n-hexane isobutane n-pentane PR PR 0 0 10 100 1 0 original 0 sundials 0 1e-3 1e-6 1e-2 #* This tab can be used by users to insert small code structures in the present simulation. For example: Steps, Ramps, Sinusoidals, ... *# #Enter your code here. #Example: #* EQUATIONS if time > 1000 * 's' then source_1.F = 100 * 'kmol/h'; else source_1.F = 200 * 'kmol/h'; end*# 2000 1000 1 858 288 0 -152 1 858 0 0 0 source source_1 48 336 0 72.5 37 62.0625 395.3 ValidPhases 1 "Vapour-Liquid" 4 Composition 1 0.5 1 Composition 2 0.3 1 Composition 3 0.2 1 Fw 'kg/h' 1 749.552 1 T_Cdeg 'K' 1 65.85 1 P 'atm' 1 3 1 sink sink_1 724 339 0 72.5 37 746.712 398.3 T_Cdeg 1 30 1 heater heater_2 376 88 0 94 74 444.4 151.654 Kvalues 1 "no" 4 Pdrop 'kPa' 1 2 1 simple_source simple_source_1 35 100 0 68 30 25.0625 159.3 MolarComposition 1 1 1 MolarComposition 2 0 1 MolarComposition 3 0 1 F 'kmol/h' 1 1 1 T 'K' 1 330 1 P 'atm' 1 1 1 simple_sink simple_sink_1 680 103 0 68 30 678.712 162.3 cooler cooler_2 376 313 0 94 72 424.4 394.9 Pdrop 'kPa' 1 15 1 S001 97 109.768 370 111.6 simple_source_1 Outlet heater_2 Inlet S002 464 111.6 674 112.924 heater_2 Outlet simple_sink_1 Inlet S003 417 307 417 156 cooler_2 Heat heater_2 Heat S004 114.5 349.447 370 351.28 source_1 Outlet cooler_2 Inlet S005 464 351.28 718 352.64 cooler_2 Outlet sink_1 Inlet