ABC
Cabin heater,3.11.2-2Caetano, EF2.2.9-1/2.2.9-9, 2.5.16-1/2.5.16-5Calcium carbonate, fouling of heat exchangers by,3.17.6-11Calcium sulphate, fouling of heat exchangers by,3.17.6-12CALFLO, heat transfer media,5.5.15-54/5.5.15-55Calorically perfect gas,2.2.1-9CANDU Reactor, fouling problems in,3.17.9-4/3.17.9-6Capillary number,2.13.5-2Caproic acid, see Hexanoic acidCarbon dioxide:Carbon disulfide:Carbon monoxide:Carbon nanotubesCarbon steel:Carbon-manganese steels4.5.4-4, 4.5.4-9Carbon-molybdenum steels,4.5.4-9Carbon tetrachloride:Carbonyl sulfide:Carboxylic acids:Carmen-Kozeny equation (see Blake-Carmen-Kozeny equation)Carnot cycle in refrigeration,3.26.2-2/3.26.2-4Carnot factor,1.9.2-2Carreau fluid (non-Newtonian),2.2.8-7Carryover of solids in fluidized beds,2.2.6-3Cashman, B L,4.3.9-1/4.3.9-6Cast iron, thermal and mechanical properties,5.5.12-12Cavallini, A,2.13.6-1/2.13.6-30Cavitation as source of damage in heat exchangers,4.5.3-1Celata, G P2.13.1-1/2.13.1-3, 2.13.2-1/2.13.2-20Cell method, for heat exchanger effectiveness,1.6.1-1/1.6.12-1Cement kilns,3.11.2-6/3.11.2-7CEN code for pressure vessels,4.3.1-4Centrifugal dryer,3.13.2-4CeramicsCertification of heat exchangers,4.7.7-1CFD codes, in analysis of radiation systems with interactions,Chan, S H,3.17.6-16/3.17.6-19Channel emissivity,2.9.7-11/2.9.7-12Channel flow, heat and mass transfer in,2.1.7-1/2.1.7-2Chapman-Rubescin formula for viscosity variation with temperature,2.2.1-11Checkerwork pattern packing for regenerators,3.15.2-1/3.15.2-2Chemical exergy,1.9.3-2/1.9.3-3Chemical formulas of commonly used fluids5.5.1-1/5.5.1-178, 5.5.10-1/5.5.10-175, 5.5.11-1/5.5.11-174Chemical industry, fouling of heat exchangers in,3.17.5-5Chemical species conservation, in porous media,2.11.1-6Chemical reactions, exergy analysis of,1.9.4-3Chemical reaction fouling,3.17.2-2Chemical reactions, numerical calculation of flows involving,1.4.3-2/1.4.3-3Chen, LChen correlation for forced convective boiling,2.7.3-13/2.7.3-15Chen method, for enthalpy of vaporisation,5.1.3-5Chenoweth, J M,4.6.1-1/4.6.6-4Chevron troughs as corrugation design in plate heat exchangers,3.7.1-4/3.7.1-5CHF (see Critical heat flux)Chillers, construction features of,4.2.3-9Chilton-Colburn analogy,1.2.3-6Chisholm, D2.6.7-1/2.6.7-4, 3.10.1-1/3.10.2-2, 3.10.6-1/3.10.7-3Chisholm correlations:Chlorine:Chloroacetic acid:Chlorobenzene:Chlorobutane:Chlorodifluoromethane (see Refrigerant 22)1-Chloro-1,1-difluoroethane (Refrigerant 142b):Chloroethane (Refrigerant 160):Chloroform, see TrichloromethaneChloromethane (Refrigerant 40):Chloropentane:1,2-Chloropentafluoroethane (Refrigerant 115):3-Chloropropene, (see Allyl Chloride)Chloroprene (2-Chloro-1,3-butadiene):1-Chloropropane:2-Chloropropane:m-Chlorotoluene:o-Chlorotoluene:Chlorotrifluoroethylene:Chlorotrifluoromethane (see Refrigerant 13)Choice of heat transfer equipment (see Selection of heat transfer equipment)Chromium-molybdenum steels,4.5.4-9Chudnovsky, Y,3.25.1-1/3.25.6-7Chugging flow (gas-liquid), in shell-and-tube heat exchangers,2.3.2-5/2.3.2-6Chung et al method, for viscosity of low pressure gases,5.1.4-1/5.1.4-2Church and Prausnitz methods:Churchill, S W,2.5.7-1/2.5.9-7Churchill and Chu correlations for free convective heat transfer:Churn flow, regions of occurrence of,2.3.2-1/2.3.2-2Circles, radiative heat transfer shape factors between parallel coaxial,2.9.3-3Circular girth flanges, design according to ASME VIII code,4.3.4-13/4.3.4-15Circular cross section helical coils (see Helical coils of circular cross section)Circular cylinders (see Cylinders)Circulating fluidized beds,2.2.6-13/2.2.6-21Circulation, modes of in free convection: in enclosures heated from below,2.5.8-6CISE correlations for void fractions,2.3.2-14/2.3.2-15Clad plate (see Explosively clad plate)Clapeyron-Clausius relationship (see Clausius-Clapeyron relationship)Clausius-Clapeyron relationship:Cleaning:Climbing film evaporator,3.5.2-5/3.5.2-6Climbing film plate evaporator,3.7.4-4/3.7.4-6Closed circuit cooling towers,3.12.1-3/3.12.1-4Closed distillation process,2.1.7-8Coalescence of bubbles in fluidized beds,2.2.6-9/2.2.6-10Coatings for corrosion protection4.5.2-5/4.5.2-6, 4.15.5-1/4.15.5-6Cocurrent flow:Codes, mechanical design:Coefficient of expansion (see Thermal expansion coefficient)CogenerationCoiled tubes (see Helical coils; Curved ducts)Colburn and Drew method for binary vapor condensation,2.6.3-22.6.3-7/2.6.3-13Colburn and Hougen method for condensation in presence of noncondensable gases2.6.3-2, 2.6.3-7/2.6.3-13Colburn equation for single-phase heat transfer outside tube banks,3.3.2-1Colburn j factor:Cold insulation, of heat exchangers,4.15.2-5/4.15.5-6Colebrook-White equation for friction factor in rough circular pipe,2.2.2-3Coles, law of the wake,2.2.1-26Collier, J G,2.7.1-1/2.7.8-13Column internal reboiler (see Internal reboilers)Combined free and forced convection heat transfer:Combined heat and mass transfer,2.1.6-1/2.1.6-4Combining flow, loss coefficients in,2.2.2-21Combustion air heater for waste heat boilers,3.16.2-13/3.16.2-14Combustion chambers (see Furnaces)Combustion model for furnaces,3.11.7-4/3.11.7-5Compact flanges,4.14.8-2/14.14.8-3Compact heat exchangers (see Plate fin heat exchangers)Compartment dryers,3.13.2-3Composite curves, in the pinch analysis method for heat exchanger network analysis:Compressed liquids, density of:Compressible flow:Compression, exergy analysis of1.9.4-2/1.9.4-3, 1.9.5-5Compressive stress, in heat exchanger tubes,4.3.3-12Computer-aided design, of evaporators,3.5.8-2/3.5.8-4Computer program for Monte Carlo calculations of radiative heat transfer,2.9.4-4/2.9.4-5Computer simulation, of fouling,3.17.4-2Computer software for mechanical design,4.3.9-1/4.3.9-6Concentration, choice of evaporator type for,3.5.5-2Concentric annuli, see AnnuliConcentric spheres, free convective heat transfer in,2.5.8-16Concurrency corrections in plate heat exchangers,3.7.2-5/3.7.2-6Condensation:Concrete, lightweight, submerged combustion system for,2.10.4-24/2.10.4-29Condensation curves:Condenser/preheater tubes, in multistage flash evaporation,3.22.2-8/3.22.2-11Condensers:Conduction, heat:Conductors, thermal conductivity of,5.4.3-2/5.4.3-3Cones, under internal pressure, EN13445 guidelines for,4.3.3-4/4.3.3-5Cones, vertical:Confinement number,2.13.5-2Conical shells, mechanical design of:Conjugate radiation interactions2.9.8-13, 2.9.8-3, 2.9.8-5/2.9.8-7Connors equation for fluid elastic instability,4.6.4-2Conservation equations:Constantinon and Gani method, for estimating normal boiling point,5.1.3-7Construction elements of heat exchangers,4.1.1-2/4.1.2-3Contact angle,2.3.1-2Contact resistance:Continuity equation:Continuum model, for fluids,2.2.1-1Continuum theories, for non-Newtonian fluids,2.2.8-8/2.2.8-10Contraction, sudden, pressure drop in:Control:Control volume method, in finite difference solutions for conduction,2.4.7-5/2.4.7-6Convection, interaction of radiation with,2.9.8-12/2.9.8-23Convection effects, on heat transfer in kettle reboilers,3.6.2-3/3.6.2-4Convective boiling (see Boiling)Convective heat transfer, single-phase:Conversion charts, for units, l-lviConversion factors:Conveyor, gravity:Cooling curves, in condensation,2.6.3-2/2.6.3-5Cooling towers:Cooling water fouling,3.17.6-11/3.17.6-20Cooper correlation, for nucleate boiling,2.7.2-7/2.7.2-8Cooper, Anthony,3.7.1-1/3.7.4-7Copper, thermal and mechanical properties,5.5.12-10Copper alloys,4.5.7-1/4.5.7-9Core-annular flow, see Annular flow (liquid-liquid)Correlation, general nature of,1.2.3-5/1.2.3-6Corresponding states principle
DEFGHIJKLMNOPQRSTUVWXYZfor density of pure gases,5.1.2-2for density of gas mixtures,5.2.1-1/5.2.1-2for surface tension of pure fluids,5.5.1-3for vapour pressure,5.1.2-3/5.1.2-4
Corrosion:Corrugation design, for plate heat exchangers3.7.1-4/3.7.1-5, 4.4.2-3/4.4.2-4Costing of heat exchangers:Coulomb (SI unit), xxviiiCountercurrent flow:Counterflow (see Countercurrent flow)Coupled thermal fields, in transient conduction,2.4.3-12Cowie, R C,4.8.2-1/4.8.2-5Cowper stove regenerator,3.15.1-2Crank-Nicolson differencing scheme, in finite difference method,2.4.7-17Creeping flow, in combined free and forced convection around immersed bodies,2.5.9-3m-Cresol:o-Cresol:p-Cresol:Crevice corrosion, in stainless steels,4.5.6-12/4.5.6-13Criss-cross strip baffles, see Strip bafflesCritical constantsCritical density, of commonly used fluids,5.5.1-1/5.5.1-178Critical flow, in gas-liquid systems,2.3.2-26/2.3.2-29Critical heat flux:Critical pressure:Critical Rayleigh number, in free convection,2.5.8-2/2.5.8-3Critical temperature:Critical velocity, in stratification in bends and horizontal tubes,2.7.4-2Critical volume (see also Critical density)Crocco's integral, (see Busemann-Crocco integral)Cross counterflow heat exchangers,1.1.1-2Crossflow:Crossflow shells (see X-shells)Crude oil, fouling of heat exchangers:Cryogenic plant, entropy generation in,1.8.4-5/1.8.4-7CrystallizationCrystallization fouling,3.17.7-1/3.17.7-2Cumene (see Isopropylbenzene)Curved ducts:Currie, R,4.12.1/4.12.6Cut-and-twist factor, in enhancement of heat transfer in double pipe heat exchangers,3.2.3-1C-value method for heat exchanger costing,4.8.1-5/4.8.1-9Cyclic equilibrium, in regenerators,3.15.10-1/3.15.10-7Cycling, of expansion bellows,4.10.2-4Cyclobutane:Cyclohexane:Cyclohexanol:Cyclohexene:Cyclopentane:Cyclopentene:Cyclopropane:Cylinders:Cylindrical contacts, thermal contact resistance in,2.4.6-5/2.4.6-6Cylindrical coordinates, finite difference equations for conduction in,2.4.7-27/2.4.7-31Cylindrical enclosures containing porous medium, natural convection in,2.11.6-4/2.11.6-5Cylindrical shell, analytical basis of code rules for,4.3.2-4