- Timestamp:
- May 24, 2008, 6:35:24 PM (15 years ago)
- Location:
- trunk
- Files:
-
- 4 edited
Legend:
- Unmodified
- Added
- Removed
-
trunk/eml/heat_exchangers/DoublePipe.mso
r478 r525 19 19 using "HEX_Engine"; 20 20 21 Model DoublePipe_Geometry 22 23 ATTRIBUTES 24 Pallete = false; 25 Brief = "double pipe geometrical parameters."; 26 Info = 27 "to be documented."; 28 29 PARAMETERS 30 31 outer PP as Plugin (Brief="External Physical Properties", Type="PP"); 32 outer NComp as Integer (Brief="Number of Components",Hidden=true); 33 34 M(NComp) as molweight (Brief="Component Mol Weight",Hidden=true); 35 36 Pi as constant (Brief="Pi Number",Default=3.14159265, Symbol = "\pi",Hidden=true); 37 DoInner as length (Brief="Outside Diameter of Inner Pipe",Lower=1e-6); 38 DiInner as length (Brief="Inside Diameter of Inner Pipe",Lower=1e-10); 39 DiOuter as length (Brief="Inside Diameter of Outer pipe",Lower=1e-10); 40 Lpipe as length (Brief="Effective Tube Length of one segment of Pipe",Lower=0.1, Symbol = "L_{pipe}"); 41 Kwall as conductivity (Brief="Tube Wall Material Thermal Conductivity",Default=1.0, Symbol = "K_{wall}"); 42 Rfi as positive (Brief="Inside Fouling Resistance",Unit='m^2*K/kW',Default=1e-6,Lower=0); 43 Rfo as positive (Brief="Outside Fouling Resistance",Unit='m^2*K/kW',Default=1e-6,Lower=0); 44 45 SET 46 47 #"Component Molecular Weight" 48 M = PP.MolecularWeight(); 49 50 #"Pi Number" 51 Pi = 3.14159265; 52 53 end 21 54 22 55 Model DoublePipe_Basic … … 31 64 32 65 outer PP as Plugin (Brief="External Physical Properties", Type="PP"); 33 outer NComp as Integer (Brief="Number of Components" );34 35 M(NComp) as molweight (Brief="Component Mol Weight" );36 37 HotSide as Switcher (Brief="Flag for Fluid Alocation ",Valid=["outer","inner"],Default="outer");38 innerFlowRegime as Switcher (Brief="Inner Flow Regime ",Valid=["laminar","transition","turbulent"],Default="laminar" );39 outerFlowRegime as Switcher (Brief="Outer Flow Regime ",Valid=["laminar","transition","turbulent"],Default="laminar" );66 outer NComp as Integer (Brief="Number of Components",Hidden=true); 67 68 M(NComp) as molweight (Brief="Component Mol Weight",Hidden=true); 69 70 HotSide as Switcher (Brief="Flag for Fluid Alocation ",Valid=["outer","inner"],Default="outer",Hidden=true); 71 innerFlowRegime as Switcher (Brief="Inner Flow Regime ",Valid=["laminar","transition","turbulent"],Default="laminar",Hidden=true); 72 outerFlowRegime as Switcher (Brief="Outer Flow Regime ",Valid=["laminar","transition","turbulent"],Default="laminar",Hidden=true); 40 73 41 74 InnerLaminarCorrelation as Switcher (Brief="Heat Transfer Correlation in Laminar Flow for the Inner Side",Valid=["Hausen","Schlunder"],Default="Hausen"); 42 InnerTransitionCorrelation as Switcher 75 InnerTransitionCorrelation as Switcher (Brief="Heat Transfer Correlation in Transition Flow for the Inner Side",Valid=["Gnielinski","Hausen"],Default="Gnielinski"); 43 76 InnerTurbulentCorrelation as Switcher (Brief="Heat Transfer Correlation in Turbulent Flow for the Inner Side",Valid=["Petukhov","SiederTate"],Default="Petukhov"); 44 77 … … 47 80 OuterTurbulentCorrelation as Switcher (Brief="Heat Transfer Correlation in Turbulent Flow for the Outer Side",Valid=["Petukhov","SiederTate"],Default="Petukhov"); 48 81 49 CalculationApproach as Switcher (Brief="Options for convergence Calculations ",Valid=["Simplified","Full"],Default="Full"); 50 Qestimated as power (Brief="Estimated Duty", Default=70, Lower=1e-6, Upper=1e10); 51 52 Pi as constant (Brief="Pi Number",Default=3.14159265, Symbol = "\pi"); 53 DoInner as length (Brief="Outside Diameter of Inner Pipe",Lower=1e-6); 54 DiInner as length (Brief="Inside Diameter of Inner Pipe",Lower=1e-10); 55 DiOuter as length (Brief="Inside Diameter of Outer pipe",Lower=1e-10); 56 Lpipe as length (Brief="Effective Tube Length of one segment of Pipe",Lower=0.1, Symbol = "L_{pipe}"); 57 Kwall as conductivity (Brief="Tube Wall Material Thermal Conductivity",Default=1.0, Symbol = "K_{wall}"); 58 Rfi as positive (Brief="Inside Fouling Resistance",Unit='m^2*K/kW',Default=1e-6,Lower=0); 59 Rfo as positive (Brief="Outside Fouling Resistance",Unit='m^2*K/kW',Default=1e-6,Lower=0); 82 CalculationApproach as Switcher (Brief="Options for convergence Calculations ",Valid=["Simplified","Full"],Default="Full"); 83 Qestimated as power (Brief="Estimated Duty", Default=70, Lower=1e-6, Upper=1e10); 60 84 61 85 VARIABLES 62 86 63 in InletInner as stream (Brief="Inlet Inner Stream", PosX=0, PosY=0.5225, Symbol="_{inInner}"); 64 in InletOuter as stream (Brief="Inlet Outer Stream", PosX=0.2805, PosY=0, Symbol="_{inOuter}"); 65 out OutletInner as streamPH (Brief="Outlet Inner Stream", PosX=1, PosY=0.5225, Symbol="_{outInner}"); 66 out OutletOuter as streamPH (Brief="Outlet Outer Stream", PosX=0.7264, PosY=1, Symbol="_{outOuter}"); 87 Geometry as DoublePipe_Geometry (Brief="Double pipe geometry",Symbol=" "); 88 in InletInner as stream (Brief="Inlet Inner Stream", PosX=0, PosY=0.5225, Symbol="_{inInner}"); 89 in InletOuter as stream (Brief="Inlet Outer Stream", PosX=0.2805, PosY=0, Symbol="_{inOuter}"); 90 out OutletInner as streamPH (Brief="Outlet Inner Stream", PosX=1, PosY=0.5225, Symbol="_{outInner}"); 91 out OutletOuter as streamPH (Brief="Outlet Outer Stream", PosX=0.7264, PosY=1, Symbol="_{outOuter}"); 67 92 68 93 Details as Details_Main (Brief="Some Details in the Heat Exchanger", Symbol=" "); … … 72 97 SET 73 98 74 #"Component Molecular Weight"75 M = PP.MolecularWeight();76 77 #"Pi Number"78 Pi = 3.14159265;79 80 99 #"Inner Pipe Cross Sectional Area for Flow" 81 Inner.HeatTransfer.As= Pi*DiInner*DiInner/4;100 Inner.HeatTransfer.As=Geometry.Pi*Geometry.DiInner*Geometry.DiInner/4; 82 101 83 102 #"Outer Pipe Cross Sectional Area for Flow" 84 Outer.HeatTransfer.As= Pi*(DiOuter*DiOuter - DoInner*DoInner)/4;103 Outer.HeatTransfer.As=Geometry.Pi*(Geometry.DiOuter*Geometry.DiOuter - Geometry.DoInner*Geometry.DoInner)/4; 85 104 86 105 #"Inner Pipe Hydraulic Diameter for Heat Transfer" 87 Inner.HeatTransfer.Dh= DiInner;106 Inner.HeatTransfer.Dh=Geometry.DiInner; 88 107 89 108 #"Outer Pipe Hydraulic Diameter for Heat Transfer" 90 Outer.HeatTransfer.Dh=( DiOuter*DiOuter-DoInner*DoInner)/DoInner;109 Outer.HeatTransfer.Dh=(Geometry.DiOuter*Geometry.DiOuter-Geometry.DoInner*Geometry.DoInner)/Geometry.DoInner; 91 110 92 111 #"Inner Pipe Hydraulic Diameter for Pressure Drop" 93 Inner.PressureDrop.Dh= DiInner;112 Inner.PressureDrop.Dh=Geometry.DiInner; 94 113 95 114 #"Outer Pipe Hydraulic Diameter for Pressure Drop" 96 Outer.PressureDrop.Dh= DiOuter-DoInner;115 Outer.PressureDrop.Dh=Geometry.DiOuter-Geometry.DoInner; 97 116 98 117 EQUATIONS … … 272 291 273 292 "Exchange Surface Area for one segment of pipe" 274 Details.A= Pi*DoInner*Lpipe;293 Details.A=Geometry.Pi*Geometry.DoInner*Geometry.Lpipe; 275 294 276 295 switch innerFlowRegime … … 338 357 339 358 "Nusselt Number" 340 Inner.HeatTransfer.Nu = 3.665 + ((0.19*(( DiInner/Lpipe)*Inner.HeatTransfer.Re*Inner.HeatTransfer.PR)^0.8)/(1+0.117*((DiInner/Lpipe)*Inner.HeatTransfer.Re*Inner.HeatTransfer.PR)^0.467));359 Inner.HeatTransfer.Nu = 3.665 + ((0.19*((Geometry.DiInner/Geometry.Lpipe)*Inner.HeatTransfer.Re*Inner.HeatTransfer.PR)^0.8)/(1+0.117*((Geometry.DiInner/Geometry.Lpipe)*Inner.HeatTransfer.Re*Inner.HeatTransfer.PR)^0.467)); 341 360 342 361 case "Schlunder": 343 362 344 363 "Nusselt Number" 345 Inner.HeatTransfer.Nu = (49.027896+4.173281*Inner.HeatTransfer.Re*Inner.HeatTransfer.PR*( DiInner/Lpipe))^(1/3);364 Inner.HeatTransfer.Nu = (49.027896+4.173281*Inner.HeatTransfer.Re*Inner.HeatTransfer.PR*(Geometry.DiInner/Geometry.Lpipe))^(1/3); 346 365 347 366 end … … 364 383 365 384 "Nusselt Number" 366 Inner.HeatTransfer.Nu =0.116*(Inner.HeatTransfer.Re^(0.667)-125)*Inner.HeatTransfer.PR^(0.333)*(1+( DiInner/Lpipe)^0.667);385 Inner.HeatTransfer.Nu =0.116*(Inner.HeatTransfer.Re^(0.667)-125)*Inner.HeatTransfer.PR^(0.333)*(1+(Geometry.DiInner/Geometry.Lpipe)^0.667); 367 386 368 387 end … … 409 428 410 429 "Nusselt Number" 411 Outer.HeatTransfer.Nu = 3.665 + ((0.19*((Outer.HeatTransfer.Dh/ Lpipe)*Outer.HeatTransfer.Re*Outer.HeatTransfer.PR)^0.8)/(1+0.117*((Outer.HeatTransfer.Dh/Lpipe)*Outer.HeatTransfer.Re*Outer.HeatTransfer.PR)^0.467));430 Outer.HeatTransfer.Nu = 3.665 + ((0.19*((Outer.HeatTransfer.Dh/Geometry.Lpipe)*Outer.HeatTransfer.Re*Outer.HeatTransfer.PR)^0.8)/(1+0.117*((Outer.HeatTransfer.Dh/Geometry.Lpipe)*Outer.HeatTransfer.Re*Outer.HeatTransfer.PR)^0.467)); 412 431 413 432 case "Schlunder": 414 433 415 434 "Nusselt Number" 416 Outer.HeatTransfer.Nu = (49.027896+4.173281*Outer.HeatTransfer.Re*Outer.HeatTransfer.PR*(Outer.HeatTransfer.Dh/ Lpipe))^(1/3);435 Outer.HeatTransfer.Nu = (49.027896+4.173281*Outer.HeatTransfer.Re*Outer.HeatTransfer.PR*(Outer.HeatTransfer.Dh/Geometry.Lpipe))^(1/3); 417 436 418 437 end … … 435 454 436 455 "Nusselt Number" 437 Outer.HeatTransfer.Nu = 0.116*(Outer.HeatTransfer.Re^(0.667)-125)*Outer.HeatTransfer.PR^(0.333)*(1+(Outer.HeatTransfer.Dh/ Lpipe)^0.667);456 Outer.HeatTransfer.Nu = 0.116*(Outer.HeatTransfer.Re^(0.667)-125)*Outer.HeatTransfer.PR^(0.333)*(1+(Outer.HeatTransfer.Dh/Geometry.Lpipe)^0.667); 438 457 439 458 … … 473 492 474 493 "Inner Pipe Film Coefficient" 475 Inner.HeatTransfer.hcoeff = (Inner.HeatTransfer.Nu*Inner.Properties.Average.K/ DiInner)*Inner.HeatTransfer.Phi;494 Inner.HeatTransfer.hcoeff = (Inner.HeatTransfer.Nu*Inner.Properties.Average.K/Geometry.DiInner)*Inner.HeatTransfer.Phi; 476 495 477 496 "Outer Pipe Film Coefficient" … … 495 514 496 515 "Outer Pipe Pressure Drop for friction" 497 Outer.PressureDrop.Pd_fric = (2*Outer.PressureDrop.fi* Lpipe*Outer.Properties.Average.rho*Outer.HeatTransfer.Vmean^2)/(Outer.PressureDrop.Dh*Outer.HeatTransfer.Phi);516 Outer.PressureDrop.Pd_fric = (2*Outer.PressureDrop.fi*Geometry.Lpipe*Outer.Properties.Average.rho*Outer.HeatTransfer.Vmean^2)/(Outer.PressureDrop.Dh*Outer.HeatTransfer.Phi); 498 517 499 518 "Inner Pipe Pressure Drop for friction" 500 Inner.PressureDrop.Pd_fric = (2*Inner.PressureDrop.fi* Lpipe*Inner.Properties.Average.rho*Inner.HeatTransfer.Vmean^2)/(DiInner*Inner.HeatTransfer.Phi);519 Inner.PressureDrop.Pd_fric = (2*Inner.PressureDrop.fi*Geometry.Lpipe*Inner.Properties.Average.rho*Inner.HeatTransfer.Vmean^2)/(Geometry.DiInner*Inner.HeatTransfer.Phi); 501 520 502 521 … … 504 523 505 524 "Total Pressure Drop Outer Stream" 506 Outer.PressureDrop.Pdrop = 0*'kPa';525 Outer.PressureDrop.Pdrop = Outer.PressureDrop.Pd_fric; 507 526 508 527 "Total Pressure Drop Inner Stream" 509 Inner.PressureDrop.Pdrop = 0*'kPa';528 Inner.PressureDrop.Pdrop = Inner.PressureDrop.Pd_fric; 510 529 511 530 "Pressure Drop Outer Stream" 512 OutletOuter.P = InletOuter.P ;531 OutletOuter.P = InletOuter.P - Outer.PressureDrop.Pdrop; 513 532 514 533 "Pressure Drop Inner Stream" 515 OutletInner.P = InletInner.P ;534 OutletInner.P = InletInner.P - Inner.PressureDrop.Pdrop; 516 535 517 536 "Outer Pipe Pressure Drop for friction" 518 Outer.PressureDrop.Pd_fric = 0 *'kPa';537 Outer.PressureDrop.Pd_fric = 0.01*InletOuter.P; 519 538 520 539 "Inner Pipe Pressure Drop for friction" 521 Inner.PressureDrop.Pd_fric = 0 *'kPa';540 Inner.PressureDrop.Pd_fric = 0.01*InletInner.P; 522 541 523 542 end … … 560 579 561 580 "Overall Heat Transfer Coefficient Clean" 562 Details.Uc*(( DoInner/(Inner.HeatTransfer.hcoeff*DiInner) )+(DoInner*ln(DoInner/DiInner)/(2*Kwall))+(1/(Outer.HeatTransfer.hcoeff)))=1;581 Details.Uc*((Geometry.DoInner/(Inner.HeatTransfer.hcoeff*Geometry.DiInner) )+(Geometry.DoInner*ln(Geometry.DoInner/Geometry.DiInner)/(2*Geometry.Kwall))+(1/(Outer.HeatTransfer.hcoeff)))=1; 563 582 564 583 "Overall Heat Transfer Coefficient Dirty" 565 Details.Ud*( Rfi*(DoInner/DiInner) + Rfo + (DoInner/(Inner.HeatTransfer.hcoeff*DiInner) )+(DoInner*ln(DoInner/DiInner)/(2*Kwall))+(1/(Outer.HeatTransfer.hcoeff)))=1;584 Details.Ud*(Geometry.Rfi*(Geometry.DoInner/Geometry.DiInner) + Geometry.Rfo + (Geometry.DoInner/(Inner.HeatTransfer.hcoeff*Geometry.DiInner) )+(Geometry.DoInner*ln(Geometry.DoInner/Geometry.DiInner)/(2*Geometry.Kwall))+(1/(Outer.HeatTransfer.hcoeff)))=1; 566 585 567 586 end … … 624 643 625 644 "Number of Units Transference" 626 Method.NTU*Method.Cmin = Details.Ud* Pi*DoInner*Lpipe;645 Method.NTU*Method.Cmin = Details.Ud*Geometry.Pi*Geometry.DoInner*Geometry.Lpipe; 627 646 628 647 "Minimum Heat Capacity" … … 796 815 797 816 "Duty" 798 Details.Q = Details.Ud* Pi*DoInner*Lpipe*Method.LMTD;817 Details.Q = Details.Ud*Geometry.Pi*Geometry.DoInner*Geometry.Lpipe*Method.LMTD; 799 818 800 819 case "Simplified": -
trunk/sample/heat_exchangers/DPHE_diagram.pfd
r475 r525 16 16 <Integration_Index>0</Integration_Index> 17 17 <Integration_Text>original</Integration_Text> 18 <Guess_File>sample/heat_exchangers/DPHE_diagram.rlt</Guess_File> 19 <NLASolver_File_Index>0</NLASolver_File_Index> 20 <NLASolver_File_Text>sundials</NLASolver_File_Text> 18 <NLASolver_File_Index>1</NLASolver_File_Index> 19 <NLASolver_File_Text>nlasolver</NLASolver_File_Text> 21 20 <DAESolver_File_Index>0</DAESolver_File_Index> 22 21 <DAESolver_File_Text>sundials</DAESolver_File_Text> … … 29 28 <Show_Grid>1</Show_Grid> 30 29 <Snap_to_Grid>1</Snap_to_Grid> 31 <Width>9 35</Width>32 <Height>3 84</Height>30 <Width>915</Width> 31 <Height>316</Height> 33 32 <X>0</X> 34 33 <Y>0</Y> … … 38 37 <Show_Grid>1</Show_Grid> 39 38 <Snap_to_Grid>1</Snap_to_Grid> 40 <Width>9 35</Width>39 <Width>915</Width> 41 40 <Height>0</Height> 42 41 <X>0</X> … … 47 46 <Id_String>simple_source_1</Id_String> 48 47 <Block_Name>cold_in</Block_Name> 49 <Image_File_Name> /home/bicca/Desktop/biblioteca/biblioteca/trunk/eml/icon/Source.png</Image_File_Name>48 <Image_File_Name>E:\Gerson\biblioteca\trunk\eml\icon/Source.png</Image_File_Name> 50 49 <X>20.5714</X> 51 50 <Y>21.8571</Y> … … 86 85 <Desc>Outlet.z</Desc> 87 86 <Index>0</Index> 87 <Values>0</Values> 88 <Status>1</Status> 89 <Index>1</Index> 88 90 <Values>1</Values> 89 <Status>1</Status>90 <Index>1</Index>91 <Values>0</Values>92 91 <Status>1</Status> 93 92 </Variables> … … 110 109 <Id_String>simple_source_2</Id_String> 111 110 <Block_Name>hot_in</Block_Name> 112 <Image_File_Name> /home/bicca/Desktop/biblioteca/biblioteca/trunk/eml/icon/Source.png</Image_File_Name>111 <Image_File_Name>E:\Gerson\biblioteca\trunk\eml\icon/Source.png</Image_File_Name> 113 112 <X>42</X> 114 113 <Y>221</Y> … … 149 148 <Desc>Outlet.z</Desc> 150 149 <Index>0</Index> 150 <Values>1</Values> 151 <Status>1</Status> 152 <Index>1</Index> 151 153 <Values>0</Values> 152 <Status>1</Status>153 <Index>1</Index>154 <Values>1</Values>155 154 <Status>1</Status> 156 155 </Variables> … … 173 172 <Id_String>DoublePipe_LMTD_1</Id_String> 174 173 <Block_Name>DPHE</Block_Name> 175 <Image_File_Name> /home/bicca/Desktop/biblioteca/biblioteca/trunk/eml/heat_exchangers/icon/DoublePipe.png</Image_File_Name>176 <X>28 8</X>177 <Y> 99</Y>174 <Image_File_Name>E:\Gerson\biblioteca\trunk\eml\heat_exchangers\icon/DoublePipe.png</Image_File_Name> 175 <X>285.143</X> 176 <Y>100.429</Y> 178 177 <Z>0</Z> 179 178 <Width>278</Width> … … 186 185 <Base_Models> 187 186 <Block_Properties> 187 <Model_File_Path>heat_exchangers\DoublePipe</Model_File_Path> 188 <Instance_Id>Geometry.</Instance_Id> 189 <Model_Name>DoublePipe_Geometry</Model_Name> 190 <T_Connection>0</T_Connection> 191 <Parameters> 192 <Desc>Geometry.DoInner</Desc> 193 <Index>0</Index> 194 <Values>0.04826</Values> 195 <Status>4</Status> 196 <Unit>m</Unit> 197 </Parameters> 198 <Parameters> 199 <Desc>Geometry.DiInner</Desc> 200 <Index>0</Index> 201 <Values>0.04089</Values> 202 <Status>4</Status> 203 <Unit>m</Unit> 204 </Parameters> 205 <Parameters> 206 <Desc>Geometry.DiOuter</Desc> 207 <Index>0</Index> 208 <Values>0.07793</Values> 209 <Status>4</Status> 210 <Unit>m</Unit> 211 </Parameters> 212 <Parameters> 213 <Desc>Geometry.Lpipe</Desc> 214 <Index>0</Index> 215 <Values>3</Values> 216 <Status>4</Status> 217 <Unit>m</Unit> 218 </Parameters> 219 <Parameters> 220 <Desc>Geometry.Kwall</Desc> 221 <Index>0</Index> 222 <Values>0.057</Values> 223 <Status>4</Status> 224 <Unit>kW/m/K</Unit> 225 </Parameters> 226 <Parameters> 227 <Desc>Geometry.Rfi</Desc> 228 <Index>0</Index> 229 <Values>0.0018</Values> 230 <Status>4</Status> 231 <Unit>m^2*K/kW</Unit> 232 </Parameters> 233 <Parameters> 234 <Desc>Geometry.Rfo</Desc> 235 <Index>0</Index> 236 <Values>0.0021</Values> 237 <Status>4</Status> 238 <Unit>m^2*K/kW</Unit> 239 </Parameters> 240 </Block_Properties> 241 </Base_Models> 242 <Model_File_Path>heat_exchangers\DoublePipe</Model_File_Path> 243 <Instance_Id>Geometry.</Instance_Id> 244 <Model_Name>Geometry</Model_Name> 245 <T_Connection>0</T_Connection> 246 </Block_Properties> 247 </Sub_Models> 248 <Sub_Models> 249 <Block_Properties> 250 <Base_Models> 251 <Block_Properties> 188 252 <Model_File_Path>streams</Model_File_Path> 189 253 <Instance_Id>InletInner.</Instance_Id> … … 192 256 </Block_Properties> 193 257 </Base_Models> 194 <Model_File_Path>heat_exchangers /DoublePipe</Model_File_Path>258 <Model_File_Path>heat_exchangers\DoublePipe</Model_File_Path> 195 259 <Instance_Id>InletInner.</Instance_Id> 196 260 <Model_Name>InletInner</Model_Name> … … 208 272 </Block_Properties> 209 273 </Base_Models> 210 <Model_File_Path>heat_exchangers /DoublePipe</Model_File_Path>274 <Model_File_Path>heat_exchangers\DoublePipe</Model_File_Path> 211 275 <Instance_Id>InletOuter.</Instance_Id> 212 276 <Model_Name>InletOuter</Model_Name> … … 224 288 <Model_Name>stream</Model_Name> 225 289 <T_Connection>2</T_Connection> 290 <Variables> 291 <Desc>OutletInner.T</Desc> 292 <Index>0</Index> 293 <Values>377</Values> 294 <Status>3</Status> 295 <Unit>K</Unit> 296 </Variables> 226 297 </Block_Properties> 227 298 </Base_Models> … … 232 303 </Block_Properties> 233 304 </Base_Models> 234 <Model_File_Path>heat_exchangers /DoublePipe</Model_File_Path>305 <Model_File_Path>heat_exchangers\DoublePipe</Model_File_Path> 235 306 <Instance_Id>OutletInner.</Instance_Id> 236 307 <Model_Name>OutletInner</Model_Name> … … 256 327 </Block_Properties> 257 328 </Base_Models> 258 <Model_File_Path>heat_exchangers /DoublePipe</Model_File_Path>329 <Model_File_Path>heat_exchangers\DoublePipe</Model_File_Path> 259 330 <Instance_Id>OutletOuter.</Instance_Id> 260 331 <Model_Name>OutletOuter</Model_Name> … … 266 337 <Base_Models> 267 338 <Block_Properties> 268 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>339 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 269 340 <Instance_Id>Details.</Instance_Id> 270 341 <Model_Name>Details_Main</Model_Name> … … 272 343 </Block_Properties> 273 344 </Base_Models> 274 <Model_File_Path>heat_exchangers /DoublePipe</Model_File_Path>345 <Model_File_Path>heat_exchangers\DoublePipe</Model_File_Path> 275 346 <Instance_Id>Details.</Instance_Id> 276 347 <Model_Name>Details</Model_Name> … … 286 357 <Base_Models> 287 358 <Block_Properties> 288 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>359 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 289 360 <Instance_Id>Inner.HeatTransfer.</Instance_Id> 290 361 <Model_Name>DoublePipe_HeatTransfer</Model_Name> … … 292 363 </Block_Properties> 293 364 </Base_Models> 294 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>365 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 295 366 <Instance_Id>Inner.HeatTransfer.</Instance_Id> 296 367 <Model_Name>HeatTransfer</Model_Name> … … 302 373 <Base_Models> 303 374 <Block_Properties> 304 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>375 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 305 376 <Instance_Id>Inner.PressureDrop.</Instance_Id> 306 377 <Model_Name>DoublePipe_PressureDrop</Model_Name> … … 308 379 </Block_Properties> 309 380 </Base_Models> 310 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>381 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 311 382 <Instance_Id>Inner.PressureDrop.</Instance_Id> 312 383 <Model_Name>PressureDrop</Model_Name> … … 322 393 <Base_Models> 323 394 <Block_Properties> 324 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>395 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 325 396 <Instance_Id>Inner.Properties.Inlet.</Instance_Id> 326 397 <Model_Name>Properties_In_Out</Model_Name> … … 328 399 </Block_Properties> 329 400 </Base_Models> 330 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>401 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 331 402 <Instance_Id>Inner.Properties.Inlet.</Instance_Id> 332 403 <Model_Name>Inlet</Model_Name> … … 338 409 <Base_Models> 339 410 <Block_Properties> 340 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>411 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 341 412 <Instance_Id>Inner.Properties.Average.</Instance_Id> 342 413 <Model_Name>Properties_Average</Model_Name> … … 344 415 </Block_Properties> 345 416 </Base_Models> 346 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>417 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 347 418 <Instance_Id>Inner.Properties.Average.</Instance_Id> 348 419 <Model_Name>Average</Model_Name> … … 354 425 <Base_Models> 355 426 <Block_Properties> 356 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>427 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 357 428 <Instance_Id>Inner.Properties.Outlet.</Instance_Id> 358 429 <Model_Name>Properties_In_Out</Model_Name> … … 360 431 </Block_Properties> 361 432 </Base_Models> 362 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>433 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 363 434 <Instance_Id>Inner.Properties.Outlet.</Instance_Id> 364 435 <Model_Name>Outlet</Model_Name> … … 370 441 <Base_Models> 371 442 <Block_Properties> 372 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>443 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 373 444 <Instance_Id>Inner.Properties.Wall.</Instance_Id> 374 445 <Model_Name>Properties_Wall</Model_Name> … … 376 447 </Block_Properties> 377 448 </Base_Models> 378 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>449 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 379 450 <Instance_Id>Inner.Properties.Wall.</Instance_Id> 380 451 <Model_Name>Wall</Model_Name> … … 382 453 </Block_Properties> 383 454 </Sub_Models> 384 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>455 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 385 456 <Instance_Id>Inner.Properties.</Instance_Id> 386 457 <Model_Name>Physical_Properties</Model_Name> … … 388 459 </Block_Properties> 389 460 </Base_Models> 390 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>461 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 391 462 <Instance_Id>Inner.Properties.</Instance_Id> 392 463 <Model_Name>Properties</Model_Name> … … 394 465 </Block_Properties> 395 466 </Sub_Models> 396 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>467 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 397 468 <Instance_Id>Inner.</Instance_Id> 398 469 <Model_Name>Main_DoublePipe</Model_Name> … … 400 471 </Block_Properties> 401 472 </Base_Models> 402 <Model_File_Path>heat_exchangers /DoublePipe</Model_File_Path>473 <Model_File_Path>heat_exchangers\DoublePipe</Model_File_Path> 403 474 <Instance_Id>Inner.</Instance_Id> 404 475 <Model_Name>Inner</Model_Name> … … 414 485 <Base_Models> 415 486 <Block_Properties> 416 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>487 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 417 488 <Instance_Id>Outer.HeatTransfer.</Instance_Id> 418 489 <Model_Name>DoublePipe_HeatTransfer</Model_Name> … … 420 491 </Block_Properties> 421 492 </Base_Models> 422 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>493 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 423 494 <Instance_Id>Outer.HeatTransfer.</Instance_Id> 424 495 <Model_Name>HeatTransfer</Model_Name> … … 430 501 <Base_Models> 431 502 <Block_Properties> 432 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>503 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 433 504 <Instance_Id>Outer.PressureDrop.</Instance_Id> 434 505 <Model_Name>DoublePipe_PressureDrop</Model_Name> … … 436 507 </Block_Properties> 437 508 </Base_Models> 438 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>509 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 439 510 <Instance_Id>Outer.PressureDrop.</Instance_Id> 440 511 <Model_Name>PressureDrop</Model_Name> … … 450 521 <Base_Models> 451 522 <Block_Properties> 452 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>523 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 453 524 <Instance_Id>Outer.Properties.Inlet.</Instance_Id> 454 525 <Model_Name>Properties_In_Out</Model_Name> … … 456 527 </Block_Properties> 457 528 </Base_Models> 458 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>529 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 459 530 <Instance_Id>Outer.Properties.Inlet.</Instance_Id> 460 531 <Model_Name>Inlet</Model_Name> … … 466 537 <Base_Models> 467 538 <Block_Properties> 468 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>539 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 469 540 <Instance_Id>Outer.Properties.Average.</Instance_Id> 470 541 <Model_Name>Properties_Average</Model_Name> … … 472 543 </Block_Properties> 473 544 </Base_Models> 474 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>545 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 475 546 <Instance_Id>Outer.Properties.Average.</Instance_Id> 476 547 <Model_Name>Average</Model_Name> … … 482 553 <Base_Models> 483 554 <Block_Properties> 484 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>555 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 485 556 <Instance_Id>Outer.Properties.Outlet.</Instance_Id> 486 557 <Model_Name>Properties_In_Out</Model_Name> … … 488 559 </Block_Properties> 489 560 </Base_Models> 490 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>561 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 491 562 <Instance_Id>Outer.Properties.Outlet.</Instance_Id> 492 563 <Model_Name>Outlet</Model_Name> … … 498 569 <Base_Models> 499 570 <Block_Properties> 500 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>571 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 501 572 <Instance_Id>Outer.Properties.Wall.</Instance_Id> 502 573 <Model_Name>Properties_Wall</Model_Name> … … 504 575 </Block_Properties> 505 576 </Base_Models> 506 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>577 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 507 578 <Instance_Id>Outer.Properties.Wall.</Instance_Id> 508 579 <Model_Name>Wall</Model_Name> … … 510 581 </Block_Properties> 511 582 </Sub_Models> 512 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>583 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 513 584 <Instance_Id>Outer.Properties.</Instance_Id> 514 585 <Model_Name>Physical_Properties</Model_Name> … … 516 587 </Block_Properties> 517 588 </Base_Models> 518 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>589 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 519 590 <Instance_Id>Outer.Properties.</Instance_Id> 520 591 <Model_Name>Properties</Model_Name> … … 522 593 </Block_Properties> 523 594 </Sub_Models> 524 <Model_File_Path>heat_exchangers /HEX_Engine</Model_File_Path>595 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 525 596 <Instance_Id>Outer.</Instance_Id> 526 597 <Model_Name>Main_DoublePipe</Model_Name> … … 528 599 </Block_Properties> 529 600 </Base_Models> 530 <Model_File_Path>heat_exchangers /DoublePipe</Model_File_Path>601 <Model_File_Path>heat_exchangers\DoublePipe</Model_File_Path> 531 602 <Instance_Id>Outer.</Instance_Id> 532 603 <Model_Name>Outer</Model_Name> … … 534 605 </Block_Properties> 535 606 </Sub_Models> 536 <Model_File_Path>heat_exchangers /DoublePipe</Model_File_Path>607 <Model_File_Path>heat_exchangers\DoublePipe</Model_File_Path> 537 608 <Instance_Id></Instance_Id> 538 609 <Model_Name>DoublePipe_Basic</Model_Name> … … 577 648 <Desc>CalculationApproach</Desc> 578 649 <Index>0</Index> 579 <Values> Full</Values>650 <Values>Simplified</Values> 580 651 <Status>4</Status> 581 652 </Parameters> … … 583 654 <Desc>Qestimated</Desc> 584 655 <Index>0</Index> 585 <Values> 0.5</Values>656 <Values>1</Values> 586 657 <Status>4</Status> 587 658 <Unit>kW</Unit> 588 659 </Parameters> 589 <Parameters> 590 <Desc>DoInner</Desc> 591 <Index>0</Index> 592 <Values>0.04826</Values> 593 <Status>4</Status> 594 <Unit>m</Unit> 595 </Parameters> 596 <Parameters> 597 <Desc>DiInner</Desc> 598 <Index>0</Index> 599 <Values>0.04089</Values> 600 <Status>4</Status> 601 <Unit>m</Unit> 602 </Parameters> 603 <Parameters> 604 <Desc>DiOuter</Desc> 605 <Index>0</Index> 606 <Values>0.07793</Values> 607 <Status>4</Status> 608 <Unit>m</Unit> 609 </Parameters> 610 <Parameters> 611 <Desc>Lpipe</Desc> 612 <Index>0</Index> 613 <Values>2</Values> 614 <Status>4</Status> 615 <Unit>m</Unit> 616 </Parameters> 617 <Parameters> 618 <Desc>Kwall</Desc> 619 <Index>0</Index> 620 <Values>0.057</Values> 621 <Status>4</Status> 622 <Unit>kW/m/K</Unit> 623 </Parameters> 624 <Parameters> 625 <Desc>Rfi</Desc> 626 <Index>0</Index> 627 <Values>0.0018</Values> 628 <Status>4</Status> 629 <Unit>m^2*K/kW</Unit> 630 </Parameters> 631 <Parameters> 632 <Desc>Rfo</Desc> 633 <Index>0</Index> 634 <Values>0.0021</Values> 635 <Status>4</Status> 636 <Unit>m^2*K/kW</Unit> 637 </Parameters> 638 </Block_Properties> 639 </Base_Models> 640 <Sub_Models> 641 <Block_Properties> 642 <Base_Models> 643 <Block_Properties> 644 <Model_File_Path>heat_exchangers/HEX_Engine</Model_File_Path> 660 </Block_Properties> 661 </Base_Models> 662 <Sub_Models> 663 <Block_Properties> 664 <Base_Models> 665 <Block_Properties> 666 <Model_File_Path>heat_exchangers\HEX_Engine</Model_File_Path> 645 667 <Instance_Id>Method.</Instance_Id> 646 668 <Model_Name>LMTD_Basic</Model_Name> … … 648 670 </Block_Properties> 649 671 </Base_Models> 650 <Model_File_Path>heat_exchangers 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<Model_File_Path>streams</Model_File_Path>684 <Instance_Id>Inlet.</Instance_Id>685 <Model_Name>stream</Model_Name>686 <T_Connection>1</T_Connection>687 </Block_Properties>688 </Base_Models>689 <Model_File_Path>mixers_splitters/splitter</Model_File_Path>690 <Instance_Id>Inlet.</Instance_Id>691 <Model_Name>Inlet</Model_Name>692 <T_Connection>1</T_Connection>693 </Block_Properties>694 </Sub_Models>695 <Sub_Models>696 <Block_Properties>697 <Base_Models>698 <Block_Properties>699 <Model_File_Path>streams</Model_File_Path>700 <Instance_Id>Outlet1.</Instance_Id>701 <Model_Name>stream</Model_Name>702 <T_Connection>2</T_Connection>703 </Block_Properties>704 </Base_Models>705 <Model_File_Path>mixers_splitters/splitter</Model_File_Path>706 <Instance_Id>Outlet1.</Instance_Id>707 <Model_Name>Outlet1</Model_Name>708 <T_Connection>2</T_Connection>709 </Block_Properties>710 </Sub_Models>711 <Sub_Models>712 <Block_Properties>713 <Base_Models>714 <Block_Properties>715 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<Id_String>simple_sink_1</Id_String> 693 <Block_Name>cold_out</Block_Name> 694 <Image_File_Name>E:\Gerson\biblioteca\trunk\eml\icon/Sink.png</Image_File_Name> 695 <X>697.143</X> 696 <Y>291.429</Y> 746 697 <Z>0</Z> 747 698 <Width>72.5</Width> … … 771 722 </Block> 772 723 <Block> 773 <Type>sink</Type>774 <Id_String>sink_1</Id_String>775 <Block_Name>cold_out2</Block_Name>776 <Image_File_Name>/home/bicca/Desktop/biblioteca/biblioteca/trunk/eml/icon/Sink.png</Image_File_Name>777 <X>825</X>778 <Y>295</Y>779 <Z>0</Z>780 <Width>72.5</Width>781 <Height>37</Height>782 <Block_Properties>783 <Sub_Models>784 <Block_Properties>785 <Base_Models>786 <Block_Properties>787 <Model_File_Path>streams</Model_File_Path>788 <Instance_Id>Inlet.</Instance_Id>789 <Model_Name>stream</Model_Name>790 <T_Connection>1</T_Connection>791 </Block_Properties>792 </Base_Models>793 <Model_File_Path>streams</Model_File_Path>794 <Instance_Id>Inlet.</Instance_Id>795 <Model_Name>Inlet</Model_Name>796 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<Y1>240.447</Y1> 853 <X2>28 8</X2>854 <Y2>13 7.665</Y2>771 <X2>285.143</X2> 772 <Y2>139.094</Y2> 855 773 <Block_Source>simple_source_2</Block_Source> 856 774 <Port_Source>simple_source_2.Outlet</Port_Source> … … 859 777 </Line> 860 778 <Line> 861 <Line_Name>line_ 7</Line_Name>862 <X1>48 9.939</X1>863 <Y1>17 3</Y1>864 <X2> 553</X2>865 <Y2> 271</Y2>779 <Line_Name>line_3</Line_Name> 780 <X1>487.082</X1> 781 <Y1>174.429</Y1> 782 <X2>701.429</X2> 783 <Y2>307.143</Y2> 866 784 <Block_Source>DoublePipe_LMTD_1</Block_Source> 867 785 <Port_Source>DoublePipe_LMTD_1.OutletOuter</Port_Source> 868 <Block_Target>s plitter_1</Block_Target>869 <Port_Target>s plitter_1.Inlet</Port_Target>786 <Block_Target>simple_sink_1</Block_Target> 787 <Port_Target>simple_sink_1.Inlet</Port_Target> 870 788 </Line> 871 789 <Line> 872 <Line_Name>line_8</Line_Name> 873 <X1>651</X1> 874 <Y1>256.373</Y1> 875 <X2>821</X2> 876 <Y2>155</Y2> 877 <Block_Source>splitter_1</Block_Source> 878 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<Port_Target>simple_sink_2.Inlet</Port_Target> 903 799 </Line> 904 800 </Diagram> -
trunk/sample/heat_exchangers/DPHE_diagram.rlt
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189 190 0 191 DiInner 192 1 1 1 0.04089 0 193 194 0 195 DiOuter 196 1 1 1 0.07793 0 197 198 0 199 Lpipe 200 1 1 1 2 0 201 202 0 203 Kwall 204 1 1 1 57 0 205 206 0 207 Rfi 208 1 1 1 0.0018 0 209 210 0 211 Rfo 212 1 1 1 0.0021 0 213 214 0 215 InletInner 301 302 0 303 OutletInner 304 0 1 305 streamPH 216 306 0 1 217 307 stream … … 228 318 0 229 319 T 230 1 1 1 373.15 0 231 232 0 233 P 234 1 1 1 5.62546 0 320 1 1 1 353.385 0 321 322 0 323 P 324 1 1 1 5.56921 0 325 326 0 327 h 328 1 1 1 -43522.1 0 329 330 0 331 v 332 1 1 1 0 0 333 334 0 335 z 336 1 2 1 1 1 0 0 337 338 0 339 340 3 341 x 342 1 2 1 1 1 -9.69422e-025 0 343 344 0 345 y 346 1 2 1 1 1 0 0 347 348 0 349 s 350 1 1 1 -186.244 0 351 352 0 353 354 0 355 OutletOuter 356 0 1 357 streamPH 358 0 1 359 stream 360 0 0 361 362 7 363 NComp 364 0 0 365 366 0 367 F 368 1 1 1 3 0 369 370 0 371 T 372 1 1 1 344.714 0 373 374 0 375 P 376 1 1 1 4.88527 0 377 378 0 379 h 380 1 1 1 -41975.2 0 381 382 0 383 v 384 1 1 1 0 0 235 385 236 386 0 237 387 z 238 388 1 2 1 0 1 1 0 239 240 0241 h242 1 1 1 -39638.5 0243 244 0245 v246 1 1 1 0 0247 248 0249 250 0251 InletOuter252 0 1253 stream254 0 0255 256 7257 NComp258 0 0259 260 0261 F262 1 1 1 3 0263 264 0265 T266 1 1 1 330 0267 268 0269 P270 1 1 1 4.93462 0271 272 0273 z274 1 2 1 1 1 0 0275 276 0277 h278 1 1 1 -47617 0279 280 0281 v282 1 1 1 0 0283 284 0285 286 0287 OutletInner288 0 1289 streamPH290 0 1291 stream292 0 0293 294 7295 NComp296 0 0297 298 0299 F300 1 1 1 1 0301 302 0303 T304 1 1 1 351.262 0305 306 0307 P308 1 1 1 5.62546 0309 310 0311 z312 1 2 1 0 1 1 0313 314 0315 h316 1 1 1 -41438.5 0317 318 0319 v320 1 1 1 0 0321 389 322 390 0 … … 332 400 0 333 401 s 334 1 1 1 -205.822 0 335 336 0 337 338 0 339 OutletOuter 340 0 1 341 streamPH 342 0 1 343 stream 344 0 0 345 346 7 347 NComp 348 0 0 349 350 0 351 F 352 1 1 1 3 0 353 354 0 355 T 356 1 1 1 333.498 0 357 358 0 359 P 360 1 1 1 4.93462 0 361 362 0 363 z 364 1 2 1 1 1 0 0 365 366 0 367 h 368 1 1 1 -47017 0 369 370 0 371 v 372 1 1 1 0 0 373 374 0 375 376 3 377 x 378 1 2 1 1 1 0 0 379 380 0 381 y 382 1 2 1 1 1 0 0 383 384 0 385 s 386 1 1 1 -196.401 0 402 1 1 1 -207.36 0 387 403 388 404 0 … … 396 412 4 397 413 A 398 1 1 1 0. 3032270414 1 1 1 0.45484 0 399 415 400 416 0 401 417 Q 402 1 1 1 0.50418 1 1 1 1 0 403 419 404 420 0 405 421 Uc 406 1 1 1 0.02 385440422 1 1 1 0.0227611 0 407 423 408 424 0 409 425 Ud 410 1 1 1 0.02 38520426 1 1 1 0.0227589 0 411 427 412 428 0 … … 434 450 0 435 451 Re 436 1 1 1 504.830452 1 1 1 691.051 0 437 453 438 454 0 439 455 hcoeff 440 1 1 1 0.0 839960456 1 1 1 0.0336668 0 441 457 442 458 0 443 459 fi 444 1 1 1 0.0 931132 0460 1 1 1 0.0804702 0 445 461 446 462 0 447 463 Nu 448 1 1 1 5.164980464 1 1 1 8.31205 0 449 465 450 466 0 451 467 PR 452 1 1 1 2.060620468 1 1 1 13.3624 0 453 469 454 470 0 455 471 Phi 456 1 1 1 0.97 26730472 1 1 1 0.970882 0 457 473 458 474 0 459 475 Vmean 460 1 1 1 0.0 04714130476 1 1 1 0.0180309 0 461 477 462 478 0 … … 474 490 0 475 491 Pdrop 476 1 1 1 00492 1 1 1 5.7 0 477 493 478 494 0 479 495 Pd_fric 480 1 1 1 00496 1 1 1 5.7 0 481 497 482 498 0 … … 486 502 0 487 503 fi 488 1 1 1 0.0 3169380504 1 1 1 0.0231531 0 489 505 490 506 0 491 507 Re 492 1 1 1 504.830508 1 1 1 691.051 0 493 509 494 510 0 … … 508 524 2 509 525 Fw 510 1 1 1 18.01520526 1 1 1 75 0 511 527 512 528 0 513 529 rho 514 1 1 1 8 00.4870530 1 1 1 873.684 0 515 531 516 532 0 … … 524 540 7 525 541 Mw 526 1 1 1 18.01520527 528 0 529 T 530 1 1 1 36 2.2060531 532 0 533 P 534 1 1 1 5 700542 1 1 1 75 0 543 544 0 545 T 546 1 1 1 363.267 0 547 548 0 549 P 550 1 1 1 567.15 0 535 551 536 552 0 537 553 rho 538 1 1 1 8 08.3710554 1 1 1 879.867 0 539 555 540 556 0 541 557 Mu 542 1 1 1 0. 3086630558 1 1 1 0.938732 0 543 559 544 560 0 545 561 Cp 546 1 1 1 82.22310562 1 1 1 182.117 0 547 563 548 564 0 549 565 K 550 1 1 1 0. 6836610566 1 1 1 0.170587 0 551 567 552 568 0 … … 560 576 2 561 577 Fw 562 1 1 1 18.01520578 1 1 1 75 0 563 579 564 580 0 565 581 rho 566 1 1 1 8 15.9230582 1 1 1 885.837 0 567 583 568 584 0 … … 576 592 2 577 593 Mu 578 1 1 1 0.3762150594 1 1 1 1.15934 0 579 595 580 596 0 581 597 Twall 582 1 1 1 3 46.9770598 1 1 1 350.312 0 583 599 584 600 0 … … 610 626 0 611 627 Re 612 1 1 1 1234.690628 1 1 1 3810.3 0 613 629 614 630 0 615 631 hcoeff 616 1 1 1 0. 03597170632 1 1 1 0.11349 0 617 633 618 634 0 619 635 fi 620 1 1 1 0.0 630133 0636 1 1 1 0.0420963 0 621 637 622 638 0 623 639 Nu 624 1 1 1 1 5.20950640 1 1 1 12.9232 0 625 641 626 642 0 627 643 PR 628 1 1 1 17.35750644 1 1 1 0.708888 0 629 645 630 646 0 631 647 Phi 632 1 1 1 1.0 42720648 1 1 1 1.02634 0 633 649 634 650 0 635 651 Vmean 636 1 1 1 0.02 938340652 1 1 1 0.0257609 0 637 653 638 654 0 … … 650 666 0 651 667 Pdrop 652 1 1 1 00668 1 1 1 5 0 653 669 654 670 0 655 671 Pd_fric 656 1 1 1 00672 1 1 1 5 0 657 673 658 674 0 … … 662 678 0 663 679 fi 664 1 1 1 0.0 3388440680 1 1 1 0.0109799 0 665 681 666 682 0 667 683 Re 668 1 1 1 472.1940684 1 1 1 1457.21 0 669 685 670 686 0 … … 684 700 2 685 701 Fw 686 1 1 1 2 79.3840702 1 1 1 225 0 687 703 688 704 0 689 705 rho 690 1 1 1 8 99.1450706 1 1 1 829.713 0 691 707 692 708 0 … … 700 716 7 701 717 Mw 702 1 1 1 93.1280703 704 0 705 T 706 1 1 1 33 1.7490707 708 0 709 P 710 1 1 1 5000718 1 1 1 75 0 719 720 0 721 T 722 1 1 1 337.357 0 723 724 0 725 P 726 1 1 1 497.5 0 711 727 712 728 0 713 729 rho 714 1 1 1 8 98.1840730 1 1 1 825.062 0 715 731 716 732 0 717 733 Mu 718 1 1 1 1.65830734 1 1 1 0.432756 0 719 735 720 736 0 721 737 Cp 722 1 1 1 171.5290738 1 1 1 81.5541 0 723 739 724 740 0 725 741 K 726 1 1 1 0. 175969 0742 1 1 1 0.663819 0 727 743 728 744 0 … … 736 752 2 737 753 Fw 738 1 1 1 2 79.3840754 1 1 1 225 0 739 755 740 756 0 741 757 rho 742 1 1 1 8 97.2170758 1 1 1 820.28 0 743 759 744 760 0 … … 752 768 2 753 769 Mu 754 1 1 1 1.229990770 1 1 1 0.359403 0 755 771 756 772 0 757 773 Twall 758 1 1 1 3 46.9770774 1 1 1 350.312 0 759 775 760 776 0 … … 774 790 4 775 791 DT0 776 1 1 1 39.65210792 1 1 1 28.4359 0 777 793 778 794 0 779 795 DTL 780 1 1 1 2 1.2620796 1 1 1 23.3846 0 781 797 782 798 0 783 799 LMTD 784 1 1 1 2 9.50810800 1 1 1 25.828 0 785 801 786 802 0 … … 793 809 794 810 0 795 splitter_1 796 0 1 797 s plitter798 0 0 799 800 4 811 cold_out 812 0 1 813 simple_sink 814 0 0 815 816 1 801 817 Inlet 802 818 0 1 … … 814 830 0 815 831 T 816 1 1 1 333.498 0 817 818 0 819 P 820 1 1 1 4.93462 0 832 1 1 1 344.714 0 833 834 0 835 P 836 1 1 1 4.88527 0 837 838 0 839 h 840 1 1 1 -41975.2 0 841 842 0 843 v 844 1 1 1 0 0 845 846 0 847 z 848 1 2 1 0 1 1 0 849 850 0 851 852 0 853 854 0 855 hot_out 856 0 1 857 simple_sink 858 0 0 859 860 1 861 Inlet 862 0 1 863 stream 864 0 0 865 866 7 867 NComp 868 0 0 869 870 0 871 F 872 1 1 1 1 0 873 874 0 875 T 876 1 1 1 353.385 0 877 878 0 879 P 880 1 1 1 5.56921 0 881 882 0 883 h 884 1 1 1 -43522.1 0 885 886 0 887 v 888 1 1 1 0 0 821 889 822 890 0 … … 825 893 826 894 0 827 h 828 1 1 1 -47017 0 829 830 0 831 v 832 1 1 1 0 0 833 834 0 835 836 0 837 Outlet1 838 0 1 839 stream 840 0 0 841 842 7 843 NComp 844 0 0 845 846 0 847 F 848 1 1 1 2.1 0 849 850 0 851 T 852 1 1 1 333.498 0 853 854 0 855 P 856 1 1 1 4.93462 0 857 858 0 859 z 860 1 2 1 1 1 0 0 861 862 0 863 h 864 1 1 1 -47017 0 865 866 0 867 v 868 1 1 1 0 0 869 870 0 871 872 0 873 Outlet2 874 0 1 875 stream 876 0 0 877 878 7 879 NComp 880 0 0 881 882 0 883 F 884 1 1 1 0.9 0 885 886 0 887 T 888 1 1 1 333.498 0 889 890 0 891 P 892 1 1 1 4.93462 0 893 894 0 895 z 896 1 2 1 1 1 0 0 897 898 0 899 h 900 1 1 1 -47017 0 901 902 0 903 v 904 1 1 1 0 0 905 906 0 907 908 0 909 frac 910 1 1 1 0.7 0 911 912 0 913 914 0 915 cold_out1 916 0 1 917 simple_sink 918 0 0 919 920 1 921 Inlet 922 0 1 923 stream 924 0 0 925 926 7 927 NComp 928 0 0 929 930 0 931 F 932 1 1 1 2.1 0 933 934 0 935 T 936 1 1 1 333.498 0 937 938 0 939 P 940 1 1 1 4.93462 0 941 942 0 943 z 944 1 2 1 1 1 0 0 945 946 0 947 h 948 1 1 1 -47017 0 949 950 0 951 v 952 1 1 1 0 0 953 954 0 955 956 0 957 958 0 959 cold_out2 960 0 1 961 sink 962 0 0 963 964 14 965 NComp 966 0 0 967 968 0 969 M 970 1 2 1 93.128 1 18.0152 0 971 972 0 973 Inlet 974 0 1 975 stream 976 0 0 977 978 7 979 NComp 980 0 0 981 982 0 983 F 984 1 1 1 0.9 0 985 986 0 987 T 988 1 1 1 333.498 0 989 990 0 991 P 992 1 1 1 4.93462 0 993 994 0 995 z 996 1 2 1 1 1 0 0 997 998 0 999 h 1000 1 1 1 -47017 0 1001 1002 0 1003 v 1004 1 1 1 0 0 1005 1006 0 1007 1008 0 1009 v 1010 1 1 1 0 0 1011 1012 0 1013 x 1014 1 2 1 1 1 0 0 1015 1016 0 1017 y 1018 1 2 1 1 1 0 0 1019 1020 0 1021 zmass 1022 1 2 1 1 1 0 0 1023 1024 0 1025 Mw 1026 1 1 1 93.128 0 1027 1028 0 1029 vm 1030 1 1 1 0.000103797 0 1031 1032 0 1033 rho 1034 1 1 1 897.217 0 1035 1036 0 1037 rhom 1038 1 1 1 9.63423 0 1039 1040 0 1041 Fw 1042 1 1 1 83.8152 0 1043 1044 0 1045 Fvol 1046 1 1 1 0.0934169 0 1047 1048 0 1049 s 1050 1 1 1 -196.401 0 1051 1052 0 1053 1054 0 1055 hot_out 1056 0 1 1057 simple_sink 1058 0 0 1059 1060 1 1061 Inlet 1062 0 1 1063 stream 1064 0 0 1065 1066 7 1067 NComp 1068 0 0 1069 1070 0 1071 F 1072 1 1 1 1 0 1073 1074 0 1075 T 1076 1 1 1 351.262 0 1077 1078 0 1079 P 1080 1 1 1 5.62546 0 1081 1082 0 1083 z 1084 1 2 1 0 1 1 0 1085 1086 0 1087 h 1088 1 1 1 -41438.5 0 1089 1090 0 1091 v 1092 1 1 1 0 0 1093 1094 0 1095 1096 0 1097 1098 0 895 896 0 897 898 0 -
trunk/sample/heat_exchangers/Sample_DoublePipe.mso
r236 r525 67 67 #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ 68 68 69 exchanger. DoInner = 0.04826*'m';70 exchanger. DiInner = 0.04089*'m';71 exchanger. DiOuter = 0.07793*'m';72 exchanger. Kwall = 0.057 *'kW/m/K';73 exchanger. Lpipe = 3*'m';69 exchanger.Geometry.DoInner = 0.04826*'m'; 70 exchanger.Geometry.DiInner = 0.04089*'m'; 71 exchanger.Geometry.DiOuter = 0.07793*'m'; 72 exchanger.Geometry.Kwall = 0.057 *'kW/m/K'; 73 exchanger.Geometry.Lpipe = 3*'m'; 74 74 75 75 #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ 76 76 # Fouling 77 77 #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ 78 exchanger. Rfi = 0.0018*'m^2*K/kW';79 exchanger. Rfo = 0.0021*'m^2*K/kW';78 exchanger.Geometry.Rfi = 0.0018*'m^2*K/kW'; 79 exchanger.Geometry.Rfo = 0.0021*'m^2*K/kW'; 80 80 81 81 SPECIFY … … 145 145 #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ 146 146 147 exchanger. DoInner = 0.04826*'m';148 exchanger. DiInner = 0.04089*'m';149 exchanger. DiOuter = 0.07793*'m';150 exchanger. Kwall = 0.057 *'kW/m/K';151 exchanger. Lpipe = 3*'m';147 exchanger.Geometry.DoInner = 0.04826*'m'; 148 exchanger.Geometry.DiInner = 0.04089*'m'; 149 exchanger.Geometry.DiOuter = 0.07793*'m'; 150 exchanger.Geometry.Kwall = 0.057 *'kW/m/K'; 151 exchanger.Geometry.Lpipe = 3*'m'; 152 152 153 153 #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ 154 154 # Fouling 155 155 #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ 156 exchanger. Rfi = 0.0018*'m^2*K/kW';157 exchanger. Rfo = 0.0021*'m^2*K/kW';156 exchanger.Geometry.Rfi = 0.0018*'m^2*K/kW'; 157 exchanger.Geometry.Rfo = 0.0021*'m^2*K/kW'; 158 158 159 159 SPECIFY
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