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-lvi
DEFGHIJKLMNOPQRSTUVWXYZarea, ldensity, liiienergy (work), liienthalpy, lvforce, liiheat transfer coefficient, liiilength, lmass, lmass flux, limass rate of flow, liipower, liipressure, lvspecific heat capacity, livtemperature, lvithermal conductivity, livvelocity, liviscosity, livvolume flow rate, livolume, l
Conversion 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 principleCorrosion: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