Consider the idealized scheme shown below in which 100.0 mol/min of a reactive species A is fed to the process along with 20.0 mol/min of inserts. That stream is mixed with a recycle stream and fed to a reactor in which the single-pass conversion of A to P according to the reaction 1A-3P is 0.050 (that is, 1 molecule of A produces 3 of P). The reactor products are fed to a separator in which all of the P is removed and sent to a product stream as pure P. The other output of the separator consists solely of A and inserts; it is split into a recycle stream that feeds the mixer and a purge stream that is further processed elsewhere. The overall conversion of A in the process is 0.90. A1 (mol A/min) Rp.1 (mol P/min) nin1 (mol In/min) Feed MAZ (mol A/min) Np,7 (mol P/min) nin (mol In/min) MIXER SPLIT Purge MAC (mol A/min) np.6 (mol P/min) nin,6 (mol In/min) 14,2 (mol A/min) nie 2 (mol P/min) nina (mol In/min) nas (mol A/min) nps (mol P/min) nins (mol In/min) Product REACTOR SEPARATOR A3 (mol A/min) np,3 (mol P/min) ning (mol In/min) NA4 (mol A/min) np.4 (mol P/min) ning (mol In/min) Calculate the flow rate of each species in each stream of the process and enter the results into the table below. NA Stream Component Flow np. (mol/min) (mol/min) nini (mol/min) 1 i i 2 i i 3 4 i i 5 1 0 6 i i 7