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Last change
on this file since 4 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:
1005 bytes
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| Line | |
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| 1 | using "stage_separators/reboiler"; |
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| 2 | |
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| 3 | FlowSheet reboiler_Test |
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| 4 | PARAMETERS |
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| 5 | PP as CalcObject(Brief="Physical Properties",File="vrpp"); |
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| 6 | NComp as Integer; |
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| 7 | |
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| 8 | VARIABLES |
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| 9 | Q as heat_rate (Brief="Heat supplied"); |
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| 10 | |
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| 11 | SET |
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| 12 | PP.Components = [ "isobutane", "n-pentane"]; |
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| 13 | PP.LiquidModel = "PR"; |
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| 14 | PP.VapourModel = "PR"; |
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| 15 | NComp = PP.NumberOfComponents; |
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| 16 | |
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| 17 | DEVICES |
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| 18 | r1 as reboiler; |
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| 19 | feed as stream_therm; |
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| 20 | s1 as stream_therm; |
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| 21 | |
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| 22 | CONNECTIONS |
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| 23 | feed to r1.Inlet; |
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| 24 | s1 to r1.InletL; |
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| 25 | Q to r1.Q; |
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| 26 | |
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| 27 | SPECIFY |
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| 28 | feed.F = 0 * "kmol/h"; |
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| 29 | feed.T = 328 * "K"; |
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| 30 | feed.P = 180 * "kPa"; |
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| 31 | feed.z = [0.5, 0.5]; |
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| 32 | feed.v = 0; |
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| 33 | |
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| 34 | s1.P = 185 * "kPa"; |
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| 35 | s1.T = 327.7 * "K"; |
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| 36 | s1.F = 180 * "kmol/h"; |
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| 37 | s1.z = [0.006061, 0.9939]; |
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| 38 | s1.v = 0.0; |
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| 39 | |
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| 40 | r1.OutletL.F = 28.4 * "kmol/h"; |
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| 41 | r1.OutletV.F = 151.6 * "kmol/h"; |
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| 42 | |
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| 43 | Q = 3.7743e6 * "kJ/h"; |
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| 44 | |
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| 45 | SET |
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| 46 | r1.V = 2 * "m^3"; |
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| 47 | r1.Across = 1 * "m^2"; |
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| 48 | |
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| 49 | INITIAL |
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| 50 | r1.OutletL.T = 320 *"K"; |
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| 51 | r1.Level = 1 * "m"; |
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| 52 | r1.OutletL.z(2) = 0.9; |
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| 53 | |
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| 54 | OPTIONS |
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| 55 | relativeAccuracy = 1e-5; |
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| 56 | outputLevel = "high"; |
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| 57 | |
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| 58 | time = [0:20:1000]; |
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| 59 | end |
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