Index:

M

• McNaught, J. M., 2.6.2-1/2.6.2-19
• Macdonald equation, for fixed-bed pressure drop, 2.2.5-3
• Mach number, 2.2.1-13
• effect in flow in microchannels, 2.13.2-16
• effect on turbulent flow over flat plate, 2.2.1-35
• incompressible duct flows with heat transfer, 2.2.2-13
• Macrolayer consumption model for critical heat flux in pool boiling, 2.7.2-13
• Maddox, R. N., 5.2.2-1/5.2.5-5, 5.5.1-1/5.5.1-62, 5.5.4-1/5.5.4-9
• Magnetic fields, effect on properties of rheologically complex materials, 5.3.8-1/5.3.8-2
• Magnetic devices, for fouling mitigation, 3.17.8-5
• Maintenance, of paintings and coatings, 4.15.5-5/4.15.5-6
• Manifolds (see Headers)
• Marlotherm, heat transfer media, 5.5.15-48/5.5.15-50
• Martensitic stainless steels, 4.5.6-3/4.5.6-5
• Martin, H., 2.4.1-1/2.4.5-4, 2.5.5-1/2.5.6-11, 2.8.4-1/2.8.4-14
• Martinelli and Boelter equations for combined free and forced convection, 2.5.10-2/2.5.10-3
• Martinelli and Nelson correlations:
• for frictional pressure gradient, 2.3.2-10/2.3.2-11
• for void fraction, 2.3.2-14
• Maruyama, S., 2.13.7-1/2.13.7-33
• Mass, conversion of units, xxxi, xlv-lvi
• chart for, l
• Mass absorption coefficient, 2.9.5-2
• Mass extinction coefficient, 2.9.5-2
• Mass flux, unit conversion chart for, lii
• Mass fraction, in multicomponent mixtures, 1.2.1-2
• Mass and heat transfer, combined:
• in condensation, 2.1.6-2/2.1.6-4
• in drying, 2.1.6-1/2.1.6-2
• Mass scattering coefficient, 2.9.5-2
• Mass transfer:
• analogy with heat transfer, 2.1.5-1/2.1.5-4
• in cooling towers, 3.12.2-2/3.12.2-5
• in condensation: in mixtures, 2.6.3-7/2.6.3-25
• of binary mixtures, 2.6.3-7/2.6.3-13
• of multicomponent mixtures, 2.6.3-13/2.6.3-25
• of single vapor with noncondensables, 2.6.3-8
• with impinging jets, 2.5.6-1/2.5.6-10
• in fixed beds, 2.5.4-2/2.5.4-6
• in fluidized beds, 2.5.5-3/2.5.5-6
• in nonuniform systems, 2.1.4-2/2.1.4-4
• volumetric coefficient for, 1.1.2-2
• Mass transfer coefficient:
• in fixed beds, 2.5.4-1/2.5.4-6
• individual definition, 1.2.2-2/1.2.2-3, 2.1.5-2/2.1.5-3
• Materials of construction, for heat exchangers, 4.5.1-1/4.5.3-7
• in EN13445, 4.3.3-2
• materials for corrosive service, 4.5.2-2/4.5.2-6
• austenitic stainless steels, 4.5.2-4
• carbon and low-alloy steels, 4.5.2-2/4.5.2-3, 4.5.4-1/4.5.4-12
• coatings, 4.5.2-5/4.5.2-6
• copper base alloys, 4.5.2-4/4.5.2-5
• explosively clad plate, 4.5.5-1/4.5.5-6
• ferritic chromium stainless steels, 4.5.2-3
• low-alloy steels, 4.5.2-3
• nickel based alloys, 4.5.2-5
• nonmetallic materials, 4.5.2-6
• titanium, 4.5.2-5
• materials for noncorrosive service, 4.5.2-2
• product forms, 4.5.2-1/4.5.2-2
• shells, channels, covers, and bonnets, 4.5.2-1/4.5.2-2
• tubes, 4.5.2-1
• tubesheets, 4.5.2-1
• testing and inspection of, 4.7.2-1
• Mathematical symbols, xli
• Matovosian, Robert, 5.5.5-1/5.5.5-3
• Matrix heat exchangers (see Plate fin heat exchangers)
• Matrix inversion techniques, in radiative heat transfer, 2.9.3-7/2.9.3-8
• Maximum heat flux:
• by conduction in solids, 2.1.1-2
• in condensation, 2.1.7-4/2.1.7-6
• under free molecule conditions in gases, 2.1.1-2
• Maximum mass flux:
• in condensation, 2.1.7-4/2.1.7-6
• under free molecule conditions, 2.1.1-2
• Maximum shear stress, under free molecule conditions, 2.1.1-2
• Maximum velocities (in shell-and-tube heat exchangers), 3.3.5-15, 4.5.3-3
• Maxwell model, for non-Newtonian fluid, 2.2.8-8/2.2.8-9
• Maxwell principle, for physical quantities, xx
• Maxwell-Stefan equations, for multicomponent diffusion, 2.6.3-13
• Maxwell velocity of a vapor, as limiting phenomenon in condensation, 2.1.7-4/2.1.7-6
• Maxwell's equations, for electromagnetic radiation, 2.9.2-7/2.9.2-8
• Mayhew, Y. R., xix-xliii, xlv-lvi
• Mean beam length concept, in radiative heat transfer:
• tables of geometric mean beam lengths, 2.9.6-5
• theory of, 2.9.6-2/2.9.6-3
• Mean phase content, 2.3.1-3
• Mean temperature difference:
• application in shell-and-tube heat exchangers, 3.3.5-17
• concept of, 3.1.1-3/3.1.1-4
• effective, in kettle reboilers, 3.6.2-5
• F-factor correction method for, 1.5.2-1/1.5.3-16
• in air cooled heat exchangers, 3.8.5-3/3.8.5-6
• in condensers, 3.4.8-1/3.4.8-3
• in double pipe heat exchangers, 3.2.3-1/3.2.3-3
• (See also Logarithmic mean temperature difference; Arithmetic mean temperature difference)
• Measurement of fouling resistance, 3.17.4-1/3.17.4-3
• Mechanical agitators, for agitated vessels, 3.14.2-1/3.14.2-2
• heat transfer correlations for, 3.14.3-1/3.14.3-6
• Mechanical design of heat exchangers:
• air-cooled heat exchangers, 4.4.1-1/4.4.1-7
• basic principles, 4.1.1-1/4.1.8-5
• expansion joints, 4.1.6-1
• flanges, 4.1.7-1/4.1.7-2
• gaskets, 4.12.1-1/4.12.5-1
• heads, openings, and branches, 4.1.8-1/4.1.8-3
• introduction to, 4.1.1-1/4.1.1-5
• methods of analysis, 4.1.2-1/4.1.2-12
• shells, 4.1.3-1/4.1.3-3
• tube plates, 4.1.4-1/4.1.4-5
• tubes, 4.1.5-1
• block-type, 4.4.4-4
• direct-contact, 4.4.4-6/4.4.4-8
• double-pipe exchangers, 3.2.5-1/3.2.5-2, 4.4.4-1/4.4.4-2
• EN13445 guidelines for, 4.3.3-1/4.3.3-25
• heat pipes, 4.4.4-9/4.4.4-11
• helical (Hampson) coils, 4.4.4-8/4.4.4-9
• jacketed heaters, 4.4.4-3/4.4.4-4
• plate fin heat exchangers, 4.4.3-1/4.4.3-9
• plate heat exchangers, 4.4.2-1/4.4.2-5
• PN5500 guidelines for, 4.3.2-1/4.3.2-17
• shell-and-tube heat exchangers: constructional features, 4.2.1-1/4.2.6-13
• design codes for, 4.3.1-1/4.3.5-1
• example of design, 4.3.1-1/4.3.6-30
• saddle supports, 4.3.8-1/4.3.8-7
• scraped surface, 4.4.4-5/4.4.4-7
• software for, 4.3.9-1/4.3.9-6
• factors affecting results, 4.3.9-1/4.3.9-2
• software quality, 4.3.9-2/4.3.9-4
• spiral plate, 4.4.4-5
• tubular and panel immersion, 4.4.4-2/4.4.4-3
• waste heat boilers, 3.16.3-1
• Mechanical draft cooling towers, 3.12.1-2/3.12.1-3
• thermal performance and design, 3.12.2-1/3.12.2-15
• Mechanical draft fan coolers, 3.8.2-1/3.8.2-2
• Mechanical loads, specifications in EN13445, 4.3.3-2
• Mechanically agitated systems for direct contact heat transfer, 3.19.1-4
• Mediatherm, heat transfer medium, 5.5.15-51
• Melo, L. F., 3.17.6-19/3.17.6-20
• Melting, thermal conduction in, 2.4.4-1/2.4.4-2
• Melting point:
• estimation of, 5.1.3-8/5.1.3-9
• of commonly used substances, 5.5.1-1/5.5.1-178
• Membrane-wall waste heat boilers, 3.16.2-3/3.16.2-4
• Mercury:
• liquid properties, 5.5.10-171
• saturation properties, 5.5.1-172
• superheated gaseous, physical properties, 5.5.11-174
• thermodynamic properties, 5.5.2-36
• Merilo correlation, for critical heat flux in horizontal tubes, 2.7.4-7/2.7.4-8
• Merkel's equation, in cooling tower design, 3.12.2-2/3.12.2-5
• Mertz, R., 2.13.4-1/2.13.4-27
• Mesitylene, see 1,3,5-Trimethylbenzene
• Metais and Eckert diagrams, for regimes of convection:
• in horizontal pipes, 2.2.6-7, 2.5.10-1/2.5.10-2
• in vertical pipes, 2.5.10-2
• Metals:
• condensation, 2.6.2-15/2.6.2-16
• density, 5.4.1-1
• liquid, single-phase heat transfer in, 2.5.13-1/2.5.13-10
• spectral absorptivity, 2.9.2-11/2.9.2-12
• in thermal energy storage and regenerators, 3.15.9-4
• Metallic coatings, 4.15.5-5
• Metastable equilibrium, of vapor and liquid, 2.7.1-1
• Methane:
• liquid properties, 5.5.10-5
• saturation properties, 5.5.1-9
• superheated gaseous: physical properties, 5.5.11-5
• thermodynamic properties, 5.5.2-2
• transport properties at elevated pressure, 5.5.14-3
• Methanol:
• liquid properties, 5.5.10-61
• saturation properties, 5.5.1-64
• superheated gaseous: physical properties, 5.5.11-61
• thermodynamic properties, 5.5.2-11
• transport properties of gases at elevated pressure, 5.5.14-22
• Methyl acetate:
• liquid properties, 5.5.10-76
• saturation properties, 5.5.1-78
• superheated vapor properties, 5.5.11-76
• Methylacetylene:
• liquid properties, 5.5.10-37
• saturation properties, 5.5.1-40
• superheated vapor properties, 5.5.11-37
• Methyl acrylate:
• liquid properties, 5.5.10-82
• saturation properties, 5.5.1-83
• superheated vapor properties, 5.5.11-82
• Methyl amine
• liquid properties, 5.5.10-138
• saturation properties, 5.5.1-138
• superheated vapor properties, 5.5.11-137
• n-Methylaniline:
• liquid properties, 5.5.10-147
• saturation properties, 5.5.1-147
• superheated vapor properties, 5.5.11-146
• Methyl benzoate:
• liquid properties, 5.5.10-40
• saturation properties, 5.5.1-84
• superheated vapor properties, 5.5.11-83
• Methylbromide (see Bromomethane)
• 2-Methyl-1,3-Butadiene (Isoprene):
• liquid properties, 5.5.10-36
• saturation properties, 5.5.1-39
• superheated vapor properties, 5.5.11-36
• 2-Methylbutane (isopentane):
• liquid properties, 5.5.10-15
• saturation properties, 5.5.1-19
• superheated vapor properties, 5.5.11-15
• Methylbutanoate:
• liquid properties, 5.5.10-81
• saturation properties, 5.5.1-82
• superheated vapor properties, 5.5.11-81
• 2-Methyl-2-butene:
• liquid properties, 5.5.10-31
• saturation properties, 5.5.1-35
• superheated vapor properties, 5.5.11-31
• Methylchloride (see Chloromethane)
• Methylcyclohexane:
• liquid properties, 5.5.10-43
• saturation properties, 5.5.1-46
• superheated vapor properties, 5.5.11-43
• Methylcyclopentane:
• liquid properties, 5.5.10-40
• saturation properties, 5.5.1-43
• superheated vapor properties, 5.5.11-40
• Methylethylketone:
• liquid properties, 5.5.10-90
• saturation properties, 5.5.1-91
• superheated vapor properties, 5.5.11-90
• Methyl formate:
• liquid properties, 5.5.10-74
• saturation properties, 5.5.1-76
• superheated vapor properties, 5.5.11-74
• Methyl fluorate:
• liquid properties, 5.5.10-16
• saturation properties, 5.5.1-108
• 2-Methylhexane:
• liquid properties, 5.5.10-17
• saturation properties, 5.5.1-21
• superheated vapor properties, 5.5.11-17
• Methy iodide (see Iodomethane)
• Methylisobutylketone:
• liquid properties, 5.5.10-91
• saturation properties, 5.5.1-92
• superheated vapor properties, 5.5.11-92
• Methylmercaptan:
• liquid properties, 5.5.10-154
• saturation properties, 5.5.1-153
• superheated vapor properties, 5.5.11-153
• 1-Methylnaphthalene:
• liquid properties, 5.5.10-59
• saturation properties, 5.5.1-62
• superheated vapor properties, 5.5.11-59
• 2-Methylnaphthalene:
• liquid properties, 5.5.10-59
• saturation properties, 5.5.1-62
• superheated vapor properties, 5.5.11-59
• 2-Methylpentane:
• liquid properties, 5.5.10-16
• saturation properties, 5.5.1-20
• superheated vapor properties, 5.5.11-16
• 3-Methylpentane:
• liquid properties, 5.5.10-16
• saturation properties, 5.5.1-20
• superheated vapor properties, 5.5.11-16
• 2-Methylpropane (isobutane):
• liquid properties, 5.5.10-15
• saturation properties, 5.5.1-19
• superheated vapor properties, 5.5.11-15
• 2-Methylpropene:
• liquid properties, 5.5.10-31
• saturation properties, 5.5.1-35
• superheated vapor properties, 5.5.11-31
• Methyl propionate:
• liquid properties, 5.5.10-80
• saturation properties, 5.5.1-81
• superheated vapor properties, 5.5.11-80
• Methylpropylether:
• liquid properties, 5.5.10-101
• saturation properties, 5.5.1-102
• superheated vapor properties, 5.5.11-101
• Methylpropyl ketone:
• liquid properties, 5.5.10-91
• saturation properties, 5.5.1-91
• superheated vapor properties, 5.5.11-91
• Methyl salicylate:
• liquid properties, 5.5.10-84
• saturation properties, 5.5.1-85
• superheated vapor properties, 5.5.11-84
• Methyl-t-butyl ether:
• liquid properties, 5.5.10-102
• saturation properties, 5.5.1-103
• superheated vapor properties, 5.5.11-102
• Microchannels, heat transfer and fluid flow in, 2.13.1-1/2.13.8-26
• boiling and evaporation in, 2.13.4-1/2.13.4-27
• critical heat flux in, 2.13.4-19/2.13.4-23
• flow boiling heat transfer in, 2.13.4-6/2.13.4-13
• models for, 2.13.4-13/2.13.4-14
• onset of nucleate boiling in, 2.13.4-14/2.13.4-16
• pressure drop in, 2.13.4-16/2.13.4-19
• two-phase flow in, 2.13.4-4/2.13.4-6
• void fraction in, 2.13.4-3/2.13.4-4
• condensation in, 2.13.6-1/2.13.6-30
• application of, 2.13.6-1/2.13.6-2
• flow regimes in horizontal channels with, 2.13.6-2/2.13.6-5
• flow regimes in vertical channels with, 2.13.6-5
• heat transfer coefficient in, 2.13.6-19/2.13.6-27
• pressure drop in, 2.13.6-5/2.13.6-19
• in micro heat pipes, 2.13.8-1/2.13.8-26
• applications, 2.13.8-1, 2.13.8-22/2.13.8-23
• experimental studies of, 2.13.8-4/2.13.8-14
• modelling of, 2.13.8-14/2.13.8-22
• types of heat pipe, 2.13.8-1/2.13.8-4
• introduction to, 2.13.1-1/2.13.1-3
• molecular dynamics methods for, 2.13.7-1/2.13.7-33
• applications in macroscale and nanoscale heat transfer, 2.13.7-13/2.13.7-26
• basic method of, 2.13.7-2/2.13.7-13
• nanoscale heat transfer, 2.13.7-13/2.13.7-26
• single phase convective heat transfer in, 2.13.3-1/2.13.3-17
• in circular microchannels (micropipes) 2.13.3-2/2.13.3-8
• in non-circular microchannels, 2.13.3-8
• interfacial effects in, 2.13.3-13/2.13.3-14
• laminar, 2.13.3-8/2.13.3-11
• theoretical analyses for, 2.13.3-12/2.13.3-13
• turbulent, 2.13.3-11/2.13.3-12
• single-phase fluid flow in, 2.13.2-1/2.13.2-20
• compressibility effects in, 2.13.2-13/2.13.2-18
• effects of electrostatic charges on, 2.13.2-10/2.13.2-11
• effects of surface roughness on, 2.13.2-5/2.13.2-9
• friction factors in incompressible flow in, 2.13.2-1/2.13.2-11
• laminar-turbulent transition in, 2.13.2-11/2.13.2-13
• two-phase flow in, 2.13.5-1/2.13.5-20
• flow patterns in, 2.13.5-5/2.13.5-12
• 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
• studies of, 2.13.5-2/2.13.5-4
• void fraction in, 2.13.5-12/2.13.5-14
• Micro-fin tubes, in augmentation of condensation, 2.6.6-18/2.6.6-20, 2.6.6-25
• Micropipes (circular microchannels), single phase heat transfer in, 2.13.1-1/2.13.1-3
• Microsystems, description of, 2.13.1-1/2.13.1-3
• Mie scattering, in pulverized coal combustion, 2.9.8-17
• Miller, C. J., 4.5.4-1/4.5.4-12, 4.5.6-1/4.5.6-14
• Miller, E. R., 3.17.6-22/3.17.6-25, 3.17.7-11/3.17.7-14, 3.17.8-19/3.17.8-22
• Mineral oils, as heat transfer media, physical properties of, 5.5.15-28/5.5.15-39
• Minimum fluidization velocity, 2.2.6-3/2.2.6-5
• Minimum heat flux in pool boiling:
• of binary and multicomponent mixtures, 2.7.7-5/2.7.7-6
• of pure components, 2.7.2-13/2.7.2-14
• Minimum tubeside velocity, in shell-and-tube heat exchangers, 3.3.5-16
• Minimum velocity for fluidization, 2.2.6-3/2.2.6-5
• Minimum wetting rate, for binary mixtures, 2.7.8-11
• Mirror-image concept, in radiative heat transfer, 2.9.4-1/2.9.4-2
• Mirrors, spectral characteristics of reflectance from, 2.9.2-17
• Mist flow:
• in axial flow reboilers, 3.6.2-12
• heat transfer in (see Postdryout heat transfer)
• onset, as mechanism for critical heat flux in reboilers, 3.6.2-10/3.6.2-12
• Mitigation of fouling, 3.17.8-1/3.17.8-13
• chemical treatment, 3.17.8-5/3.17.8-8
• in gas side fouling, 3.17.8-8/3.17.8-13
• physical techniques, 3.17.8-1/3.17.8-5
• Mixed convection occurrence in horiozntal circular pipe, Metais and Eckert diagram for, 2.2.2-7
• in porous media, 2.11.7-1
• Mixing length, in turbulent flow, 2.2.1-17
• Mixing vessel (see Agitated vessel)
• Mixtures:
• condensers for, 3.4.4-2/3.4.4-3
• of gases, radiation properties, 2.9.5-11/2.9.5-12
• (See also Binary mixtures; Multicomponent mixtures)
• Modelling, of fouling:
• computer simulation, 3.17.4-2
• laboratory, 3.17.4-2
• on-line, 3.17.4-1/3.17.4-2
• Models, theory of, 2.2.1-15
• Modes of heat transfer, Nusselt description, 2.1.0-2
• Modulus of elasticity:
• aluminum alloys, 5.5.12-11
• carbon and low-alloy steels, 5.5.12-3/5.5.12-6
• cast iron, 5.5.12-12
• copper and copper alloys, 5.5.12-10
• for heat exchanger construction materials, 5.5.12-1/5.5.12-13
• high chrome steels, 5.5.12-7/5.5.12-8
• nickel and nickel alloys, 5.5.12-8/5.5.12-9
• titanium, 5.5.12-12
• zirconium, 5.5.12-12
• (See also Young's modulus)
• Moffat, R. S. M., 4.7.11-1/4.7.11-7
• Molecular dynamics methods, 2.13.7-1/2.13.7-33
• applications to microscale systems, 2.13.7-13/2.13.7-26
• heat conduction and heat transfer, 2.13.7-12/2.13.7-26
• interaction of fluids with carbon nanotubes, 2.13.7-20
• nucleation and phase change, 2.13.7-20/2.13.7-23
• liquid-vapour interface, 2.13.7-13/2.13.7-15
• solid-liquid-vapour interactions, 2.13.7-15/2.13.7-19
• basic method of, 2.13.7-2/2.13.7-13
• boundary and initial conditions for, 2.13.7-10/2.13.7-12
• effective pair potential for water, 2.13.7-4/2.13.7-7
• embedded atom method (EAM) for potential, 2.13.7-7 2.13.7-10
• equation of motion and potential function, 2.13.7-2
• integration of Newtonian equation for, 2.13.7-10
• Lennard-Jones potential, 2.13.7-3/2.13.7-4
• many bodied potential for carbon and silicon, 2.13.7-6 2.13.7-7
• pair potential for solid metals, 2.13.7-7/2.13.7-10
• potential for larger molecules in liquid phase, 2.13.7-5/2.13.7-6
• prediction of thermophysical properties using, 2.13.7-12/2.13.7-13
• Molecular gas radiation properties, 2.9.5-8/2.9.5-11
• Molecular weight:
• of commonly used fluids, 5.5.1-1/5.5.1-178, 5.5.10-1/5.5.10-175, 5.5.11-1/5.5.11-174
• Mollier chart, for humid air, 3.13.1-1
• description of drying processes in terms of, 3.13.3-4/3.13.3-5
• Momentum equation:
• in boundary layer, 2.2.1-20
• in compressible duct flow, 2.2.2-12
• differential form for single-phase flow, 2.2.1-6/2.2.1-9
• in gas-liquid flows, 2.3.2-8/2.3.2-9
• homogeneous model, 2.3.2-8
• separated flow model, 2.3.2-8/2.3.2-9
• in heat exchanger calculations, 1.2.6-5/1.2.6-7
• integral form for single-phase flow, 2.2.1-2/2.2.1-6
• in multiphase flows: homogeneous flow, 2.3.1-5
• separated flow, 2.3.1-7
• in non-Newtonian flow, 2.5.12-5
• in turbulent flow, 2.2.1-16
• Monitoring, on line, of fouling, 3.17.4-1
• Monochloroacetic acid:
• liquid properties, 5.5.10-98
• superheated vapor properties, 5.5.11-98
• Monotube waste heat boilers, 3.16.2-8
• Monte Carlo methods, in radiative heat transfer, 2.9.4-2/2.9.4-5
• for radiative heat transfer with an isothermal gas, 2.9.6-8/2.9.6-9
• Moody chart:
• for critical two-phase flow, 2.3.2-28
• for single-phase friction factor in circular pipes, 1.2.3-3, 2.2.2-2
• Morris, M., 4.3.1-1/4.3.1-5, 4.3.4-1/4.3.5-11, 4.3.6-1/4.3.6-30, 4.10.1-1/4.10.2-8, 4.13.1-1/4.13.6-3, 4.14.1-1/4.14.8-4
• Mostinski correlations:
• for critical heat flux, 3.6.2-5
• for nucleate boiling, 2.7.2-5
• application to kettle reboilers, 3.6.2-1
• Moving bed, heat transfer to, 2.8.3-3/2.8.3-7
• Moving belt, heat transfer to, 2.1.3-2/2.1.3-3
• MSF, see Multiphase flash evaporation
• Muchowski, E., 2.8.3-1/2.8.3-9
• Mueller, A. C., 3.4.2-1/3.4.4-3, 3.4.6-1/3.4.9-5
• Muller-Steinhagen, H., 3.17.6-7/3.17.6-8, 3.17.7-3, 3.17.7-22/3.17.7-23
• Multicomponent mixtures:
• air-cooled condensers for, 3.8.9-3/3.8.9-4
• boiling of, in kettle reboilers, 3.6.2-4/3.6.2-5
• boiling of, in evaporators, 3.5.7-4/3.5.7-5
• condensation of, 2.6.3-7/2.6.3-9, 2.6.4-1/2.6.4-16
• diffusion in, 2.1.5-1/2.1.5-4
• forced convective boiling of, 2.7.8-1/2.7.8-14
• combined heat and mass transfer in, 2.7.8-2/2.7.8-9
• critical heat flux in, 2.7.8-9/2.7.8-11
• maldistribution effects in, 2.7.8-5/2.7.8-9
• saturated nucleate, 2.7.8-1/2.7.8-2
• two-phase forced convective, 2.7.8-2/2.7.8-11
• of gases, radiation properties of, 2.9.5-11/2.9.5-12
• phase equilibria in, 2.7.6-3/2.7.6-5
• physical properties, 5.2.1-1/5.2.5-5
• diffusion coefficients, 5.2.5-1/5.2.5-5
• interfacial tension, 5.2.4-1/5.2.4-3
• thermodynamic properties, 5.2.2-1/5.2.2-9
• thermophysical properties, 5.2.3-1/5.2.3-9
• pool boiling, 2.7.7-1/2.7.7-11
• critical heat flux, 2.7.7-6/2.7.7-8
• film boiling, 2.7.7-8/2.7.7-9
• minimum heat flux, 2.7.7-8
• nucleate boiling, 2.7.7-1/2.7.7-6
• transition boiling, 2.7.7-8
• Multidimensional systems, heat conduction in, 2.4.3-10/2.4.3-12
• Multiflux methods, for radiative heat transfer in nonisothermal gases, 2.9.7-6/2.9.7-7
• Multipass shell-and-tube heat exchangers, 1.1.1-2
• Multiphase fluid flow and pressure drop:
• introduction and fundamentals, 2.3.1-1/2.3.1-10
• classification of multiphase flows, 2.3.1-1/2.3.1-2
• conservation equations for, 2.3.1-3/2.3.1-7
• design parameters in, 2.3.1-2/2.3.1-3
• drift flux models for, 2.3.1-7/2.3.1-10
• liquid-liquid-gas flow, 2.3.6-1/2.3.6-10
• annular flow in, 2.3.6-3
• bubbly flow in, 2.3.6-3
• flow patterns in, 2.3.6-1/2.3.6-4
• homogeneous model for, 2.3.6-8/2.3.6-9
• phase inversion in, 2.3.6-9
• slug flow in, 2.3.6-1/2.3.6-3, 2.3.6-7/2.3.6-8
• stratified flow in, 2.3.6-1, 2.3.6-4/2.3.6-6
• liquid-liquid flow, 2.3.5-1/2.3.5-40
• core annular, 2.3.5-10/2.3.5-14
• dispersed, 2.3.5-14/2.3.5-24
• flow patterns, 2.3.5-1/2.3.5-7
• stratified, 2.3.5-7/2.3.5-10
• solid-gas flow, 2.3.3-1/2.3.3-10
• flow patterns in, 2.3.3-2
• pressure drop in, 2.3.3-2, 2.3.3-4/2.3.3-8
• principles of pneumatic conveyance, 2.3.3-1/2.3.3-2
• solid-liquid flow, 2.3.4-1/2.3.4-7
• flow regimes in, 2.3.4-1/2.3.4-2
• pressure drop in, 2.3.4-3/2.3.4-6
• Multiple duties, in plate heat exchangers, 3.7.1-2
• Multiple effect evaporation, 3.5.3-1/3.5.3-2
• in plate evaporators, 3.7.4-2/3.7.4-3
• Multiple hairpin heat exchanger, 3.1.2-2
• Multirod clusters (see Rod bundles)
• Multistage flash evaporation (MSF)
• brine transfer devices in, 3.22.2-30/3.22.2-34
• condenser/preheater tubes in, 3.22.2-8/3.22.2-11
• heat transfer equations for, 3.22.2-9/3.22.2-11
• tube configurations for, 3.22.2-9
• tube materials for, 3.22.2-8/3.22.2-9
• ejectors for, 3.22.2-14/3.22.2-23
• fundamentals of, 3.22.2-14/3.22.2-15
• models for, 3.22.2-15/3.22.2-23
• mathematical models for
• once through (MSF-OT), 3.22.2-40/3.22.2-45
• with brine recirculation (MSF), 3.22.2-45/3.22.2-50
• processes in:
• once through (MSF-OT), 3.22.2-4/3.22.2-5
• with brine recirculation (MSF), 3.22.2-5/3.22.2-7
• venting systems for, 3.22.2-11/3.22.2-14
• design of vent line orifice, 3.22.2-12/3.22.2-14
• wire mesh demisters for, 3.22.2-23/3.22.2-30
• Multizone model, for furnaces, 3.11.6-1/3.11.6-4
• Murray, I., 4.4.4-1/4.4.4-11