NB: Use the digits in your student number, as indicated, where student number is glven by: EFGJKLNP 1.1 AI.I.OCATTON OF PROCFSSFS Group I kinolilir Group IT Group III Distillation of Hexane - Heptane feed mixture at a flow rate of (20+2)2) kmoliar Group IV The fered will enter the divellation calumn at (40,2N) mols of the moen wularlle component. The purtly of the more valuable prodtuct must be no less than 95 mark. The cutering fond is (I +109% partially vaporized. Design Reyuirements: 1) Reseirt:h the spoxilic exinupomenis af the mixiure, their uses amud ruarket iemnarkl far eatch, is the more volattle product. 2) Repuor the plase bedaviour fur the syslers. 3) Slate the operaling and slrean condilions; feed stream, colunin pressure, etc: 4) Prrform basic column sizing, and design. State and justify all your assumptions and design. - Calculace the number of theorecical trays iminimum number, Nrir, theorecical number, N1, include an efficiency to detennine the actual'teal number of trays: else pw:ketl lueighhli - Conduct a procoss simulation of your disrillation process and report on parameters including compoocnt flow rates, composirion, enthalpy, condichser and reboller duties, and reflex ratio. 2 Colunn specifications idiameter: beight, packingtrays - type, size amount, and indicate reasons for the choices) -. Provide the timnemsisming of the relhux tinum rexpuirest for the disillite 5) Prwibe ant ilhusirative driwing, wr your tawer- Inchude all column internal and external dimensions. (6) Undertake an equipment coscing of the distillation column 7) Presumt all line work tione in a report lortiat with stricl deliverables. Normal Manglrs: T1mes New Roman font size 11:1.15 line spacing must be usod. Tahulated dara may lase no line spacing. 1.2 FINAI. DISTCN REPORT The final design report must concain the following: (a) An introduction contalning: - Component uses and market demand. Connpoxient pruperties and phase belaviour in the foran of ars equilibriuns x ? use A.SPF.N to abraln the VI.E. hehavikui if them is n phase hrhavlour repo ywir system. Also Teport the thermodynamic model weed to ohtain th hehavinuri] l'roject maragervent including a work breakdown structure and newor. describing all activities and dhe critical pach. (b) Lesign coetaining