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272     10 The Use of SMB for the Manufacture of Enantiopure Drug Substances: From …


                 The total column length is:
                 L = 1.43 m (8 columns of 18 cm length)

                 The velocity is then:
                 u = 0.0064 m s –1

                 The column diameter is then determined using the mean flow rate in the SMB.

                                         ∅=    ⋅ 4 Q mean  = 049 m
                                                        .
                                               π ⋅u
               and Equation (21) gives the shift period: ∆T = 0.92 min.

                 Using simulation software (essentially solving the mass balance equation in the
               transitory regime), one can show that the internal profiles of the products in the sys-
               tem are given by the profiles presented in Figure 10.6. Samples were taken between
               columns at half periods.


                 C (g/L)
               0,6

               0,5

               0,4

               0,3

               0,2

               0,1

                0
                Eluent                         Extract                     Feed                      Raffinate

               Figure 10.6. Internal profile (simulated) obtained for the separation under linear conditions.

                 This simulation shows that the purity of the raffinate collected over a complete
               cycle is about 97.0 % and the extract is about 98.5 %. These results are close to the
               target and adequate purity can be reached with minor changes in flowrates. Further
               details will be given in the next section.
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