isobutane n-pentane propylene benzene isobutene PR PR 0 0 1 30 1 0 original 0 sundials 0 sundials 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 -181 1 858 0 0 -15 source source_2 8 56 0 68 30 16.0625 104.3 CompositionBasis 1 "Molar" 4 ValidPhases 1 "Vapour-Liquid" 4 Composition 1 0.20 1 Composition 2 0.15 1 Composition 3 0.15 1 Composition 4 0.30 1 Composition 5 0.20 1 F 'kmol/h' 1 500 1 T 'K' 1 338 1 P 'kPa' 1 507 1 info_stream info_stream_1 317 58 0 51 32 302.6 99.1539 info_stream info_stream_2 308 280 0 51 32 310.6 339.154 heater heater_2 540 45 0 94 74 611.4 115.654 Pdrop 'kPa' 1 12 1 cooler cooler_3 540 257 0 94 72 581.4 344.9 Pdrop 'kPa' 1 3 1 info_stream info_stream_3 762 63 0 51 32 747.6 117.154 info_stream info_stream_4 789 284 0 51 32 767.6 343.154 sink sink_1 1015 63 0 68 30 1037.71 122.3 sink sink_2 1008 286 0 68 30 1029.71 345.3 T_Cdeg 1 400 1 source source_1 35 274 0 81.5 29.8 39.0625 318.3 CompositionBasis 1 "Molar" 4 ValidPhases 1 "Vapour-Liquid" 4 Composition 1 0.20 1 Composition 2 0.15 1 Composition 3 0.15 1 Composition 4 0.30 1 Composition 5 0.20 1 F 'kmol/h' 1 500 1 T 'K' 1 500 1 P 'kPa' 1 507 1 S001 70 65.768 311 68 source_2 Outlet info_stream_1 Inlet S002 362 68 534 68.6 info_stream_1 Outlet heater_2 Inlet S003 628 68.6 756 73 heater_2 Outlet info_stream_3 Inlet S004 807 73 1009 72.924 info_stream_3 Outlet sink_1 Inlet S005 581 251 581 113 cooler_3 Heat heater_2 Heat S006 628 295.28 783 294 cooler_3 Outlet info_stream_4 Inlet S007 834 294 1002 295.924 info_stream_4 Outlet sink_2 Inlet S008 353 290 534 295.28 info_stream_2 Outlet cooler_3 Inlet S009 110.5 283.663 302 290 source_1 Outlet info_stream_2 Inlet