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Separator Design                                              351


            m)  in diameter  and 20  ft (6.70  m)  high.  These data  can be  use  as a guide  to  esti-
            mate the motor power.

                 10
                                I             I
                          Sources of Experimental Dita
                         O Karr'*, RFC
                                  25
                         A  Karr and Lo , RFC
                                     17
                         a  Reman and Olney , RDC
             s   R
             j:   6


                 4
                                                    Low-vucoilty systems





                               10           20           30          40
                                      Intel-facial tension, dynes/cm

            Figure 6.23  Effect  of  Intel-facial Tension  on  NETS for  the  RDC and  RFC
            Extractors (Source: Reference 6.31 with permission).

            Table 6.33  Calculation Procedure for Sizing the Karr, Reciprocating-Plate
            Extractor____________________________________

            Refer to Figure 6.16 for meaning of the numerical subscripts.

            1. Calculate mass  fraction  of the  key component in the  leaving heavy phase, x k,
                                                                           2
            from Equation 6.32.3.

            2. Calculate the maximum slope of the operating line from Equation 6.32.1.
            3.  Calculate  the  ratio  of  the  feed  mass  flow  rate  to  the  solvent  mass  flow  rate,
            m F/m s, from Equation 6.32.4, and the operating solvent flow rate, m s.

            4.  Calculate the  mass  fraction  of  the  key  component  in the  entering  light phase,
            yik, in the light phase from Equation 6.32.2.

            5. Calculate the extraction factor, A E, from Equation 6.32.13.

            6. Calculate the number of equilibrium stages, N, from Equation 6.32.5.
                                                   e



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