| 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 sepComp_n and sepComp |
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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_sepComp.mso 80 2006-12-08 19:46:22Z paula $ |
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| 24 | *--------------------------------------------------------------------*# |
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| 25 | |
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| 26 | using "mixers_splitters/sepComp"; |
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| 27 | |
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| 28 | FlowSheet Sample_sepComp_n |
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| 29 | PARAMETERS |
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| 30 | PP as CalcObject(Brief="Physical Properties",File="vrpp"); |
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| 31 | NComp as Integer; |
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| 32 | |
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| 33 | DEVICES |
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| 34 | stream as stream_therm; |
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| 35 | sep as sepComp_n; |
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| 36 | |
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| 37 | CONNECTIONS |
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| 38 | stream to sep.Inlet; |
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| 39 | |
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| 40 | SET |
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| 41 | PP.Components = [ "isobutane", "benzene"]; |
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| 42 | PP.LiquidModel = "PR"; |
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| 43 | PP.VapourModel = "PR"; |
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| 44 | NComp = PP.NumberOfComponents; |
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| 45 | sep.mainComp = 1; |
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| 46 | sep.NOutlet = 3; |
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| 47 | |
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| 48 | SPECIFY |
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| 49 | stream.F = 30 * "kmol/h"; |
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| 50 | stream.P = 120 * "kPa"; |
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| 51 | stream.T = 290 * "K"; |
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| 52 | stream.z = [0.6, 0.4]; |
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| 53 | stream.v = 0; |
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| 54 | sep.Outlet(1).z(1) = 0.7; |
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| 55 | sep.Outlet(2).z(1) = 0.1; |
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| 56 | sep.frac(1) = 0.4; |
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| 57 | sep.frac(2) = 0.2; |
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| 58 | # sep.recovery(1) = 0.533333; |
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| 59 | # sep.recovery(2) = 0.033333; |
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| 60 | |
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| 61 | OPTIONS |
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| 62 | relativeAccuracy = 1e-7; |
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| 63 | |
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| 64 | end |
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| 65 | |
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| 66 | |
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| 67 | FlowSheet Sample_sepComp |
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| 68 | PARAMETERS |
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| 69 | PP as CalcObject(Brief="Physical Properties",File="vrpp"); |
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| 70 | NComp as Integer; |
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| 71 | |
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| 72 | DEVICES |
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| 73 | stream as streamTP; |
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| 74 | sep as sepComp; |
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| 75 | |
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| 76 | CONNECTIONS |
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| 77 | stream to sep.Inlet; |
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| 78 | |
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| 79 | SET |
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| 80 | PP.Components = [ "isobutane", "benzene"]; |
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| 81 | PP.LiquidModel = "PR"; |
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| 82 | PP.VapourModel = "PR"; |
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| 83 | NComp = PP.NumberOfComponents; |
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| 84 | sep.mainComp = 1; |
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| 85 | |
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| 86 | SPECIFY |
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| 87 | stream.F = 30 * "kmol/h"; |
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| 88 | stream.P = 120 * "kPa"; |
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| 89 | stream.T = 290 * "K"; |
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| 90 | stream.z = [0.6, 0.4]; |
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| 91 | sep.Outlet1.z(1) = 0.7; |
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| 92 | sep.frac = 0.4; |
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| 93 | # sep.recovery = 0.533333; |
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| 94 | |
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| 95 | OPTIONS |
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| 96 | relativeAccuracy = 1e-7; |
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| 97 | |
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| 98 | end |
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