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Introduction 35
approach this goal. Normally contactors of this type are used when the equilibrium vapor
pressure of the absorbate over the product liquid is extremely low and can be neglected.
Under these conditions, the equation for the number of transfer units reduces to
NN = In (Y(1 -E)) ( 1-24)
where E = absorption efficiency, expressed as a fraction.
In accordance with equation 1-24, removal efficiency and NoG are related as follows:
Removal Efficiency, % NOG
90 2.3
95 3.0
99 4.6
The NOG values can be used to extrapolate test or operating data on a spray contactor to
other systems or conditions. For example, if one spray unit provides 90% removal (2.3 trans-
fer units), it can be expected that two identical units in series will provide about 99%
removal (4.6 transfer units). Since commercial spray systems are widely variable, the devel-
opment of a generalized design approach based on fundamentals is quite difficult. As a
result, spray contactors are usually designed on the basis of previous experience with similar
systems.
American Institute of Chemical Engineers, 1958, Bubble Tray Design Manual, Prediction of
Fractionation Eficiency, NY: AIChE.
American Society of Heating, Refrigerating, and Air-conditioning Engineers, 1988,
ASHU Handbook Equipment Volume, Chapt. 11, “Industrial Gas Cleaning and Air Pol-
lution Control.”
Astarita, G., and Savage D. W., 1980, Chemical Engineering Science, Vol. 35, p. 649.
Astarita, G., 1967, Mass Transfer with Chemical Reactions, Elsevier, Amsterdam.
Astarita, G., Savage, D. W., and Bisio, A., 1983, Gas Treating with Chemical Solvents, John
Wiley & Sons, NY.
Barnicki, S. D., and Davis, J. F., 1989, Chem. Eng., Vol. 96, No. 10, October, pp. 140 and
141, November, p. 202.
Biddulph, M. W., 1977, Hydro. Process., Vol. 56, No. 10, October, p. 145.
Biddulph, M. W., Thomas, C. P., and Burton, A. C., 1993, Chem. Eng. Progr.., Vol. 89, No.
12, December, p. 56.
Billet, R., 1989, Packed Tower Analysis nnd Design, Ruhr University, Bochum, Germany.
Blecker, H. G., and Nichols, T. M., 1973, Capital and Operating Costs of Pollution Control
Equipment Modules, Data Manual, Vol. 2., EPA-R5-73-023b, July, PB-224536.
Bolles, W. L., 1963, “Tray Hydraulics-Bubble Cap Trays,” Chapt. 14 in Design of Equilib-
rium Stage Processes, B. D. Smith, Ed., McGraw-Hill, New York, NY.
Bolles, W. L., 1976, Chem. Eng. Prog., Vol. 72, No. 9, September, pp. 43-49.