A |
Area of opening, in.2, or duct cross section, ft2 |
A, B |
Factors used in Q5.26 |
BD |
Blowdown, fraction |
BHP |
Boiler horsepower |
C |
Corrosion allowance, in. |
Cc |
Initial investment, $ |
Cd |
Coefficient of discharge |
Ce |
Cost of electricity, $/kWh |
Cp |
Specific heat, Btu/lb °F |
Dp |
Tube or outer diameter, in. |
Di |
Tube or pipe inner diameter, in. |
E |
Escalation factor |
E |
Sealing efficiency, %; ligament efficiency, fraction |
F |
Factor defined in Eq. (33) |
G |
Gas mass velocity, lb/ft2 h |
H |
Enthalpy, Btu/lb |
H |
Height of liquid column, in. |
Hg, hf |
Enthalpy of saturated vapor and liquid, Btu/lb |
Hg |
Head of gas column, ft |
H |
Head of liquid, ft |
Hw |
Differential pressure across damper, in. WC |
I |
Interest rate |
L |
Distance, ft |
LCC |
Life-cycle cost, $ |
M |
Moisture in air, lb/lb |
MW |
Molecular weight |
N |
Annual period of operation, h |
Pw |
Partial pressure of water vapor, psia |
P |
Gas pressure, psia; design pressure, psig |
DP |
Differential pressure, psi |
PWL |
Sound power level |
Q |
Volumetric flow, gpm or cfm |
Q |
Energy, Btu/h |
R |
Radius of drum, in. |
RH |
Relative humidity |
S |
Specific gravity |
Sa |
Allowable stress, psi |
SBV |
Steam by volume |
SPL |
Sound pressure level, dB |
SVP |
Saturated vapor pressure, psia |
T Fluid temperature, °F
Tw Minimum wall thickness of pipe or tube, in.
T Life of plant, years
V Specific volume, cu ft; subscripts g and f stand for saturated vapor and
Liquid
V s Volume of drum ends, straight section, cu in.
V g Velocity of gas
W Mass flow, lb/h
X Steam quality
Y Volume fraction
P Density, lb/cu ft; subscript g stands for gas