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where
G = Gas mass velocity, (lb/ft 2 -s).
F = Packing factor = 160 for 1-inch Raschig rings.
Ψ = Ratio, density of water/density of liquid.
µ L = Viscosity of liquid (cp).
p L = Liquid density.
p = Gas densit y.
g c = 32.2 lb-ft/lb-s 2 .
From USEPA's generalized flooding and pressure drop correction graph,
Ψ () =
02
.
2
GF
ppg
L
Lc
019
.
Solve the abscissa for the flooding gas mass velocity ( G f ) in lb/ft 2 -s. The G value becomes G f for
this case. Thus,
05
.
05
.
(
)
(0.19)
Ψµ 02
ppg
(. )( 224 0 075
0196
.)(.
)(
32 2
.)
Lc
2
G
=
=
= 0 400
.
lb/ft -s
f
()
.
02
.
(
160 118
)()(.)
F
L
Calculate the actual gas mass velocity ( G act ) in lb/ft 2 -s:
G act = 0.6 G f = 0.6 × 0.400 = 0.240 lb/ft 2 -s = 864 lb/ft 2 hr
Calculate the diameter of the column in feet:
S = (mass flowrate of gas stream)/ G act = 5000/ G act
S = π D 2 /4
π
D 2 /4 = 5000/ G act
D = [(4(5000))/(π G act )] 0.5 = 2.71 ft
REFERENCES AND RECOMMENDED READING
Calvert, S.J., Goldschmid, D., Leith, D., and Metha, D. (1972). Wet Scrubber System Study . Vol 1. Scrubber
Handbook , EPA R2-72-118a. U.S. Environmental Protection Agency, Washington, DC.
Cooper, D. and Alley, F. (1994). Air Pollution Control: A Design Approach , 2nd ed. Waveland Press, Prospect
Heights, IL.
Corbitt, R.A. (1990). Standard Handbook of Environmental Engineering . McGraw-Hill, New York.
Heumann, W.L. and Subramania, V. (1997). Particle scrubbing, in Heumann, W.L., Ed., Industrial Air Pollution
Control Systems . McGraw-Hill, New York.
Lapple, C.E. and Kamack, H.J. (1955). Performance of wet dust scrubbers. Chemical Engineering Progress ,
51, 110-121.
Nukiyama, S. and Tanasawa, Y. (1983). An experiment on atomization of liquid by means of air stream (in
Japanese). Transactions of the Japan Society of Mechanical Engineers , 4, 86.
Perry, R. and Green, D., Eds. (1984). Perry's Chemical Engineers' Handbook , 6th ed.. McGraw-Hill, New
York.
Semrau, K.T. (1960). Correlation of dust scrubber efficiency. Journal of the Air Pollution Control Association ,
10, 200-207.
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