Changeset 602 for branches/gui/eml/heat_exchangers
- Timestamp:
- Aug 17, 2008, 8:19:15 PM (15 years ago)
- Location:
- branches/gui/eml/heat_exchangers
- Files:
-
- 5 edited
Legend:
- Unmodified
- Added
- Removed
-
branches/gui/eml/heat_exchangers/heater.mso
r574 r602 29 29 30 30 PARAMETERS 31 outer PP as Plugin(Brief="Physical Properties", Type="PP");31 outer PP as Plugin (Brief="Physical Properties", Type="PP"); 32 32 outer NComp as Integer (Brief="Number of Components"); 33 Ninlet as Integer (Brief="Number of Inlet Streams"); 34 Kvalues as Switcher (Brief="Option for Display Phase Equilibrium K-values",Valid=["yes","no"], Default="yes"); 33 Kvalues as Switcher (Brief="Option for Display Phase Equilibrium K-values",Valid=["yes","no"], Default="yes"); 35 34 36 35 VARIABLES 37 QDuty as power (Brief = "Actual Duty",Symbol="Q_{Duty}"); 38 Vfrac as fraction (Brief = "Vapor fraction Outlet Stream",Symbol="V_{frac}"); 39 Lfrac as fraction (Brief = "Liquid fraction Outlet Stream",Symbol="L_{frac}"); 40 Kvalue(NComp) as Real (Brief = "Phase Equilibrium K-values",Symbol="K_{value}"); 41 Pratio(Ninlet ) as positive (Brief = "Pressure Ratio for each stream", Symbol ="P_{ratio}"); 42 Pdrop(Ninlet ) as press_delta (Brief = "Pressure Drop for each stream", DisplayUnit = 'kPa', Symbol ="\Delta P"); 43 in Inlet(Ninlet ) as stream (Brief = "Inlet Streams", PosX=0, PosY=0.4833, Symbol="^{in}"); 44 out Outlet as streamPH (Brief = "Outlet Stream", PosX=1, PosY=0.4782, Symbol="^{out}"); 36 Duty as power (Brief = "Actual Duty",Symbol="Q_{Duty}"); 37 Vfrac as fraction (Brief = "Vapor fraction Outlet Stream",Symbol="V_{frac}"); 38 Lfrac as fraction (Brief = "Liquid fraction Outlet Stream",Symbol="L_{frac}"); 39 Kvalue(NComp) as Real (Brief = "Phase Equilibrium K-values",Lower=1E-30,Upper=1E30,Symbol="K_{value}"); 40 Pratio as positive (Brief = "Pressure Ratio", Symbol ="P_{ratio}"); 41 Pdrop as press_delta (Brief = "Pressure Drop", DisplayUnit = 'kPa', Symbol ="\Delta P"); 42 43 in Inlet as stream (Brief = "Inlet Stream", PosX=0, PosY=0.45, Symbol="^{in}"); 44 out Outlet as streamPH (Brief = "Outlet Stream", PosX=1, PosY=0.45, Symbol="^{out}"); 45 45 46 46 EQUATIONS 47 47 48 48 "Flow" 49 Outlet.F = sum(Inlet.F);49 Outlet.F = Inlet.F; 50 50 51 51 for j in [1 : NComp] do 52 52 53 53 "Composition" 54 Outlet.F*Outlet.z(j) = sum(Inlet.F*Inlet.z(j));54 Outlet.F*Outlet.z(j) = Inlet.F*Inlet.z(j); 55 55 56 56 end … … 63 63 64 64 "Heat Duty" 65 QDuty = Outlet.F*Outlet.h - sum(Inlet.F*Inlet.h);65 Duty = Outlet.F*Outlet.h - Inlet.F*Inlet.h; 66 66 67 67 "Pressure Drop" … … 72 72 73 73 switch Kvalues # Fix for better convergence !!! 74 74 75 case "yes": 75 76 "K-values Phase Equilibrium" … … 81 82 82 83 end 84 83 85 end 84 86 … … 93 95 94 96 == Specify == 95 * The Inlet stream s: Any Number97 * The Inlet stream 96 98 * Specify: 97 99 **The outlet temperature and the outlet pressure or … … 105 107 106 108 EQUATIONS 107 "Net Duty" 108 Heat = QDuty; 109 110 "Duty Specification" 111 Heat = Duty; 109 112 110 113 end … … 120 123 121 124 == Specify == 122 * The Inlet stream s: Any Number125 * The Inlet stream 123 126 * Specify: 124 127 **The outlet temperature and the outlet pressure or … … 132 135 133 136 EQUATIONS 134 "Net Duty" 135 Heat = -QDuty; 137 138 "Duty Specification" 139 Heat = -Duty; 136 140 137 141 end -
branches/gui/eml/heat_exchangers/icon/cooler.svg
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branches/gui/eml/heat_exchangers/icon/heater.svg
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