- Timestamp:
- Aug 15, 2008, 10:31:59 PM (15 years ago)
- Location:
- branches/gui
- Files:
-
- 2 edited
-
eml/pressure_changers/compressor.mso (modified) (6 diffs)
-
sample/pressure_changers/compressor_diagram.pfd (modified) (29 diffs)
Legend:
- Unmodified
- Added
- Removed
-
branches/gui/eml/pressure_changers/compressor.mso
r598 r599 21 21 22 22 Model centrifugal_compressor 23 24 # Do Not Forget to Update The Losses by Mechanical Efficiency !!!! 23 25 24 26 ATTRIBUTES … … 38 40 VARIABLES 39 41 40 PolyCoeff as positive (Brief = "Polytropic Coefficient", Lower= 0);41 IseCoeff as positive (Brief = "Isentropic Coefficient", Lower=1 e-3);42 Cp as cp_mol (Brief = "Heat Capacity ");43 Cv as cv_mol (Brief = "Heat Capacity ");42 PolyCoeff as positive (Brief = "Polytropic Coefficient", Lower=1E-6); 43 IseCoeff as positive (Brief = "Isentropic Coefficient", Lower=1E-6); 44 Cp as cp_mol (Brief = "Heat Capacity at constant Pressure"); 45 Cv as cv_mol (Brief = "Heat Capacity at constant Volume"); 44 46 Pratio as positive (Brief = "Pressure Ratio", Symbol ="P_{ratio}"); 45 47 Pdrop as press_delta (Brief = "Pressure Drop", DisplayUnit = 'kPa', Symbol ="\Delta P"); 48 Pincrease as press_delta (Brief = "Pressure Increase", DisplayUnit = 'kPa', Symbol ="P_{incr}"); 46 49 47 Head as energy_mass (Brief = " IsentropicHead");50 Head as energy_mass (Brief = "Head"); 48 51 Tiso as temperature (Brief = "Isentropic Temperature"); 49 52 … … 86 89 Outlet.P = Inlet.P - Pdrop; 87 90 91 "Pressure Increase" 92 Outlet.P = Inlet.P + Pincrease; 93 88 94 "Mass Density" 89 95 rho = PP.VapourDensity(Inlet.T, Inlet.P, Inlet.z); … … 104 110 IseCoeff * Cv = Cp; 105 111 106 #+++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++107 112 switch CompressorType 108 113 … … 110 115 111 116 "Isentropic Head" 112 Head = (0.5*Zfac_in+0.5*Zfac_out)*(1/Mwm)*(IseCoeff/(IseCoeff-1 ))*Rgas*Inlet.T*((Outlet.P/Inlet.P)^((IseCoeff-1)/IseCoeff) - 1);117 Head = (0.5*Zfac_in+0.5*Zfac_out)*(1/Mwm)*(IseCoeff/(IseCoeff-1.001))*Rgas*Inlet.T*((Outlet.P/Inlet.P)^((IseCoeff-1.001)/IseCoeff) - 1); 113 118 114 119 "Fluid Power" 115 120 FluidPower*IsentropicEff = Head*sum(Mw*Inlet.z)*Inlet.F; 116 121 122 "Discharge Temperature" 123 Outlet.T = Inlet.T*((Outlet.P/Inlet.P)^((IseCoeff-1.001)/IseCoeff)); 124 117 125 case "Polytropic Operation": 118 126 119 127 "Polytropic Head" 120 Head = (0.5*Zfac_in+0.5*Zfac_out)*(1/Mwm)*(PolyCoeff/(PolyCoeff-1 ))*Rgas*Inlet.T*((Outlet.P/Inlet.P)^((PolyCoeff-1)/PolyCoeff) - 1);128 Head = (0.5*Zfac_in+0.5*Zfac_out)*(1/Mwm)*(PolyCoeff/(PolyCoeff-1.001))*Rgas*Inlet.T*((Outlet.P/Inlet.P)^((PolyCoeff-1.001)/PolyCoeff) - 1); 121 129 122 130 "Fluid Power" 123 131 FluidPower*PolytropicEff = Head*sum(Mw*Inlet.z)*Inlet.F; 132 133 "Discharge Temperature" 134 Outlet.T = Inlet.T*((Outlet.P/Inlet.P)^((PolyCoeff-1.001)/PolyCoeff)); 124 135 125 136 end … … 128 139 PP.VapourEntropy(Tiso, Outlet.P, Outlet.z) = PP.VapourEntropy(Inlet.T, Inlet.P, Inlet.z); 129 140 130 "Discharge Temperature"131 IsentropicEff * (Outlet.T- Inlet.T) = (Tiso - Inlet.T);141 #"Calculate Politropic Coefficient" 142 #PolyCoeff*(ln(Outlet.T/Inlet.T)) = (PolyCoeff-1)*(ln(Outlet.P/Inlet.P)); 132 143 133 "Calculate Politropic Coefficient" 134 PolyCoeff*(ln(Outlet.T/Inlet.T)) = (PolyCoeff-1)*(ln(Outlet.P/Inlet.P)); 135 136 #"Polytropic Efficiency" 137 #PolytropicEff * (PolyCoeff-1) * IseCoeff = PolyCoeff * (IseCoeff-1); 144 "Polytropic Efficiency" 145 PolytropicEff * (PolyCoeff-1) * IseCoeff = PolyCoeff * (IseCoeff-1); 138 146 139 147 "Fluid Power" -
branches/gui/sample/pressure_changers/compressor_diagram.pfd
r598 r599 4 4 <Physical_Properties> 5 5 <Component>propane</Component> 6 <Liquid_Model>IdealLiquid</Liquid_Model> 7 <Vapour_Model>Ideal</Vapour_Model> 6 <Component>water</Component> 7 <Liquid_Model>PR</Liquid_Model> 8 <Vapour_Model>PR</Vapour_Model> 8 9 </Physical_Properties> 9 10 <Options> … … 56 57 <Block_Properties> 57 58 <Model_File_Path>pressure_changers\compressor</Model_File_Path> 58 <Instance_Id>c entrifugal_compressor_1</Instance_Id>59 <Instance_Id>compressor</Instance_Id> 59 60 <Model_Name>centrifugal_compressor</Model_Name> 60 61 <T_Connection>0</T_Connection> … … 155 156 <Desc>T</Desc> 156 157 <Index>0</Index> 157 <Values>36 0.964</Values>158 <Values>366.309</Values> 158 159 <Status>0</Status> 159 160 <Unit>K</Unit> … … 169 170 <Desc>h</Desc> 170 171 <Index>0</Index> 171 <Values> 4885.42</Values>172 <Values>5347.07</Values> 172 173 <Status>0</Status> 173 174 <Unit>kJ/kmol</Unit> … … 225 226 <Desc>PolyCoeff</Desc> 226 227 <Index>0</Index> 227 <Values>1.1 6046</Values>228 <Values>1.17609</Values> 228 229 <Status>0</Status> 229 230 </Variables> … … 262 263 </Variables> 263 264 <Variables> 265 <Desc>Pincrease</Desc> 266 <Index>0</Index> 267 <Values>300</Values> 268 <Status>0</Status> 269 <Unit>kPa</Unit> 270 </Variables> 271 <Variables> 264 272 <Desc>Head</Desc> 265 273 <Index>0</Index> 266 <Values>8 4.2848</Values>274 <Values>86.5153</Values> 267 275 <Status>0</Status> 268 276 <Unit>kJ/kg</Unit> … … 296 304 <Desc>FluidPower</Desc> 297 305 <Index>0</Index> 298 <Values>5. 50613</Values>306 <Values>5.65185</Values> 299 307 <Status>0</Status> 300 308 <Unit>kW</Unit> … … 329 337 <Desc>WorkIn</Desc> 330 338 <Index>0</Index> 331 <Values>-5. 50613</Values>339 <Values>-5.65185</Values> 332 340 <Status>0</Status> 333 341 <Unit>kW</Unit> … … 346 354 <Block_Properties> 347 355 <Model_File_Path>streams</Model_File_Path> 348 <Instance_Id> work_source_1</Instance_Id>356 <Instance_Id>inlet_work</Instance_Id> 349 357 <Model_Name>work_source</Model_Name> 350 358 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