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 streams |
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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: Rafael de Pelegrini Soares |
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23 | * $Id: sample_streams.mso 83 2006-12-08 20:29:34Z paula $ |
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24 | *--------------------------------------------------------------------*# |
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25 | |
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26 | using "streams"; |
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27 | |
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28 | FlowSheet SampleStreams |
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29 | PARAMETERS |
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30 | NComp as Integer(Default=5); |
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31 | |
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32 | DEVICES |
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33 | s1 as stream; |
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34 | |
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35 | SPECIFY |
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36 | s1.F = 10 * "kmol/h"; |
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37 | s1.T = 300 * "K"; |
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38 | s1.P = 1 * "atm"; |
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39 | s1.z = 1/NComp; |
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40 | s1.h = 5 * "J/kmol"; |
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41 | s1.v = 0.0; |
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42 | |
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43 | OPTIONS |
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44 | mode = "steady"; |
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45 | end |
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46 | |
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47 | FlowSheet SampleStreamsTherm |
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48 | PARAMETERS |
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49 | PP as CalcObject(Brief="Physical Properties", File="vrpp"); |
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50 | NComp as Integer; |
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51 | |
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52 | SET |
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53 | PP.LiquidModel = "IdealLiquid"; |
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54 | PP.VapourModel = "Ideal"; |
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55 | PP.Components = [ "isobutane", "benzene", "ethanol" ]; |
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56 | NComp = PP.NumberOfComponents; |
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57 | |
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58 | DEVICES |
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59 | sl as stream_therm; |
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60 | sv as stream_therm; |
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61 | |
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62 | SPECIFY |
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63 | sl.F = 10 * "kmol/h"; |
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64 | sl.T = 300 * "K"; |
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65 | sl.P = 100 * "kPa"; |
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66 | sl.z = [0.24596, 0.370278, 0.383762]; |
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67 | sl.v = 0.0; #liquid stream |
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68 | |
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69 | |
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70 | sv.F = 10 * "kmol/h"; |
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71 | #sv.h = 20248 * "J/mol"; |
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72 | sv.T = 300 * "K"; |
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73 | sv.P = 100 * "kPa"; |
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74 | #sv.z = [0.824212, 0.12577, 0.0500176]; |
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75 | sv.v = 1.0; #vapor stream |
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76 | |
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77 | EQUATIONS |
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78 | "Liquid-Vapour equilibrium" |
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79 | PP.VapourFugacityCoefficient(sv.T, sv.P, sv.z) * sv.z = |
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80 | PP.LiquidFugacityCoefficient(sl.T, sl.P, sl.z) * sl.z; |
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81 | |
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82 | OPTIONS |
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83 | #mode = "steady"; |
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84 | end |
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