source: branches/new_gui/streams/sources.mso @ 887

Last change on this file since 887 was 887, checked in by gerson bicca, 14 years ago

added folder for streams
File size: 18.7 KB
Line 
1#*-------------------------------------------------------------------
2* EMSO Model Library (EML) Copyright (C) 2004 - 2007 ALSOC.
3*
4* This LIBRARY is free software; you can distribute it and/or modify
5* it under the therms of the ALSOC FREE LICENSE as available at
6* http://www.enq.ufrgs.br/alsoc.
7*
8* EMSO Copyright (C) 2004 - 2007 ALSOC, original code
9* from http://www.rps.eng.br Copyright (C) 2002-2004.
10* All rights reserved.
11*
12* EMSO is distributed under the therms of the ALSOC LICENSE as
13* available at http://www.enq.ufrgs.br/alsoc.
14*
15*--------------------------------------------------------------------
16* Model of source streams
17*----------------------------------------------------------------------
18* Author: Paula B. Staudt and Rafael de P. Soares
19* $Id: sources.mso 757 2009-06-03 20:07:22Z bicca $
20*---------------------------------------------------------------------*#
21
22using "streams";
23
24Model energy_source
25        ATTRIBUTES
26        Pallete = true;
27        Icon = "icon/energy_source";
28        Brief = "Energy stream source";
29
30        VARIABLES
31        out OutletQ             as power(Brief = "Outlet energy stream", PosX=1, PosY=0.40, Symbol="_{out}");
32
33end
34
35Model energy_source2
36        ATTRIBUTES
37        Pallete = true;
38        Icon = "icon/energy_source2";
39        Brief = "Energy stream source";
40
41        VARIABLES
42        out OutletQ             as power(Brief = "Outlet energy stream", PosX=0, PosY=0.40, Symbol="_{out}");
43
44end
45
46Model info_stream
47        ATTRIBUTES
48        Pallete = true;
49        Icon = "icon/Info_Stream";
50        Brief = "Material stream information";
51        Info = "
52        This model should be used for middle streams when additional
53        information about the stream is desired.
54
55        Some of the additional informations calculated by this models are:
56         * Mass density
57         * Mass flow
58         * Mass compostions
59         * Specific volume
60         * Vapour fraction
61         * Volumetric flow
62         * Liquid and Vapour compositions
63         * Viscosity
64         * Heat Capacity
65         * Thermal Conductivity
66         * Temperature in Celsius Degrees
67        ";
68
69PARAMETERS
70        outer PP                        as Plugin                       (Brief = "External Physical Properties", Type="PP");
71        outer NComp     as Integer                      (Brief = "Number of chemical components", Lower = 1);
72                  M(NComp)      as molweight    (Brief = "Component Mol Weight");
73       
74SET
75
76        M   = PP.MolecularWeight();
77       
78VARIABLES
79
80        in      Inlet           as stream               (Brief = "Inlet Stream", PosX=0, PosY=0.50, Protected=true , Symbol="_{in}");
81        out     Outlet          as stream               (Brief = "Outlet Stream", PosX=1, PosY=0.50, Protected=true , Symbol="_{out}");
82       
83        v                                               as fraction                     (Brief = "Vapourization fraction",Hidden=true);
84        x(NComp)                        as fraction                     (Brief = "Liquid Molar Fraction",Hidden=true);
85        y(NComp)                        as fraction                     (Brief = "Vapour Molar Fraction",Hidden=true);
86       
87        F(NComp)        as flow_mol             (Brief = "Component Molar Flow",Protected=true);
88        FwTotal         as flow_mass            (Brief = "Total Mass Flow",Protected=true);
89        Fw(NComp)               as flow_mass            (Brief = "Component Mass Flow",Protected=true);
90        FvolTotal           as flow_vol         (Brief = "Total Volumetric Flow",Protected=true);
91        T_Cdeg                          as temperature          (Brief = "Temperature in °C", Lower=-200,Protected=true);
92
93        Mu                                      as viscosity            (Brief="Stream Viscosity",Lower=0.0001, Symbol = "\mu",Protected=true);
94        Cp                                      as cp_mol                       (Brief="Stream Molar Heat Capacity", Upper=1e10,Protected=true);       
95        K                                               as conductivity         (Brief="Stream Thermal Conductivity", Default=1.0, Lower=1e-5, Upper=500,Protected=true);
96        Mw                                      as molweight            (Brief = "Average Mol Weight",Protected=true);
97        vm                                      as volume_mol   (Brief = "Molar Volume",Protected=true);       
98        rho                                     as dens_mass            (Brief = "Stream Mass Density",Protected=true);
99        rhom                                    as dens_mol             (Brief = "Stream Molar Density",Protected=true);
100        s                                               as entr_mol             (Brief = "Stream Entropy",Protected=true);
101        zmass(NComp)    as fraction                     (Brief = "Mass Fraction",Protected=true);
102       
103EQUATIONS
104
105"Flash Calculation"
106        [v, x, y] = PP.FlashPH(Inlet.P, Inlet.h, Inlet.z);
107       
108"Average Molecular Weight"
109        Mw = sum(M*Inlet.z);
110
111"Mass Density"
112        rho * ((1-v)/PP.LiquidDensity(Inlet.T,Inlet.P,x) + v/PP.VapourDensity(Inlet.T,Inlet.P,y)) = 1;
113       
114"Mass or Molar Density"
115        rhom * Mw = rho;
116
117"Total Flow Mass"
118        FwTotal =  Mw*Inlet.F;
119
120"Component Flow Mass"
121        Fw      =  FwTotal*zmass;
122
123"Molar Volume"
124        vm = (1-v)*PP.LiquidVolume(Inlet.T, Inlet.P, x) + v*PP.VapourVolume(Inlet.T,Inlet.P,y);
125       
126"Total Volumetric Flow"
127        FvolTotal = Inlet.F*vm ;
128       
129"Mass Fraction"
130        zmass = M*Inlet.z / Mw;
131
132"Stream Heat Capacity"
133        Cp      =       (1-v)*PP.LiquidCp(Inlet.T, Inlet.P, x) + v*PP.VapourCp(Inlet.T,Inlet.P,y);
134
135"Stream Viscosity"
136        Mu      =       (1-v)*PP.LiquidViscosity(Inlet.T, Inlet.P, x) + v*PP.VapourViscosity(Inlet.T,Inlet.P,y);
137
138"Stream ThermalConductivity"
139        K       =       (1-v)*PP.LiquidThermalConductivity(Inlet.T, Inlet.P, x) + v*PP.VapourThermalConductivity(Inlet.T,Inlet.P,y);
140
141"Stream Overall Entropy"
142        s = (1-v)*PP.LiquidEntropy(Inlet.T, Inlet.P, x) + v*PP.VapourEntropy(Inlet.T, Inlet.P, y);
143       
144"Temperature in °C"
145        T_Cdeg = Inlet.T - 273.15 * 'K';
146
147"Outlet Flow"
148        Outlet.F = Inlet.F;
149
150"Component Molar Flow"
151        F = Inlet.F*Inlet.z;
152
153"Outlet Temperature"
154        Outlet.T = Inlet.T;
155
156"Outlet Pressure"
157        Outlet.P = Inlet.P;
158
159"Outlet Vapour Fraction"
160        Outlet.v = Inlet.v;
161
162"Outlet Enthalpy"
163        Outlet.h = Inlet.h;
164
165"Outlet Composition"
166        Outlet.z= Inlet.z;
167
168end
169
170Model source
171
172ATTRIBUTES
173        Pallete = true;
174        Icon = "icon/Source";
175        Brief = "Material stream source";
176        Info = "
177        This model should be used for boundary streams.
178        Usually these streams are known and come from another process
179        units.
180
181        The user should specify:
182         * Total molar (mass or volumetric) flow
183         * Temperature
184         * Pressure
185         * Molar or mass composition
186       
187        No matter the specification set, the model will calculate some
188        additional properties:
189         * Mass density
190         * Mass flow
191         * Mass compostions
192         * Specific volume
193         * Vapour fraction
194         * Volumetric flow
195         * Liquid and Vapour compositions
196        ";
197
198PARAMETERS
199        outer PP                                                as Plugin                       (Brief = "External Physical Properties", Type="PP");
200        outer NComp                             as Integer                      (Brief = "Number of chemical components", Lower = 1);
201                  M(NComp)                              as molweight    (Brief = "Component Mol Weight");
202                  CompositionBasis              as Switcher             (Brief = "Molar or Mass Composition", Valid = ["Molar", "Mass"], Default="Molar");
203                  ValidPhases                           as Switcher             (Brief = "Valid Phases for Flash Calculation", Valid = ["Vapour-Only", "Liquid-Only","Vapour-Liquid"], Default="Vapour-Liquid");
204       
205
206SET
207
208        M   = PP.MolecularWeight();
209
210VARIABLES
211
212        out Outlet                      as stream                       (Brief = "Outlet stream", PosX=1, PosY=0.5256, Symbol="_{out}",Protected=true);
213       
214        Composition(NComp) as fraction                  (Brief = "Stream Composition");
215        SumOfComposition as positive                    (Brief = "Sum of Stream Composition",Protected=true);
216        F                                                               as flow_mol             (Brief = "Stream Molar Flow Rate");
217        Fw                                                      as flow_mass            (Brief = "Stream Mass Flow");
218        Fvol                                    as flow_vol        (Brief = "Volumetric Flow");
219        T                                                               as temperature  (Brief = "Stream Temperature");
220        T_Cdeg                                          as temperature  (Brief = "Temperature in °C", Lower=-200);
221        P                                                               as pressure             (Brief = "Stream Pressure");
222       
223        x(NComp)                        as fraction                     (Brief = "Liquid Molar Fraction",Hidden=true);
224        y(NComp)                        as fraction                     (Brief = "Vapour Molar Fraction",Hidden=true);
225       
226        Mw                                              as molweight                    (Brief = "Average Mol Weight",Protected=true);
227        vm                                              as volume_mol           (Brief = "Molar Volume",Protected=true);       
228        rho                                             as dens_mass                    (Brief = "Stream Mass Density",Protected=true);
229        rhom                                            as dens_mol                     (Brief = "Stream Molar Density",Protected=true);
230       
231        zmass(NComp)            as fraction                             (Brief = "Mass Fraction",Protected=true);
232       
233        EQUATIONS
234
235switch CompositionBasis
236
237        case "Molar":
238"Stream Molar Composition"
239        Outlet.z = Composition/sum(Composition);
240
241"Stream Mass Composition"
242        zmass = M*Outlet.z / Mw;
243
244        case "Mass":
245"Stream Mass Composition"
246        zmass = Composition/sum(Composition);
247
248"Stream Molar Composition"
249        Outlet.z*sum(zmass/M) = zmass/M;
250
251end
252
253switch ValidPhases
254       
255        case "Liquid-Only":
256
257"Vapour Fraction"
258        Outlet.v = 0;
259
260"Liquid Composition"
261        x = Outlet.z;
262
263"Vapour Composition"
264        y = Outlet.z;
265
266"Overall Enthalpy"
267        Outlet.h = PP.LiquidEnthalpy(Outlet.T, Outlet.P, x);
268
269"Molar Volume"
270        vm = PP.LiquidVolume(Outlet.T, Outlet.P, x);
271
272        case "Vapour-Only":
273
274"Vapor Fraction"
275        Outlet.v = 1;
276
277"Liquid Composition"
278        x = Outlet.z;
279
280"Vapour Composition"
281        y = Outlet.z;
282
283"Overall Enthalpy"
284        Outlet.h = PP.VapourEnthalpy(Outlet.T, Outlet.P, y);
285
286"Molar Volume"
287        vm = PP.VapourVolume(Outlet.T, Outlet.P, y);
288
289
290        case "Vapour-Liquid":
291
292"Flash Calculation"
293        [Outlet.v, x, y] = PP.Flash(Outlet.T, Outlet.P, Outlet.z);
294
295"Overall Enthalpy"
296        Outlet.h = (1-Outlet.v)*PP.LiquidEnthalpy(Outlet.T, Outlet.P, x) + Outlet.v*PP.VapourEnthalpy(Outlet.T, Outlet.P, y);
297
298"Molar Volume"
299        vm = (1-Outlet.v)*PP.LiquidVolume(Outlet.T, Outlet.P, x) + Outlet.v*PP.VapourVolume(Outlet.T,Outlet.P,y);
300
301end
302
303"Sum of Composition"
304        SumOfComposition = sum(Composition);
305
306"Molar Density"
307        rhom * vm = 1;
308
309"Average Molecular Weight"
310        Mw = sum(M*Outlet.z);
311
312"Mass or Molar Density"
313        rhom * Mw = rho;
314
315"Flow Mass"
316        Fw      =  Mw*Outlet.F;
317
318"Volumetric Flow"
319        Fvol = Outlet.F*vm ;
320       
321"Temperature in °C"
322        T_Cdeg = Outlet.T - 273.15 * 'K';
323
324"Equate Flow"
325        Outlet.F = F;
326
327"Equate Pressures"
328        Outlet.P = P;
329
330"Equate Temperatures"
331        Outlet.T = T;
332
333end
334
335Model source2
336
337ATTRIBUTES
338        Pallete = true;
339        Icon = "icon/Source2";
340        Brief = "Material stream source";
341        Info = "
342        This model should be used for boundary streams.
343        Usually these streams are known and come from another process
344        units.
345
346        The user should specify:
347         * Total molar (mass or volumetric) flow
348         * Temperature
349         * Pressure
350         * Molar or mass composition
351       
352        No matter the specification set, the model will calculate some
353        additional properties:
354         * Mass density
355         * Mass flow
356         * Mass compostions
357         * Specific volume
358         * Vapour fraction
359         * Volumetric flow
360         * Liquid and Vapour compositions
361        ";
362
363PARAMETERS
364        outer PP                                                as Plugin                       (Brief = "External Physical Properties", Type="PP");
365        outer NComp                             as Integer                      (Brief = "Number of chemical components", Lower = 1);
366                  M(NComp)                              as molweight    (Brief = "Component Mol Weight");
367                  CompositionBasis              as Switcher             (Brief = "Molar or Mass Composition", Valid = ["Molar", "Mass"], Default="Molar");
368                  ValidPhases                           as Switcher             (Brief = "Valid Phases for Flash Calculation", Valid = ["Vapour-Only", "Liquid-Only","Vapour-Liquid"], Default="Vapour-Liquid");
369       
370
371SET
372
373        M   = PP.MolecularWeight();
374
375VARIABLES
376
377        out Outlet                      as stream                       (Brief = "Outlet stream", PosX=0, PosY=0.5256, Symbol="_{out}",Protected=true);
378       
379        Composition(NComp) as fraction                  (Brief = "Stream Composition");
380        SumOfComposition as positive                    (Brief = "Sum of Stream Composition",Protected=true);
381        F                                                               as flow_mol             (Brief = "Stream Molar Flow Rate");
382        Fw                                                      as flow_mass            (Brief = "Stream Mass Flow");
383        Fvol                                    as flow_vol        (Brief = "Volumetric Flow");
384        T                                                               as temperature  (Brief = "Stream Temperature");
385        T_Cdeg                                          as temperature  (Brief = "Temperature in °C", Lower=-200);
386        P                                                               as pressure             (Brief = "Stream Pressure");
387       
388        x(NComp)                        as fraction                     (Brief = "Liquid Molar Fraction",Hidden=true);
389        y(NComp)                        as fraction                     (Brief = "Vapour Molar Fraction",Hidden=true);
390       
391        Mw                                              as molweight                    (Brief = "Average Mol Weight",Protected=true);
392        vm                                              as volume_mol           (Brief = "Molar Volume",Protected=true);       
393        rho                                             as dens_mass                    (Brief = "Stream Mass Density",Protected=true);
394        rhom                                            as dens_mol                     (Brief = "Stream Molar Density",Protected=true);
395       
396        zmass(NComp)            as fraction                             (Brief = "Mass Fraction",Protected=true);
397       
398        EQUATIONS
399
400switch CompositionBasis
401
402        case "Molar":
403"Stream Molar Composition"
404        Outlet.z = Composition/sum(Composition);
405
406"Stream Mass Composition"
407        zmass = M*Outlet.z / Mw;
408
409        case "Mass":
410"Stream Mass Composition"
411        zmass = Composition/sum(Composition);
412
413"Stream Molar Composition"
414        Outlet.z*sum(zmass/M) = zmass/M;
415
416end
417
418switch ValidPhases
419       
420        case "Liquid-Only":
421
422"Vapour Fraction"
423        Outlet.v = 0;
424
425"Liquid Composition"
426        x = Outlet.z;
427
428"Vapour Composition"
429        y = Outlet.z;
430
431"Overall Enthalpy"
432        Outlet.h = PP.LiquidEnthalpy(Outlet.T, Outlet.P, x);
433
434"Molar Volume"
435        vm = PP.LiquidVolume(Outlet.T, Outlet.P, x);
436
437        case "Vapour-Only":
438
439"Vapor Fraction"
440        Outlet.v = 1;
441
442"Liquid Composition"
443        x = Outlet.z;
444
445"Vapour Composition"
446        y = Outlet.z;
447
448"Overall Enthalpy"
449        Outlet.h = PP.VapourEnthalpy(Outlet.T, Outlet.P, y);
450
451"Molar Volume"
452        vm = PP.VapourVolume(Outlet.T, Outlet.P, y);
453
454
455        case "Vapour-Liquid":
456
457"Flash Calculation"
458        [Outlet.v, x, y] = PP.Flash(Outlet.T, Outlet.P, Outlet.z);
459
460"Overall Enthalpy"
461        Outlet.h = (1-Outlet.v)*PP.LiquidEnthalpy(Outlet.T, Outlet.P, x) + Outlet.v*PP.VapourEnthalpy(Outlet.T, Outlet.P, y);
462
463"Molar Volume"
464        vm = (1-Outlet.v)*PP.LiquidVolume(Outlet.T, Outlet.P, x) + Outlet.v*PP.VapourVolume(Outlet.T,Outlet.P,y);
465
466end
467
468"Sum of Composition"
469        SumOfComposition = sum(Composition);
470
471"Molar Density"
472        rhom * vm = 1;
473
474"Average Molecular Weight"
475        Mw = sum(M*Outlet.z);
476
477"Mass or Molar Density"
478        rhom * Mw = rho;
479
480"Flow Mass"
481        Fw      =  Mw*Outlet.F;
482
483"Volumetric Flow"
484        Fvol = Outlet.F*vm ;
485       
486"Temperature in °C"
487        T_Cdeg = Outlet.T - 273.15 * 'K';
488
489"Equate Flow"
490        Outlet.F = F;
491
492"Equate Pressures"
493        Outlet.P = P;
494
495"Equate Temperatures"
496        Outlet.T = T;
497
498end
499
500Model simple_source
501
502ATTRIBUTES
503        Pallete = true;
504        Icon = "icon/Source";
505        Brief = "Simple Material stream source";
506        Info = "
507        This model should be used for boundary streams.
508        Usually these streams are known and come from another process
509        units.
510
511        The user should specify:
512         * Total molar flow
513         * Temperature
514         * Pressure
515         * Molar composition
516";
517
518PARAMETERS
519        outer PP                                                as Plugin                       (Brief = "External Physical Properties", Type="PP");
520        outer NComp                             as Integer                      (Brief = "Number of chemical components", Lower = 1);
521                  M(NComp)                              as molweight    (Brief = "Component Mol Weight");
522                  ValidPhases                           as Switcher             (Brief = "Valid Phases for Flash Calculation", Valid = ["Vapour-Only", "Liquid-Only","Vapour-Liquid"], Default="Vapour-Liquid");
523       
524
525SET
526
527        M   = PP.MolecularWeight();
528
529VARIABLES
530
531        out Outlet                      as stream                       (Brief = "Outlet stream", PosX=1, PosY=0.5256, Symbol="_{out}",Protected=true);
532       
533        MolarComposition(NComp) as fraction                     (Brief = "Stream Molar Composition");
534        SumOfComposition as positive                    (Brief = "Sum of Stream Composition",Protected=true);
535        F                                                               as flow_mol             (Brief = "Stream Molar Flow Rate");
536        T                                                               as temperature  (Brief = "Stream Temperature");
537        T_Cdeg                                          as temperature  (Brief = "Temperature in °C", Lower=-200);
538        P                                                               as pressure             (Brief = "Stream Pressure");
539       
540        x(NComp)                        as fraction                     (Brief = "Liquid Molar Fraction",Hidden=true);
541        y(NComp)                        as fraction                     (Brief = "Vapour Molar Fraction",Hidden=true);
542       
543
544EQUATIONS
545
546"Sum of Composition"
547        SumOfComposition = sum(MolarComposition);
548       
549"Stream Molar Composition"
550        Outlet.z = MolarComposition/sum(MolarComposition);
551
552
553switch ValidPhases
554       
555        case "Liquid-Only":
556
557"Vapour Fraction"
558        Outlet.v = 0;
559
560"Liquid Composition"
561        x = Outlet.z;
562
563"Vapour Composition"
564        y = Outlet.z;
565
566"Overall Enthalpy"
567        Outlet.h = PP.LiquidEnthalpy(Outlet.T, Outlet.P, x);
568
569
570        case "Vapour-Only":
571
572"Vapor Fraction"
573        Outlet.v = 1;
574
575"Liquid Composition"
576        x = Outlet.z;
577
578"Vapour Composition"
579        y = Outlet.z;
580
581"Overall Enthalpy"
582        Outlet.h = PP.VapourEnthalpy(Outlet.T, Outlet.P, y);
583
584
585        case "Vapour-Liquid":
586
587"Flash Calculation"
588        [Outlet.v, x, y] = PP.Flash(Outlet.T, Outlet.P, Outlet.z);
589
590"Overall Enthalpy"
591        Outlet.h = (1-Outlet.v)*PP.LiquidEnthalpy(Outlet.T, Outlet.P, x) + Outlet.v*PP.VapourEnthalpy(Outlet.T, Outlet.P, y);
592
593
594end
595
596"Temperature in °C"
597        T_Cdeg = Outlet.T - 273.15 * 'K';
598
599"Equate Flow"
600        Outlet.F = F;
601
602"Equate Pressures"
603        Outlet.P = P;
604
605"Equate Temperatures"
606        Outlet.T = T;
607
608end
609
610Model simple_source2
611
612ATTRIBUTES
613        Pallete = true;
614        Icon = "icon/Source2";
615        Brief = "Simple Material stream source";
616        Info = "
617        This model should be used for boundary streams.
618        Usually these streams are known and come from another process
619        units.
620
621        The user should specify:
622         * Total molar flow
623         * Temperature
624         * Pressure
625         * Molar composition
626";
627
628PARAMETERS
629        outer PP                                                as Plugin                       (Brief = "External Physical Properties", Type="PP");
630        outer NComp                             as Integer                      (Brief = "Number of chemical components", Lower = 1);
631                  M(NComp)                              as molweight    (Brief = "Component Mol Weight");
632                  ValidPhases                           as Switcher             (Brief = "Valid Phases for Flash Calculation", Valid = ["Vapour-Only", "Liquid-Only","Vapour-Liquid"], Default="Vapour-Liquid");
633       
634
635SET
636
637        M   = PP.MolecularWeight();
638
639VARIABLES
640
641        out Outlet                      as stream                       (Brief = "Outlet stream", PosX=1, PosY=0.5256, Symbol="_{out}",Protected=true);
642       
643        MolarComposition(NComp) as fraction                     (Brief = "Stream Molar Composition");
644        SumOfComposition as positive                    (Brief = "Sum of Stream Composition",Protected=true);
645        F                                                               as flow_mol             (Brief = "Stream Molar Flow Rate");
646        T                                                               as temperature  (Brief = "Stream Temperature");
647        T_Cdeg                                          as temperature  (Brief = "Temperature in °C", Lower=-200);
648        P                                                               as pressure             (Brief = "Stream Pressure");
649       
650        x(NComp)                        as fraction                     (Brief = "Liquid Molar Fraction",Hidden=true);
651        y(NComp)                        as fraction                     (Brief = "Vapour Molar Fraction",Hidden=true);
652       
653
654EQUATIONS
655
656"Sum of Composition"
657        SumOfComposition = sum(MolarComposition);
658       
659"Stream Molar Composition"
660        Outlet.z = MolarComposition/sum(MolarComposition);
661
662
663switch ValidPhases
664       
665        case "Liquid-Only":
666
667"Vapour Fraction"
668        Outlet.v = 0;
669
670"Liquid Composition"
671        x = Outlet.z;
672
673"Vapour Composition"
674        y = Outlet.z;
675
676"Overall Enthalpy"
677        Outlet.h = PP.LiquidEnthalpy(Outlet.T, Outlet.P, x);
678
679
680        case "Vapour-Only":
681
682"Vapor Fraction"
683        Outlet.v = 1;
684
685"Liquid Composition"
686        x = Outlet.z;
687
688"Vapour Composition"
689        y = Outlet.z;
690
691"Overall Enthalpy"
692        Outlet.h = PP.VapourEnthalpy(Outlet.T, Outlet.P, y);
693
694
695        case "Vapour-Liquid":
696
697"Flash Calculation"
698        [Outlet.v, x, y] = PP.Flash(Outlet.T, Outlet.P, Outlet.z);
699
700"Overall Enthalpy"
701        Outlet.h = (1-Outlet.v)*PP.LiquidEnthalpy(Outlet.T, Outlet.P, x) + Outlet.v*PP.VapourEnthalpy(Outlet.T, Outlet.P, y);
702
703
704end
705
706"Temperature in °C"
707        T_Cdeg = Outlet.T - 273.15 * 'K';
708
709"Equate Flow"
710        Outlet.F = F;
711
712"Equate Pressures"
713        Outlet.P = P;
714
715"Equate Temperatures"
716        Outlet.T = T;
717
718end
719
720Model sourceNoFlow
721
722ATTRIBUTES
723        Pallete = true;
724        Icon = "icon/SourceNoFlow";
725        Brief = "Simple Material stream source with no flow.";
726        Info = "
727        This model should be used for boundary streams.
728        Usually these streams are known and come from another process
729        units.";
730
731PARAMETERS
732        outer PP                                as Plugin                       (Brief = "External Physical Properties", Type="PP");
733        outer NComp             as Integer                      (Brief = "Number of chemical components", Lower = 1);
734
735VARIABLES
736
737        out Outlet                      as stream                       (Brief = "Outlet stream", PosX=1, PosY=0.5256, Symbol="_{out}",Protected=true);
738
739EQUATIONS
740
741"Stream Molar Composition"
742        Outlet.z = 1/NComp;
743
744"Stream Molar Enthalpy"
745        Outlet.h = 0 * 'J/mol';
746
747"Stream Temperature"
748        Outlet.T = 300 * 'K';
749
750"Stream Molar Flow"
751        Outlet.F = 0 * 'kmol/h';
752
753"Stream Pressure"
754        Outlet.P = 1 * 'atm';
755
756"Stream Vapour Fraction"
757        Outlet.v = 0;
758
759end
760
761Model work_source
762        ATTRIBUTES
763        Pallete = true;
764        Icon = "icon/work_source";
765        Brief = "Work stream source";
766
767        VARIABLES
768        out Work                as power(Brief = "Outlet work stream", PosX=1, PosY=0.46, Symbol="_{out}");
769
770end
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