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Baffle leakage in shell-and-tube heat exchangers:
Baffles in shell-and-tube heat exchangers:
Baker flow regime map for horizontal gas-liquid flow,
Balance equation (applied to complete equipment),
Band dryer:
Bandel and Schlunder correlations, for boiling in horizontal tubes,
Basket-type evaporator,
Barbosa, J R Jr,
Bateman, G,
Bayonet tube heat exchangers, constructional features of,
Bayonet tube evaporators,
Beaton, C F,
Index to Compounds and Properties by Section
Properties of Saturated Fluids
Thermodynamic Properties of Superheated Fluids
Physical Properties of Liquids at Temperatures Below Their Boiling Point
Transport Properties of Superheated Gases
Thermal and vechanical Properties of Heat Exchanger Construction Materials
Transport Properties of Fluids at Elevated Pressures
Beer-Lambert law,
Bejan, A,
Bell-Delaware method for shell-side heat transfer and pressure drop in shell-and-tube heat exchangers,
Bell and Ghaly method for calculation of multicomponent condensation,
Benard cells in free convection in horizontal fluid layers,
Bends:
Benzaldehyde:
Benzene:
Benzoic acid:
Benzonitrile:
Benzophenone:
Benzyl alcohol:
Benzyl chloride:
Berenson equation for pool film boiling from a horizontal surface,
Bergles, Arthur E,
Bernoulli equation, application to flow across cylinders,
Bimetallic tubes:
Binary mixtures:
Bingham fluid (non-Newtonian),
Biofouling,
Biot number:
Biphenyl:
Bismarck A,
Black liquor, in pulp and paper industry, fouling of heat exchangers by,
Black surface:
Blackbody radiation,
Blades, in scraped surface heat exchangers,
Blake-Carmen-Kozeny equation,
Blasius equation for friction factor,
Blenkin, R,
Blunt bodies, drag coefficients for,
Boilers:
Boiling:
Boiling curve:
Boiling length:
Boiling number, definition,
Boiling point, normal,
Boiling range (in multicomponent mixtures):
Boiling surface in boiling in vertical tubes,
Boiling Water Reactor (BWR), fouling problems in,
Bolted channel head in shell-and-tube exchanger,
Bolted cone head in shell-and-tube heat exchanger,
Bolted joints, thermal contact resistance in,
Bolting,
Bolting of flanges in shell-and-tube heat exchangers,
Boltzmann's constant,
Bonnet head, in shell-and-tube heat exchanger,
Borishanski, V M,
Borishanski correlation for nucleate pool boiling,
Bott, T R,
Boundary layer:
Boussinesq approximations:
Boussinesq number, definition,
Bowring correlations for critical heat flux,
Bracket supports for heat exchangers:
Brauner, N,
Brazed plate exchanger,
Brazing in plate fin heat exchanger construction,
Bricks, drying of,
Brine recirculation, in multistage flash-evaporation,
Brinkman number,
Brittle fracture,
Bromine:
Bromley equation for film boiling from horizontal cylinders,
Bromobenzene:
Bromoethane:
Bromomethane:
Bromotrifluoromethane (Refrigerant 13B1):
Brush and cage system, for fouling mitigation,
BS 5500 code for mechanical design of shell-and-tube heat exchangers (see also PD 5500),
Bubble crowding as mechanism of critical heat flux,
Bubble flow:
Bubbles:
Bulk viscosity,
Bundle-induced convection in kettle reboilers,
Bundle layout, in condensers
Buoyancy effects:
Buoyancy-induced flow in channels, free convective heat transfer with,
Busemann-Crocco integral, application in boundary layer equations,
1,2-Butadiene:
1,3-Butadiene:
Butane:
1-Butanol:
2-Butanol:
Butene-1:
cis-2-Butene:
trans-2-Butene:
Butterworth, D,
Butyl acetate:
t-Butyl alcohol:
Butylamine:
Butylbenzene:
n-Butylbenzene:
n-Butylcyclohexane:
Butylcyclopentane:
Butylene oxide:
Butyr-aldehyde:
Butyric acid:
Butyronitrile:
Bypass (shell-and-tube bundle):
Index
HEDH
A
B
Baffle leakage in shell-and-tube heat exchangers:
Baffles in shell-and-tube heat exchangers:
Baker flow regime map for horizontal gas-liquid flow,
Balance equation (applied to complete equipment),
Band dryer:
Bandel and Schlunder correlations, for boiling in horizontal tubes,
Basket-type evaporator,
Barbosa, J R Jr,
Bateman, G,
Bayonet tube heat exchangers, constructional features of,
Bayonet tube evaporators,
Beaton, C F,
C
D
E
F
G
H
I
J
K
L
M
N
O
P
Q
R
S
T
U
V
W
X
Y
Z
Index to Compounds and Properties by Section
Properties of Saturated Fluids
Thermodynamic Properties of Superheated Fluids
Physical Properties of Liquids at Temperatures Below Their Boiling Point
Transport Properties of Superheated Gases
Thermal and vechanical Properties of Heat Exchanger Construction Materials
Transport Properties of Fluids at Elevated Pressures
Beer-Lambert law,
Bejan, A,
Bell-Delaware method for shell-side heat transfer and pressure drop in shell-and-tube heat exchangers,
Bell and Ghaly method for calculation of multicomponent condensation,
Benard cells in free convection in horizontal fluid layers,
Bends:
Benzaldehyde:
Benzene:
Benzoic acid:
Benzonitrile:
Benzophenone:
Benzyl alcohol:
Benzyl chloride:
Berenson equation for pool film boiling from a horizontal surface,
Bergles, Arthur E,
Bernoulli equation, application to flow across cylinders,
Bimetallic tubes:
Binary mixtures:
Bingham fluid (non-Newtonian),
Biofouling,
Biot number:
Biphenyl:
Bismarck A,
Black liquor, in pulp and paper industry, fouling of heat exchangers by,
Black surface:
Blackbody radiation,
Blades, in scraped surface heat exchangers,
Blake-Carmen-Kozeny equation,
Blasius equation for friction factor,
Blenkin, R,
Blunt bodies, drag coefficients for,
Boilers:
Boiling:
Boiling curve:
Boiling length:
Boiling number, definition,
Boiling point, normal,
Boiling range (in multicomponent mixtures):
Boiling surface in boiling in vertical tubes,
Boiling Water Reactor (BWR), fouling problems in,
Bolted channel head in shell-and-tube exchanger,
Bolted cone head in shell-and-tube heat exchanger,
Bolted joints, thermal contact resistance in,
Bolting,
Bolting of flanges in shell-and-tube heat exchangers,
Boltzmann's constant,
Bonnet head, in shell-and-tube heat exchanger,
Borishanski, V M,
Borishanski correlation for nucleate pool boiling,
Bott, T R,
Boundary layer:
Boussinesq approximations:
Boussinesq number, definition,
Bowring correlations for critical heat flux,
Bracket supports for heat exchangers:
Brauner, N,
Brazed plate exchanger,
Brazing in plate fin heat exchanger construction,
Bricks, drying of,
Brine recirculation, in multistage flash-evaporation,
Brinkman number,
Brittle fracture,
Bromine:
Bromley equation for film boiling from horizontal cylinders,
Bromobenzene:
Bromoethane:
Bromomethane:
Bromotrifluoromethane (Refrigerant 13B1):
Brush and cage system, for fouling mitigation,
BS 5500 code for mechanical design of shell-and-tube heat exchangers (see also PD 5500),
Bubble crowding as mechanism of critical heat flux,
Bubble flow:
Bubbles:
Bulk viscosity,
Bundle-induced convection in kettle reboilers,
Bundle layout, in condensers
Buoyancy effects:
Buoyancy-induced flow in channels, free convective heat transfer with,
Busemann-Crocco integral, application in boundary layer equations,
1,2-Butadiene:
1,3-Butadiene:
Butane:
1-Butanol:
2-Butanol:
Butene-1:
cis-2-Butene:
trans-2-Butene:
Butterworth, D,
Butyl acetate:
t-Butyl alcohol:
Butylamine:
Butylbenzene:
n-Butylbenzene:
n-Butylcyclohexane:
Butylcyclopentane:
Butylene oxide:
Butyr-aldehyde:
Butyric acid:
Butyronitrile:
Bypass (shell-and-tube bundle):
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Transport Properties of Superheated Gases
DOI 10.1615/hedhme.a.000534
5.5 PHYSICAL PROPERTY DATA TABLES
5.5.11 Transport properties of superheated gases at atmospheric pressure
Clive F. Beaton
The tables given in this section may be regarded as being supplementary to those in Section 524, which gave thermodynamic and transport properties of saturated vapors, and those in Section 525 and Section 537, which gave data for vapour at various pressures. A list of symbols and conversion factors were given in Section 524 page 6.
This section provides data for every compound listed in Section 533 as a vapour at atmospheric pressure. The temperature range for these data depends on the availability of the published data and/or the limits of the prediction techniques used to supply the complete data tables.
For tables derived from equations, a maximum temperature of 600 °C was taken to ensure reliability in the predicted data, and a lower limit of 0 °C, even if this is below the melting point, to provide a reasonable range for interpolation.
Because the effect of pressure on these properties is negligible (Section 500 and Section 501), the values given will be valid at all temperatures at atmospheric pressure. However, for the real gas (not present in a mixture) the density below the normal boiling point will need adjusting to the ambient pressure for the particular conditions.
Additional data (when available from the published source) has been included for the heat capacity at constant volume cv,g and for the speed of source Us.
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