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Tables, labeling of, xxixxiiTaborek, J, xlv-lvi1.5.2-1/1.5.3-15, 2.4.9-1/2.4.9-17, 3.2.1-1/3.2.3-3, 3.3.1-1/3.3.12-17Taitel and Dukler flow regime map, for horizontal and inclined gas- liquid flows,2.3.2-3/2.3.2-4Tamura et al correlation, for surface tension of mixtures,5.2.4-2/5.2.4-4Tapes, twisted (see Twisted tapes)Taylor Forge method, for mechanical design of flanges, comparison with EN13445 method,4.3.3-8/4.3.3-9Taylor series expansion,2.4.7-4TCC, see Thermal contact conductanceTCR, see Thermal contact resisteanceTeflon, use in heat transfer enhancement:TEMA (Tubular Exchanger Manufacturers Association):Temperature, conversion of units for, xxvi, xlv-lviTemperature-dependent physical properties (see Physical properties, variation with temperature)Temperature distribution:Tenders for heat exchangers,4.9.3-1/4.9.3-4Terminal free fall velocity, in fluidization,2.2.6-5Ternary mixtures, diffusion and mass transfer in,2.1.5-4Tesla (SI unit), xxviiiTesting and inspection of heat exchangers:Tetrabromomethane:1,1,2,2-Tetrachloroethane:Tetrachloroethylene:Tetradecane:Tetradecene:Tetrachlorodifluoroethane (Refrigerant 112):1,1,1,2-Tetrafluoroethane (Refrigerant R134a):Tetrafluoromethane (Refrigerant 14):Tetrahydrofuran:1,2,3,4-Tetramethylbenzene:1,2,3,5-Tetramethylbenzene:1,2,4,5-Tetramethylbenzene:Thermal conduction (see Conduction, heat)Thermal conductivity:
UVWXYZconversion units for, xxxi, xlv-lvieffective, in fixed beds:effective, of wicks in heat pipes,3.10.3-1/3.10.3-2of fluids at elevated pressures,5.5.14-1/5.5.14-56of heat exchanger construction materials3.3.5-5, 5.5.12-1/5.5.12-13of heat transfer media,5.5.15-1/5.5.15-42of heavy water,5.5.9-2of liquid water,5.5.3-3of liquids below their boiling point,5.5.10-1/5.5.10-78of multicomponent mixtures,5.2.3-7/5.2.3-8of polymers,2.5.12-2/2.5.12-3of porous media,2.11.2-1of pure fluids,5.1.4-5/5.1.4-17of rheologically complex materials,5.3.1-1/5.3.2-3of saturated vapors and liquids,5.5.1-1/5.5.1-178of seawater,5.5.13-2of solids,5.4.3-1/5.4.3-3of superheated gases,5.5.11-1/5.5.11-175of water,5.3.3-26/5.3.3-27
Thermal contact conductance (TCC),2.4.6-1/2.4.6-7Thermal contact resistance (TCR),2.4.6-1/2.4.6-7Thermal design, constructional features affecting, in shell-and-tube heat exchangers3.1.1-1, 3.1.4-9, 4.2.5-1/4.2.5-23Thermal design integral,1.5.1-1/1.5.1-2Thermal diffusivity:Thermal energy storage:Thermal expansion, effect of, in shell-and-tube heat exchangers,3.3.4-4Thermal expansion coefficient:Thermal leakage in F-type shell-and-tube heat exchangers,1.5.2-17Thermal mixing in plate heat exchangers,3.7.2-3/3.7.2-5Thermal storage materials,3.15.0-3/3.15.0-4Thermal stress:Thermocal, heat transfer media,5.5.15-50/5.5.15-51Thermodynamic cycles in refrigeration,3.26.2-1/3.26.2-5Thermodynamic properties:Thermodynamic surface in radiative heat transfer,2.9.1-1/2.9.1-2Thermoexel surface, for enhancement of boiling,2.7.9-2Thermofluids, heat transfer medium,5.5.15-44Thermophysical properties:ThermosiphonThermosiphon reboilers (see Vertical thermosiphon reboilers; Horizontal thermosiphon reboilers)Theta (Dimensionless temperature difference)1.5.1-4Theta-NTU method:Thickness of boundary layers (displacement, momentum, energy, density, temperature),2.2.1-23Thin-wall-type expansion bellows,4.10.2-1/4.10.2-2Thiophene:Thome, J R2.13.4-1/2.13.4-27, 2.7.9-1/2.7.9-48Three-phase flows:Tie rods in shell-and-tube heat exchangers,4.2.5-8/4.2.5-9Tinker method for shell-side heat transfer in shell-and-tube heat exchangers,3.3.2-3/3.3.2-6Titanium and titanium alloys,4.5.9-1/4.5.9-15T-junctions, loss coefficients in,2.2.2-21TolerancesToluene:m-Toluidine:Tong F-factor method, for critical heat flux with nonuniform heating,2.7.3-24/2.7.3-25Tooth, A S,4.3.8-1/4.3.8-32Toroidal shells, mechanical design,4.1.3-2Torque wrench,4.13.6-2Total emissivity in gases,2.9.5-5Transcendental equations in transient conduction,2.4.3-4Transient behavior:Transition boiling:Transition flow, heat transfer in free convective flow over vertical surfaces in,2.5.7-4/2.5.7-5Transition, laminar/turbulent, in microchannels,2.13.2-11/2.13.2-13Transitional flow, in combined free and forced convection,2.5.10-8/2.5.10-11Transmission of thermal radiation in solids:Transmissivity of solids:Transport phenomena, approximate model for in dilute cases,2.1.1-1Transport properties:Transverse flow, combined free and forced convection in,2.5.9-4/2.5.9-6Treated surfaces, for augmentation of heat transfer,2.5.11-5Triangular duct:Triangular fins, in plate fin exchangers,3.9.3-1Triangular relationship, in annular gas-liquid flow,2.3.2-20Tribromomethane:1,1,1-Trichloroethane (Refrigerant 140a):Trichloroethylene:Trichlorofluoromethane (Refrigerant 11)Trichloromethane (Chloroform) (Refrigerant 20):1,1,2-Trichlorotrifluoroethane (Refrigerant 113):Tridecane:Tridecene:Triethylamine:1,1,1-Trifluoroethane (Refrigerant 143a):Trifluoromethane (Refrigerant 23):Trimethylamine:1,2,3-Trimethylbenzene:1,2,4-Trimethylbenzene:1,3,5-Trimethylbenzene:2,2,4-Trimethylpentane (Isooctane):Triphenylmethane:Triple interface (gas/solid/liquid),2.3.1-2True temperature difference, in double pipe exchangers,3.2.3-4Truelove, J S,3.11.1-1/3.11.7-6Tsotsas, E2.8.1-1/2.8.1-13, 2.8.2-1/2.8.2-17, 2.8.3-1/2.8.3-7Tube-baffle damage, in heat exchangers,4.5.3-3Tube banks, finned:Tube banks, plain:Tube banks, roughened tubes, effect of roughness on Euler number in,2.2.4-14/2.2.4-15Tube bundles:Tube counts, in shell-and-tube heat exchangers:Tube end attachment, in shell-and-tube heat exchangers,4.11.1-1/4.11.4-6Tube failure, see Tube ruptureTube inserts, heat exchangers with,3.21.1-1/3.21.2-9Tube-in-plate extended surface configurations, fin efficiency of,2.5.3-10Tube plates, in shell-and-tube heat exchangers:Tube rupture in shell-and-tube heat exchangers,4.17.2-1/4.17.2-15Tube-side passes (see Passes, tube-side)Tube-to-tubesheet attachment, in shell-and-tube heat exchangers,4.11.1-1/4.11.2-6Tubes:Tubesheets, in shell-and-tube heat exchangers (see Tube plates)Tubular Exchanger Manufacturers Association (see TEMA)Tubular immersion exchangers,4.4.4-2/4.4.4-3Tubular reactor, nonuniform heat and mass transfer in,2.1.4-3/2.1.4-4Tucker, R J,3.11.3-1/3.11.7-7Tunnel dryer,3.13.2-4Turbine agitators:Turbine exhaust condensers:Turbines, lost work inTurbulence:Turbulent boundary layers:Turbulent buffeting, as source of tube vibration,4.6.4-2Turbulent energy, integral equation for,2.2.1-20Turbulent flow:Turbulent pipe contactor, for direct contact heat transfer,3.19.1-4Turbulent transport properties,2.1.1-3Turnarounds, in heat exchangers,2.2.7-1Turner, C W,3.17.9-1/3.17.9-14Twisted tapes:Twisted tube heat exchangers,3.23.1-1/3.23.4-4Twisted tubesTwo-equation models, for turbulent boundary layers,2.2.1-18Two-phase loop with capillary pump,3.10.9-1/3.10.9-12Two-phase flows:Two-shell pass exchanger (see F-shells)