| 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 mixer |
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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: Maurício Carvalho Maciel |
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| 23 | * $Id: sample_mixer.mso 400 2007-11-09 21:41:38Z bicca $ |
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| 24 | *--------------------------------------------------------------------*# |
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| 25 | using "mixers_splitters/mixer"; |
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| 26 | |
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| 27 | FlowSheet SampleMixer |
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| 28 | |
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| 29 | PARAMETERS |
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| 30 | PP as Plugin(Brief="Physical Properties",Type="PP",Components = [ "isobutane", "benzene", "methane" ], |
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| 31 | LiquidModel = "PR", |
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| 32 | VapourModel = "PR"); |
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| 33 | |
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| 34 | NComp as Integer; |
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| 35 | |
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| 36 | DEVICES |
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| 37 | stream1 as source; |
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| 38 | stream2 as source; |
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| 39 | mixer1 as mixer; |
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| 40 | |
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| 41 | |
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| 42 | SET |
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| 43 | |
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| 44 | NComp = PP.NumberOfComponents; |
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| 45 | mixer1.Ninlet = 2; |
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| 46 | |
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| 47 | CONNECTIONS |
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| 48 | stream1.Outlet to mixer1.Inlet(1); |
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| 49 | stream2.Outlet to mixer1.Inlet(2); |
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| 50 | |
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| 51 | SPECIFY |
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| 52 | |
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| 53 | stream1.Outlet.F = 20 * 'kmol/h'; |
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| 54 | stream1.Outlet.P = 120 * 'kPa'; |
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| 55 | stream1.Outlet.T = 400 * 'K'; |
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| 56 | stream1.Outlet.z = [0.5, 0.1, 0.4]; |
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| 57 | |
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| 58 | |
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| 59 | stream2.Outlet.F = 10 * 'kmol/h'; |
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| 60 | stream2.Outlet.P = 120 * 'kPa'; |
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| 61 | stream2.Outlet.T = 290 * 'K'; |
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| 62 | stream2.Outlet.z = [0.5, 0.1, 0.4]; |
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| 63 | |
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| 64 | OPTIONS |
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| 65 | Dynamic = false; |
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| 66 | NLASolver( |
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| 67 | RelativeAccuracy = 1e-6 |
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| 68 | ); |
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| 69 | end |
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| 70 | |
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