|
Last change
on this file since 46 was
46,
checked in by Paula Bettio Staudt, 16 years ago
|
|
Fixed some sample files
|
-
Property svn:eol-style set to
native
-
Property svn:keywords set to
Id
|
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File size:
1.6 KB
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| Rev | Line | |
|---|
| [1] | 1 | using "stage_separators/tank"; |
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| 2 | |
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| 3 | FlowSheet tank_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 | SET |
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| 8 | PP.Components = ["ethane", "propane", "propylene", "1-butene", "n-hexane"]; |
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| 9 | PP.LiquidModel = "PR"; |
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| 10 | PP.VapourModel = "PR"; |
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| 11 | NComp = PP.NumberOfComponents; |
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| 12 | |
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| [46] | 13 | VARIABLES |
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| 14 | Qtank as heat_rate (Brief="Heat rate supplied to tank"); |
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| 15 | |
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| [1] | 16 | DEVICES |
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| 17 | t as tank; |
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| 18 | s as stream_therm; |
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| 19 | |
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| 20 | CONNECTIONS |
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| 21 | s to t.Inlet; |
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| [46] | 22 | Qtank to t.Q; |
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| [1] | 23 | |
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| 24 | SPECIFY |
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| 25 | s.P = 480 * "kPa"; |
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| 26 | s.T = 310 * "K"; |
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| 27 | s.F = 180 * "kmol/h"; |
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| 28 | s.z = 1.0/NComp; |
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| 29 | s.v = 0.698; |
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| [42] | 30 | |
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| [46] | 31 | Qtank = 0 * "J/s"; |
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| [1] | 32 | t.Outlet.F = 179 * "kmol/h"; |
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| 33 | |
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| 34 | SET |
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| 35 | t.Across = 2.20 * "m^2"; |
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| 36 | |
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| 37 | INITIAL |
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| 38 | t.Outlet.T = 305 *"K"; |
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| 39 | t.Level = 0.5 * "m"; |
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| 40 | t.Outlet.z([1:4]) = 1.0/NComp; |
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| 41 | |
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| 42 | OPTIONS |
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| 43 | relativeAccuracy = 1e-5; |
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| 44 | time = [0:100:1000]; |
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| 45 | end |
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| 46 | |
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| 47 | FlowSheet tank_cylindrical_Test |
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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 | SET |
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| 52 | PP.Components = ["propane", "propylene", "1-butene","1,3-butadiene", "n-hexane"]; |
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| 53 | PP.LiquidModel = "PR"; |
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| 54 | PP.VapourModel = "PR"; |
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| 55 | NComp = PP.NumberOfComponents; |
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| [46] | 56 | |
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| 57 | VARIABLES |
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| 58 | Qtank as heat_rate (Brief="Heat rate supplied to tank"); |
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| [1] | 59 | |
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| 60 | DEVICES |
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| 61 | t as tank_cylindrical; |
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| 62 | s as stream_therm; |
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| 63 | |
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| 64 | CONNECTIONS |
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| 65 | s to t.Inlet; |
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| [46] | 66 | Qtank to t.Q; |
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| [1] | 67 | |
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| 68 | SPECIFY |
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| 69 | s.F = 500 * "kmol/h"; |
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| 70 | s.T = 300 * "K"; |
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| 71 | s.P = 400 * "kPa"; |
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| 72 | s.z = 1/NComp; |
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| 73 | s.v = 0.368; |
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| 74 | |
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| [46] | 75 | Qtank = 0 * "J/s"; |
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| [1] | 76 | t.Outlet.F = 490 * "kmol/h"; |
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| 77 | |
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| 78 | SET |
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| 79 | t.radius = 0.9 * "m"; |
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| 80 | t.L = 7.12 * "m"; |
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| 81 | |
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| 82 | INITIAL |
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| 83 | t.Outlet.T = 280*"K"; |
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| 84 | t.Level = 1 * "m"; |
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| 85 | t.Outlet.z([1:4]) = 1.0/NComp; |
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| 86 | |
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| 87 | OPTIONS |
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| 88 | relativeAccuracy = 1e-5; |
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| 89 | time = [0:100:1000]; |
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| 90 | end |
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