- Timestamp:
- Aug 4, 2008, 7:45:14 PM (15 years ago)
- Location:
- branches/gui
- Files:
-
- 3 edited
-
eml/pressure_changers/valve.mso (modified) (4 diffs)
-
sample/pressure_changers/sample_valve.mso (modified) (1 diff)
-
sample/stage_separators/new_flash.pfd (modified) (100 diffs)
Legend:
- Unmodified
- Added
- Removed
-
branches/gui/eml/pressure_changers/valve.mso
r586 r587 20 20 using "streams"; 21 21 22 23 Model valve24 ATTRIBUTES25 Pallete = true;26 Icon = "icon/Valve";27 Brief = "Model of a valve.";28 Info =29 "== Model of valves ==30 * Linear;31 * Parabolic;32 * Equal;33 * Quick;34 * Hyperbolic.35 36 == Assumptions ==37 * Steady State;38 * Liquid;39 * Isentalpic.40 41 == Specify ==42 * the valve type;43 * the inlet stream;44 * the Volumetric Flow (Qv);45 * the Valve Coefficient (cv);46 * the opening (x).47 ";48 49 PARAMETERS50 valve_type as Switcher (Valid = ["linear", "parabolic", "equal", "quick", "hyperbolic"], Default = "linear");51 outer PP as Plugin (Brief = "External Physical Properties", Type = "PP");52 outer NComp as Integer (Brief = "Number of chemical components", Lower = 1);53 rho60F as dens_mass;54 55 VARIABLES56 Pratio as positive (Brief = "Pressure Ratio", Symbol ="P_{ratio}");57 Pdrop as press_delta (Brief = "Pressure Drop", DisplayUnit = 'kPa', Symbol ="\Delta P");58 Qv as flow_vol (Brief = "Volumetric Flow");59 fc as positive (Brief = "Opening Function");60 cv as positive (Brief = "Valve Coefficient", Unit = 'm^3/h/kPa^0.5');61 Gf as positive (Brief = "Specific Gravity");62 rho as dens_mass;63 vm as vol_mol (Brief = "Mixture Molar Volume");64 x as fraction (Brief = "Opening");65 in Inlet as stream (Brief = "Inlet stream", PosX=0, PosY=0.7365, Symbol="_{in}");66 out Outlet as streamPH (Brief = "Outlet stream", PosX=1, PosY=0.7365, Symbol="_{out}");67 68 SET69 rho60F = 999.02 * 'kg/m^3';70 71 EQUATIONS72 "Pressure Drop"73 Outlet.P = Inlet.P - Pdrop;74 75 "Pressure Ratio"76 Outlet.P = Inlet.P * Pratio;77 78 "Enthalpy Balance"79 Outlet.h = Inlet.h;80 81 "Molar Balance"82 Outlet.F = Inlet.F;83 84 "Calculate Outlet Composition"85 Outlet.z = Inlet.z;86 87 if Pdrop > 0 then88 "Valve Equation - Flow"89 Qv = fc*cv*sqrt(Pdrop/Gf);90 else91 "Valve Equation - Closed"92 Qv = 0 * 'm^3/h';93 end94 95 "Calculate Gf"96 Gf = rho/rho60F;97 98 "Calculate Specific Mass"99 rho = PP.LiquidDensity(Inlet.T,Inlet.P,Inlet.z);100 101 "Calculate Mass Flow"102 Qv = Inlet.F*vm;103 104 "Calculate Liquid Molar Volume"105 vm = PP.LiquidVolume(Inlet.T,Inlet.P,Inlet.z);106 107 switch valve_type108 case "linear":109 110 "Opening Equation"111 fc = x;112 113 case "parabolic":114 115 "Opening Equation"116 fc = x^2;117 118 case "equal":119 120 "Opening Equation"121 fc = x^2/(2-x^4)^(1/2);122 123 case "quick":124 125 "Opening Equation"126 fc = 10*x/sqrt(1+99*x^2);127 128 case "hyperbolic":129 130 "Opening Equation"131 fc = 0.1*x/sqrt(1-0.99*x^2);132 133 end134 135 end136 137 22 #*------------------------------------------------------------------- 138 23 * Model of a valve (simplified) … … 214 99 end 215 100 216 217 101 Model valve_flow 218 102 ATTRIBUTES … … 260 144 end 261 145 262 Model valve_liquid_test 146 Model valve 147 263 148 ATTRIBUTES 264 149 Pallete = true; 265 150 Icon = "icon/Valve"; 266 Brief = "testing Model of a valve."; 267 268 151 Brief = "Model of a valve."; 152 Info = 153 "== Model of valves == 154 * Linear; 155 * Parabolic; 156 * Equal; 157 * Quick; 158 * Hyperbolic. 159 160 == Assumptions == 161 * First Order Dynamic; 162 * Only Liquid or Only Vapour; 163 * Isentalpic. 164 165 == Specify == 166 * the valve type; 167 * the Valve Coefficient (Cv); 168 * the valve time constant (Tau). 169 "; 170 269 171 PARAMETERS 270 valve_type as Switcher (Valid = ["linear", "parabolic", "equal", "quick", "hyperbolic"], Default = "linear"); 271 outer PP as Plugin (Brief = "External Physical Properties", Type = "PP");172 173 outer PP as Plugin (Brief = "External Physical Properties", Type = "PP"); 272 174 outer NComp as Integer (Brief = "Number of chemical components", Lower = 1); 273 rho60F as dens_mass; 274 tau as time_sec (Brief="valve time constant"); 175 176 ValveType as Switcher (Valid = ["linear", "parabolic", "equal", "quick", "hyperbolic"], Default = "linear"); 177 ValidPhases as Switcher (Brief = "Valid Phases for Flash Calculation", Valid = ["Vapour-Only", "Liquid-Only"], Default="Liquid-Only"); 178 Tau as time_sec (Brief="valve time constant"); 179 rho60F as dens_mass (Brief = "Water Mass Density at 60 F",Hidden=true); 275 180 276 181 VARIABLES 277 Pdrop as press_delta (Brief = "Pressure Drop", DisplayUnit = 'kPa', Symbol ="\Delta P"); 278 Qv as flow_vol (Brief = "Volumetric Flow"); 279 fc as positive (Brief = "Opening Function"); 280 cv as positive (Brief = "Valve Coefficient", Unit = 'm^3/h/kPa^0.5'); 281 Gf as positive (Brief = "Specific Gravity"); 282 rho as dens_mass; 283 vm as vol_mol (Brief = "Mixture Molar Volume"); 284 vactual as fraction (Brief = "Actual valve stem position"); 285 vsp as fraction (Brief = "Valve stem position"); 286 in Inlet as stream (Brief = "Inlet stream", PosX=0, PosY=0.7365, Symbol="_{in}"); 287 out Outlet as streamPH (Brief = "Outlet stream", PosX=1, PosY=0.7365, Symbol="_{out}"); 288 in vsignal as fraction (Brief="Flow Signal", PosX=0.5, PosY=0); 289 182 183 Pdrop as press_delta (Brief = "Pressure Drop", DisplayUnit = 'kPa', Symbol ="\Delta P"); 184 Fvol as flow_vol (Brief = "Volumetric Flow"); 185 fc as positive (Brief = "Opening Function",Hidden=true); 186 Cv as Real (Brief="Valve Flow Coefficient", Unit='gal/min/psi^0.5'); 187 StemPosition as fraction (Brief = "Actual valve stem position"); 188 189 190 vm as vol_mol (Brief = "Mixture Molar Volume"); 191 rho as dens_mass (Brief = "Mixture Mass Density"); 192 vsp as fraction (Brief = "Valve stem position",Hidden=true); 193 194 in Inlet as stream (Brief = "Inlet stream", PosX=0, PosY=0.7365, Symbol="_{in}"); 195 out Outlet as streamPH (Brief = "Outlet stream", PosX=1, PosY=0.7365, Symbol="_{out}"); 196 in vsignal as fraction (Brief = "Flow Signal", PosX=0.5, PosY=0); 197 290 198 SET 291 rho60F = 999.02 * 'kg/m^3'; 199 200 rho60F = 984.252 * 'kg/m^3'; 292 201 293 202 EQUATIONS 294 203 295 "valve dynamics" 296 tau*diff(vactual) = vsp-vactual; 297 298 vsp=vsignal; 204 "First order valve dynamics" 205 Tau*diff(StemPosition) = vsp-StemPosition; 206 207 "Flow Signal" 208 vsp = vsignal; 299 209 300 210 "Pressure Drop" … … 310 220 Outlet.z = Inlet.z; 311 221 312 if Pdrop > 0 then # update the flow equation !!!! 313 314 "Valve Equation - Flow" 315 Qv = 1000*fc*cv*sqrt(Pdrop/Gf); 316 222 switch ValidPhases 223 224 case "Liquid-Only": 225 226 if Pdrop > 0 then 227 228 "Valve Equation - Liquid Flow" 229 Fvol = fc*(Cv/sqrt(1/rho60F))*sqrt(Pdrop/rho); 230 317 231 else 318 232 319 "Valve Equation - Closed" 320 Qv = 0.1*fc*cv*sqrt(Pdrop/Gf); 321 322 end 323 324 "Calculate Gf" 325 Gf = rho/rho60F; 326 327 "Calculate Specific Mass" 233 "Valve Equation - Liquid Flow" 234 Fvol = fc*(Cv/sqrt(1/rho60F))*sqrt(Pdrop/rho); 235 236 end 237 238 "Liquid Mass Density" 328 239 rho = PP.LiquidDensity(Inlet.T,Inlet.P,Inlet.z); 329 240 241 "Liquid Molar Volume" 242 vm = PP.LiquidVolume(Inlet.T,Inlet.P,Inlet.z); 243 244 case "Vapour-Only": 245 246 if Pdrop > 0 then #Update for gas flow !!!! 247 248 "Valve Equation - Vapour Flow" 249 Fvol = fc*(Cv/sqrt(1/rho60F))*sqrt(Pdrop/rho); 250 251 else 252 253 "Valve Equation - Vapour Flow" 254 Fvol = fc*(Cv/sqrt(1/rho60F))*sqrt(Pdrop/rho); 255 256 end 257 258 "Vapour Mass Density" 259 rho = PP.VapourDensity(Inlet.T,Inlet.P,Inlet.z); 260 261 "Vapour Molar Volume" 262 vm = PP.VapourVolume(Inlet.T,Inlet.P,Inlet.z); 263 264 end 265 330 266 "Calculate Mass Flow" 331 Qv = Inlet.F*vm; 332 333 "Calculate Liquid Molar Volume" 334 vm = PP.LiquidVolume(Inlet.T,Inlet.P,Inlet.z); 335 336 switch valve_type # update the valve characteristic !!!! 267 Fvol = Inlet.F*vm; 268 269 switch ValveType #Update the valve Type 270 337 271 case "linear": 338 272 339 273 "Opening Equation" 340 fc = vactual;274 fc = StemPosition; 341 275 342 276 case "parabolic": 343 277 344 278 "Opening Equation" 345 fc = vactual^2;279 fc = StemPosition^2; 346 280 347 281 case "equal": 348 282 349 283 "Opening Equation" 350 fc = vactual^2/(2-vactual^4)^(1/2);284 fc = StemPosition^2/(2-StemPosition^4)^(1/2); 351 285 352 286 case "quick": 353 287 354 288 "Opening Equation" 355 fc = 10* vactual/sqrt(1+99*vactual^2);289 fc = 10*StemPosition/sqrt(1+99*StemPosition^2); 356 290 357 291 case "hyperbolic": 358 292 359 293 "Opening Equation" 360 fc = 0.1* vactual/sqrt(1-0.99*vactual^2);294 fc = 0.1*StemPosition/sqrt(1-0.99*StemPosition^2); 361 295 362 296 end -
branches/gui/sample/pressure_changers/sample_valve.mso
r578 r587 104 104 end 105 105 106 FlowSheet valve_linear_Test107 108 DEVICES109 S1 as source;110 V1 as valve;111 112 CONNECTIONS113 S1.Outlet to V1.Inlet;114 115 PARAMETERS116 PP as Plugin(Brief="Physical Properties",117 Type="PP",118 Components = [ "isobutane", "benzene"],119 LiquidModel = "PR",120 VapourModel = "PR"121 );122 NComp as Integer (Default= 1);123 124 SET125 NComp = PP.NumberOfComponents;126 V1.valve_type = "linear"; #"parabolic", "equal", "quick", "hyperbolic"127 128 SPECIFY129 S1.P = 2169.78 * 'kPa';130 S1.T = 394.26 * 'K' ;131 S1.Composition = [0.001848, 0.9982];132 133 V1.Qv = 113.56 * 'm^3/h';134 V1.x = 0.5;135 V1.cv = 10 * 'm^3/h/kPa^0.5';136 137 OPTIONS138 Dynamic = false;139 NLASolver(140 RelativeAccuracy = 1e-6141 );142 end -
branches/gui/sample/stage_separators/new_flash.pfd
r586 r587 35 35 <Snap_to_Grid>1</Snap_to_Grid> 36 36 <Width>1260</Width> 37 <Height>5 79</Height>37 <Height>587</Height> 38 38 <X>0</X> 39 39 <Y>0</Y> … … 127 127 <Desc>h</Desc> 128 128 <Index>0</Index> 129 <Values>-23082. 2</Values>129 <Values>-23082.6</Values> 130 130 <Status>0</Status> 131 131 <Unit>kJ/kmol</Unit> … … 180 180 <Desc>F</Desc> 181 181 <Index>0</Index> 182 <Values> 81.1819</Values>182 <Values>509.512</Values> 183 183 <Status>0</Status> 184 184 <Unit>kmol/h</Unit> … … 187 187 <Desc>T</Desc> 188 188 <Index>0</Index> 189 <Values>3 34.247</Values>189 <Values>364.012</Values> 190 190 <Status>2</Status> 191 191 <Unit>K</Unit> … … 194 194 <Desc>P</Desc> 195 195 <Index>0</Index> 196 <Values> 0.340226</Values>196 <Values>2.80147</Values> 197 197 <Status>0</Status> 198 198 <Unit>atm</Unit> … … 201 201 <Desc>h</Desc> 202 202 <Index>0</Index> 203 <Values>- 26620</Values>203 <Values>-18720.5</Values> 204 204 <Status>0</Status> 205 205 <Unit>kJ/kmol</Unit> … … 214 214 <Desc>z</Desc> 215 215 <Index>0</Index> 216 <Values>0. 0891495</Values>216 <Values>0.233839</Values> 217 217 <Status>2</Status> 218 218 <Index>1</Index> 219 <Values>0.3 23369</Values>219 <Values>0.317813</Values> 220 220 <Status>2</Status> 221 221 <Index>2</Index> 222 <Values>0. 587482</Values>222 <Values>0.448348</Values> 223 223 <Status>0</Status> 224 224 </Variables> … … 262 262 <Desc>F</Desc> 263 263 <Index>0</Index> 264 <Values> 50.0155</Values>264 <Values>288.972</Values> 265 265 <Status>0</Status> 266 266 <Unit>kmol/h</Unit> … … 269 269 <Desc>T</Desc> 270 270 <Index>0</Index> 271 <Values>3 34.247</Values>271 <Values>364.012</Values> 272 272 <Status>0</Status> 273 273 <Unit>K</Unit> … … 276 276 <Desc>P</Desc> 277 277 <Index>0</Index> 278 <Values> 0.340226</Values>278 <Values>2.80147</Values> 279 279 <Status>0</Status> 280 280 <Unit>atm</Unit> … … 283 283 <Desc>h</Desc> 284 284 <Index>0</Index> 285 <Values> 3669.33</Values>285 <Values>6620.99</Values> 286 286 <Status>0</Status> 287 287 <Unit>kJ/kmol</Unit> … … 296 296 <Desc>z</Desc> 297 297 <Index>0</Index> 298 <Values>0. 663177</Values>298 <Values>0.79049</Values> 299 299 <Status>0</Status> 300 300 <Index>1</Index> 301 <Values>0. 264821</Values>301 <Values>0.16218</Values> 302 302 <Status>0</Status> 303 303 <Index>2</Index> 304 <Values>0.0 720022</Values>304 <Values>0.0473294</Values> 305 305 <Status>0</Status> 306 306 </Variables> … … 374 374 <Desc>M</Desc> 375 375 <Index>0</Index> 376 <Values> 0.59078</Values>376 <Values>1.9899</Values> 377 377 <Status>0</Status> 378 378 <Unit>kmol</Unit> 379 379 <Index>1</Index> 380 <Values> 1.80584</Values>380 <Values>2.64235</Values> 381 381 <Status>0</Status> 382 382 <Unit>kmol</Unit> 383 383 <Index>2</Index> 384 <Values>3. 52285</Values>384 <Values>3.71527</Values> 385 385 <Status>0</Status> 386 386 <Unit>kmol</Unit> … … 389 389 <Desc>ML</Desc> 390 390 <Index>0</Index> 391 <Values> 5.86318</Values>391 <Values>8.27939</Values> 392 392 <Status>0</Status> 393 393 <Unit>kmol</Unit> … … 396 396 <Desc>MV</Desc> 397 397 <Index>0</Index> 398 <Values>0. 623904</Values>398 <Values>0.0681311</Values> 399 399 <Status>0</Status> 400 400 <Unit>kmol</Unit> … … 403 403 <Desc>E</Desc> 404 404 <Index>0</Index> 405 <Values>-1 69612</Values>405 <Values>-155111</Values> 406 406 <Status>0</Status> 407 407 <Unit>kJ</Unit> … … 410 410 <Desc>vL</Desc> 411 411 <Index>0</Index> 412 <Values>0.0001 62558</Values>412 <Values>0.00015825</Values> 413 413 <Status>0</Status> 414 414 <Unit>m^3/mol</Unit> … … 417 417 <Desc>vV</Desc> 418 418 <Index>0</Index> 419 <Values>0.0 433191</Values>419 <Values>0.0101245</Values> 420 420 <Status>0</Status> 421 421 <Unit>m^3/mol</Unit> … … 424 424 <Desc>Level</Desc> 425 425 <Index>0</Index> 426 <Values> 4.72115</Values>426 <Values>6.67284</Values> 427 427 <Status>0</Status> 428 428 <Unit>m</Unit> … … 438 438 <Desc>vfrac</Desc> 439 439 <Index>0</Index> 440 <Values>0. 100031</Values>440 <Values>0.577945</Values> 441 441 <Status>0</Status> 442 442 </Variables> … … 444 444 <Desc>Pratio</Desc> 445 445 <Index>0</Index> 446 <Values>0. 125003</Values>446 <Values>0.560293</Values> 447 447 <Status>0</Status> 448 448 </Variables> … … 450 450 <Desc>Pdrop</Desc> 451 451 <Index>0</Index> 452 <Values> 531.756</Values>452 <Values>222.766</Values> 453 453 <Status>0</Status> 454 454 <Unit>kPa</Unit> … … 457 457 <Desc>TI</Desc> 458 458 <Index>0</Index> 459 <Values> 61.097</Values>459 <Values>90.862</Values> 460 460 <Status>0</Status> 461 461 </Variables> … … 463 463 <Desc>PI</Desc> 464 464 <Index>0</Index> 465 <Values> -0.248027</Values>465 <Values>2.80147</Values> 466 466 <Status>0</Status> 467 467 </Variables> … … 469 469 <Desc>LI</Desc> 470 470 <Index>0</Index> 471 <Values>0. 463498</Values>471 <Values>0.5</Values> 472 472 <Status>2</Status> 473 473 </Variables> … … 530 530 <Desc>h</Desc> 531 531 <Index>0</Index> 532 <Values>-23082. 2</Values>532 <Values>-23082.6</Values> 533 533 <Status>0</Status> 534 534 <Unit>kJ/kmol</Unit> … … 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