat transfer in, 2.9.6-1/2.9.6-9
    • nonisothermal, radiative heat transfer in, 2.9.7-1/2.9.7-13
    • radiation properties, 2.9.5-1/2.9.5-12
      • equation of transfer for, 2.9.5-1/2.9.5-2
      • gas mixtures, 2.9.5-11/2.9.5-12
      • measurement of, 2.9.5-2/2.9.5-4
      • molecular, 2.9.5-8/2.9.5-11
      • physics of, 2.9.5-4
      • spectral, band and total property definition, 2.9.5-4/2.9.5-8
    • superheated, thermodynamic properties of, tables, 5.5.2-1/5.5.2-21
    • transport properties tables: for low pressure, 5.5.11-1/5.5.11-174
      • for elevated pressure, 5.5.14-1/5.5.14-56
  • Gasketed plate heat exchangers (see Plate heat exchangers)
  • Gaskets:
    • for shell-and-tube heat exchangers, 4.12.1-1/4.12.5-1
      • assembly and bolting up, 4.12.5-1
      • flange surface finish for, 4.12.4-1
      • materials for, 4.12.2-1/4.12.2-6
      • specification of, 4.12.3-1/4.12.3-2
    • for graphite block exchangers, 4.4.4-4
    • in plate heat exchangers, design and properties, 4.4.2-4/4.4.2-5
    • pressure energised, 4.14.8-1/4.14.8-2
      • Delta ring seal, 4.14.8-1/4.14.8-2
      • hollow-metal o-ring seal, 4.14.8-1
  • Gauss-Seidel method, for solution of implicit equations, 2.4.7-21/2.4.7-22
    • program for, 2.4.7-32/2.4.7-33
  • Gee, C., 4.12.1-1, 4.12.3-1/4.12.5-1
  • Geometric optics models for radiative heat transfer from surfaces, 2.9.4-8
  • geothermal brines, fouling of heat exchangers by, 3.17.6-16/3.17.6-17
  • Germany, Federal Republic of, mechanical design of heat exchangers in:
    • guide to national practice, 4.3.5-4
  • Gersten, K., 2.2.1-1/2.2.3-9
  • Girth flanges, in shell-and-tube heat exchangers, 4.14.2, 4.14.5-1/4.14.5-3
    • constructional details of, 4.2.6-3
    • design of, 4.14.5-1/4.14.5-3
    • EN13445 code rules for, 4.3.3-7/4.3.3-9, 4.3.3-16/4.3.3-18
      • alternative rules for, 4.3.3-16/4.3.3-18
      • comparison of EN13445 method with original Taylor Forge method, 4.3.3-8/4.3.3-9
      • lap jointed, 4.3.3-9
      • with full face gaskets, 4.3.3-9
    • PD5500 code rules for, 4.3.2-7/4.3.2-9
  • Glycerol (glycerine):
    • liquid properties, 5.5.10-71
    • saturation properties, 5.5.1-72
    • superheated vapor properties, 5.5.11-71
  • Gn (heat generation number), 2.5.12-6
  • Gnielinski, V., 2.5.1-1/2.5.4-6, 2.5.14-1/2.5.14-4
  • Gnielinski correlation, for heat transfer in tube banks, 2.5.3-5/2.5.3-9
  • Gomez-Thodas method, for vapour pressure, 5.1.3-2/5.1.3-3
  • Goodness factor, as a basis for comparison of plate fin heat exchanger surfaces, 3.9.7-1/3.9.7-3
  • Goody narrow band model for gas radiation properties, 2.9.5-5
  • Gorenflo correlation, for nucleate boiling, 2.7.2-8/2.7.2-10
  • Graetz number:
    • definition, 1.2.3-5, 2.1.3-2
    • in non-Newtonian flows, 2.5.12-6/2.5.12-7
  • Graetz problem (see Nusselt-Graetz problem)
  • Granular products, moving, heat transfer to, 2.8.3-1/2.8.3-7
  • Graphite, density of, 5.4.1-1
  • Graphite block heat exchanger, 4.4.4-4
  • Graphite, exfoliated, for gaskets, 4.12.2-2
  • Graphs, labeling of, xxixxii
  • Grashof number, 1.2.3-4, 2.2.1-11, 2.2.2-6
    • in free convection over immersed bodies, 2.5.7-2
  • Gravitational acceleration, effect in pool boiling, 2.7.2-9
  • Gravity conveyor:
    • air-activated, 2.3.3-2
    • fluidized bed, 2.3.3-7/2.3.3-9
  • Gray (SI unit), xxviii
  • Gregorig effect in enhancement of condensation, 2.6.6-4
  • Grid baffles:
    • in longitudinal flow over tube bundles, 3.3.12-4/3.3.12-6
    • heat transfer in, 3.3.12-10/3.3.12-12
    • mechanism of flow in, 3.3.12-6/3.3.12-7
    • orifice baffles, 3.3.12-6
    • pressure drop in, 3.3.12-7/3.3.12-10
    • rod baffles, 3.3.12-4/3.3.12-5
    • strip baffles, 3.3.12-5/3.3.12-6
    • use with low finned tubes, 3.3.12-12/3.3.12-13
  • Grid selection, for finite difference method, 2.4.7-3/2.4.7-5
  • Groeneveld correlation for postdryout heat transfer, 2.7.3-31
  • Groeneveld and Delorme correlation for postdryout heat transfer, 2.7.3-41
  • Groll, M., 2.13.3-1/2.13.3-27, 2.13.8-1/2.13.8-26
  • Gross plastic deformation
    • EN13445 guidelines on, 4.3.3-18/4.3.3-19
    • PD5500 guidelines on, 4.3.2-13/4.3.2-14
  • Group contribution parameters tables, 5.5.4-10
  • Guerrieri and Talty correlations for forced convective heat transfer in two-phase flow, 2.7.3-13
  • Gungor and Winterton correlation, for forced convective boiling, 2.7.3-26
  • Guo, Z. Y., 2.13.2-1/2.13.1-20
  • Gylys, J., 2.12.1-1/2.12.2-10