Last change
on this file since 1 was
1,
checked in by Rafael de Pelegrini Soares, 17 years ago
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Initial import of the library
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-
Property svn:eol-style set to
native
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Property svn:keywords set to
Id
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File size:
1.0 KB
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Rev | Line | |
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[1] | 1 | using "stage_separators/batch_dist"; |
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| 2 | |
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| 3 | |
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| 4 | FlowSheet TesteBatch |
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| 5 | |
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| 6 | PARAMETERS |
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| 7 | PP as CalcObject(Brief="Physical Properties",File="vrpp"); |
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| 8 | NComp as Integer; |
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| 9 | |
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| 10 | SET |
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| 11 | PP.Components = [ "isobutane", "n-pentane" ]; |
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| 12 | PP.LiquidModel = "PR"; |
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| 13 | PP.VapourModel = "PR"; |
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| 14 | NComp = PP.NumberOfComponents; |
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| 15 | |
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| 16 | DEVICES |
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| 17 | batch as Diff_Dist; |
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| 18 | reflux as stream_therm; |
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| 19 | feed as stream_therm; |
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| 20 | |
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| 21 | CONNECTIONS |
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| 22 | reflux to batch.InletL; |
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| 23 | feed to batch.Inlet; |
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| 24 | |
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| 25 | EQUATIONS |
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| 26 | if batch.Level > 1E-3 then |
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| 27 | batch.OutletV.F = 150 * "kmol/h"; |
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| 28 | batch.Q = 3.7743e6 * "kJ/h"; |
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| 29 | else |
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| 30 | batch.OutletV.F = 0 * "kmol/h"; |
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| 31 | batch.Q = 0 * "kJ/h"; |
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| 32 | end |
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| 33 | |
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| 34 | SPECIFY |
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| 35 | reflux.F = 0 * "kmol/h"; |
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| 36 | reflux.T = 328 * "K"; |
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| 37 | reflux.P = 180 * "kPa"; |
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| 38 | reflux.z = [0.5, 0.5]; |
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| 39 | reflux.v = 0; |
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| 40 | |
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| 41 | feed.F = 0 * "kmol/h"; |
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| 42 | feed.T = 328 * "K"; |
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| 43 | feed.P = 180 * "kPa"; |
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| 44 | feed.z = [0.5, 0.5]; |
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| 45 | feed.v = 0; |
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| 46 | |
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| 47 | SET |
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| 48 | batch.V = 3 * "m^3"; |
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| 49 | batch.Across = 1 * "m^2"; |
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| 50 | |
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| 51 | INITIAL |
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| 52 | batch.T = 298 *"K"; |
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| 53 | batch.Level = 2.5 * "m"; |
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| 54 | batch.x(2) = 0.2; |
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| 55 | |
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| 56 | OPTIONS |
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| 57 | relativeAccuracy = 1e-5; |
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| 58 | outputLevel = "high"; |
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| 59 | |
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| 60 | time = [0:0.1:20]*"min"; |
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| 61 | end |
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