Page 298 - Applied Process Design For Chemical And Petrochemical Plants Volume II
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            Figure 9-21 H.  Updated generalized pressure-drop correlation reamnged version of earlier Eckert and Leva, using linear scale for the ordinate
            and use of capacity factor, C,.  Used by permission of Strigle, R.  F.,  Jr.,  Packed Tower Design and Applications; Random and Structured Pack-
            ings, 2nd ed. 0 Gulf Publishing Co. p. 21 (1994). Note: G = gas, Ib/ft2-hr, L = liquid, Ib/ft2-hr.
























                            FIOLV  parameter, x = A {P=/A
                                       G
                 L =  liquid mass rate               Data Range   7
                 G = gas mass rate                   j   5s0573  j
                 fi =  liquid density                            -.         Figure 9-211.  Norton  IMTP  Packing,  Efficient Capacity
                 po = gas density                    :   0.075j15l.l   '    Correlation for random metal packing only for non-foam-
                 V  = scperficial gas velocity, mle or ftis                 ing systems. Norton recommends designing up to 90% of
                                                                            efficient capacity:
                 x = + u'$ FIOW parameter                                    Efficient Capacity, CSc = C,  [g] [&I   -0.11
                                                                                                    0.16
                 u-surface  tension. dynelcm                                                                  ,ft/sec.
                 11-iiquic!  viscosity. cp
                 v-!,quic  kinematic visccsiiy. cs
                                                                            Used by permission of Norton Chemical Process Prod-
                                                                            ucts Corp.,  Bull. IHP-1 (9/87).
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