Changeset 151 for branches/newlanguage
- Timestamp:
- Feb 5, 2007, 6:47:59 PM (17 years ago)
- Location:
- branches/newlanguage/sample/heat_exchangers
- Files:
-
- 2 edited
Legend:
- Unmodified
- Added
- Removed
-
branches/newlanguage/sample/heat_exchangers/Sample_DoublePipe.mso
r139 r151 36 36 37 37 exchanger as DoublePipe_LMTD; 38 streamhot as source; 39 streamcold as source; 38 # exchanger as DoublePipe_NTU; 39 streamhot as liquid_stream; 40 streamcold as liquid_stream; 40 41 41 42 CONNECTIONS 42 43 43 streamhot .Outletto exchanger.Inlet.Hot;44 streamcold .Outletto exchanger.Inlet.Cold;44 streamhot to exchanger.Inlet.Hot; 45 streamcold to exchanger.Inlet.Cold; 45 46 46 47 SET … … 55 56 #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ 56 57 57 exchanger.HE.FlowDirection = "Counter"; 58 exchanger.HE.TurbulentFlow = "SiederTate"; 58 exchanger.FlowDirection = "counter"; 59 exchanger.InnerTurbulentCorrelation = "SiederTate"; 60 61 exchanger.OuterTurbulentCorrelation = "SiederTate"; 62 exchanger.OuterLaminarCorrelation = "Schlunder"; 59 63 60 64 #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ … … 62 66 #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ 63 67 64 exchanger.H E.HotSide = "Inner";68 exchanger.HotSide = "inner"; 65 69 exchanger.DoInner = 0.04826*"m"; 66 70 exchanger.DiInner = 0.04089*"m"; … … 73 77 # Hot Stream 74 78 #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ 75 streamhot. Outlet.F = 10 * "kmol/h";76 streamhot. Outlet.T = (68+273.15) * "K";77 streamhot. Outlet.P = 5.4 * "bar";78 streamhot. Outlet.z = [1,0];79 streamhot.F = 10 * "kmol/h"; 80 streamhot.T = (68+273.15) * "K"; 81 streamhot.P = 5.4 * "bar"; 82 streamhot.z = [1,0]; 79 83 80 84 #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ 81 85 # Cold Stream 82 86 #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ 83 streamcold. Outlet.F = 5 * "kmol/h";84 streamcold. Outlet.P = 5.1 * "bar";85 streamcold. Outlet.T = (23+273.15) * "K";86 streamcold. Outlet.z = [0,1];87 streamcold.F = 5 * "kmol/h"; 88 streamcold.P = 5.1 * "bar"; 89 streamcold.T = (23+273.15) * "K"; 90 streamcold.z = [0,1]; 87 91 #===================================================================== 88 92 # Fouling … … 94 98 95 99 Dynamic = false; 100 #GuessFile = "Pipe"; 96 101 97 102 end -
branches/newlanguage/sample/heat_exchangers/Sample_DoublePipe_Series.mso
r139 r151 8 8 DEVICES 9 9 10 Pipe(2) as DoublePipe_ LMTD;10 Pipe(2) as DoublePipe_NTU; 11 11 streamhot as source; 12 12 streamcold as source; … … 14 14 CONNECTIONS 15 15 16 streamhot Outlet.to Pipe(1).Inlet.Hot;16 streamhot.Outlet to Pipe(1).Inlet.Hot; 17 17 Pipe(1).Outlet.Hot to Pipe(2).Inlet.Hot; 18 18 19 streamcold Outlet.to Pipe(1).Inlet.Cold;19 streamcold.Outlet to Pipe(1).Inlet.Cold; 20 20 Pipe(1).Outlet.Cold to Pipe(2).Inlet.Cold; 21 21 22 22 PARAMETERS 23 23 24 PP as CalcObject(File="vrpp");24 PP as Plugin(File="vrpp"); 25 25 NComp as Integer; 26 26 … … 36 36 #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ 37 37 38 Pipe. HE.FlowDirection = "Cocurrent";39 Pipe. HE.TurbulentFlow= "SiederTate";38 Pipe.FlowDirection = "cocurrent"; 39 Pipe.InnerTurbulentCorrelation = "SiederTate"; 40 40 41 41 #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ … … 43 43 #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ 44 44 45 Pipe.H E.HotSide = "Inner";45 Pipe.HotSide = "inner"; 46 46 Pipe.DoInner = 0.04826*"m"; 47 47 Pipe.DiInner = 0.04089*"m";
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