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Last change
on this file since 33 was
33,
checked in by Argimiro Resende Secchi, 17 years ago
|
|
clean up.
|
-
Property svn:eol-style set to
native
-
Property svn:keywords set to
Id
|
|
File size:
1.2 KB
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| Line | |
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| 1 | using "pressure_changers/valve"; |
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| 2 | |
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| 3 | FlowSheet valve_Test_V |
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| 4 | # with vapour conditions |
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| 5 | PARAMETERS |
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| 6 | PP as CalcObject(Brief="Physical Properties",File="vrpp"); |
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| 7 | NComp as Integer; |
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| 8 | |
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| 9 | SET |
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| 10 | PP.Components = [ "isobutane", "n-pentane"]; |
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| 11 | PP.LiquidModel = "PR"; |
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| 12 | PP.VapourModel = "PR"; |
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| 13 | NComp = PP.NumberOfComponents; |
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| 14 | |
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| 15 | DEVICES |
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| 16 | v1 as valve; |
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| 17 | s1 as stream_therm; |
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| 18 | |
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| 19 | CONNECTIONS |
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| 20 | s1 to v1.Inlet; |
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| 21 | |
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| 22 | SPECIFY |
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| 23 | s1.P = 150 * "kPa"; |
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| 24 | s1.T = 281.75 * "K"; |
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| 25 | s1.z = [0.664, 0.336]; |
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| 26 | s1.v = 0.0; |
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| 27 | |
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| 28 | v1.x = 0.866; |
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| 29 | v1.Outlet.P = 148 * "kPa"; |
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| 30 | |
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| 31 | SET |
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| 32 | v1.k = 20 * "gal/min/psi^0.5"; |
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| 33 | |
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| 34 | OPTIONS |
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| 35 | relativeAccuracy = 1e-6; |
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| 36 | time = [0:20:1000]; |
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| 37 | mode = "steady"; |
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| 38 | |
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| 39 | end |
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| 40 | |
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| 41 | FlowSheet valve_Test_L |
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| 42 | #with liquid conditions |
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| 43 | PARAMETERS |
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| 44 | PP as CalcObject(Brief="Physical Properties",File="vrpp"); |
|---|
| 45 | NComp as Integer; |
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| 46 | |
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| 47 | SET |
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| 48 | PP.Components = [ "isobutane", "n-pentane"]; |
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| 49 | PP.LiquidModel = "PR"; |
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| 50 | PP.VapourModel = "PR"; |
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| 51 | NComp = PP.NumberOfComponents; |
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| 52 | |
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| 53 | DEVICES |
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| 54 | v1 as valve; |
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| 55 | s1 as stream_therm; |
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| 56 | |
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| 57 | CONNECTIONS |
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| 58 | s1 to v1.Inlet; |
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| 59 | |
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| 60 | SPECIFY |
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| 61 | s1.P = 185 * "kPa"; |
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| 62 | s1.T = 328.12 * "K"; |
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| 63 | s1.z = [0.001848, 0.9982]; |
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| 64 | s1.v = 0.0; |
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| 65 | |
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| 66 | v1.x = 0.3363; |
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| 67 | v1.Outlet.P = 183 * "kPa"; |
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| 68 | |
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| 69 | SET |
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| 70 | v1.k = 20 * "gal/min/psi^0.5"; |
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| 71 | |
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| 72 | OPTIONS |
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| 73 | relativeAccuracy = 1e-6; |
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| 74 | time = [0:20:1000]; |
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| 75 | mode = "steady"; |
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| 76 | |
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| 77 | end |
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