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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.
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