please complete the schematic diagran on the right side and answer part A)1,2,3,4

thank you

Problem Statement Troubleshooting distillation column operation A dostillaice column is used to fractionale A and B. The feed has 55 molke B and 45mol in h The flow rate of the feed ii 900kg/h Feed entersat 2 bar Ichesk the ferd coedition for your group as indicated in ifie previoes alidel. Accordine to ASPEN termieology, thay no I the condenset). The column is cquiphod with a lotal condenser and a paitial rebolke. The tecovery fraction of the light kry ia the dintillate is 98%, waile the recovery fraction of the hicavy key is 96% in the bothom strcarm. Part A : 1. Draw a schematic diagram of the separation unit with all the given information shown on the diagrm. 2 Carry on Material balance ont the given Systern to obtain flowrates and compositions of top and bottocn streams 3. Carry on Energy Balance calculations to obtain condenser and reboiler dutics in (K/h) 4. Use FUG method (Fenske-Underwood-Gilliland method) to calculate the minamum number of stages, actual number of stages, optimum feed location and actual reflus ratio. Note that the actual reflux to minimam reflux ratio is 1.5 Troubleshooting distillation column operation A distillation column is used to fractionate A and B. The feed has 55mol%B and 45mol%A. The flow rate of the feed is 900kg/h. Feed enters at 2 bar /check the feed condition for your group as indicated in the previous slide]. According to ASPEN terminology, tray no 1 is the condenser). The column is equipped with a total condenser and a partial reboiler. The recovery fraction of the light key in the distillate is 98%, while the recovery fraction of the heavy key is 96% in the bottom stream. Part A : 1. Draw a schematic diagram of the separation unit with all the given information shown on the diagram. 2. Carry on Material balance on the given System to obtain flowrates and compositions of top and bottom streams 3. Carry on Energy Balance calculations to obtain condenser and reboiler duties in (KJ/h) 4. Use FUG method (Fenske-Underwood-Gilliland method) to calculate the minimum number of stages, actual number of stages, optimum feed location and actual reflux ratio. Note that the actual reflux to minimum reflux ratio is 1.5