|
Last change
on this file since 1 was
1,
checked in by Rafael de Pelegrini Soares, 16 years ago
|
|
Initial import of the library
|
-
Property svn:eol-style set to
native
-
Property svn:keywords set to
Id
|
|
File size:
1.3 KB
|
| Line | |
|---|
| 1 | |
|---|
| 2 | |
|---|
| 3 | using "mixers_splitters/sepComp"; |
|---|
| 4 | |
|---|
| 5 | FlowSheet Sample_sepComp_n |
|---|
| 6 | PARAMETERS |
|---|
| 7 | PP as CalcObject(Brief="Physical Properties",File="vrpp"); |
|---|
| 8 | NComp as Integer; |
|---|
| 9 | |
|---|
| 10 | DEVICES |
|---|
| 11 | stream as stream_therm; |
|---|
| 12 | sep as sepComp_n; |
|---|
| 13 | |
|---|
| 14 | CONNECTIONS |
|---|
| 15 | stream to sep.Inlet; |
|---|
| 16 | |
|---|
| 17 | SET |
|---|
| 18 | PP.Components = [ "isobutane", "n-pentane"]; |
|---|
| 19 | PP.LiquidModel = "PR"; |
|---|
| 20 | PP.VapourModel = "PR"; |
|---|
| 21 | NComp = PP.NumberOfComponents; |
|---|
| 22 | sep.mainComp = 1; |
|---|
| 23 | sep.NOutlet = 3; |
|---|
| 24 | |
|---|
| 25 | SPECIFY |
|---|
| 26 | stream.F = 30 * "kmol/h"; |
|---|
| 27 | stream.P = 120 * "kPa"; |
|---|
| 28 | stream.T = 290 * "K"; |
|---|
| 29 | stream.z = [0.6, 0.4]; |
|---|
| 30 | stream.v = 0; |
|---|
| 31 | sep.Outlet(1).z(1) = 0.7; |
|---|
| 32 | sep.Outlet(2).z(1) = 0.1; |
|---|
| 33 | sep.frac(1) = 0.4; |
|---|
| 34 | sep.frac(2) = 0.2; |
|---|
| 35 | # sep.recovery(1) = 0.533333; |
|---|
| 36 | # sep.recovery(2) = 0.033333; |
|---|
| 37 | |
|---|
| 38 | OPTIONS |
|---|
| 39 | outputLevel = "high"; |
|---|
| 40 | relativeAccuracy = 1e-7; |
|---|
| 41 | |
|---|
| 42 | end |
|---|
| 43 | |
|---|
| 44 | |
|---|
| 45 | FlowSheet Sample_sepComp |
|---|
| 46 | PARAMETERS |
|---|
| 47 | PP as CalcObject(Brief="Physical Properties",File="vrpp"); |
|---|
| 48 | NComp as Integer; |
|---|
| 49 | |
|---|
| 50 | DEVICES |
|---|
| 51 | stream as streamTP; |
|---|
| 52 | sep as sepComp; |
|---|
| 53 | |
|---|
| 54 | CONNECTIONS |
|---|
| 55 | stream to sep.Inlet; |
|---|
| 56 | |
|---|
| 57 | SET |
|---|
| 58 | PP.Components = [ "isobutane", "n-pentane"]; |
|---|
| 59 | PP.LiquidModel = "PR"; |
|---|
| 60 | PP.VapourModel = "PR"; |
|---|
| 61 | NComp = PP.NumberOfComponents; |
|---|
| 62 | sep.mainComp = 1; |
|---|
| 63 | |
|---|
| 64 | SPECIFY |
|---|
| 65 | stream.F = 30 * "kmol/h"; |
|---|
| 66 | stream.P = 120 * "kPa"; |
|---|
| 67 | stream.T = 290 * "K"; |
|---|
| 68 | stream.z = [0.6, 0.4]; |
|---|
| 69 | sep.Outlet1.z(1) = 0.7; |
|---|
| 70 | sep.frac = 0.4; |
|---|
| 71 | # sep.recovery = 0.533333; |
|---|
| 72 | |
|---|
| 73 | OPTIONS |
|---|
| 74 | outputLevel = "high"; |
|---|
| 75 | relativeAccuracy = 1e-7; |
|---|
| 76 | |
|---|
| 77 | end |
|---|
Note: See
TracBrowser
for help on using the repository browser.
