- Timestamp:
- Feb 16, 2009, 5:23:57 PM (14 years ago)
- Location:
- branches/gui
- Files:
-
- 4 edited
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eml/stage_separators/flash.mso (modified) (6 diffs)
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eml/stage_separators/icon/Flash.png (modified) (previous)
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sample/stage_separators/Sample_flash_PIDincr.pfd (modified) (77 diffs)
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sample/stage_separators/sample_flash_steady.pfd (modified) (49 diffs)
Legend:
- Unmodified
- Added
- Removed
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branches/gui/eml/stage_separators/flash.mso
r711 r714 27 27 Info = 28 28 "== Assumptions == 29 * both phases are perfectly mixed.29 * Both phases are perfectly mixed. 30 30 31 31 == Specify == 32 * the feed stream;33 * the outlet flows: OutletV.F and OutletL.F.32 * The feed stream; 33 * The outlet flows: OutletVapour.F and OutletLiquid.F. 34 34 35 35 == Initial Conditions == … … 83 83 INITIAL 84 84 85 # initial level Percent85 # Initial level Percent 86 86 LI = Levelpercent_Initial; 87 87 88 # initial Outlet Liquid Temperature88 # Initial Outlet Liquid Temperature 89 89 OutletLiquid.T = Temperature_Initial; 90 90 91 # initial Outlet Liquid Composition Normalized91 # Initial Outlet Liquid Composition Normalized 92 92 OutletLiquid.z(1:NComp - 1) = Composition_Initial(1:NComp - 1)/sum(Composition_Initial); 93 93 … … 140 140 VesselVolume = LiquidHoldup * vL + VapourHoldup * vV; 141 141 142 "Temperature indicator Celsius Degree"142 "Temperature indicator in Celsius Degree" 143 143 TI * 'K' = OutletLiquid.T - 273.15*'K'; 144 144 … … 169 169 170 170 #*---------------------------------------------------------------------- 171 * Model of a Steady State flash171 * Model of a steady-state flash. 172 172 *---------------------------------------------------------------------*# 173 173 Model flash_steady 174 ATTRIBUTES 175 Pallete = true; 176 Icon = "icon/Flash"; 177 Brief = "Model of a Steady State flash."; 178 Info = 179 "== Assumptions == 180 * both phases are perfectly mixed. 181 182 == Specify == 183 * the feed stream; 184 * the outlet pressure (OutletV.P); 185 * the outlet temperature OR the heat supplied. 186 "; 187 188 PARAMETERS 189 outer PP as Plugin(Brief = "External Physical Properties", Type="PP"); 190 191 VARIABLES 192 in Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421, Symbol="_{in}"); 193 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1, Symbol="_{outL}"); 194 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0, Symbol="_{outV}"); 195 in InletQ as power (Brief="Rate of heat supply", PosX=1, PosY=0.7559, Symbol="_{in}"); 196 vfrac as fraction (Brief="Vapourization fraction", Symbol="\phi"); 197 Pratio as positive (Brief = "Pressure Ratio", Symbol ="P_{ratio}"); 198 Pdrop as press_delta (Brief = "Pressure Drop", DisplayUnit = 'kPa', Symbol ="\Delta P"); 199 200 EQUATIONS 201 "The flash calculation" 202 [vfrac, OutletL.z, OutletV.z] = PP.Flash(OutletV.T, OutletV.P, Inlet.z); 203 204 "Global Molar Balance" 205 Inlet.F = OutletV.F + OutletL.F; 206 207 "Vaporization Fraction" 208 OutletV.F = Inlet.F * vfrac; 209 210 "Energy Balance" 211 Inlet.F*Inlet.h + InletQ = OutletL.F*OutletL.h + OutletV.F*OutletV.h; 212 213 "Thermal Equilibrium" 214 OutletV.T = OutletL.T; 215 216 "Mechanical Equilibrium" 217 OutletV.P = OutletL.P; 218 219 "Pressure Drop" 220 OutletL.P = Inlet.P - Pdrop; 221 222 "Pressure Ratio" 223 OutletL.P = Inlet.P * Pratio; 224 end 225 226 #*---------------------------------------------------------------------- 227 * Model of a steady-state PH flash. 228 *---------------------------------------------------------------------*# 229 Model FlashPHSteady 230 ATTRIBUTES 174 175 ATTRIBUTES 231 176 Pallete = true; 232 177 Icon = "icon/Flash"; … … 239 184 240 185 == Specify == 241 * the feed stream;242 * the heat duty;243 * the outlet pressure.186 * The feed stream; 187 * The heat duty; 188 * The outlet pressure. 244 189 "; 245 190 246 PARAMETERS 247 outer PP as Plugin(Brief = "External Physical Properties", Type="PP"); 248 outer NComp as Integer; 249 250 VARIABLES 251 in Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421, Symbol="_{in}"); 252 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1, Symbol="_{outL}"); 253 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0, Symbol="_{outV}"); 254 in InletQ as power (Brief="Rate of heat supply", PosX=1, PosY=0.7559, Symbol="_{in}"); 255 vfrac as fraction(Brief="Vaporization fraction", Symbol="\phi"); 256 h as enth_mol(Brief="Mixture enthalpy"); 257 Pratio as positive (Brief = "Pressure Ratio", Symbol ="P_{ratio}"); 258 Pdrop as press_delta (Brief = "Pressure Drop", DisplayUnit = 'kPa', Symbol ="\Delta P"); 259 260 EQUATIONS 261 262 "Chemical equilibrium" 263 [vfrac,OutletL.z,OutletV.z]=PP.FlashPH(OutletL.P,h,Inlet.z); 264 265 "Global Molar Balance" 266 Inlet.F = OutletV.F + OutletL.F; 267 OutletV.F = Inlet.F * vfrac; 268 269 "Energy Balance" 191 PARAMETERS 192 193 outer PP as Plugin(Brief = "External Physical Properties", Type="PP"); 194 outer NComp as Integer; 195 196 VARIABLES 197 198 in Inlet as stream (Brief="Feed Stream", PosX=0, PosY=0.5421, Symbol="_{in}"); 199 out OutletLiquid as liquid_stream (Brief="Liquid outlet stream", PosX=0.4790, PosY=1, Symbol="_{outL}"); 200 out OutletVapour as vapour_stream (Brief="Vapour outlet stream", PosX=0.4877, PosY=0, Symbol="_{outV}"); 201 in InletQ as power (Brief="Rate of heat supply", PosX=1, PosY=0.7559, Symbol="_{in}"); 202 203 vfrac as fraction (Brief="Vaporization fraction", Symbol="\phi"); 204 h as enth_mol (Brief="Mixture enthalpy"); 205 Pratio as positive (Brief = "Pressure Ratio", Symbol ="P_{ratio}"); 206 Pdrop as press_delta (Brief = "Pressure Drop", DisplayUnit = 'kPa', Symbol ="\Delta P"); 207 208 EQUATIONS 209 210 if vfrac > 0 and vfrac <1 211 212 then 213 "The flash calculation" 214 [vfrac, OutletLiquid.z, OutletVapour.z] = PP.Flash(OutletVapour.T, OutletVapour.P, Inlet.z); 215 216 else 217 "Chemical equilibrium" 218 [vfrac,OutletLiquid.z,OutletVapour.z]=PP.FlashPH(OutletLiquid.P,h,Inlet.z); 219 220 end 221 222 "Global Molar Balance" 223 Inlet.F = OutletVapour.F + OutletLiquid.F; 224 225 "Vapour Fraction" 226 OutletVapour.F = Inlet.F * vfrac; 227 228 "Energy Balance" 270 229 Inlet.F*(h - Inlet.h) = InletQ; 271 Inlet.F*h = Inlet.F*(1-vfrac)*OutletL.h + Inlet.F*vfrac*OutletV.h; 272 273 "Thermal Equilibrium" 274 OutletV.T = OutletL.T; 275 276 "Mechanical Equilibrium" 277 OutletV.P = OutletL.P; 278 279 "Pressure Drop" 280 OutletL.P = Inlet.P - Pdrop; 281 282 "Pressure Ratio" 283 OutletL.P = Inlet.P * Pratio; 230 Inlet.F*h = Inlet.F*(1-vfrac)*OutletLiquid.h + Inlet.F*vfrac*OutletVapour.h; 231 232 "Thermal Equilibrium" 233 OutletVapour.T = OutletLiquid.T; 234 235 "Mechanical Equilibrium" 236 OutletVapour.P = OutletLiquid.P; 237 238 "Pressure Drop" 239 OutletLiquid.P = Inlet.P - Pdrop; 240 241 "Pressure Ratio" 242 OutletLiquid.P = Inlet.P * Pratio; 243 284 244 end 285 245 … … 288 248 * It is recommended to use [v,x,y]=PP.FlashPH(P,h,z) instead of. 289 249 *---------------------------------------------------------------------*# 290 Model FlashPHSteady A250 Model FlashPHSteady 291 251 ATTRIBUTES 292 252 Pallete = true; 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branches/gui/sample/stage_separators/Sample_flash_PIDincr.pfd
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branches/gui/sample/stage_separators/sample_flash_steady.pfd
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