| 1 | #*------------------------------------------------------------------- |
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| 2 | * EMSO Model Library (EML) Copyright (C) 2004 - 2007 ALSOC. |
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| 3 | * |
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| 4 | * This LIBRARY is free software; you can distribute it and/or modify |
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| 5 | * it under the therms of the ALSOC FREE LICENSE as available at |
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| 6 | * http://www.enq.ufrgs.br/alsoc. |
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| 7 | * |
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| 8 | * EMSO Copyright (C) 2004 - 2007 ALSOC, original code |
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| 9 | * from http://www.rps.eng.br Copyright (C) 2002-2004. |
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| 10 | * All rights reserved. |
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| 11 | * |
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| 12 | * EMSO is distributed under the therms of the ALSOC LICENSE as |
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| 13 | * available at http://www.enq.ufrgs.br/alsoc. |
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| 14 | * |
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| 15 | *-------------------------------------------------------------------- |
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| 16 | * Sample file for model Hidraulic turbine |
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| 17 | *-------------------------------------------------------------------- |
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| 18 | * |
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| 19 | * This sample file needs VRTherm DEMO (www.vrtech.com.br) to run. |
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| 20 | * |
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| 21 | *---------------------------------------------------------------------- |
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| 22 | * Author: Andrey Copat, Estefane S. Horn, Marcos L. Alencastro |
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| 23 | * $Id: sample_turbine.mso 585 2008-07-28 23:31:29Z bicca $ |
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| 24 | *--------------------------------------------------------------------*# |
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| 25 | |
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| 26 | using "pressure_changers/turbine"; |
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| 27 | |
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| 28 | FlowSheet HTurbine_HT1 |
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| 29 | |
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| 30 | DEVICES |
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| 31 | S1 as source; |
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| 32 | HT1 as HidraulicTurbine; |
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| 33 | |
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| 34 | CONNECTIONS |
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| 35 | S1.Outlet to HT1.Inlet; |
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| 36 | |
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| 37 | PARAMETERS |
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| 38 | PP as Plugin (Brief="External Physical Properties", |
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| 39 | Type="PP", |
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| 40 | Components = ["water", "benzene"], |
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| 41 | LiquidModel = "PR", |
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| 42 | VapourModel = "PR" |
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| 43 | ); |
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| 44 | Mw as positive (Brief = "Molar Mass", Unit = 'kg/kmol'); |
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| 45 | NComp as Integer (Default= 1); |
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| 46 | |
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| 47 | SET |
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| 48 | NComp = PP.NumberOfComponents(); |
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| 49 | |
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| 50 | S1.ValidPhases = "Vapour-Liquid"; |
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| 51 | S1.CompositionBasis = "Molar"; |
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| 52 | |
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| 53 | SPECIFY |
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| 54 | HT1.Beta = 425e-6 / 'K'; |
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| 55 | HT1.Meff = 0.95; |
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| 56 | HT1.Eff = 0.72; |
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| 57 | |
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| 58 | S1.F = 1000 * 'kmol/h'; |
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| 59 | S1.P = 5 * 'atm' ; |
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| 60 | S1.T = 298 * 'K' ; |
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| 61 | S1.Composition = [1]; |
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| 62 | |
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| 63 | #HT1.Pdrop = 100 * 'kPa'; |
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| 64 | HT1.Outlet.P = 1 * 'atm'; |
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| 65 | |
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| 66 | end |
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