AB
Baffle leakage in shell-and-tube heat exchangers:Baffle pipes in agitated vessels,3.14.2-3/3.14.2-4Baffles in shell-and-tube heat exchangers:Baffle tray columns, for direct contact heat transfer,3.19.5-2Baker flow regime map for horizontal gas-liquid flow,2.3.2-3Balance equation (applied to complete equipment),1.2.4-1/1.2.4-7Balanced regenerators,3.15.6-2Band dryer:Bandel and Schlunder correlations, for boiling in horizontal tubes,2.7.4-4/2.7.4-5Banks of tubes (see Tube banks)Barometric condenser,3.20.1-2Barrels for shell-and-tube heat exchangers (see Shells)Basket-type evaporator,3.5.2-3/3.5.2-4Barbosa, J R Jr,3.26.1-1/3.26.6-5Bateman, G,4.11.4-1/4.11.4-6Bayonet tube heat exchangers, constructional features of,4.2.3-9/4.2.3-10Bayonet tube waste heat boilers,3.16.2-7Bayonet tube evaporators,3.5.2-1/3.5.2-2Beaton, C F,5.5.0-1/5.5.0-12, 5.5.1-1/5.5.1-178, 5.5.2-1/5.5.2-44, 5.5.10-1/5.5.10-175, 5.5.11-1/5.5.11-175, 5.5.12-1/5.5.12-13, 5.5.14-1/5.5.14-56Becquerel (SI unit), xxviiiBeer-Lambert law,2.9.5-5Bejan, A,1.8.1-1/1.8.4-7, 2.11.1-1/2.11.7-4Bell, Kenneth J,3.1.1-1/3.1.4-9Bell-Delaware method for shell-side heat transfer and pressure drop in shell-and-tube heat exchangers,3.3.2-5/3.3.2-6Bell and Ghaly method for calculation of multicomponent condensation,2.6.3-5/2.6.3-6Bellows, expansion, for shell-and-tube heat exchangers (see Expansion bellows)Benard cells in free convection in horizontal fluid layers,2.5.8-1/2.5.8-3Bends:Benzaldehyde:Benzene:
CDEFGHIJKLMNOPQRSTUVWXYZliquid properties,5.5.10-47saturation properties,5.5.1-50superheated gaseous: physical properties,5.5.11-47
Benzoic acid:Benzonitrile:Benzophenone:Benzyl alcohol:Benzyl chloride:Berenson equation for pool film boiling from a horizontal surface,2.7.2-14Bergles, Arthur E,2.5.11-1/2.5.11-12Bernoulli equation, application to flow across cylinders,2.2.4-1Bimetallic tubes:Binary mixtures:Bingham fluid (non-Newtonian),2.2.8-7Biofouling,3.17.2-2/3.17.2-3, 3.17.6-10/3.17.6-11, 3.17.6-15Biot number:Biphenyl:Bismarck A,2.14.1-1/2.14.4-6Black liquor, in pulp and paper industry, fouling of heat exchangers by,3.17.6-7/3.17.8-7Black surface:Blackbody radiation,2.9.1-3/2.9.1-5Blades, in scraped surface heat exchangers,3.24.1-10/3.24.1-11Blake-Carmen-Kozeny equation,2.2.5-2Blasius equation for friction factor,2.2.2-3Blast furnace stoves, heat transfer in,3.15.11-6/3.15.11-7Blenkin, R,4.3.7-1/4.3.7-15Block-type heat exchanger,4.4.4-4Blowing (see Injection)Blunt bodies, drag coefficients for,2.2.3-7Bodnar criterion for water fouling,Boilers:Boiling:Boiling curve:Boiling length:Boiling number, definition,2.7.4-5Boiling point, normal,5.1.3-7/5.1.3-12Boiling range (in multicomponent mixtures):Boiling surface in boiling in vertical tubes,2.7.3-5Boiling Water Reactor (BWR), fouling problems in,3.17.9-6/3.17.9-8Bolted channel head in shell-and-tube exchanger,4.2.4-1Bolted cone head in shell-and-tube heat exchanger,4.2.4-2Bolted joints, thermal contact resistance in,2.4.6-3/2.4.6-4Bolting,4.13.1-1/4.13.6-3Bolting of flanges in shell-and-tube heat exchangers,4.2.6-4/4.2.6-5Boltzmann's constant,2.9.1-3Bonnet head, in shell-and-tube heat exchanger,4.2.4-1/4.2.4-2Borishanski, V M,2.5.13-1/2.5.13-4Borishanski correlation for nucleate pool boiling,2.7.2-5Bott, T R,3.17.5-1/3.17.5-2, 3.17.6-10/3.17.6-11, 3.17.6-27/3.17.6-28, 3.17.6-30, 3.17.6-5/3.17.6-6, 3.17.7-22, 3.17.7-7/3.17.7-8, 3.17.8-1/3.17.8-5Boundary layer:Boussinesq approximations:Boussinesq number, definition,2.5.7-2Bowring correlations for critical heat flux,2.7.3-16/2.7.3-18Bracket supports for heat exchangers:Branches, mechanical design aspects,4.1.8-1/4.1.8-2Brauner, N,2.3.5-1/2.3.5-40Brazed plate exchanger,4.4.2-5Brazing in plate fin heat exchanger construction,4.4.3-3/4.4.3-4Bricks, drying of,3.13.5-2/3.13.5-5Brine recirculation, in multistage flash-evaporation,3.22.2-5/3.22.2-7Brinkman model, for flow in porous media,2.11.4-4Brinkman number,2.5.12-7British Standards Institute code for mechanical design of heat exchangers (see BS 5500 code)Brittle fracture,4.3.2-16Bromine:Bromley equation for film boiling from horizontal cylinders,2.7.2-19Bromobenzene:Bromoethane:Bromomethane:Bromotrifluoromethane (Refrigerant 13B1):Brush and cage system, for fouling mitigation,3.17.8-2BS 5500 code for mechanical design of shell-and-tube heat exchangers (see also PD 5500),4.3.1-4Bubble crowding as mechanism of critical heat flux,2.7.2-13, 2.7.3-22Bubble flow:Bubble-type direct-contact condensers,3.20.4-1/3.20.4-5Bubbles:Bulk viscosity,2.2.1-2Bundle-induced convection in kettle reboilers,3.6.2-3/3.6.2-5Bundle layout, in condensers3.4.3-6Buoyancy effects:Buoyancy-induced flow in channels, free convective heat transfer with,2.5.7-19/2.5.7-20Burnout (see Critical heat flux)Busemann-Crocco integral, application in boundary layer equations,2.2.1-221,2-Butadiene:1,3-Butadiene:Butane:1-Butanol:2-Butanol:tert-Butanol, (see tert-Butyl alcohol)Butene-1:cis-2-Butene:trans-2-Butene:Butterworth, D,2.6.1-1/2.6.1-2, 3.4.1-1/3.4.1-2, 3.4.3-1/3.4.3-8, 3.4.4-1/3.4.4-3, 3.4.5-1/3.4.5-4Butyl acetate:sec-Butyl alcohol (see -2Butanol)t-Butyl alcohol:Butylamine:Butylbenzene:n-Butylbenzene:Butyl chloride (see Chlorobutane)n-Butylcyclohexane:Butylcyclopentane:Butylene oxide:1-Butyne (see ethyl acetate)2-Butyne (see Dimethyl-Acetylene)Butyr-aldehyde:Butyric acid:Butyronitrile:BWR, see Boiling Water ReactorBypass (shell-and-tube bundle):