source: branches/gui/eml/streams.mso @ 739

Last change on this file since 739 was 739, checked in by gerson bicca, 14 years ago

updates (changes in icons/models/samples)

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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 basic streams
17*----------------------------------------------------------------------
18* Author: Paula B. Staudt and Rafael de P. Soares
19* $Id: streams.mso 739 2009-02-27 22:18:32Z bicca $
20*---------------------------------------------------------------------*#
21
22using "types";
23
24Model stream
25        ATTRIBUTES
26        Pallete = false;
27        Brief = "General Material Stream";
28        Info =
29        "This is the basic building block for the EML models.
30        Every model should have input and output streams derived
31        from this model.";
32       
33        PARAMETERS
34        outer NComp as Integer (Brief = "Number of chemical components", Lower = 1);
35
36        VARIABLES
37        F as flow_mol                   (Brief = "Stream Molar Flow Rate");
38        T as temperature                (Brief = "Stream Temperature");
39        P as pressure                   (Brief = "Stream Pressure");
40        h as enth_mol                   (Brief = "Stream Enthalpy");
41        v as fraction                   (Brief = "Vapourization fraction");
42        z(NComp) as fraction    (Brief = "Stream Molar Fraction");
43end
44
45Model liquid_stream as stream
46        ATTRIBUTES
47        Pallete = false;
48        Brief = "Liquid Material Stream";
49        Info =
50        "Model for liquid material streams.
51        This model should be used only when the phase of the stream
52        is known ''a priori''.";
53
54        PARAMETERS
55        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
56       
57        EQUATIONS
58        "Liquid Enthalpy"
59        h = PP.LiquidEnthalpy(T, P, z);
60        "Liquid stream"
61        v = 0;
62end
63
64Model vapour_stream as stream
65        ATTRIBUTES
66        Pallete = false;
67        Brief = "Vapour Material Stream";
68        Info =
69        "Model for vapour material streams.
70        This model should be used only when the phase of the stream
71        is known ''a priori''.";
72
73        PARAMETERS
74        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
75       
76        EQUATIONS
77        "Vapour Enthalpy"
78        h = PP.VapourEnthalpy(T, P, z);
79        "Vapour stream"
80        v = 1;
81end
82
83Model streamPH as stream
84        ATTRIBUTES
85        Brief = "Stream with built-in flash calculation";
86        Info = "
87        This model should be used when the vaporization fraction
88        is unknown.
89       
90        The built-in flash calculation will determine the stream
91        state as a function of the overall composition '''z''', the
92        pressure '''P''' and the enthalpy '''h'''.
93       
94        Additionally, the liquid composition '''x''' and the vapor
95        composition '''y''' are calculated.     
96        ";
97        Pallete = false;
98       
99        PARAMETERS
100        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
101       
102        VARIABLES
103        x(NComp) as fraction    (Brief = "Liquid Molar Fraction",Hidden=true);
104        y(NComp) as fraction    (Brief = "Vapour Molar Fraction",Hidden=true);
105
106        EQUATIONS
107        "Flash Calculation"
108        [v, x, y] = PP.FlashPH(P, h, z);
109       
110        "Enthalpy"
111        h = (1-v)*PP.LiquidEnthalpy(T, P, x) + v*PP.VapourEnthalpy(T, P, y);
112       
113end
114
115Model streamPHS as streamPH
116        ATTRIBUTES
117        Brief = "Stream with built-in flash calculation";
118        Info = "
119        This model should be used when the vaporization fraction
120        is unknown.
121       
122        The built-in flash calculation will determine the stream
123        state as a function of the overall composition '''z''', the
124        pressure '''P''' and the enthalpy '''h'''.
125       
126        Additionally, the liquid composition '''x''', the vapor
127        composition '''y''' and the stream entropy are calculated.     
128        ";
129        Pallete = false;
130       
131PARAMETERS
132        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
133       
134VARIABLES
135        s as entr_mol   (Brief = "Stream Entropy");
136
137EQUATIONS
138
139"Entropy"
140        s = (1-v)*PP.LiquidEntropy(T, P, x) +   v*PP.VapourEntropy(T, P, y);
141       
142end
143
144Model sink
145        ATTRIBUTES
146        Pallete = true;
147        Icon = "icon/Sink";
148        Brief = "Material stream sink";
149        Info = "
150        This model should be used for boundary streams when additional
151        information about the stream is desired.
152
153        Some of the additional informations calculated by this models are:
154         * Mass density
155         * Mass flow
156         * Mass compostions
157         * Specific volume
158         * Vapour fraction
159         * Volumetric flow
160         * Liquid and Vapour compositions
161        ";
162
163        PARAMETERS
164        outer PP                        as Plugin               (Brief = "External Physical Properties", Type="PP");
165        outer NComp             as Integer              (Brief = "Number of chemical components", Lower = 1);
166                  M(NComp)      as molweight    (Brief = "Component Mol Weight");
167       
168        SET
169
170        M   = PP.MolecularWeight();
171       
172        VARIABLES
173        in Inlet                as stream               (Brief = "Inlet Stream", PosX=0, PosY=0.5308, Protected=true,Symbol="_{in}");
174        v                               as fraction             (Brief = "Vapourization fraction",Hidden=true);
175        x(NComp)                as fraction             (Brief = "Liquid Molar Fraction",Hidden=true);
176        y(NComp)                as fraction             (Brief = "Vapour Molar Fraction",Hidden=true);
177        zmass(NComp)    as fraction             (Brief = "Mass Fraction");
178        Mw                              as molweight    (Brief = "Average Mol Weight");
179        vm                              as volume_mol   (Brief = "Molar Volume");       
180        rho                             as dens_mass    (Brief = "Stream Mass Density");
181        rhom                    as dens_mol             (Brief = "Stream Molar Density");
182        Fw                              as flow_mass    (Brief = "Stream Mass Flow");
183        Fvol            as flow_vol     (Brief = "Volumetric Flow");
184        T_Cdeg                  as temperature  (Brief = "Temperature in °C", Lower=-200);
185
186        EQUATIONS
187        "Flash Calculation"
188        [v, x, y] = PP.FlashPH(Inlet.P, Inlet.h, Inlet.z);
189       
190        "Average Molecular Weight"
191        Mw = sum(M*Inlet.z);
192
193        "Molar Density"
194                rhom * vm = 1;
195               
196        "Mass or Molar Density"
197        rhom * Mw = rho;
198
199        "Flow Mass"
200        Fw      =  Mw*Inlet.F;
201
202        "Molar Volume"
203        vm = (1-v)*PP.LiquidVolume(Inlet.T, Inlet.P, x) + v*PP.VapourVolume(Inlet.T,Inlet.P,y);
204       
205        "Volumetric Flow"
206        Fvol = Inlet.F*vm ;
207       
208        "Mass Fraction"
209        zmass = M*Inlet.z / Mw;
210       
211        "Temperature in °C"
212        T_Cdeg = Inlet.T - 273.15 * 'K';
213
214end
215
216Model simple_sink
217        ATTRIBUTES
218        Pallete = true;
219        Icon = "icon/Sink";
220        Brief = "Simple material stream sink";
221        Info = "
222        This model should be used for boundary streams when no additional
223        information about the stream is desired.
224        ";
225       
226        VARIABLES
227        in Inlet                as stream       (Brief = "Inlet Stream", PosX=0, PosY=0.5308, Protected=true,Symbol="_{in}");
228end
229
230Model energy_source
231        ATTRIBUTES
232        Pallete = true;
233        Icon = "icon/energy_source";
234        Brief = "Energy stream source";
235
236        VARIABLES
237        out OutletQ             as power(Brief = "Outlet energy stream", PosX=1, PosY=0.40, Symbol="_{out}");
238
239end
240
241Model work_source
242        ATTRIBUTES
243        Pallete = true;
244        Icon = "icon/work_source";
245        Brief = "Work stream source";
246
247        VARIABLES
248        out Work                as power(Brief = "Outlet work stream", PosX=1, PosY=0.46, Symbol="_{out}");
249
250end
251
252Model info_stream
253        ATTRIBUTES
254        Pallete = true;
255        Icon = "icon/Info_Stream";
256        Brief = "Material stream information";
257        Info = "
258        This model should be used for middle streams when additional
259        information about the stream is desired.
260
261        Some of the additional informations calculated by this models are:
262         * Mass density
263         * Mass flow
264         * Mass compostions
265         * Specific volume
266         * Vapour fraction
267         * Volumetric flow
268         * Liquid and Vapour compositions
269         * Viscosity
270         * Heat Capacity
271         * Thermal Conductivity
272         * Temperature in Celsius Degrees
273        ";
274
275PARAMETERS
276        outer PP                        as Plugin                       (Brief = "External Physical Properties", Type="PP");
277        outer NComp     as Integer                      (Brief = "Number of chemical components", Lower = 1);
278                  M(NComp)      as molweight    (Brief = "Component Mol Weight");
279       
280SET
281
282        M   = PP.MolecularWeight();
283       
284VARIABLES
285
286        in      Inlet           as stream               (Brief = "Inlet Stream", PosX=0, PosY=0.50, Protected=true , Symbol="_{in}");
287        out     Outlet          as stream               (Brief = "Outlet Stream", PosX=1, PosY=0.50, Protected=true , Symbol="_{out}");
288       
289        v                                               as fraction                     (Brief = "Vapourization fraction",Hidden=true);
290        x(NComp)                        as fraction                     (Brief = "Liquid Molar Fraction",Hidden=true);
291        y(NComp)                        as fraction                     (Brief = "Vapour Molar Fraction",Hidden=true);
292       
293        F(NComp)        as flow_mol             (Brief = "Component Molar Flow",Protected=true);
294        FwTotal         as flow_mass            (Brief = "Total Mass Flow",Protected=true);
295        Fw(NComp)               as flow_mass            (Brief = "Component Mass Flow",Protected=true);
296        FvolTotal           as flow_vol         (Brief = "Total Volumetric Flow",Protected=true);
297        T_Cdeg                          as temperature          (Brief = "Temperature in °C", Lower=-200,Protected=true);
298
299        Mu                                      as viscosity            (Brief="Stream Viscosity",Lower=0.0001, Symbol = "\mu",Protected=true);
300        Cp                                      as cp_mol                       (Brief="Stream Molar Heat Capacity", Upper=1e10,Protected=true);       
301        K                                               as conductivity         (Brief="Stream Thermal Conductivity", Default=1.0, Lower=1e-5, Upper=500,Protected=true);
302        Mw                                      as molweight            (Brief = "Average Mol Weight",Protected=true);
303        vm                                      as volume_mol   (Brief = "Molar Volume",Protected=true);       
304        rho                                     as dens_mass            (Brief = "Stream Mass Density",Protected=true);
305        rhom                                    as dens_mol             (Brief = "Stream Molar Density",Protected=true);
306        s                                               as entr_mol             (Brief = "Stream Entropy",Protected=true);
307        zmass(NComp)    as fraction                     (Brief = "Mass Fraction",Protected=true);
308       
309EQUATIONS
310
311"Flash Calculation"
312        [v, x, y] = PP.FlashPH(Inlet.P, Inlet.h, Inlet.z);
313       
314"Average Molecular Weight"
315        Mw = sum(M*Inlet.z);
316
317"Mass Density"
318        rho * ((1-v)/PP.LiquidDensity(Inlet.T,Inlet.P,x) + v/PP.VapourDensity(Inlet.T,Inlet.P,y)) = 1;
319       
320"Mass or Molar Density"
321        rhom * Mw = rho;
322
323"Total Flow Mass"
324        FwTotal =  Mw*Inlet.F;
325
326"Component Flow Mass"
327        Fw      =  FwTotal*zmass;
328
329"Molar Volume"
330        vm = (1-v)*PP.LiquidVolume(Inlet.T, Inlet.P, x) + v*PP.VapourVolume(Inlet.T,Inlet.P,y);
331       
332"Total Volumetric Flow"
333        FvolTotal = Inlet.F*vm ;
334       
335"Mass Fraction"
336        zmass = M*Inlet.z / Mw;
337
338"Stream Heat Capacity"
339        Cp      =       (1-v)*PP.LiquidCp(Inlet.T, Inlet.P, x) + v*PP.VapourCp(Inlet.T,Inlet.P,y);
340
341"Stream Viscosity"
342        Mu      =       (1-v)*PP.LiquidViscosity(Inlet.T, Inlet.P, x) + v*PP.VapourViscosity(Inlet.T,Inlet.P,y);
343
344"Stream ThermalConductivity"
345        K       =       (1-v)*PP.LiquidThermalConductivity(Inlet.T, Inlet.P, x) + v*PP.VapourThermalConductivity(Inlet.T,Inlet.P,y);
346
347"Stream Overall Entropy"
348        s = (1-v)*PP.LiquidEntropy(Inlet.T, Inlet.P, x) + v*PP.VapourEntropy(Inlet.T, Inlet.P, y);
349       
350"Temperature in °C"
351        T_Cdeg = Inlet.T - 273.15 * 'K';
352
353"Outlet Flow"
354        Outlet.F = Inlet.F;
355
356"Component Molar Flow"
357        F = Inlet.F*Inlet.z;
358
359"Outlet Temperature"
360        Outlet.T = Inlet.T;
361
362"Outlet Pressure"
363        Outlet.P = Inlet.P;
364
365"Outlet Vapour Fraction"
366        Outlet.v = Inlet.v;
367
368"Outlet Enthalpy"
369        Outlet.h = Inlet.h;
370
371"Outlet Composition"
372        Outlet.z= Inlet.z;
373
374end
375
376Model source
377
378ATTRIBUTES
379        Pallete = true;
380        Icon = "icon/Source";
381        Brief = "Material stream source";
382        Info = "
383        This model should be used for boundary streams.
384        Usually these streams are known and come from another process
385        units.
386
387        The user should specify:
388         * Total molar (mass or volumetric) flow
389         * Temperature
390         * Pressure
391         * Molar or mass composition
392       
393        No matter the specification set, the model will calculate some
394        additional properties:
395         * Mass density
396         * Mass flow
397         * Mass compostions
398         * Specific volume
399         * Vapour fraction
400         * Volumetric flow
401         * Liquid and Vapour compositions
402        ";
403
404PARAMETERS
405        outer PP                                                as Plugin                       (Brief = "External Physical Properties", Type="PP");
406        outer NComp                             as Integer                      (Brief = "Number of chemical components", Lower = 1);
407                  M(NComp)                              as molweight    (Brief = "Component Mol Weight");
408                  CompositionBasis              as Switcher             (Brief = "Molar or Mass Composition", Valid = ["Molar", "Mass"], Default="Molar");
409                  ValidPhases                           as Switcher             (Brief = "Valid Phases for Flash Calculation", Valid = ["Vapour-Only", "Liquid-Only","Vapour-Liquid"], Default="Vapour-Liquid");
410       
411
412SET
413
414        M   = PP.MolecularWeight();
415
416VARIABLES
417
418        out Outlet                      as stream                       (Brief = "Outlet stream", PosX=1, PosY=0.5256, Symbol="_{out}",Protected=true);
419       
420        Composition(NComp) as fraction                  (Brief = "Stream Composition");
421        SumOfComposition as positive                    (Brief = "Sum of Stream Composition",Protected=true);
422        F                                                               as flow_mol             (Brief = "Stream Molar Flow Rate");
423        Fw                                                      as flow_mass            (Brief = "Stream Mass Flow");
424        Fvol                                    as flow_vol        (Brief = "Volumetric Flow");
425        T                                                               as temperature  (Brief = "Stream Temperature");
426        T_Cdeg                                          as temperature  (Brief = "Temperature in °C", Lower=-200);
427        P                                                               as pressure             (Brief = "Stream Pressure");
428       
429        x(NComp)                        as fraction                     (Brief = "Liquid Molar Fraction",Hidden=true);
430        y(NComp)                        as fraction                     (Brief = "Vapour Molar Fraction",Hidden=true);
431       
432        Mw                                              as molweight                    (Brief = "Average Mol Weight",Protected=true);
433        vm                                              as volume_mol           (Brief = "Molar Volume",Protected=true);       
434        rho                                             as dens_mass                    (Brief = "Stream Mass Density",Protected=true);
435        rhom                                            as dens_mol                     (Brief = "Stream Molar Density",Protected=true);
436       
437        zmass(NComp)            as fraction                             (Brief = "Mass Fraction",Protected=true);
438       
439        EQUATIONS
440
441switch CompositionBasis
442
443        case "Molar":
444"Stream Molar Composition"
445        Outlet.z = Composition/sum(Composition);
446
447"Stream Mass Composition"
448        zmass = M*Outlet.z / Mw;
449
450        case "Mass":
451"Stream Mass Composition"
452        zmass = Composition/sum(Composition);
453
454"Stream Molar Composition"
455        Outlet.z*sum(zmass/M) = zmass/M;
456
457end
458
459switch ValidPhases
460       
461        case "Liquid-Only":
462
463"Vapour Fraction"
464        Outlet.v = 0;
465
466"Liquid Composition"
467        x = Outlet.z;
468
469"Vapour Composition"
470        y = Outlet.z;
471
472"Overall Enthalpy"
473        Outlet.h = PP.LiquidEnthalpy(Outlet.T, Outlet.P, x);
474
475"Molar Volume"
476        vm = PP.LiquidVolume(Outlet.T, Outlet.P, x);
477
478        case "Vapour-Only":
479
480"Vapor Fraction"
481        Outlet.v = 1;
482
483"Liquid Composition"
484        x = Outlet.z;
485
486"Vapour Composition"
487        y = Outlet.z;
488
489"Overall Enthalpy"
490        Outlet.h = PP.VapourEnthalpy(Outlet.T, Outlet.P, y);
491
492"Molar Volume"
493        vm = PP.VapourVolume(Outlet.T, Outlet.P, y);
494
495
496        case "Vapour-Liquid":
497
498"Flash Calculation"
499        [Outlet.v, x, y] = PP.Flash(Outlet.T, Outlet.P, Outlet.z);
500
501"Overall Enthalpy"
502        Outlet.h = (1-Outlet.v)*PP.LiquidEnthalpy(Outlet.T, Outlet.P, x) + Outlet.v*PP.VapourEnthalpy(Outlet.T, Outlet.P, y);
503
504"Molar Volume"
505        vm = (1-Outlet.v)*PP.LiquidVolume(Outlet.T, Outlet.P, x) + Outlet.v*PP.VapourVolume(Outlet.T,Outlet.P,y);
506
507end
508
509"Sum of Composition"
510        SumOfComposition = sum(Composition);
511
512"Molar Density"
513        rhom * vm = 1;
514
515"Average Molecular Weight"
516        Mw = sum(M*Outlet.z);
517
518"Mass or Molar Density"
519        rhom * Mw = rho;
520
521"Flow Mass"
522        Fw      =  Mw*Outlet.F;
523
524"Volumetric Flow"
525        Fvol = Outlet.F*vm ;
526       
527"Temperature in °C"
528        T_Cdeg = Outlet.T - 273.15 * 'K';
529
530"Equate Flow"
531        Outlet.F = F;
532
533"Equate Pressures"
534        Outlet.P = P;
535
536"Equate Temperatures"
537        Outlet.T = T;
538
539end
540
541Model simple_source
542
543ATTRIBUTES
544        Pallete = true;
545        Icon = "icon/Source";
546        Brief = "Simple Material stream source";
547        Info = "
548        This model should be used for boundary streams.
549        Usually these streams are known and come from another process
550        units.
551
552        The user should specify:
553         * Total molar flow
554         * Temperature
555         * Pressure
556         * Molar composition
557";
558
559PARAMETERS
560        outer PP                                                as Plugin                       (Brief = "External Physical Properties", Type="PP");
561        outer NComp                             as Integer                      (Brief = "Number of chemical components", Lower = 1);
562                  M(NComp)                              as molweight    (Brief = "Component Mol Weight");
563                  ValidPhases                           as Switcher             (Brief = "Valid Phases for Flash Calculation", Valid = ["Vapour-Only", "Liquid-Only","Vapour-Liquid"], Default="Vapour-Liquid");
564       
565
566SET
567
568        M   = PP.MolecularWeight();
569
570VARIABLES
571
572        out Outlet                      as stream                       (Brief = "Outlet stream", PosX=1, PosY=0.5256, Symbol="_{out}",Protected=true);
573       
574        MolarComposition(NComp) as fraction                     (Brief = "Stream Molar Composition");
575        SumOfComposition as positive                    (Brief = "Sum of Stream Composition",Protected=true);
576        F                                                               as flow_mol             (Brief = "Stream Molar Flow Rate");
577        T                                                               as temperature  (Brief = "Stream Temperature");
578        T_Cdeg                                          as temperature  (Brief = "Temperature in °C", Lower=-200);
579        P                                                               as pressure             (Brief = "Stream Pressure");
580       
581        x(NComp)                        as fraction                     (Brief = "Liquid Molar Fraction",Hidden=true);
582        y(NComp)                        as fraction                     (Brief = "Vapour Molar Fraction",Hidden=true);
583       
584
585EQUATIONS
586
587"Sum of Composition"
588        SumOfComposition = sum(MolarComposition);
589       
590"Stream Molar Composition"
591        Outlet.z = MolarComposition/sum(MolarComposition);
592
593
594switch ValidPhases
595       
596        case "Liquid-Only":
597
598"Vapour Fraction"
599        Outlet.v = 0;
600
601"Liquid Composition"
602        x = Outlet.z;
603
604"Vapour Composition"
605        y = Outlet.z;
606
607"Overall Enthalpy"
608        Outlet.h = PP.LiquidEnthalpy(Outlet.T, Outlet.P, x);
609
610
611        case "Vapour-Only":
612
613"Vapor Fraction"
614        Outlet.v = 1;
615
616"Liquid Composition"
617        x = Outlet.z;
618
619"Vapour Composition"
620        y = Outlet.z;
621
622"Overall Enthalpy"
623        Outlet.h = PP.VapourEnthalpy(Outlet.T, Outlet.P, y);
624
625
626        case "Vapour-Liquid":
627
628"Flash Calculation"
629        [Outlet.v, x, y] = PP.Flash(Outlet.T, Outlet.P, Outlet.z);
630
631"Overall Enthalpy"
632        Outlet.h = (1-Outlet.v)*PP.LiquidEnthalpy(Outlet.T, Outlet.P, x) + Outlet.v*PP.VapourEnthalpy(Outlet.T, Outlet.P, y);
633
634
635end
636
637"Temperature in °C"
638        T_Cdeg = Outlet.T - 273.15 * 'K';
639
640"Equate Flow"
641        Outlet.F = F;
642
643"Equate Pressures"
644        Outlet.P = P;
645
646"Equate Temperatures"
647        Outlet.T = T;
648
649end
650
651Model sourceNoFlow
652
653ATTRIBUTES
654        Pallete = true;
655        Icon = "icon/SourceNoFlow";
656        Brief = "Simple Material stream source with no flow.";
657        Info = "
658        This model should be used for boundary streams.
659        Usually these streams are known and come from another process
660        units.";
661
662PARAMETERS
663        outer PP                                as Plugin                       (Brief = "External Physical Properties", Type="PP");
664        outer NComp             as Integer                      (Brief = "Number of chemical components", Lower = 1);
665
666VARIABLES
667
668        out Outlet                      as stream                       (Brief = "Outlet stream", PosX=1, PosY=0.5256, Symbol="_{out}",Protected=true);
669
670EQUATIONS
671
672"Stream Molar Composition"
673        Outlet.z = 1/NComp;
674
675"Stream Molar Enthalpy"
676        Outlet.h = 0 * 'J/mol';
677
678"Stream Temperature"
679        Outlet.T = 300 * 'K';
680
681"Stream Molar Flow"
682        Outlet.F = 0 * 'kmol/h';
683
684"Stream Pressure"
685        Outlet.P = 1 * 'atm';
686
687"Stream Vapour Fraction"
688        Outlet.v = 0;
689
690end
691
692Model sinkNoFlow
693        ATTRIBUTES
694        Pallete = true;
695        Icon = "icon/SinkNoFlow";
696        Brief = "Simple material stream sink";
697        Info = "
698        This model should be used for seal an outlet material stream port.
699        ";
700       
701        VARIABLES
702        in Inlet                as stream       (Brief = "Inlet Stream", PosX=0, PosY=0.5308, Protected=true,Symbol="_{in}");
703
704EQUATIONS
705"Stream Molar Flow"
706        Inlet.F = 0 * 'kmol/h';
707       
708end
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