| 1 | #*---------------------------------------------- |
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| 2 | * FlowSheet generated automaticaly by EMSO-GUI |
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| 3 | *----------------------------------------------*# |
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| 4 | |
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| 5 | using "streams"; |
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| 6 | using "heat_exchangers/heater"; |
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| 7 | |
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| 8 | FlowSheet Cooler_Diagram |
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| 9 | PARAMETERS |
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| 10 | PP as Plugin(Brief="Physical Properties", |
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| 11 | Type="PP", |
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| 12 | Components = ["n-hexane","isobutane","n-pentane"], |
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| 13 | LiquidModel = "PR", |
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| 14 | VapourModel = "PR" |
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| 15 | ); |
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| 16 | NComp as Integer; |
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| 17 | SET |
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| 18 | NComp = PP.NumberOfComponents; |
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| 19 | |
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| 20 | DEVICES |
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| 21 | source_1 as source; |
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| 22 | |
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| 23 | SET |
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| 24 | source_1.ValidPhases = "Vapour-Liquid"; |
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| 25 | |
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| 26 | SPECIFY |
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| 27 | source_1.Composition(1) = 0.5; |
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| 28 | source_1.Composition(2) = 0.3; |
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| 29 | source_1.Composition(3) = 0.2; |
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| 30 | source_1.Fw = 749.552 * 'kg/h'; |
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| 31 | source_1.T_Cdeg = 65.85 * 'K'; |
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| 32 | source_1.P = 3 * 'atm'; |
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| 33 | |
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| 34 | INITIAL |
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| 35 | |
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| 36 | GUESS |
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| 37 | |
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| 38 | DEVICES |
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| 39 | heater_1 as heater; |
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| 40 | |
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| 41 | SET |
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| 42 | heater_1.Kvalues = "no"; |
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| 43 | |
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| 44 | SPECIFY |
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| 45 | heater_1.Outlet.P = 1 * 'atm'; |
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| 46 | |
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| 47 | INITIAL |
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| 48 | |
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| 49 | GUESS |
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| 50 | |
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| 51 | DEVICES |
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| 52 | simple_source_1 as simple_source; |
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| 53 | |
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| 54 | SET |
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| 55 | |
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| 56 | SPECIFY |
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| 57 | simple_source_1.MolarComposition(1) = 1; |
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| 58 | simple_source_1.MolarComposition(2) = 0; |
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| 59 | simple_source_1.MolarComposition(3) = 0; |
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| 60 | simple_source_1.F = 1 * 'kmol/h'; |
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| 61 | simple_source_1.T = 300 * 'K'; |
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| 62 | simple_source_1.P = 1 * 'atm'; |
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| 63 | |
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| 64 | INITIAL |
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| 65 | |
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| 66 | GUESS |
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| 67 | |
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| 68 | DEVICES |
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| 69 | simple_sink_1 as simple_sink; |
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| 70 | |
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| 71 | SET |
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| 72 | |
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| 73 | SPECIFY |
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| 74 | |
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| 75 | INITIAL |
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| 76 | |
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| 77 | GUESS |
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| 78 | |
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| 79 | DEVICES |
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| 80 | cooler_1 as cooler; |
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| 81 | |
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| 82 | SET |
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| 83 | cooler_1.Kvalues = "no"; |
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| 84 | |
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| 85 | SPECIFY |
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| 86 | cooler_1.Pdrop = 15 * 'kPa'; |
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| 87 | cooler_1.Outlet.T = 303 * 'K'; |
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| 88 | |
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| 89 | INITIAL |
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| 90 | |
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| 91 | GUESS |
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| 92 | |
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| 93 | DEVICES |
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| 94 | simple_sink_1_1 as simple_sink; |
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| 95 | |
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| 96 | SET |
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| 97 | |
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| 98 | SPECIFY |
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| 99 | |
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| 100 | INITIAL |
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| 101 | |
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| 102 | GUESS |
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| 103 | |
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| 104 | CONNECTIONS |
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| 105 | simple_source_1.Outlet to heater_1.Inlet; |
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| 106 | heater_1.Outlet to simple_sink_1.Inlet; |
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| 107 | source_1.Outlet to cooler_1.Inlet; |
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| 108 | cooler_1.Heat to heater_1.Heat; |
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| 109 | cooler_1.Outlet to simple_sink_1_1.Inlet; |
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| 110 | |
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| 111 | OPTIONS |
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| 112 | Dynamic = false; |
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| 113 | Integration = "original"; |
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| 114 | NLASolver( |
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| 115 | File = "sundials", |
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| 116 | RelativeAccuracy = 1e-3, |
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| 117 | AbsoluteAccuracy = 1e-6, |
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| 118 | MaxIterations = 100 |
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| 119 | ); |
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| 120 | DAESolver( |
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| 121 | File = "sundials", |
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| 122 | RelativeAccuracy = 1e-3, |
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| 123 | AbsoluteAccuracy = 1e-6, |
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| 124 | EventAccuracy = 1e-2 |
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| 125 | ); |
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| 126 | end |
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