Context Navigation

column.mso @ 992

Last change on this file since 992 was 910, checked in by Argimiro Resende Secchi, 13 years ago
Checking new EML.
File size: 105.0 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	* File containg models of columns: distillation, stripping, absorbers
17	* rectifier, ....
18	*
19	* The default nomenclature is:
20	* Type_Column_reboilertype_condensertyper
21	*
22	* where:
23	* Type = refluxed or reboiled or section
24	* Column = Stripping, Absorption, Rectifier, Distillation
25	* Reboiler type (if exists) = kettle or thermosyphon
26	* Condenser type (if exists) = with subccoling or without subcooling
27	*
28	*-----------------------------------------------------------------------
29	* Author: Paula B. Staudt
30	* $Id: column.mso 511 2008-05-12 17:25:33Z paula $
31	---------------------------------------------------------------------#
32
33	using "tray";
34	using "reboiler";
35	using "condenser";
36	using "mixers_splitters/splitter";
37	using "pressure_changers/pump";
38
39	Model ControlSection
40
41	ATTRIBUTES
42	Pallete = false;
43	Brief = "Control variables for column section.";
44
45	PARAMETERS
46	outer NComp as Integer (Brief="Number of components");
47
48	Tindicator_TrayNumber as Integer (Brief="Temperature Indicator in the tray");
49	Pindicator_TrayNumber as Integer (Brief="Pressure Indicator in the tray");
50	zindicator_TrayNumber as Integer (Brief="Composition Indicator in the tray");
51	zindicator_Component as Integer (Brief="Component to indicate");
52
53	end
54
55	Model InitializeSection
56
57	ATTRIBUTES
58	Pallete = false;
59	Brief = "Initial conditions for column section.";
60
61	PARAMETERS
62	outer NComp as Integer (Brief="Number of components");
63
64	TopTemperature as temperature (Brief = "Tray Temperature at Column Top", Default = 300);
65	BottomTemperature as temperature (Brief = "Tray Temperature at Column Bottom", Default = 330);
66	LevelFraction as fraction (Brief = "Tray Level Fraction", Default = 0.5);
67
68	TopComposition(NComp) as fraction (Brief = "Component Molar Fraction at Column Top", Default = 0.30);
69	BottomComposition(NComp) as fraction (Brief = "Component Molar Fraction at Column Bottom", Default = 0.30);
70
71	end
72
73	Model InitializeStage
74
75	ATTRIBUTES
76	Pallete = false;
77	Brief = "Initial conditions for Packed column section.";
78
79	PARAMETERS
80	outer NComp as Integer (Brief="Number of components");
81
82	TopStageTemperature as temperature (Brief = "Tray Temperature at Column Top", Default = 300);
83	BottomStageTemperature as temperature (Brief = "Tray Temperature at Column Bottom", Default = 300);
84
85	TopStageComposition(NComp) as fraction (Brief = "Component Molar Fraction at Top");
86	BottomStageComposition(NComp) as fraction (Brief = "Component Molar Fraction at Bottom");
87	ColumnHoldup as positive (Brief = "Column holdup", Default=0.1);
88
89	end
90
91
92	Model SectionColumnBasic
93
94	ATTRIBUTES
95	Pallete = false;
96	Brief = "Model of a basic column section.";
97	Info =
98	"Model of a basic column section containing a vetor of TRAYS numbered from the top-down.";
99
100	PARAMETERS
101	outer PP as Plugin (Brief="External Physical Properties", Type="PP");
102	outer NComp as Integer (Brief="Number of components");
103
104	NumberOfFeeds as Integer (Brief="Number of Feed Trays",Default=3,Protected=true);
105	FeedTrayLocation(NumberOfFeeds) as Integer (Brief="Feed tray Location",Default=2);
106	NumberOfTrays as Integer (Brief="Number of trays", Default=8);
107	LiqSideTrayIndex(NumberOfTrays) as Integer (Brief="Liquid Side Tray Index", Default=0,Hidden=true);
108	VapSideTrayIndex(NumberOfTrays) as Integer (Brief="Vapour Side Tray Index", Default=0,Hidden=true);
109
110	LiquidSideStreamLocation as Integer (Brief="Liquid Side Stream Location", Default=2);
111	VapourSideStreamLocation as Integer (Brief="Vapour Side Stream Location", Default=2);
112
113	VapourFlowModel as Switcher (Valid = ["Reepmeyer", "Feehery_Fv", "Roffel_Fv", "Klingberg", "Wang_Fv", "Elgue"], Default = "Reepmeyer");
114	LiquidFlowModel as Switcher (Valid = ["Francis", "Wang_Fl", "Olsen", "Feehery_Fl", "Roffel_Fl"], Default = "Francis");
115
116	TrayDiameter as length (Brief="Tray Diameter",Default=1.600);
117	TraySpacing as length (Brief="Tray Spacing",Default=0.600);
118	Fraction_HoleArea as fraction (Brief="Fraction of the active area that is occupied by the holes with respect to the total tray area",Default=0.10);
119	Fraction_DowncomerArea as fraction (Brief="Fraction of the downcomer area with respect to the total tray area",Default=0.20);
120	WeirLength as length (Brief="Weir length", Default = 1);
121	WeirHeight as length (Brief="Weir height", Default= 0.05);
122	TrayLiquidPasses as positive (Brief="Number of liquid passes in the tray", Lower = 1,Default=1);
123	HeatSupply as heat_rate (Brief="Rate of heat supply",Default = 0);
124	AerationFraction as Real (Brief="Aeration fraction", Default = 1);
125	DryPdropCoeff as Real (Brief="Dry pressure drop coefficient", Default= 0.60);
126	MurphreeEff as Real (Brief="Murphree efficiency for All Trays", Default= 1);
127
128	VARIABLES
129
130	INITIALIZATION as InitializeSection (Brief="Column Model Initialization");
131	CONTROL as ControlSection (Brief="Column Model Control");
132
133	out TCI as control_signal (Brief="Temperature Indicator", Protected = true, PosX=1, PosY=0.73);
134	out PCI as control_signal (Brief="Pressure Indicator", Protected = true, PosX=0, PosY=0.24);
135
136	in LiquidInlet as stream (Brief="Liquid Inlet in the section", PosX=0.70, PosY=0);
137	out VapourOutlet as vapour_stream (Brief="Vapour Outlet in the section", PosX=0.30, PosY=0);
138
139	out VapourDrawOff as vapour_stream (Brief="Vapour Draw Off Port in the section", PosX=1, PosY=0.35,Protected = true);
140	out LiquidDrawOff as liquid_stream (Brief="Liquid Draw Off Port in the section", PosX=1, PosY=0.65,Protected = true);
141
142	TRAYS(NumberOfTrays) as tray (Brief="Number of trays in the Column Section",Protected=true);
143	VapourDrawOffFlow as flow_mol (Brief="Vapour Draw Off Stream Molar Flow Rate");
144	LiquidDrawOffFlow as flow_mol (Brief="Vapour Draw Off Stream Molar Flow Rate");
145
146	in VapourInlet as stream (Brief="Vapour Inlet in the section", PosX=0.30, PosY=1);
147	out LiquidOutlet as liquid_stream (Brief="Liquid Outlet in the section", PosX=0.70, PosY=1);
148
149	LiquidConnector as stream (Brief="Liquid connection in the middle TRAYS", PosX=0.75, PosY=1,Hidden=true);
150	VapourConnector as stream (Brief="Vapour connection in the middle TRAYS", PosX=0.55, PosY=0,Hidden=true);
151
152	SET
153	VapSideTrayIndex(VapourSideStreamLocation) =1;
154	LiqSideTrayIndex(LiquidSideStreamLocation) =1;
155
156	TRAYS.TrayDiameter_ = TrayDiameter;
157	TRAYS.TraySpacing_ = TraySpacing;
158	TRAYS.Fraction_HoleArea_ = Fraction_HoleArea;
159	TRAYS.Fraction_DowncomerArea_ = Fraction_DowncomerArea;
160	TRAYS.WeirLength_ = WeirLength;
161	TRAYS.WeirHeight_ = WeirHeight;
162	TRAYS.TrayLiquidPasses_ = TrayLiquidPasses;
163	TRAYS.HeatSupply_ = HeatSupply;
164	TRAYS.AerationFraction_ = AerationFraction;
165	TRAYS.DryPdropCoeff_ = DryPdropCoeff;
166	TRAYS.MurphreeEff_ = MurphreeEff;
167
168	CONNECTIONS
169	TRAYS([2:NumberOfTrays]).OutletVapour to TRAYS([1:NumberOfTrays-1]).InletVapour;
170	TRAYS([1:NumberOfTrays-1]).OutletLiquid to TRAYS([2:NumberOfTrays]).InletLiquid;
171
172	LiquidConnector to TRAYS(1).InletLiquid;
173	VapourConnector to TRAYS(NumberOfTrays).InletVapour;
174
175	INITIAL
176
177	for i in 1:NumberOfTrays do
178
179	"The initial temperature of the TRAYS"
180	TRAYS(i).OutletLiquid.T = INITIALIZATION.TopTemperature+(INITIALIZATION.BottomTemperature-INITIALIZATION.TopTemperature)*((i-1)/(NumberOfTrays-1));
181
182	"The initial Level of the TRAYS"
183	TRAYS(i).Level = INITIALIZATION.LevelFraction*WeirHeight;
184	end
185
186	for i in 1:NComp-1 do
187
188	for j in 1:NumberOfTrays do
189
190	"The initial composition of the TRAYS - Normalized"
191	TRAYS(j).OutletLiquid.z(i) = INITIALIZATION.TopComposition(i)/sum(INITIALIZATION.TopComposition) +(INITIALIZATION.BottomComposition(i)/sum(INITIALIZATION.BottomComposition)-INITIALIZATION.TopComposition(i)/sum(INITIALIZATION.TopComposition) )*((j-1)/(NumberOfTrays-1));
192	end
193
194	end
195
196	EQUATIONS
197
198	"Tray Temperature Indicator"
199	#TCI*'K' = TRAYS(min([NumberOfTrays, CONTROL.Tindicator_TrayNumber])).OutletVapour.T;
200	TCI*'K' = TRAYS(CONTROL.Tindicator_TrayNumber).OutletVapour.T;
201
202	"Tray Pressure Indicator"
203	#PCI*'atm' = TRAYS(min([NumberOfTrays, CONTROL.Pindicator_TrayNumber])).OutletVapour.P;
204	PCI*'atm' = TRAYS(CONTROL.Pindicator_TrayNumber).OutletVapour.P;
205
206	switch LiquidFlowModel
207
208	case "Francis":
209	TRAYS.LFlowModel = 1;
210	case "Wang_Fl":
211	TRAYS.LFlowModel = 2;
212
213	case "Olsen":
214	TRAYS.LFlowModel = 3;
215
216	case "Feehery_Fl":
217	TRAYS.LFlowModel = 4;
218
219	case "Roffel_Fl":
220	TRAYS.LFlowModel = 5;
221
222	end
223
224	switch VapourFlowModel
225
226	case "Reepmeyer":
227	TRAYS.VFlowModel = 1;
228
229	case "Feehery_Fv":
230	TRAYS.VFlowModel = 2;
231
232	case "Roffel_Fv":
233	TRAYS.VFlowModel = 3;
234
235	case "Klingberg":
236	TRAYS.VFlowModel = 4;
237
238	case "Wang_Fv":
239	TRAYS.VFlowModel = 5;
240
241	case "Elgue":
242	TRAYS.VFlowModel = 6;
243
244	end
245
246	"Liquid Inlet Flow"
247	LiquidConnector.F = LiquidInlet.F;
248
249	"Liquid Inlet Temperature"
250	LiquidConnector.T = LiquidInlet.T;
251
252	"Liquid Inlet Pressure"
253	LiquidConnector.P = LiquidInlet.P;
254
255	"Liquid Inlet Composition"
256	LiquidConnector.z = LiquidInlet.z;
257
258	"Liquid Inlet Vapour Fraction"
259	LiquidConnector.v = LiquidInlet.v;
260
261	"Liquid Inlet Enthalpy"
262	LiquidConnector.h = LiquidInlet.h;
263
264	"Vapour Inlet Flow"
265	VapourConnector.F = VapourInlet.F;
266
267	"Vapour Inlet Temperature"
268	VapourConnector.T = VapourInlet.T;
269
270	"Vapour Inlet Pressure"
271	VapourConnector.P = VapourInlet.P;
272
273	"Vapour Inlet Composition"
274	VapourConnector.z = VapourInlet.z;
275
276	"Vapour Inlet Vapour Fraction"
277	VapourConnector.v = VapourInlet.v;
278
279	"Vapour Inlet Enthalpy"
280	VapourConnector.h = VapourInlet.h;
281
282	"Liquid Outlet Flow"
283	LiquidOutlet.F = TRAYS(NumberOfTrays).OutletLiquid.F;
284
285	"Liquid Outlet Temperature"
286	LiquidOutlet.T = TRAYS(NumberOfTrays).OutletLiquid.T;
287
288	"Liquid Outlet Pressure"
289	LiquidOutlet.P = TRAYS(NumberOfTrays).OutletLiquid.P;
290
291	"Liquid Outlet Composition"
292	LiquidOutlet.z = TRAYS(NumberOfTrays).OutletLiquid.z;
293
294	"Vapour Outlet Flow"
295	VapourOutlet.F = TRAYS(1).OutletVapour.F;
296
297	"Vapour Outlet Temperature"
298	VapourOutlet.T = TRAYS(1).OutletVapour.T;
299
300	"Vapour Outlet Pressure"
301	VapourOutlet.P = TRAYS(1).OutletVapour.P;
302
303	"Vapour Outlet Composition"
304	VapourOutlet.z = TRAYS(1).OutletVapour.z;
305
306	"Vapour Draw Off Stream - Flow"
307	VapourDrawOff.F*VapSideTrayIndex= TRAYS.VapourSideStream.F;
308
309	"Vapour Draw Off Stream - Temperature"
310	VapourDrawOff.T = TRAYS(VapourSideStreamLocation).VapourSideStream.T;
311
312	"Vapour Draw Off Stream - Pressure"
313	VapourDrawOff.P = TRAYS(VapourSideStreamLocation).VapourSideStream.P;
314
315	"Vapour Draw Off Stream - Composition"
316	VapourDrawOff.z = TRAYS(VapourSideStreamLocation).VapourSideStream.z;
317
318	"Vapour Draw Off Stream"
319	VapourDrawOffFlow = VapourDrawOff.F;
320
321	"Liquid Draw Off Stream - Flow"
322	LiquidDrawOff.F*LiqSideTrayIndex= TRAYS.LiquidSideStream.F;
323
324	"Liquid Draw Off Stream - Temperature"
325	LiquidDrawOff.T = TRAYS(LiquidSideStreamLocation).LiquidSideStream.T;
326
327	"Liquid Draw Off Stream - Pressure"
328	LiquidDrawOff.P = TRAYS(LiquidSideStreamLocation).LiquidSideStream.P;
329
330	"Liquid Draw Off Stream - Composition"
331	LiquidDrawOff.z = TRAYS(LiquidSideStreamLocation).LiquidSideStream.z;
332
333	"Liquid Draw Off Stream"
334	LiquidDrawOffFlow = LiquidDrawOff.F;
335
336	end
337
338	Model Section_Column as SectionColumnBasic
339
340	ATTRIBUTES
341	Pallete = true;
342	Icon = "icon/SectionColumn";
343	Brief = "Model of a column section.";
344	Info =
345	"== Model of a column section containing ==
346	* NumberOfTrays TRAYS.
347	* One Feed Inlet.
348
349	== Specify ==
350	* the feed stream of each tray (Inlet);
351	* the Murphree eficiency for each tray Emv;
352	* the InletLiquid stream of the top tray;
353	* the InletVapour stream of the bottom tray.
354
355	== Initial Conditions ==
356	* the TRAYS temperature (OutletLiquid.T);
357	* the TRAYS liquid level (Level) OR the TRAYS liquid flow (OutletLiquid.F);
358	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions for each tray.
359	";
360
361	SET
362	NumberOfFeeds = 1;
363
364	VARIABLES
365
366	in FeedTray as stream (Brief="Feed stream", PosX=0, PosY=0.55);
367
368	EQUATIONS
369	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
370	# Equating Feed Tray Variables to Trays Variables
371	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
372	for i in 1:NumberOfTrays do
373
374	if i equal FeedTrayLocation(1) then
375
376	"FeedTrayTop Inlet Flow"
377	FeedTray.F= TRAYS(i).Inlet.F;
378
379	"FeedTrayTop Inlet Temperature"
380	FeedTray.T = TRAYS(i).Inlet.T;
381
382	"FeedTrayTop Inlet Pressure"
383	FeedTray.P = TRAYS(i).Inlet.P;
384
385	"FeedTrayTop Inlet Composition"
386	FeedTray.z = TRAYS(i).Inlet.z;
387
388	"FeedTrayTop Inlet Vapour Fraction"
389	FeedTray.v = TRAYS(i).Inlet.v;
390
391	"FeedTrayTop Inlet Enthalpy"
392	FeedTray.h = TRAYS(i).Inlet.h;
393
394	else
395
396	"Inlet Tray - Flow Sealed"
397	0*'mol/h'= TRAYS(i).Inlet.F;
398
399	"Inlet Tray - Temperature"
400	300*'K' = TRAYS(i).Inlet.T;
401
402	"Inlet Tray - Pressure"
403	1*'atm' = TRAYS(i).Inlet.P;
404
405	"Inlet Tray - Composition"
406	0.1 = TRAYS(i).Inlet.z;
407
408	"Inlet Tray - Vapour Fraction"
409	0 = TRAYS(i).Inlet.v;
410
411	"Inlet Tray - Enthalpy"
412	0*'J/mol' = TRAYS(i).Inlet.h;
413
414	end
415
416	end
417
418	end
419
420	Model Section_Column2 as SectionColumnBasic
421
422	ATTRIBUTES
423	Pallete = true;
424	Icon = "icon/SectionColumn";
425	Brief = "Model of a column section.";
426	Info =
427	"== Model of a column section containing ==
428	* NumberOfTrays TRAYS.
429	* Two Feed Inlets.
430
431	== Specify ==
432	* the feed stream of each tray (Inlet);
433	* the Murphree eficiency for each tray Emv;
434	* the InletLiquid stream of the top tray;
435	* the InletVapour stream of the bottom tray.
436
437	== Initial Conditions ==
438	* the TRAYS temperature (OutletLiquid.T);
439	* the TRAYS liquid level (Level) OR the TRAYS liquid flow (OutletLiquid.F);
440	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions for each tray.
441	";
442
443	SET
444	NumberOfFeeds = 2;
445
446	VARIABLES
447
448	in FeedTrayOne as stream (Brief="Feed stream", PosX=0, PosY=0.45);
449	in FeedTrayTwo as stream (Brief="Feed stream", PosX=0, PosY=0.65);
450
451	EQUATIONS
452
453	for i in 1:NumberOfTrays do
454
455	if i equal FeedTrayLocation(1) then
456
457	"FeedTrayTop Inlet Flow"
458	FeedTrayOne.F= TRAYS(i).Inlet.F;
459
460	"FeedTrayTop Inlet Temperature"
461	FeedTrayOne.T = TRAYS(i).Inlet.T;
462
463	"FeedTrayTop Inlet Pressure"
464	FeedTrayOne.P = TRAYS(i).Inlet.P;
465
466	"FeedTrayTop Inlet Composition"
467	FeedTrayOne.z = TRAYS(i).Inlet.z;
468
469	"FeedTrayTop Inlet Vapour Fraction"
470	FeedTrayOne.v = TRAYS(i).Inlet.v;
471
472	"FeedTrayTop Inlet Enthalpy"
473	FeedTrayOne.h = TRAYS(i).Inlet.h;
474
475	else if i equal FeedTrayLocation(2) then
476
477	"FeedTrayBottom Inlet Flow"
478	FeedTrayTwo.F= TRAYS(i).Inlet.F;
479
480	"FeedTrayBottom Inlet Temperature"
481	FeedTrayTwo.T = TRAYS(i).Inlet.T;
482
483	"FeedTrayBottom Inlet Pressure"
484	FeedTrayTwo.P = TRAYS(i).Inlet.P;
485
486	"FeedTrayBottom Inlet Composition"
487	FeedTrayTwo.z = TRAYS(i).Inlet.z;
488
489	"FeedTrayBottom Inlet Vapour Fraction"
490	FeedTrayTwo.v = TRAYS(i).Inlet.v;
491
492	"FeedTrayBottom Inlet Enthalpy"
493	FeedTrayTwo.h = TRAYS(i).Inlet.h;
494
495	else
496
497	"Inlet Tray - Flow Sealed"
498	0*'mol/h'= TRAYS(i).Inlet.F;
499
500	"Inlet Tray - Temperature"
501	300*'K' = TRAYS(i).Inlet.T;
502
503	"Inlet Tray - Pressure"
504	1*'atm' = TRAYS(i).Inlet.P;
505
506	"Inlet Tray - Composition"
507	0.1 = TRAYS(i).Inlet.z;
508
509	"Inlet Tray - Vapour Fraction"
510	0 = TRAYS(i).Inlet.v;
511
512	"Inlet Tray - Enthalpy"
513	0*'J/mol' = TRAYS(i).Inlet.h;
514
515	end
516
517	end
518
519	end
520
521	end
522
523	Model Section_Column3 as SectionColumnBasic
524
525	ATTRIBUTES
526	Pallete = true;
527	Icon = "icon/SectionColumn";
528	Brief = "Model of a column section.";
529	Info =
530	"== Model of a column section containing ==
531	* NumberOfTrays TRAYS.
532	* Three Feed Inlets.
533
534	== Specify ==
535	* the feed stream of each tray (Inlet);
536	* the Murphree eficiency for each tray Emv;
537	* the InletLiquid stream of the top tray;
538	* the InletVapour stream of the bottom tray.
539
540	== Initial Conditions ==
541	* the TRAYS temperature (OutletLiquid.T);
542	* the TRAYS liquid level (Level) OR the TRAYS liquid flow (OutletLiquid.F);
543	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions for each tray.
544	";
545
546	SET
547	NumberOfFeeds = 3;
548
549	VARIABLES
550
551	in FeedTrayOne as stream (Brief="Feed stream", PosX=0, PosY=0.45);
552	in FeedTrayTwo as stream (Brief="Feed stream", PosX=0, PosY=0.65);
553	in FeedTrayThree as stream (Brief="Feed stream", PosX=0, PosY=0.85);
554
555	EQUATIONS
556
557	for i in 1:NumberOfTrays do
558
559	if i equal FeedTrayLocation(1) then
560
561	"FeedTrayTop Inlet Flow"
562	FeedTrayOne.F= TRAYS(i).Inlet.F;
563
564	"FeedTrayTop Inlet Temperature"
565	FeedTrayOne.T = TRAYS(i).Inlet.T;
566
567	"FeedTrayTop Inlet Pressure"
568	FeedTrayOne.P = TRAYS(i).Inlet.P;
569
570	"FeedTrayTop Inlet Composition"
571	FeedTrayOne.z = TRAYS(i).Inlet.z;
572
573	"FeedTrayTop Inlet Vapour Fraction"
574	FeedTrayOne.v = TRAYS(i).Inlet.v;
575
576	"FeedTrayTop Inlet Enthalpy"
577	FeedTrayOne.h = TRAYS(i).Inlet.h;
578
579	else if i equal FeedTrayLocation(2) then
580
581	"FeedTrayBottom Inlet Flow"
582	FeedTrayTwo.F= TRAYS(i).Inlet.F;
583
584	"FeedTrayBottom Inlet Temperature"
585	FeedTrayTwo.T = TRAYS(i).Inlet.T;
586
587	"FeedTrayBottom Inlet Pressure"
588	FeedTrayTwo.P = TRAYS(i).Inlet.P;
589
590	"FeedTrayBottom Inlet Composition"
591	FeedTrayTwo.z = TRAYS(i).Inlet.z;
592
593	"FeedTrayBottom Inlet Vapour Fraction"
594	FeedTrayTwo.v = TRAYS(i).Inlet.v;
595
596	"FeedTrayBottom Inlet Enthalpy"
597	FeedTrayTwo.h = TRAYS(i).Inlet.h;
598
599	else if i equal FeedTrayLocation(3) then
600
601	"FeedTrayBottom Inlet Flow"
602	FeedTrayThree.F= TRAYS(i).Inlet.F;
603
604	"FeedTrayBottom Inlet Temperature"
605	FeedTrayThree.T = TRAYS(i).Inlet.T;
606
607	"FeedTrayBottom Inlet Pressure"
608	FeedTrayThree.P = TRAYS(i).Inlet.P;
609
610	"FeedTrayBottom Inlet Composition"
611	FeedTrayThree.z = TRAYS(i).Inlet.z;
612
613	"FeedTrayBottom Inlet Vapour Fraction"
614	FeedTrayThree.v = TRAYS(i).Inlet.v;
615
616	"FeedTrayBottom Inlet Enthalpy"
617	FeedTrayThree.h = TRAYS(i).Inlet.h;
618
619	else
620
621	"Inlet Tray - Flow Sealed"
622	0*'mol/h'= TRAYS(i).Inlet.F;
623
624	"Inlet Tray - Temperature"
625	300*'K' = TRAYS(i).Inlet.T;
626
627	"Inlet Tray - Pressure"
628	1*'atm' = TRAYS(i).Inlet.P;
629
630	"Inlet Tray - Composition"
631	0.1 = TRAYS(i).Inlet.z;
632
633	"Inlet Tray - Vapour Fraction"
634	0 = TRAYS(i).Inlet.v;
635
636	"Inlet Tray - Enthalpy"
637	0*'J/mol' = TRAYS(i).Inlet.h;
638
639	end
640
641	end
642
643	end
644
645	end
646
647	end
648
649
650	Model Packed_Section_ColumnBasic
651
652	ATTRIBUTES
653	Pallete = false;
654	Icon = "icon/PackedSectionColumn";
655	Brief = "Model of a packed column section.";
656	Info =
657	"== Model of a packed column section containing ==
658	* NStages theoretical stages.
659
660	== Specify ==
661	* the feed stream of each tray (Inlet);
662	* the InletLiquid stream of the top tray;
663	* the InletVapour stream of the bottom tray;
664	* the total pressure drop (dP) of the section.
665
666	== Initial Conditions ==
667	* the stages temperature (OutletLiquid.T);
668	* the stages liquid holdup;
669	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions for each tray.
670	";
671
672	PARAMETERS
673
674	outer PP as Plugin (Brief = "External Physical Properties", Type="PP");
675	outer NComp as Integer (Brief="Number of components",Protected=true);
676
677
678	NumberOfFeeds as Integer (Brief="Number of Feed Stages",Default=3,Protected=true);
679	NumberOfStages as Integer (Brief="Number of Stages", Default=3);
680	FeedStageLocation(NumberOfFeeds) as Integer (Brief="Feed Stage Location",Default=2);
681
682	PackingHeight as length (Brief="Height of packing");
683	HeatSupply as heat_rate (Brief="Rate of heat supply");
684	ColumnDiameter as length (Brief="Column diameter");
685	VoidFraction as Real (Brief="Void fraction of packing, (m^3 void space/m^3 packed bed)");
686	ResistanceCoeff as positive (Brief="Resistance coefficient on the liquid load", Default=1);
687	AreaPerPackingVol as Real (Brief="surface area per packing volume", Unit='m^2/m^3');
688	HETP as length (Brief="The Height Equivalent to a Theoretical Plate",Protected=true);
689
690	VARIABLES
691
692	INITIALIZATION as InitializeStage (Brief = "Column Model Initialization");
693	CONTROL as ControlSection (Brief="Column Model Control");
694
695	out TCI as control_signal (Brief="Temperature Indicator", Protected = true, PosX=1, PosY=0.73);
696	out PCI as control_signal (Brief="Pressure Indicator", Protected = true, PosX=0, PosY=0.24);
697	out zCI as control_signal (Brief="Composition control", Protected = true, PosX=1, PosY=0.8);
698
699	in LiquidInlet as stream (Brief="Liquid Inlet in the section", PosX=0.70, PosY=0,Protected=true);
700	out VapourOutlet as vapour_stream (Brief="Vapour Outlet in the section", PosX=0.30, PosY=0,Protected=true);
701
702	in VapourInlet as stream (Brief="Vapour Inlet in the section", PosX=0.30, PosY=1,Protected=true);
703	out LiquidOutlet as liquid_stream (Brief="Liquid Outlet in the section", PosX=0.70, PosY=1,Protected=true);
704
705	LiquidConnector as stream (Brief="Liquid connection at the middle STAGES", PosX=0.75, PosY=1,Hidden=true);
706	VapourConnector as stream (Brief="Vapour connection at the middle STAGES", PosX=0.55, PosY=0,Hidden=true);
707
708	STAGES(NumberOfStages) as packedStage (Brief="Column Stages",Protected=true);
709	PressureDrop as pressure (Brief="Column Pressure Drop", Protected=true);
710
711	SET
712
713	STAGES.Number_Stages = NumberOfStages;
714	STAGES.HeightOfPacking = PackingHeight;
715	STAGES.HeatOnStage = HeatSupply;
716	STAGES.ColumnInternalDiameter = ColumnDiameter;
717	STAGES.PackingVoidFraction = VoidFraction;
718	STAGES.LiquidResistanceCoeff = ResistanceCoeff ;
719	STAGES.AreaPerPackingVolume = AreaPerPackingVol;
720
721	HETP = PackingHeight/NumberOfStages;
722
723	CONNECTIONS
724
725	STAGES([2:NumberOfStages]).OutletVapour to STAGES([1:NumberOfStages-1]).InletVapour;
726	STAGES([1:NumberOfStages-1]).OutletLiquid to STAGES([2:NumberOfStages]).InletLiquid;
727	LiquidConnector to STAGES(1).InletLiquid;
728	VapourConnector to STAGES(NumberOfStages).InletVapour;
729
730	EQUATIONS
731
732	LiquidConnector.F= LiquidInlet.F;
733	LiquidConnector.T = LiquidInlet.T;
734	LiquidConnector.P = LiquidInlet.P;
735	LiquidConnector.z = LiquidInlet.z;
736	LiquidConnector.v = LiquidInlet.v;
737	LiquidConnector.h = LiquidInlet.h;
738
739	VapourConnector.F= VapourInlet.F;
740	VapourConnector.T = VapourInlet.T;
741	VapourConnector.P = VapourInlet.P;
742	VapourConnector.z = VapourInlet.z;
743	VapourConnector.v = VapourInlet.v;
744	VapourConnector.h = VapourInlet.h;
745
746	LiquidOutlet.F= STAGES(NumberOfStages).OutletLiquid.F;
747	LiquidOutlet.T = STAGES(NumberOfStages).OutletLiquid.T;
748	LiquidOutlet.P = STAGES(NumberOfStages).OutletLiquid.P;
749	LiquidOutlet.z = STAGES(NumberOfStages).OutletLiquid.z;
750
751	VapourOutlet.F= STAGES(1).OutletVapour.F;
752	VapourOutlet.T = STAGES(1).OutletVapour.T;
753	VapourOutlet.P = STAGES(1).OutletVapour.P;
754	VapourOutlet.z = STAGES(1).OutletVapour.z;
755
756	"Tray Temperature Indicator"
757	#TCI*'K' = TRAYS(min([NumberOfTrays, CONTROL.Tindicator_TrayNumber])).OutletVapour.T;
758	TCI*'K' = STAGES(CONTROL.Tindicator_TrayNumber).OutletVapour.T;
759
760	"Tray Pressure Indicator"
761	#PCI*'atm' = TRAYS(min([NumberOfTrays, CONTROL.Pindicator_TrayNumber])).OutletVapour.P;
762	PCI*'atm' = STAGES(CONTROL.Pindicator_TrayNumber).OutletVapour.P;
763
764	"Tray Composition Indicator"
765	#zCI * .000001 = STAGES(CONTROL.zindicator_TrayNumber).OutletVapour.z(CONTROL.zindicator_Component) * STAGES(CONTROL.zindicator_TrayNumber).Mw(CONTROL.zindicator_Component) ; #/sum(STAGES(CONTROL.zindicator_TrayNumber).Mw*STAGES(CONTROL.zindicator_TrayNumber).OutletLiquid.z);
766	zCI * 1e-6 = STAGES(CONTROL.zindicator_TrayNumber).OutletLiquid.z(CONTROL.zindicator_Component) * STAGES(CONTROL.zindicator_TrayNumber).Mw(CONTROL.zindicator_Component) / sum(STAGES(CONTROL.zindicator_TrayNumber).Mw*STAGES(CONTROL.zindicator_TrayNumber).OutletLiquid.z);
767
768	"PressureDrop"
769	PressureDrop = STAGES(NumberOfStages).OutletLiquid.P - STAGES(1).OutletLiquid.P;
770
771	INITIAL
772
773	for i in 1:NumberOfStages do
774
775	"The initial temperature of the STAGES"
776	STAGES(i).OutletLiquid.T = INITIALIZATION.TopStageTemperature+(INITIALIZATION.BottomStageTemperature-INITIALIZATION.TopStageTemperature)*((i-1)/(NumberOfStages-1));
777
778	"The Column Holdup of the STAGES"
779	STAGES(i).hl = INITIALIZATION.ColumnHoldup;
780
781	end
782
783	for i in 1:NComp-1 do
784
785	for j in 1:NumberOfStages do
786
787	"The initial composition of the TRAYS"
788	STAGES(j).OutletLiquid.z(i) = INITIALIZATION.TopStageComposition(i)/sum(INITIALIZATION.TopStageComposition) +(INITIALIZATION.BottomStageComposition(i)/sum(INITIALIZATION.BottomStageComposition)-INITIALIZATION.TopStageComposition(i)/sum(INITIALIZATION.TopStageComposition) )*((j-1)/(NumberOfStages-1));
789
790	end
791
792	end
793
794	end
795
796	Model Packed_Section_Column as Packed_Section_ColumnBasic
797
798	ATTRIBUTES
799	Pallete = true;
800	Icon = "icon/PackedSectionColumn";
801	Brief = "Model of a packed column section.";
802	Info =
803	"== Model of a packed column section containing ==
804	* NStages theoretical stages.
805
806	== Specify ==
807	* the feed stream of each tray (Inlet);
808	* the InletLiquid stream of the top tray;
809	* the InletVapour stream of the bottom tray;
810	* the total pressure drop (dP) of the section.
811
812	== Initial Conditions ==
813	* the stages temperature (OutletLiquid.T);
814	* the stages liquid holdup;
815	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions for each tray.
816	";
817
818	SET
819	NumberOfFeeds = 1;
820
821	VARIABLES
822
823	in FeedStage as stream (Brief="Feed stream", PosX=0, PosY=0.55);
824
825	EQUATIONS
826	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
827	# Equating Feed Tray Variables to Trays Variables
828	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
829	for i in 1:NumberOfStages do
830
831	if i equal FeedStageLocation(1) then
832
833	"FeedTrayTop Inlet Flow"
834	FeedStage.F= STAGES(i).Inlet.F;
835
836	"FeedTrayTop Inlet Temperature"
837	FeedStage.T = STAGES(i).Inlet.T;
838
839	"FeedTrayTop Inlet Pressure"
840	FeedStage.P = STAGES(i).Inlet.P;
841
842	"FeedTrayTop Inlet Composition"
843	FeedStage.z = STAGES(i).Inlet.z;
844
845	"FeedTrayTop Inlet Vapour Fraction"
846	FeedStage.v = STAGES(i).Inlet.v;
847
848	"FeedTrayTop Inlet Enthalpy"
849	FeedStage.h = STAGES(i).Inlet.h;
850
851	else
852
853	"Inlet Tray - Flow Sealed"
854	0*'mol/h'= STAGES(i).Inlet.F;
855
856	"Inlet Tray - Temperature"
857	300*'K' = STAGES(i).Inlet.T;
858
859	"Inlet Tray - Pressure"
860	1*'atm' = STAGES(i).Inlet.P;
861
862	"Inlet Tray - Composition"
863	0.1 = STAGES(i).Inlet.z;
864
865	"Inlet Tray - Vapour Fraction"
866	0 = STAGES(i).Inlet.v;
867
868	"Inlet Tray - Enthalpy"
869	0*'J/mol' = STAGES(i).Inlet.h;
870
871	end
872
873	end
874
875	end
876
877	Model Packed_Section_Column2 as Packed_Section_ColumnBasic
878
879	ATTRIBUTES
880	Pallete = true;
881	Icon = "icon/PackedSectionColumn";
882	Brief = "Model of a packed column section.";
883	Info =
884	"== Model of a packed column section containing ==
885	* NStages theoretical stages.
886
887	== Specify ==
888	* the feed stream of each tray (Inlet);
889	* the InletLiquid stream of the top tray;
890	* the InletVapour stream of the bottom tray;
891	* the total pressure drop (dP) of the section.
892
893	== Initial Conditions ==
894	* the stages temperature (OutletLiquid.T);
895	* the stages liquid holdup;
896	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions for each tray.
897	";
898
899	SET
900	NumberOfFeeds = 2;
901
902	VARIABLES
903
904	in FeedStageOne as stream (Brief="Feed stream", PosX=0, PosY=0.45);
905	in FeedStageTwo as stream (Brief="Feed stream", PosX=0, PosY=0.65);
906
907	EQUATIONS
908	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
909	# Equating Feed Stage Variables to Stages Variables
910	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
911
912	for i in 1:NumberOfStages do
913
914	if i equal FeedStageLocation(1) then
915
916	"FeedTrayTop Inlet Flow"
917	FeedStageOne.F= STAGES(i).Inlet.F;
918
919	"FeedTrayTop Inlet Temperature"
920	FeedStageOne.T = STAGES(i).Inlet.T;
921
922	"FeedTrayTop Inlet Pressure"
923	FeedStageOne.P = STAGES(i).Inlet.P;
924
925	"FeedTrayTop Inlet Composition"
926	FeedStageOne.z = STAGES(i).Inlet.z;
927
928	"FeedTrayTop Inlet Vapour Fraction"
929	FeedStageOne.v = STAGES(i).Inlet.v;
930
931	"FeedTrayTop Inlet Enthalpy"
932	FeedStageOne.h = STAGES(i).Inlet.h;
933
934	else if i equal FeedStageLocation(2) then
935
936	"FeedTrayBottom Inlet Flow"
937	FeedStageTwo.F= STAGES(i).Inlet.F;
938
939	"FeedTrayBottom Inlet Temperature"
940	FeedStageTwo.T = STAGES(i).Inlet.T;
941
942	"FeedTrayBottom Inlet Pressure"
943	FeedStageTwo.P = STAGES(i).Inlet.P;
944
945	"FeedTrayBottom Inlet Composition"
946	FeedStageTwo.z = STAGES(i).Inlet.z;
947
948	"FeedTrayBottom Inlet Vapour Fraction"
949	FeedStageTwo.v = STAGES(i).Inlet.v;
950
951	"FeedTrayBottom Inlet Enthalpy"
952	FeedStageTwo.h = STAGES(i).Inlet.h;
953
954	else
955
956	"Inlet Tray - Flow Sealed"
957	0*'mol/h'= STAGES(i).Inlet.F;
958
959	"Inlet Tray - Temperature"
960	300*'K' = STAGES(i).Inlet.T;
961
962	"Inlet Tray - Pressure"
963	1*'atm' = STAGES(i).Inlet.P;
964
965	"Inlet Tray - Composition"
966	0.1 = STAGES(i).Inlet.z;
967
968	"Inlet Tray - Vapour Fraction"
969	0 = STAGES(i).Inlet.v;
970
971	"Inlet Tray - Enthalpy"
972	0*'J/mol' = STAGES(i).Inlet.h;
973
974	end
975
976	end
977
978	end
979
980	end
981
982
983	# Models to be revised
984	#*
985	Model ColumnBasic
986
987	ATTRIBUTES
988	Pallete = false;
989	Brief = "Model of a basic column.";
990	Info =
991	"Model of a basic column containing a vetor of TRAYS numbered from the top-down.";
992
993	PARAMETERS
994	outer PP as Plugin (Brief="External Physical Properties", Type="PP");
995	outer NComp as Integer (Brief="Number of components");
996
997	NumberOfFeeds as Integer (Brief="Number of Feed Trays",Default=3,Protected=true);
998	FeedTrayLocation(NumberOfFeeds) as Integer (Brief="Feed tray Location",Default=2);
999	NumberOfTrays as Integer (Brief="Number of trays", Default=8);
1000	LiqSideTrayIndex(NumberOfTrays) as Integer (Brief="Liquid Side Tray Index", Default=0,Hidden=true);
1001	VapSideTrayIndex(NumberOfTrays) as Integer (Brief="Vapour Side Tray Index", Default=0,Hidden=true);
1002	LiquidSideStreamLocation as Integer (Brief="Liquid Side Stream Location", Default=2);
1003	VapourSideStreamLocation as Integer (Brief="Vapour Side Stream Location", Default=2);
1004	g as acceleration (Brief="Gravity Acceleration",Default=9.81,Hidden=true);
1005	Mw(NComp) as molweight (Brief="Component Mol Weight",Hidden=true);
1006
1007	VapourFlowModel as Switcher (Valid = ["Reepmeyer", "Feehery_Fv", "Roffel_Fv", "Klingberg", "Wang_Fv", "Elgue"], Default = "Reepmeyer");
1008	LiquidFlowModel as Switcher (Valid = ["default", "Wang_Fl", "Olsen", "Feehery_Fl", "Roffel_Fl"], Default = "default");
1009
1010	TrayDiameter as length (Brief="Tray Diameter",Default=1.600);
1011	TraySpacing as length (Brief="Tray Spacing",Default=0.600);
1012	Fraction_HoleArea as fraction (Brief="Fraction of the active area that is occupied by the holes with respect to the total tray area",Default=0.10);
1013	Fraction_DowncomerArea as fraction (Brief="Fraction of the downcomer area with respect to the total tray area",Default=0.20);
1014	WeirLength as length (Brief="Weir length", Default = 1);
1015	WeirHeight as length (Brief="Weir height", Default= 0.05);
1016	TrayLiquidPasses as positive (Brief="Number of liquid passes in the tray", Lower = 1,Default=1);
1017	HeatSupply as heat_rate (Brief="Rate of heat supply",Default = 0);
1018	AerationFraction as Real (Brief="Aeration fraction", Default = 1);
1019	DryPdropCoeff as Real (Brief="Dry pressure drop coefficient", Default= 0.60);
1020
1021	PlateArea as area (Brief="Plate area = Atray - Adowncomer",Protected=true);
1022	TrayVolume as volume (Brief="Total Volume of the tray",Protected=true);
1023	HolesArea as area (Brief="Total holes area",Protected=true);
1024
1025	FeeheryCoeff as Real (Brief="Feeherys correlation coefficient", Unit='1/m^4', Default=1,Hidden=true);
1026	ElgueCoeff as Real (Brief="Elgues correlation coefficient", Unit='kg/m/mol^2', Default=1,Hidden=true);
1027	OlsenCoeff as Real (Brief="Olsens correlation coefficient", Default=1,Hidden=true);
1028
1029	Pi as constant (Brief="Pi Number",Default=3.14159265, Symbol = "\pi",Hidden=true);
1030	zero_flow as flow_mol (Brief = "Stream Flow closed",Default = 0, Hidden=true);
1031	low_flow as flow_mol (Brief = "Low stream Flow",Default = 1E-6, Hidden=true);
1032	VapourFlow as Switcher (Valid = ["on", "off"], Default = "on",Hidden=true);
1033	LiquidFlow as Switcher (Valid = ["on", "off"], Default = "on",Hidden=true);
1034
1035	SET
1036	VapSideTrayIndex(VapourSideStreamLocation) =1;
1037	LiqSideTrayIndex(LiquidSideStreamLocation) =1;
1038	Mw = PP.MolecularWeight();
1039	zero_flow = 0 * 'kmol/h';
1040	low_flow = 1E-6 * 'kmol/h';
1041
1042	PlateArea = 0.25Pi(TrayDiameter^2)*(1-Fraction_DowncomerArea);
1043	TrayVolume = 0.25Pi(TrayDiameter^2)*TraySpacing;
1044	HolesArea = 0.25Pi(TrayDiameter^2)*Fraction_HoleArea;
1045
1046	VARIABLES
1047
1048	INITIALIZATION as InitializeSection (Brief = "Column Model Initialization");
1049	CONTROL as ControlSection (Brief = "Control");
1050
1051	out TCI as control_signal (Brief="Temperature Indicator", Protected = true, PosX=1, PosY=0.55);
1052	out PCI as control_signal (Brief="Pressure Indicator", Protected = true, PosX=0, PosY=0.23);
1053
1054	TRAYS(NumberOfTrays) as tray (Brief="Number of trays in the Column Section");
1055	VapourDrawOffFlow as flow_mol (Brief="Vapour Draw Off Stream Molar Flow Rate");
1056	LiquidDrawOffFlow as flow_mol (Brief="Vapour Draw Off Stream Molar Flow Rate");
1057	MurphreeEff as Real (Brief="Murphree efficiency for All Trays",Lower=0.01,Upper=1);
1058
1059	out VapourDrawOff as vapour_stream (Brief="Vapour Outlet in the section", PosX=1, PosY=0.388,Protected = true);
1060	out LiquidDrawOff as liquid_stream (Brief="Liquid Outlet in the section", PosX=1, PosY=0.47,Protected = true);
1061
1062	CONNECTIONS
1063
1064	#Connecting Intermediate Trays
1065	TRAYS([2:NumberOfTrays]).OutletVapour to TRAYS([1:NumberOfTrays-1]).InletVapour;
1066	TRAYS([1:NumberOfTrays-1]).OutletLiquid to TRAYS([2:NumberOfTrays]).InletLiquid;
1067
1068	INITIAL
1069
1070	for i in 1:NumberOfTrays do
1071
1072	"The initial temperature of the TRAYS"
1073	TRAYS(i).OutletLiquid.T = INITIALIZATION.TopTemperature+(INITIALIZATION.BottomTemperature-INITIALIZATION.TopTemperature)*((i-1)/(NumberOfTrays-1));
1074
1075	"The initial Level of the TRAYS"
1076	TRAYS(i).Level = INITIALIZATION.LevelFraction*WeirHeight;
1077	end
1078
1079	for i in 1:NComp-1 do
1080
1081	for j in 1:NumberOfTrays do
1082
1083	"The initial composition of the TRAYS - Normalized"
1084	TRAYS(j).OutletLiquid.z(i) = INITIALIZATION.TopComposition(i)/sum(INITIALIZATION.TopComposition) +(INITIALIZATION.BottomComposition(i)/sum(INITIALIZATION.BottomComposition)-INITIALIZATION.TopComposition(i)/sum(INITIALIZATION.TopComposition) )*((j-1)/(NumberOfTrays-1));
1085	end
1086
1087	end
1088
1089	EQUATIONS
1090
1091	VapourDrawOff.F*VapSideTrayIndex= TRAYS.VapourSideStream.F;
1092	VapourDrawOff.T = TRAYS(VapourSideStreamLocation).VapourSideStream.T;
1093	VapourDrawOff.P = TRAYS(VapourSideStreamLocation).VapourSideStream.P;
1094	VapourDrawOff.z = TRAYS(VapourSideStreamLocation).VapourSideStream.z;
1095
1096	LiquidDrawOff.F*LiqSideTrayIndex= TRAYS.LiquidSideStream.F;
1097	LiquidDrawOff.T = TRAYS(LiquidSideStreamLocation).LiquidSideStream.T;
1098	LiquidDrawOff.P = TRAYS(LiquidSideStreamLocation).LiquidSideStream.P;
1099	LiquidDrawOff.z = TRAYS(LiquidSideStreamLocation).LiquidSideStream.z;
1100
1101	VapourDrawOffFlow = VapourDrawOff.F;
1102	LiquidDrawOffFlow = LiquidDrawOff.F;
1103
1104	"Tray Temperature Indicator"
1105	#TCI*'K' = TRAYS(min([NumberOfTrays, CONTROL.Tindicator_TrayNumber])).OutletVapour.T;
1106	TCI*'K' = TRAYS(CONTROL.Tindicator_TrayNumber).OutletVapour.T;
1107
1108	"Tray Pressure Indicator"
1109	#PCI*'atm' = TRAYS(min([NumberOfTrays, CONTROL.Pindicator_TrayNumber])).OutletVapour.P;
1110	PCI*'atm' = TRAYS(CONTROL.Pindicator_TrayNumber).OutletVapour.P;
1111
1112	for i in [1:NumberOfTrays] do
1113
1114	"Murphree Efficiency"
1115	TRAYS(i).OutletVapour.z = MurphreeEff * (TRAYS(i).yideal - TRAYS(i).InletVapour.z) + TRAYS(i).InletVapour.z;
1116
1117	"Level of clear liquid over the weir"
1118	TRAYS(i).Level = TRAYS(i).ML*TRAYS(i).vL/PlateArea;
1119
1120	"Geometry Constraint"
1121	TrayVolume = TRAYS(i).ML* TRAYS(i).vL + TRAYS(i).MV*TRAYS(i).vV;
1122
1123	"Energy Holdup"
1124	TRAYS(i).E = TRAYS(i).MLTRAYS(i).OutletLiquid.h + TRAYS(i).MVTRAYS(i).OutletVapour.h - TRAYS(i).OutletLiquid.P*TrayVolume;
1125
1126	"Energy Balance"
1127	diff(TRAYS(i).E) = ( TRAYS(i).Inlet.FTRAYS(i).Inlet.h + TRAYS(i).InletLiquid.FTRAYS(i).InletLiquid.h + TRAYS(i).InletVapour.FTRAYS(i).InletVapour.h- TRAYS(i).OutletLiquid.FTRAYS(i).OutletLiquid.h - TRAYS(i).OutletVapour.F*TRAYS(i).OutletVapour.h
1128	-TRAYS(i).VapourSideStream.FTRAYS(i).VapourSideStream.h - TRAYS(i).LiquidSideStream.FTRAYS(i).LiquidSideStream.h + HeatSupply );
1129
1130	switch LiquidFlow
1131	case "on":
1132	switch LiquidFlowModel
1133	case "default":
1134	"Francis Equation"
1135	TRAYS(i).OutletLiquid.FTRAYS(i).vL = 1.84'1/s'WeirLength((TRAYS(i).Level-(AerationFraction*WeirHeight))/(AerationFraction))^2;
1136
1137	case "Wang_Fl":
1138	TRAYS(i).OutletLiquid.FTRAYS(i).vL = 1.84'm^0.5/s'WeirLength((TRAYS(i).Level-(AerationFraction*WeirHeight))/(AerationFraction))^1.5;
1139
1140	case "Olsen":
1141	TRAYS(i).OutletLiquid.F / 'mol/s'= WeirLengthTrayLiquidPassesTRAYS(i).rhoL/sum(MwTRAYS(i).OutletVapour.z)/(0.665OlsenCoeff)^1.5 * ((TRAYS(i).MLsum(MwTRAYS(i).OutletLiquid.z)/TRAYS(i).rhoL/PlateArea)-WeirHeight)^1.5 * 'm^0.5/mol';
1142
1143	case "Feehery_Fl":
1144	TRAYS(i).OutletLiquid.F = WeirLengthTRAYS(i).rhoL/sum(MwTRAYS(i).OutletLiquid.z) * ((TRAYS(i).Level-WeirHeight)/750/'mm')^1.5 * 'm^2/s';
1145
1146	case "Roffel_Fl":
1147	TRAYS(i).OutletLiquid.F = 2/3TRAYS(i).rhoL/sum(MwTRAYS(i).OutletLiquid.z)WeirLength(TRAYS(i).MLsum(MwTRAYS(i).OutletLiquid.z)/(PlateArea1.3)/TRAYS(i).rhoL)^1.5sqrt(2*g/
1148	(2(1 - 0.3593/'Pa^0.0888545'abs(TRAYS(i).OutletVapour.Fsum(MwTRAYS(i).OutletVapour.z)/(PlateArea*1.3)/sqrt(TRAYS(i).rhoV))^0.177709)-1)); #/'(kg/m)^0.0888545/s^0.177709';
1149	end
1150	when TRAYS(i).Level < (AerationFraction *WeirHeight) switchto "off";
1151
1152	case "off":
1153	"Low level"
1154	TRAYS(i).OutletLiquid.F = 0 * 'mol/h';
1155	when TRAYS(i).Level > (AerationFraction * WeirHeight) switchto "on";
1156	end
1157
1158	switch VapourFlow
1159	case "on":
1160	switch VapourFlowModel
1161	case "Reepmeyer":
1162	TRAYS(i).InletVapour.FTRAYS(i).vV = sqrt((TRAYS(i).InletVapour.P - TRAYS(i).OutletVapour.P)/(TRAYS(i).rhoVDryPdropCoeff))*HolesArea;
1163
1164	case "Feehery_Fv":
1165	TRAYS(i).InletVapour.F = TRAYS(i).rhoV/PlateArea/FeeheryCoeff/sum(MwTRAYS(i).OutletVapour.z) sqrt(((TRAYS(i).InletVapour.P - TRAYS(i).OutletVapour.P)-(TRAYS(i).rhoVgTRAYS(i).ML*TRAYS(i).vL/PlateArea))/TRAYS(i).rhoV);
1166
1167	case "Roffel_Fv":
1168	TRAYS(i).InletVapour.F^1.08 * 0.0013 * 'kg/m/mol^1.08/s^0.921e5' = (TRAYS(i).InletVapour.P - TRAYS(i).OutletVapour.P)1e5 - (AerationFractionsum(TRAYS(i).MMw)/(PlateArea1.3)g1e5) (TRAYS(i).rhoVHolesArea/sum(MwTRAYS(i).OutletVapour.z))^1.08 * 'm^1.08/mol^1.08';
1169
1170	case "Klingberg":
1171	TRAYS(i).InletVapour.F * TRAYS(i).vV = PlateArea * sqrt(((TRAYS(i).InletVapour.P - TRAYS(i).OutletVapour.P)-TRAYS(i).rhoLgTRAYS(i).Level)/TRAYS(i).rhoV);
1172
1173	case "Wang_Fv":
1174	TRAYS(i).InletVapour.F * TRAYS(i).vV = PlateArea * sqrt(((TRAYS(i).InletVapour.P - TRAYS(i).OutletVapour.P)-TRAYS(i).rhoLgTRAYS(i).Level)/TRAYS(i).rhoV*DryPdropCoeff);
1175
1176	case "Elgue":
1177	TRAYS(i).InletVapour.F = sqrt((TRAYS(i).InletVapour.P - TRAYS(i).OutletVapour.P)/ElgueCoeff);
1178	end
1179	when TRAYS(i).InletVapour.F < 1e-6 * 'kmol/h' switchto "off";
1180
1181	case "off":
1182	TRAYS(i).InletVapour.F = 0 * 'mol/s';
1183	when TRAYS(i).InletVapour.P > TRAYS(i).OutletVapour.P switchto "on";
1184	end
1185
1186	end
1187
1188	end
1189
1190	Model Distillation_kettle_cond as ColumnBasic
1191
1192	ATTRIBUTES
1193	Pallete = true;
1194	Icon = "icon/DistillationKettleCond";
1195	Brief = "Model of a distillation column with dynamic condenser and dynamic reboiler.";
1196	Info =
1197	"== Specify ==
1198	* the feed stream of each tray (Inlet);
1199	* the Murphree eficiency for each tray Emv;
1200	* the pump pressure difference;
1201	* the heat supllied in reboiler and condenser;
1202	* the condenser vapor outlet flow (OutletVapour.F);
1203	* the reboiler liquid outlet flow (OutletLiquid.F);
1204	* both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
1205
1206	== Initial Conditions ==
1207	* the TRAYS temperature (OutletLiquid.T);
1208	* the TRAYS liquid level (Level) OR the TRAYS liquid flow (OutletLiquid.F);
1209	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions for each tray;
1210
1211	* the condenser temperature (OutletLiquid.T);
1212	* the condenser liquid level (Level);
1213	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions;
1214
1215	* the reboiler temperature (OutletLiquid.T);
1216	* the reboiler liquid level (Level);
1217	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions.
1218	";
1219
1220	SET
1221	NumberOfFeeds = 1;
1222
1223	VARIABLES
1224
1225	CONDENSER as condenser;
1226	REBOILER as reboiler;
1227	SPLITTER as splitter_column (Brief="splitter which separate reflux and distillate",Protected=true);
1228	PUMP as pump;
1229	RefluxRatio as positive (Brief="Reflux Ratio",Default=10, Lower = 0.5);
1230
1231	out TI_reb as control_signal (Brief="Temperature Indicator of Reboiler ",Protected = true, PosX=0.515, PosY=1);
1232	out LI_reb as control_signal (Brief="Level Indicator of Reboiler", Protected = true, PosX=1, PosY=0.935);
1233	out PI_reb as control_signal (Brief="Pressure Indicator of Reboiler", Protected = true, PosX=0.41, PosY=1);
1234
1235	out TI_cond as control_signal (Brief="Temperature Indicator of Condenser ", Protected = true, PosX=0.52, PosY=0);
1236	out LI_cond as control_signal (Brief="Level Indicator of Condenser", Protected = true, PosX=1, PosY=0.084);
1237	out PI_cond as control_signal (Brief="Pressure Indicator of Condenser", Protected = true, PosX=0.42, PosY=0);
1238
1239	in FeedTray as stream (Brief="Feed stream", PosX=0, PosY=0.55);
1240
1241
1242
1243	in HeatToReboiler as power (Brief="Heat supplied to Reboiler",Protected = true, PosX=1, PosY=0.855);
1244	in HeatToCondenser as power (Brief="Heat supplied to Condenser", Protected = true, PosX=1, PosY=0.01);
1245
1246
1247	ConnectorHeatReboiler as power (Brief="Heat supplied to Reboiler", Hidden=true);
1248	ConnectorHeatCondenser as power (Brief="Heat supplied to Condenser", Hidden=true);
1249
1250	in ConnectorCondenserVout as stream (Brief="Connector for Vapour outlet stream From Condenser", Hidden=true);
1251	in ConnectorReboilerLout as stream (Brief="Connector for Liquid outlet stream From Reboiler", Hidden=true);
1252	in ConnectorSplitterOut as stream (Brief="Connector for Liquid outlet stream From Top Splitter", Hidden=true);
1253
1254	out VapourDistillate as vapour_stream (Brief="Vapour outlet stream From Condenser", PosX=0.615, PosY=0);
1255	out LiquidDistillate as liquid_stream (Brief="Liquid outlet stream From Top Splitter", PosX=1, PosY=0.235);
1256	out BottomProduct as liquid_stream (Brief="Liquid outlet stream From Reboiler", PosX=0.62, PosY=1);
1257
1258	EQUATIONS
1259
1260	SPLITTER.RefluxRatio = RefluxRatio;
1261
1262	TI_reb = REBOILER.TI ;
1263	LI_reb = REBOILER.LI;
1264	PI_reb = REBOILER.PI;
1265
1266	TI_cond = CONDENSER.TI;
1267	LI_cond = CONDENSER.LI;
1268	PI_cond = CONDENSER.PI;
1269
1270	for i in 1:NumberOfTrays do
1271
1272	if i equal FeedTrayLocation(1) then
1273
1274	"FeedTrayTop Inlet Flow"
1275	FeedTray.F= TRAYS(i).Inlet.F;
1276
1277	"FeedTrayTop Inlet Temperature"
1278	FeedTray.T = TRAYS(i).Inlet.T;
1279
1280	"FeedTrayTop Inlet Pressure"
1281	FeedTray.P = TRAYS(i).Inlet.P;
1282
1283	"FeedTrayTop Inlet Composition"
1284	FeedTray.z = TRAYS(i).Inlet.z;
1285
1286	"FeedTrayTop Inlet Vapour Fraction"
1287	FeedTray.v = TRAYS(i).Inlet.v;
1288
1289	"FeedTrayTop Inlet Enthalpy"
1290	FeedTray.h = TRAYS(i).Inlet.h;
1291
1292	else
1293
1294	"Inlet Tray - Flow Sealed"
1295	0*'mol/h'= TRAYS(i).Inlet.F;
1296
1297	"Inlet Tray - Temperature"
1298	300*'K' = TRAYS(i).Inlet.T;
1299
1300	"Inlet Tray - Pressure"
1301	1*'atm' = TRAYS(i).Inlet.P;
1302
1303	"Inlet Tray - Composition"
1304	0.1 = TRAYS(i).Inlet.z;
1305
1306	"Inlet Tray - Vapour Fraction"
1307	0 = TRAYS(i).Inlet.v;
1308
1309	"Inlet Tray - Enthalpy"
1310	0*'J/mol' = TRAYS(i).Inlet.h;
1311
1312	end
1313
1314	end
1315
1316	# Condenser Connector Equations
1317	ConnectorCondenserVout.T = VapourDistillate.T;
1318	ConnectorCondenserVout.P = VapourDistillate.P;
1319	ConnectorCondenserVout.F = VapourDistillate.F;
1320	ConnectorCondenserVout.z = VapourDistillate.z;
1321
1322	# Splitter Connector Equations
1323	ConnectorSplitterOut.T = LiquidDistillate.T;
1324	ConnectorSplitterOut.P = LiquidDistillate.P;
1325	ConnectorSplitterOut.F = LiquidDistillate.F;
1326	ConnectorSplitterOut.z = LiquidDistillate.z;
1327
1328	# Reboiler Connector Equations
1329	ConnectorReboilerLout.T = BottomProduct.T;
1330	ConnectorReboilerLout.P = BottomProduct.P;
1331	ConnectorReboilerLout.F = BottomProduct.F;
1332	ConnectorReboilerLout.z = BottomProduct.z;
1333
1334	HeatToReboiler = ConnectorHeatReboiler;
1335	HeatToCondenser = ConnectorHeatCondenser;
1336
1337	CONNECTIONS
1338	#vapor
1339	REBOILER.OutletVapour to TRAYS(NumberOfTrays).InletVapour;
1340	TRAYS(1).OutletVapour to CONDENSER.InletVapour;
1341
1342	#liquid
1343	CONDENSER.OutletLiquid to SPLITTER.Inlet;
1344	SPLITTER.Reflux to PUMP.Inlet;
1345	PUMP.Outlet to TRAYS(1).InletLiquid;
1346	TRAYS(NumberOfTrays).OutletLiquid to REBOILER.InletLiquid;
1347
1348	#Connectors
1349	CONDENSER.OutletVapour to ConnectorCondenserVout;
1350	SPLITTER.Distillate to ConnectorSplitterOut;
1351	REBOILER.OutletLiquid to ConnectorReboilerLout;
1352
1353	ConnectorHeatReboiler to REBOILER.InletQ;
1354	ConnectorHeatCondenser to CONDENSER.InletQ;
1355
1356	end
1357
1358	Model Distillation_thermosyphon_subcooling as ColumnBasic
1359	ATTRIBUTES
1360	Pallete = true;
1361	Icon = "icon/DistillationThermosyphonSubcooling";
1362	Brief = "Model of a distillation column with steady condenser and steady reboiler.";
1363	Info =
1364	"== Specify ==
1365	* the feed stream of each tray (Inlet);
1366	* the Murphree eficiency for each tray Emv;
1367	* the pump head;
1368	* the condenser pressure drop;
1369	* the heat supllied in top and bottom tanks;
1370	* the heat supllied in condenser and reboiler;
1371	* the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product;
1372	* both top splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
1373
1374	== Initial Conditions ==
1375	* the TRAYS temperature (OutletLiquid.T);
1376	* the TRAYS liquid level (Level) OR the TRAYS liquid flow (OutletLiquid.F);
1377	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions for each tray;
1378
1379	* the top tank temperature (OutletLiquid.T);
1380	* the top tank liquid level (Level);
1381	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions;
1382
1383	* the bottom tank temperature (OutletLiquid.T);
1384	* the bottom tank liquid level (Level);
1385	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions.
1386	";
1387
1388	SET
1389
1390	NumberOfFeeds = 1;
1391
1392	VARIABLES
1393	CONDENSER as condenserSteady (Brief="steady state condenser with subcooling");
1394	REFLUX_DRUM as TankL (Brief="Reflux Drum");
1395	SPLITTER_TOP as splitter_column (Brief="splitter which separate reflux and distillate",Protected=true);
1396	PUMP as pump (Brief="pump in reflux stream");
1397	REBOILER as reboilerSteady (Brief="steady state reboiler (thermosyphon)");
1398	SUMP as SumpTank (Brief="vessel in the bottom of column");
1399	SPLITTER_BOTTOM as splitter2 (Brief="splitter to separate the bottom product and the stream to reboiler");
1400
1401	in FeedTray as stream (Brief="Feed stream", PosX=0, PosY=0.55);
1402
1403	RefluxRatio as positive (Brief="Reflux Ratio",Default=10, Lower = 0.5);
1404
1405	in Q_cond as power (Brief="Heat supplied to Condenser",PosX=1, PosY=0, Protected=true);
1406	in Q_reb as power (Brief="Heat supplied to Reboiler", PosX=1, PosY=0.96,Protected=true);
1407	in Q_drum as power (Brief="Heat supplied to Reflux Drum", PosX=1, PosY=0.30,Protected=true);
1408
1409	out TI_reb as control_signal (Brief="Temperature Indicator of Reboiler ",Protected = true, PosX=1, PosY=0.92);
1410	out PI_reb as control_signal (Brief="Pressure Indicator of Reboiler", Protected = true, PosX=1, PosY=0.875);
1411
1412	out TI_cond as control_signal (Brief="Temperature Indicator of Condenser ", Protected = true, PosX=0.52, PosY=0);
1413	out PI_cond as control_signal (Brief="Pressure Indicator of Condenser", Protected = true, PosX=0.42, PosY=0);
1414
1415	out TI_drum as control_signal (Brief="Temperature Indicator of Reflux Drum ", Protected = true, PosX=1, PosY=0.20);
1416	out PI_drum as control_signal (Brief="Pressure Indicator of Reflux Drum", Protected = true, PosX=1, PosY=0.155);
1417	out LI_drum as control_signal (Brief="Level Indicator of Reflux Drum", Protected = true, PosX=1, PosY=0.24);
1418
1419	out LI_sump as control_signal (Brief="Level Indicator of Column Sump", Protected = true, PosX=1, PosY=0.765);
1420	out TI_sump as control_signal (Brief="Temperature Indicator of Column Sump ",Protected = true, PosX=1, PosY=0.71);
1421
1422	out LiquidDistillate as liquid_stream (Brief="Liquid outlet stream From Top Splitter", PosX=1, PosY=0.33);
1423	out BottomProduct as liquid_stream (Brief="Liquid outlet stream From Bottom Splitter", PosX=0.06, PosY=1);
1424
1425	in ConnectorSplitterBottom as stream (Brief="Connector for Liquid outlet stream From Reboiler", Hidden=true);
1426	in ConnectorSplitterTop as stream (Brief="Connector for Liquid outlet stream From Top Splitter", Hidden=true);
1427
1428	ConnectorHeatReboiler as power (Brief="Connector for Heat supplied to Reboiler", Hidden=true);
1429	ConnectorHeatCondenser as power (Brief="Connector for Heat supplied to Condenser", Hidden=true);
1430	ConnectorHeatRefluxDrum as power (Brief="Connector for Heat supplied to Reflux Drum", Hidden=true);
1431
1432	EQUATIONS
1433
1434	SPLITTER_TOP.RefluxRatio = RefluxRatio;
1435	TI_reb = REBOILER.TI ;
1436	PI_reb = REBOILER.PI;
1437
1438	TI_cond = CONDENSER.TI;
1439	PI_cond = CONDENSER.PI;
1440
1441	TI_drum = REFLUX_DRUM.TI;
1442	PI_drum = REFLUX_DRUM.PI;
1443	LI_drum = REFLUX_DRUM.LI;
1444
1445	TI_sump = SUMP.TI;
1446	LI_sump = SUMP.LI;
1447
1448	for i in 1:NumberOfTrays do
1449
1450	if i equal FeedTrayLocation(1) then
1451
1452	"FeedTrayTop Inlet Flow"
1453	FeedTray.F= TRAYS(i).Inlet.F;
1454
1455	"FeedTrayTop Inlet Temperature"
1456	FeedTray.T = TRAYS(i).Inlet.T;
1457
1458	"FeedTrayTop Inlet Pressure"
1459	FeedTray.P = TRAYS(i).Inlet.P;
1460
1461	"FeedTrayTop Inlet Composition"
1462	FeedTray.z = TRAYS(i).Inlet.z;
1463
1464	"FeedTrayTop Inlet Vapour Fraction"
1465	FeedTray.v = TRAYS(i).Inlet.v;
1466
1467	"FeedTrayTop Inlet Enthalpy"
1468	FeedTray.h = TRAYS(i).Inlet.h;
1469
1470	else
1471
1472	"Inlet Tray - Flow Sealed"
1473	0*'mol/h'= TRAYS(i).Inlet.F;
1474
1475	"Inlet Tray - Temperature"
1476	300*'K' = TRAYS(i).Inlet.T;
1477
1478	"Inlet Tray - Pressure"
1479	1*'atm' = TRAYS(i).Inlet.P;
1480
1481	"Inlet Tray - Composition"
1482	0.1 = TRAYS(i).Inlet.z;
1483
1484	"Inlet Tray - Vapour Fraction"
1485	0 = TRAYS(i).Inlet.v;
1486
1487	"Inlet Tray - Enthalpy"
1488	0*'J/mol' = TRAYS(i).Inlet.h;
1489
1490	end
1491
1492	end
1493
1494	# Heat Connector Equations
1495	Q_cond = ConnectorHeatCondenser;
1496	Q_reb = ConnectorHeatReboiler;
1497	Q_drum = ConnectorHeatRefluxDrum;
1498
1499	# Top Splitter Connector Equations
1500	ConnectorSplitterTop.T = LiquidDistillate.T;
1501	ConnectorSplitterTop.P = LiquidDistillate.P;
1502	ConnectorSplitterTop.F = LiquidDistillate.F;
1503	ConnectorSplitterTop.z = LiquidDistillate.z;
1504
1505	# Bottom Splitter Connector Equations
1506	ConnectorSplitterBottom.T = BottomProduct.T;
1507	ConnectorSplitterBottom.P = BottomProduct.P;
1508	ConnectorSplitterBottom.F = BottomProduct.F;
1509	ConnectorSplitterBottom.z = BottomProduct.z;
1510
1511	CONNECTIONS
1512	#vapor
1513	REBOILER.OutletVapour to SUMP.InletVapour;
1514	SUMP.OutletVapour to TRAYS(NumberOfTrays).InletVapour;
1515	TRAYS(1).OutletVapour to CONDENSER.InletVapour;
1516
1517	#liquid
1518	CONDENSER.OutletLiquid to REFLUX_DRUM.Inlet;
1519	REFLUX_DRUM.OutletLiquid to SPLITTER_TOP.Inlet;
1520	SPLITTER_TOP.Reflux to PUMP.Inlet;
1521	PUMP.Outlet to TRAYS(1).InletLiquid;
1522	TRAYS(NumberOfTrays).OutletLiquid to SUMP.InletLiquid;
1523	SUMP.OutletLiquid to SPLITTER_BOTTOM.Inlet;
1524	SPLITTER_BOTTOM.Outlet2 to REBOILER.InletLiquid;
1525
1526	#Connectors
1527	ConnectorHeatCondenser to CONDENSER.InletQ;
1528	ConnectorHeatReboiler to REBOILER.InletQ;
1529	ConnectorHeatRefluxDrum to REFLUX_DRUM.InletQ;
1530	SPLITTER_TOP.Distillate to ConnectorSplitterTop;
1531	SPLITTER_BOTTOM.Outlet1 to ConnectorSplitterBottom;
1532
1533	end
1534
1535	Model Distillation_thermosyphon_cond as ColumnBasic
1536	ATTRIBUTES
1537	Pallete = true;
1538	Icon = "icon/DistillationThermosyphonCond";
1539	Brief = "Model of a distillation column with dynamic condenser and steady reboiler.";
1540	Info =
1541	"== Specify ==
1542	* the feed stream of each tray (Inlet);
1543	* the Murphree eficiency for each tray Emv;
1544	* the pump head;
1545	* the condenser vapor outlet flow (OutletVapour.F);
1546	* the heat supllied in bottom tank;
1547	* the heat supllied in condenser and reboiler;
1548	* the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product;
1549
1550	== Initial Conditions ==
1551	* the TRAYS temperature (OutletLiquid.T);
1552	* the TRAYS liquid level (Level) OR the TRAYS liquid flow (OutletLiquid.F);
1553	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions for each tray;
1554
1555	* the condenser temperature (OutletLiquid.T);
1556	* the condenser liquid level (Level);
1557	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions;
1558
1559	* the bottom tank temperature (OutletLiquid.T);
1560	* the bottom tank liquid level (Level);
1561	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions.
1562	";
1563
1564	SET
1565
1566	NumberOfFeeds = 1;
1567
1568	VARIABLES
1569	CONDENSER as condenser (Brief="dynamic condenser without subcooling");
1570	SPLITTER_TOP as splitter_column (Brief="splitter which separate reflux and distillate",Protected=true);
1571	PUMP as pump (Brief="pump in reflux stream");
1572	SUMP as SumpTank (Brief="vessel in the bottom of column");
1573	SPLITTER_BOTTOM as splitter2 (Brief="splitter who separate the bottom product and the stream to reboiler");
1574	REBOILER as reboilerSteady (Brief="steady state reboiler (thermosyphon)");
1575	RefluxRatio as positive (Brief="Reflux Ratio",Default=10, Lower = 0.5);
1576
1577	in FeedTray as stream (Brief="Feed stream", PosX=0, PosY=0.55);
1578
1579	in Q_cond as power (Brief="Heat supplied to Condenser",PosX=1, PosY=0, Protected=true);
1580	in Q_reb as power (Brief="Heat supplied to Reboiler", PosX=1, PosY=0.96,Protected=true);
1581
1582	out TI_cond as control_signal (Brief="Temperature Indicator of Condenser ", Protected = true, PosX=0.48, PosY=0);
1583	out LI_cond as control_signal (Brief="Level Indicator of Condenser", Protected = true, PosX=1, PosY=0.084);
1584	out PI_cond as control_signal (Brief="Pressure Indicator of Condenser", Protected = true, PosX=0.40, PosY=0);
1585
1586	out TI_reb as control_signal (Brief="Temperature Indicator of Reboiler ",Protected = true, PosX=1, PosY=0.92);
1587	out PI_reb as control_signal (Brief="Pressure Indicator of Reboiler", Protected = true, PosX=1, PosY=0.878);
1588
1589	out LI_sump as control_signal (Brief="Level Indicator of Column Sump", Protected = true, PosX=1, PosY=0.76);
1590	out TI_sump as control_signal (Brief="Temperature Indicator of Column Sump ",Protected = true, PosX=1, PosY=0.71);
1591
1592	out VapourDistillate as vapour_stream (Brief="Vapour outlet stream From Top Condenser", PosX=0.62, PosY=0);
1593	out LiquidDistillate as liquid_stream (Brief="Liquid outlet stream From Top Splitter", PosX=1, PosY=0.185);
1594	out BottomProduct as liquid_stream (Brief="Liquid outlet stream From Bottom Splitter", PosX=0.06, PosY=1);
1595
1596	in ConnectorSplitterBottom as stream (Brief="Connector for Liquid outlet stream From Reboiler", Hidden=true);
1597	in ConnectorSplitterTop as stream (Brief="Connector for Liquid outlet stream From Top Splitter", Hidden=true);
1598	in ConnectorCondenserVout as stream (Brief="Connector for Vapour outlet stream From Top Condenser", Hidden=true);
1599
1600	ConnectorHeatReboiler as power (Brief="Connector for Heat supplied to Reboiler", Hidden=true);
1601	ConnectorHeatCondenser as power (Brief="Connector for Heat supplied to Condenser", Hidden=true);
1602
1603	EQUATIONS
1604
1605	for i in 1:NumberOfTrays do
1606
1607	if i equal FeedTrayLocation(1) then
1608
1609	"FeedTrayTop Inlet Flow"
1610	FeedTray.F= TRAYS(i).Inlet.F;
1611
1612	"FeedTrayTop Inlet Temperature"
1613	FeedTray.T = TRAYS(i).Inlet.T;
1614
1615	"FeedTrayTop Inlet Pressure"
1616	FeedTray.P = TRAYS(i).Inlet.P;
1617
1618	"FeedTrayTop Inlet Composition"
1619	FeedTray.z = TRAYS(i).Inlet.z;
1620
1621	"FeedTrayTop Inlet Vapour Fraction"
1622	FeedTray.v = TRAYS(i).Inlet.v;
1623
1624	"FeedTrayTop Inlet Enthalpy"
1625	FeedTray.h = TRAYS(i).Inlet.h;
1626
1627	else
1628
1629	"Inlet Tray - Flow Sealed"
1630	0*'mol/h'= TRAYS(i).Inlet.F;
1631
1632	"Inlet Tray - Temperature"
1633	300*'K' = TRAYS(i).Inlet.T;
1634
1635	"Inlet Tray - Pressure"
1636	1*'atm' = TRAYS(i).Inlet.P;
1637
1638	"Inlet Tray - Composition"
1639	0.1 = TRAYS(i).Inlet.z;
1640
1641	"Inlet Tray - Vapour Fraction"
1642	0 = TRAYS(i).Inlet.v;
1643
1644	"Inlet Tray - Enthalpy"
1645	0*'J/mol' = TRAYS(i).Inlet.h;
1646
1647	end
1648
1649	end
1650
1651	SPLITTER_TOP.RefluxRatio = RefluxRatio;
1652
1653	TI_reb = REBOILER.TI ;
1654	PI_reb = REBOILER.PI;
1655
1656	TI_cond = CONDENSER.TI;
1657	PI_cond = CONDENSER.PI;
1658	LI_cond = CONDENSER.LI;
1659
1660	TI_sump = SUMP.TI;
1661	LI_sump = SUMP.LI;
1662
1663	# Heat Connector Equations
1664	Q_cond = ConnectorHeatCondenser;
1665	Q_reb = ConnectorHeatReboiler;
1666
1667	# Condenser Connector Equations
1668	ConnectorCondenserVout.T = VapourDistillate.T;
1669	ConnectorCondenserVout.P = VapourDistillate.P;
1670	ConnectorCondenserVout.F = VapourDistillate.F;
1671	ConnectorCondenserVout.z = VapourDistillate.z;
1672
1673	# Top Splitter Connector Equations
1674	ConnectorSplitterTop.T = LiquidDistillate.T;
1675	ConnectorSplitterTop.P = LiquidDistillate.P;
1676	ConnectorSplitterTop.F = LiquidDistillate.F;
1677	ConnectorSplitterTop.z = LiquidDistillate.z;
1678
1679	# Bottom Splitter Connector Equations
1680	ConnectorSplitterBottom.T = BottomProduct.T;
1681	ConnectorSplitterBottom.P = BottomProduct.P;
1682	ConnectorSplitterBottom.F = BottomProduct.F;
1683	ConnectorSplitterBottom.z = BottomProduct.z;
1684
1685	CONNECTIONS
1686	#vapor
1687	SUMP.OutletVapour to TRAYS(NumberOfTrays).InletVapour;
1688	REBOILER.OutletVapour to SUMP.InletVapour;
1689	TRAYS(1).OutletVapour to CONDENSER.InletVapour;
1690
1691	#liquid
1692	CONDENSER.OutletLiquid to SPLITTER_TOP.Inlet;
1693	SPLITTER_TOP.Reflux to PUMP.Inlet;
1694	PUMP.Outlet to TRAYS(1).InletLiquid;
1695	TRAYS(NumberOfTrays).OutletLiquid to SUMP.InletLiquid;
1696	SUMP.OutletLiquid to SPLITTER_BOTTOM.Inlet;
1697	SPLITTER_BOTTOM.Outlet2 to REBOILER.InletLiquid;
1698
1699	#Connectors
1700	ConnectorHeatCondenser to CONDENSER.InletQ;
1701	ConnectorHeatReboiler to REBOILER.InletQ;
1702	CONDENSER.OutletVapour to ConnectorCondenserVout;
1703	SPLITTER_TOP.Distillate to ConnectorSplitterTop;
1704	SPLITTER_BOTTOM.Outlet1 to ConnectorSplitterBottom;
1705
1706	end
1707
1708	Model Distillation_kettle_subcooling as ColumnBasic
1709
1710	ATTRIBUTES
1711	Pallete = true;
1712	Icon = "icon/DistillationKettleSubcooling";
1713	Brief = "Model of a distillation column with steady condenser and dynamic reboiler.";
1714	Info =
1715	"== Specify ==
1716	* the feed stream of each tray (Inlet);
1717	* the Murphree eficiency for each tray (Emv);
1718	* the pump pressure difference;
1719	* the heat supllied in reboiler and condenser;
1720	* the heat supllied in the top tank;
1721	* the condenser pressure drop;
1722	* the reboiler liquid outlet flow (OutletLiquid.F);
1723	* both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
1724
1725	== Initial Conditions ==
1726	* the TRAYS temperature (OutletLiquid.T);
1727	* the TRAYS liquid level (Level) OR the TRAYS liquid flow (OutletLiquid.F);
1728	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions for each tray;
1729
1730	* the top tank temperature (OutletLiquid.T);
1731	* the top tank liquid level (Level);
1732	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions;
1733
1734	* the reboiler temperature (OutletLiquid.T);
1735	* the reboiler liquid level (Level);
1736	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions.
1737	";
1738
1739	SET
1740
1741	NumberOfFeeds = 1;
1742
1743	VARIABLES
1744	CONDENSER as condenserSteady (Brief="steady state condenser with subcooling");
1745	REFLUX_DRUM as TankL (Brief="reflux drum");
1746	SPLITTER as splitter_column (Brief="splitter to separate reflux and distillate",Protected=true);
1747	PUMP as pump (Brief="pump in reflux stream");
1748	REBOILER as reboiler (Brief="kettle reboiler");
1749
1750	RefluxRatio as positive (Brief="Reflux Ratio",Default=10, Lower = 0.5);
1751
1752	in Q_cond as power (Brief="Heat supplied to Condenser", PosX=1, PosY=0.065, Protected=true);
1753	in Q_reb as power (Brief="Heat supplied to Reboiler", PosX=1, PosY=0.905, Protected=true);
1754	in Q_drum as power (Brief="Heat supplied to Top Vessel", PosX=1, PosY=0.30, Protected=true);
1755
1756	in FeedTray as stream (Brief="Feed stream", PosX=0, PosY=0.55);
1757
1758	out TI_reb as control_signal (Brief="Temperature Indicator of Reboiler ",Protected = true, PosX=0.515, PosY=1);
1759	out LI_reb as control_signal (Brief="Level Indicator of Reboiler", Protected = true, PosX=1, PosY=0.935);
1760	out PI_reb as control_signal (Brief="Pressure Indicator of Reboiler", Protected = true, PosX=0.41, PosY=1);
1761
1762	out TI_cond as control_signal (Brief="Temperature Indicator of Condenser ", Protected = true, PosX=0.52, PosY=0);
1763	out PI_cond as control_signal (Brief="Pressure Indicator of Condenser", Protected = true, PosX=0.42, PosY=0);
1764
1765	out TI_drum as control_signal (Brief="Temperature Indicator of Reflux Drum ", Protected = true, PosX=1, PosY=0.20);
1766	out PI_drum as control_signal (Brief="Pressure Indicator of Reflux Drum", Protected = true, PosX=1, PosY=0.155);
1767	out LI_drum as control_signal (Brief="Level Indicator of Reflux Drum", Protected = true, PosX=1, PosY=0.24);
1768
1769
1770	in ConnectorSplitterOut as stream (Brief="Connector for Liquid outlet stream From Top Splitter", Hidden=true);
1771	in ConnectorReboilerLout as stream (Brief="Connector for Liquid outlet stream From Reboiler", Hidden=true);
1772	ConnectorHeatReboiler as power (Brief="Connector for Heat supplied to Reboiler", Hidden=true);
1773	ConnectorHeatCondenser as power (Brief="Connector for Heat supplied to Condenser", Hidden=true);
1774	ConnectorHeatAccumulator as power (Brief="Connector for Heat supplied to TopVessel", Hidden=true);
1775
1776	out LiquidDistillate as liquid_stream (Brief="Liquid outlet stream From Top Splitter", PosX=1, PosY=0.33);
1777	out BottomProduct as liquid_stream (Brief="Liquid outlet stream From Reboiler", PosX=0.67, PosY=1);
1778
1779	EQUATIONS
1780
1781	SPLITTER.RefluxRatio = RefluxRatio;
1782
1783	TI_reb = REBOILER.TI ;
1784	PI_reb = REBOILER.PI;
1785	LI_reb = REBOILER.LI;
1786
1787	TI_cond = CONDENSER.TI;
1788	PI_cond = CONDENSER.PI;
1789
1790	TI_drum = REFLUX_DRUM.TI;
1791	PI_drum = REFLUX_DRUM.PI;
1792	LI_drum = REFLUX_DRUM.LI;
1793
1794	for i in 1:NumberOfTrays do
1795
1796	if i equal FeedTrayLocation(1) then
1797
1798	"FeedTrayTop Inlet Flow"
1799	FeedTray.F= TRAYS(i).Inlet.F;
1800
1801	"FeedTrayTop Inlet Temperature"
1802	FeedTray.T = TRAYS(i).Inlet.T;
1803
1804	"FeedTrayTop Inlet Pressure"
1805	FeedTray.P = TRAYS(i).Inlet.P;
1806
1807	"FeedTrayTop Inlet Composition"
1808	FeedTray.z = TRAYS(i).Inlet.z;
1809
1810	"FeedTrayTop Inlet Vapour Fraction"
1811	FeedTray.v = TRAYS(i).Inlet.v;
1812
1813	"FeedTrayTop Inlet Enthalpy"
1814	FeedTray.h = TRAYS(i).Inlet.h;
1815
1816	else
1817
1818	"Inlet Tray - Flow Sealed"
1819	0*'mol/h'= TRAYS(i).Inlet.F;
1820
1821	"Inlet Tray - Temperature"
1822	300*'K' = TRAYS(i).Inlet.T;
1823
1824	"Inlet Tray - Pressure"
1825	1*'atm' = TRAYS(i).Inlet.P;
1826
1827	"Inlet Tray - Composition"
1828	0.1 = TRAYS(i).Inlet.z;
1829
1830	"Inlet Tray - Vapour Fraction"
1831	0 = TRAYS(i).Inlet.v;
1832
1833	"Inlet Tray - Enthalpy"
1834	0*'J/mol' = TRAYS(i).Inlet.h;
1835
1836	end
1837
1838	end
1839
1840	#Heat Connectors
1841	Q_cond = ConnectorHeatCondenser;
1842	Q_reb = ConnectorHeatReboiler;
1843	Q_drum = ConnectorHeatAccumulator;
1844
1845	# Splitter Connector Equations
1846	ConnectorSplitterOut.T = LiquidDistillate.T;
1847	ConnectorSplitterOut.P = LiquidDistillate.P;
1848	ConnectorSplitterOut.F = LiquidDistillate.F;
1849	ConnectorSplitterOut.z = LiquidDistillate.z;
1850
1851	# Reboiler Connector Equations
1852	ConnectorReboilerLout.T = BottomProduct.T;
1853	ConnectorReboilerLout.P = BottomProduct.P;
1854	ConnectorReboilerLout.F = BottomProduct.F;
1855	ConnectorReboilerLout.z = BottomProduct.z;
1856
1857	CONNECTIONS
1858	#vapor
1859	REBOILER.OutletVapour to TRAYS(NumberOfTrays).InletVapour;
1860	TRAYS(1).OutletVapour to CONDENSER.InletVapour;
1861
1862	#liquid
1863	CONDENSER.OutletLiquid to REFLUX_DRUM.Inlet;
1864	REFLUX_DRUM.OutletLiquid to SPLITTER.Inlet;
1865	SPLITTER.Reflux to PUMP.Inlet;
1866	PUMP.Outlet to TRAYS(1).InletLiquid;
1867	TRAYS(NumberOfTrays).OutletLiquid to REBOILER.InletLiquid;
1868
1869	#Connectors
1870	ConnectorHeatCondenser to CONDENSER.InletQ;
1871	ConnectorHeatReboiler to REBOILER.InletQ;
1872	ConnectorHeatAccumulator to REFLUX_DRUM.InletQ;
1873
1874	SPLITTER.Distillate to ConnectorSplitterOut;
1875	REBOILER.OutletLiquid to ConnectorReboilerLout;
1876
1877	end
1878
1879	Model Rectifier as ColumnBasic
1880
1881	ATTRIBUTES
1882	Pallete = true;
1883	Icon = "icon/RefluxedCond";
1884	Brief = "Model of a rectifier column with dynamic condenser.";
1885	Info =
1886	"== Specify ==
1887	* the feed stream of each tray (Inlet);
1888	* the Murphree eficiency for each tray Emv;
1889	* the InletVapour stream of the bottom tray unless its flow;
1890	* the pump pressure difference;
1891	* the heat supllied in the condenser;
1892	* the condenser vapor outlet flow (OutletVapour.F);
1893	* both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
1894
1895	== Initial Conditions ==
1896	* the TRAYS temperature (OutletLiquid.T);
1897	* the TRAYS liquid level (Level) OR the TRAYS liquid flow (OutletLiquid.F);
1898	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions for each tray;
1899
1900	* the condenser temperature (OutletLiquid.T);
1901	* the condenser liquid level (Level);
1902	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions;
1903	";
1904
1905	SET
1906	NumberOfFeeds = 1;
1907
1908	VARIABLES
1909	CONDENSER as condenser (Brief="dymamic condenser without subcooling");
1910	SPLITTER as splitter2 (Brief="splitter which separate reflux and distillate");
1911	PUMP as pump (Brief="pump in reflux stream");
1912
1913	out TI_cond as control_signal (Brief="Temperature Indicator of Condenser ", Protected = true, PosX=0.52, PosY=0);
1914	out LI_cond as control_signal (Brief="Level Indicator of Condenser", Protected = true, PosX=1, PosY=0.084);
1915	out PI_cond as control_signal (Brief="Pressure Indicator of Condenser", Protected = true, PosX=0.42, PosY=0);
1916
1917	in FeedTray as stream (Brief="Feed stream", PosX=0, PosY=0.55);
1918
1919	out VapourDistillate as vapour_stream (Brief="Vapour outlet stream From Top Condenser", PosX=0.66, PosY=0);
1920	out LiquidDistillate as liquid_stream (Brief="Liquid outlet stream From Top Splitter", PosX=1, PosY=0.24);
1921
1922	in Q_cond as power (Brief="Heat supplied to Condenser",PosX=1, PosY=0.04, Protected = true);
1923
1924	in VapourInlet as stream (Brief="Vapour Inlet in the section", PosX=0.07, PosY=1);
1925	out LiquidOutlet as liquid_stream (Brief="Liquid Outlet in the section", PosX=0.32, PosY=1);
1926
1927	in ConnectorSplitterOut as stream (Brief="Connector for Liquid outlet stream From Top Splitter", Hidden=true);
1928	in ConnectorCondenserVout as stream (Brief="Connector for Vapour outlet stream From Top Condenser", Hidden=true);
1929	VapourConnector as stream (Brief="Vapour connection at the middle TRAYS", PosX=0.55, PosY=0,Hidden=true);
1930	ConnectorHeatCondenser as power (Brief="Connector for Heat supplied to Condenser", Hidden=true);
1931
1932	EQUATIONS
1933
1934	TI_cond = CONDENSER.TI;
1935	LI_cond = CONDENSER.LI;
1936	PI_cond = CONDENSER.PI;
1937
1938	for i in 1:NumberOfTrays do
1939
1940	if i equal FeedTrayLocation(1) then
1941
1942	"FeedTrayTop Inlet Flow"
1943	FeedTray.F= TRAYS(i).Inlet.F;
1944
1945	"FeedTrayTop Inlet Temperature"
1946	FeedTray.T = TRAYS(i).Inlet.T;
1947
1948	"FeedTrayTop Inlet Pressure"
1949	FeedTray.P = TRAYS(i).Inlet.P;
1950
1951	"FeedTrayTop Inlet Composition"
1952	FeedTray.z = TRAYS(i).Inlet.z;
1953
1954	"FeedTrayTop Inlet Vapour Fraction"
1955	FeedTray.v = TRAYS(i).Inlet.v;
1956
1957	"FeedTrayTop Inlet Enthalpy"
1958	FeedTray.h = TRAYS(i).Inlet.h;
1959
1960	else
1961
1962	"Inlet Tray - Flow Sealed"
1963	0*'mol/h'= TRAYS(i).Inlet.F;
1964
1965	"Inlet Tray - Temperature"
1966	300*'K' = TRAYS(i).Inlet.T;
1967
1968	"Inlet Tray - Pressure"
1969	1*'atm' = TRAYS(i).Inlet.P;
1970
1971	"Inlet Tray - Composition"
1972	0.1 = TRAYS(i).Inlet.z;
1973
1974	"Inlet Tray - Vapour Fraction"
1975	0 = TRAYS(i).Inlet.v;
1976
1977	"Inlet Tray - Enthalpy"
1978	0*'J/mol' = TRAYS(i).Inlet.h;
1979
1980	end
1981
1982	end
1983
1984	Q_cond = ConnectorHeatCondenser;
1985
1986	# Condenser Connector Equations
1987	ConnectorCondenserVout.T = VapourDistillate.T;
1988	ConnectorCondenserVout.P = VapourDistillate.P;
1989	ConnectorCondenserVout.F = VapourDistillate.F;
1990	ConnectorCondenserVout.z = VapourDistillate.z;
1991
1992	# Splitter Connector Equations
1993	ConnectorSplitterOut.T = LiquidDistillate.T;
1994	ConnectorSplitterOut.P = LiquidDistillate.P;
1995	ConnectorSplitterOut.F = LiquidDistillate.F;
1996	ConnectorSplitterOut.z = LiquidDistillate.z;
1997
1998	LiquidOutlet.F= TRAYS(NumberOfTrays).OutletLiquid.F;
1999	LiquidOutlet.T = TRAYS(NumberOfTrays).OutletLiquid.T;
2000	LiquidOutlet.P = TRAYS(NumberOfTrays).OutletLiquid.P;
2001	LiquidOutlet.z = TRAYS(NumberOfTrays).OutletLiquid.z;
2002
2003	VapourConnector.F= VapourInlet.F;
2004	VapourConnector.T = VapourInlet.T;
2005	VapourConnector.P = VapourInlet.P;
2006	VapourConnector.z = VapourInlet.z;
2007	VapourConnector.v = VapourInlet.v;
2008	VapourConnector.h = VapourInlet.h;
2009
2010	CONNECTIONS
2011	#vapor
2012	TRAYS(1).OutletVapour to CONDENSER.InletVapour;
2013
2014	#liquid
2015	CONDENSER.OutletLiquid to SPLITTER.Inlet;
2016	SPLITTER.Outlet2 to PUMP.Inlet;
2017	PUMP.Outlet to TRAYS(1).InletLiquid;
2018
2019	#Connectors
2020	ConnectorHeatCondenser to CONDENSER.InletQ;
2021	VapourConnector to TRAYS(NumberOfTrays).InletVapour;
2022	SPLITTER.Outlet1 to ConnectorSplitterOut;
2023	CONDENSER.OutletVapour to ConnectorCondenserVout;
2024
2025	end
2026
2027	Model PackedDistillation_kettle_cond as Packed_Section_ColumnBasic
2028	ATTRIBUTES
2029	Pallete = true;
2030	Icon = "icon/PackedDistillationKettleCond";
2031	Brief = "Model of a distillation column with dynamic condenser and dynamic reboiler.";
2032	Info =
2033	"== Specify ==
2034	* the feed stream of each tray (Inlet);
2035	* the pump pressure difference;
2036	* the total pressure drop (dP) of the packing;
2037	* the heat supllied in reboiler and condenser;
2038	* the condenser vapor outlet flow (OutletVapour.F);
2039	* the reboiler liquid outlet flow (OutletLiquid.F);
2040	* both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
2041
2042	== Initial Conditions ==
2043	* the stages temperature (OutletLiquid.T);
2044	* the stages initial molar holdup;
2045	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions for each stage;
2046
2047	* the condenser temperature (OutletLiquid.T);
2048	* the condenser liquid level (Level);
2049	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions;
2050
2051	* the reboiler temperature (OutletLiquid.T);
2052	* the reboiler liquid level (Level);
2053	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions.
2054	";
2055
2056	PARAMETERS
2057
2058	#VapourFlow as Switcher (Valid = ["on", "off"], Hidden = true ,Default = "on");
2059
2060	VARIABLES
2061	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2062	# Column Devices
2063	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2064	CONDENSER as condenser (Brief="dymamic condenser");
2065	REBOILER as reboiler (Brief="kettle reboiler");
2066	SPLITTER as splitter2 (Brief="splitter which separate reflux and distillate");
2067	PUMP as pump (Brief="pump in reflux stream");
2068	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2069	# Heat Ports
2070	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2071	in HeatToReboiler as power (Brief="Heat supplied to Reboiler",Protected = true, PosX=1, PosY=0.885);
2072	in HeatToCondenser as power (Brief="Heat supplied to Condenser", Protected = true, PosX=1, PosY=0.034);
2073	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2074	# Column Products
2075	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2076	out VapourDistillate as vapour_stream (Brief="Vapour outlet stream From Top Condenser", PosX=0.66, PosY=0);
2077	out LiquidDistillate as liquid_stream (Brief="Liquid outlet stream From Top Splitter", PosX=1, PosY=0.20);
2078	out BottomProduct as liquid_stream (Brief="Liquid outlet stream From Reboiler", PosX=0.68, PosY=1);
2079	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2080	# Column Connectors
2081	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2082	in ConnectorCondenserVout as stream (Brief="Connector for Vapour outlet stream From Top Condenser", Hidden=true);
2083	in ConnectorSplitterOut as stream (Brief="Connector for Liquid outlet stream From Top Splitter", Hidden=true);
2084	in ConnectorReboilerLout as stream (Brief="Connector for Liquid outlet stream From Reboiler", Hidden=true);
2085	ConnectorHeatReboiler as power (Brief="Heat supplied to Reboiler", Hidden=true);
2086	ConnectorHeatCondenser as power (Brief="Heat supplied to Condenser", Hidden=true);
2087
2088	CONNECTIONS
2089
2090	#vapor
2091	#REBOILER.OutletVapour to STAGES(NumberOfStages).VapourConnector;
2092	STAGES(1).OutletVapour to CONDENSER.InletVapour;
2093
2094	#liquid
2095	CONDENSER.OutletLiquid to SPLITTER.Inlet;
2096	SPLITTER.Outlet2 to PUMP.Inlet;
2097	#PUMP.Outlet to STAGES(1).InletLiquid;
2098	STAGES(NumberOfStages).OutletLiquid to REBOILER.InletLiquid;
2099
2100	#Connectors
2101	ConnectorHeatReboiler to REBOILER.InletQ;
2102	ConnectorHeatCondenser to CONDENSER.InletQ;
2103
2104	CONDENSER.OutletVapour to ConnectorCondenserVout;
2105	SPLITTER.Outlet1 to ConnectorSplitterOut;
2106	REBOILER.OutletLiquid to ConnectorReboilerLout;
2107
2108	EQUATIONS
2109	HeatToReboiler = ConnectorHeatReboiler;
2110	HeatToCondenser = ConnectorHeatCondenser;
2111
2112	# Condenser Connector Equations
2113	ConnectorCondenserVout.T = VapourDistillate.T;
2114	ConnectorCondenserVout.P = VapourDistillate.P;
2115	ConnectorCondenserVout.F = VapourDistillate.F;
2116	ConnectorCondenserVout.z = VapourDistillate.z;
2117
2118	# Splitter Connector Equations
2119	ConnectorSplitterOut.T = LiquidDistillate.T;
2120	ConnectorSplitterOut.P = LiquidDistillate.P;
2121	ConnectorSplitterOut.F = LiquidDistillate.F;
2122	ConnectorSplitterOut.z = LiquidDistillate.z;
2123
2124	# Reboiler Connector Equations
2125	ConnectorReboilerLout.T = BottomProduct.T;
2126	ConnectorReboilerLout.P = BottomProduct.P;
2127	ConnectorReboilerLout.F = BottomProduct.F;
2128	ConnectorReboilerLout.z = BottomProduct.z;
2129
2130	end
2131
2132	Model Rectifier_subcooling as Section_ColumnBasicX
2133
2134	ATTRIBUTES
2135	Pallete = true;
2136	Icon = "icon/RefluxedSubcooling";
2137	Brief = "Model of a rectifier column with steady condenser.";
2138	Info =
2139	"== Specify ==
2140	* the feed stream of each tray (Inlet);
2141	* the Murphree eficiency for each tray Emv;
2142	* the InletVapour stream of the bottom tray unless its flow;
2143	* the pump head;
2144	* the condenser pressure drop;
2145	* the heat supllied in the top tank;
2146	* the heat supllied in condenser;
2147	* both top splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
2148
2149	== Initial Conditions ==
2150	* the TRAYS temperature (OutletLiquid.T);
2151	* the TRAYS liquid level (Level) OR the TRAYS liquid flow (OutletLiquid.F);
2152	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions for each tray;
2153
2154	* the top tank temperature (OutletLiquid.T);
2155	* the top tank liquid level (Level);
2156	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions;
2157	";
2158
2159	PARAMETERS
2160	CondenserVapourFlow as Switcher (Valid = ["on", "off"], Default = "on",Hidden=true);
2161
2162	VARIABLES
2163	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2164	# Column Vapour and Liquid Draw Sides
2165	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2166	out VapourDrawOff as vapour_stream (Brief="Vapour Outlet in the section", PosX=1, PosY=0.485,Protected = true);
2167	out LiquidDrawOff as liquid_stream (Brief="Liquid Outlet in the section", PosX=1, PosY=0.535,Protected = true);
2168	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2169	# Column Devices
2170	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2171	CONDENSER as condenserSteady (Brief="steady state condenser with subcooling");
2172	ACCUMULATOR as tank_cylindrical (Brief="vessel drum (layed cilinder)");
2173	SPLITTER as splitter2 (Brief="plitter which separate reflux and distillate");
2174	PUMP as pump (Brief="pump in reflux stream");
2175	alfaTopo as Real;
2176	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2177	# Column Bottom outlets
2178	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2179	in VapourInlet as stream (Brief="Vapour Inlet in the section", PosX=0.07, PosY=1);
2180	out LiquidOutlet as liquid_stream (Brief="Liquid Outlet in the section", PosX=0.32, PosY=1);
2181	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2182	# Heat Ports
2183	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2184	in HeatToCondenser as power (Brief="Heat supplied to Condenser", PosX=1, PosY=0.070, Protected=true);
2185	in HeatToAccumulator as power (Brief="Heat supplied to Top Accumulator", PosX=1, PosY=0.23, Protected=true);
2186	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2187	# Column Top Product
2188	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2189	out LiquidDistillate as liquid_stream (Brief="Liquid outlet stream From Top Splitter", PosX=1, PosY=0.285);
2190	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2191	# Column Connectors
2192	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2193	in ConnectorSplitterTop as stream (Brief="Connector for Liquid outlet stream From Top Splitter", Hidden=true);
2194	VapourConnector as stream (Brief="Vapour connection at the middle TRAYS", PosX=0.55, PosY=0,Hidden=true);
2195	ConnectorHeatCondenser as power (Brief="Connector for Heat supplied to Condenser", Hidden=true);
2196	ConnectorHeatAccumulator as power (Brief="Connector for Heat supplied to Top Accumulator", Hidden=true);
2197
2198	EQUATIONS
2199	#Heat Connectors
2200	HeatToCondenser = ConnectorHeatCondenser;
2201	HeatToAccumulator = ConnectorHeatAccumulator;
2202
2203	LiquidOutlet.F= TRAYS(NumberOfTrays).OutletLiquid.F;
2204	LiquidOutlet.T = TRAYS(NumberOfTrays).OutletLiquid.T;
2205	LiquidOutlet.P = TRAYS(NumberOfTrays).OutletLiquid.P;
2206	LiquidOutlet.z = TRAYS(NumberOfTrays).OutletLiquid.z;
2207
2208	VapourConnector.F= VapourInlet.F;
2209	VapourConnector.T = VapourInlet.T;
2210	VapourConnector.P = VapourInlet.P;
2211	VapourConnector.z = VapourInlet.z;
2212	VapourConnector.v = VapourInlet.v;
2213	VapourConnector.h = VapourInlet.h;
2214
2215	# Splitter Connector Equations
2216	ConnectorSplitterTop.T = LiquidDistillate.T;
2217	ConnectorSplitterTop.P = LiquidDistillate.P;
2218	ConnectorSplitterTop.F = LiquidDistillate.F;
2219	ConnectorSplitterTop.z = LiquidDistillate.z;
2220
2221	VapourDrawOff.F*VapSideTrayIndex= TRAYS.VapourSideStream.F;
2222	VapourDrawOff.T = TRAYS(VapourSideStreamLocation).VapourSideStream.T;
2223	VapourDrawOff.P = TRAYS(VapourSideStreamLocation).VapourSideStream.P;
2224	VapourDrawOff.z = TRAYS(VapourSideStreamLocation).VapourSideStream.z;
2225
2226	LiquidDrawOff.F*LiqSideTrayIndex= TRAYS.LiquidSideStream.F;
2227	LiquidDrawOff.T = TRAYS(LiquidSideStreamLocation).LiquidSideStream.T;
2228	LiquidDrawOff.P = TRAYS(LiquidSideStreamLocation).LiquidSideStream.P;
2229	LiquidDrawOff.z = TRAYS(LiquidSideStreamLocation).LiquidSideStream.z;
2230
2231	VapourDrawOffFlow = VapourDrawOff.F;
2232	LiquidDrawOffFlow = LiquidDrawOff.F;
2233
2234	switch CondenserVapourFlow
2235
2236	case "on":
2237	CONDENSER.InletVapour.FTRAYS(1).vV = alfaTopo Ah * sqrt(2*(TRAYS(1).OutletVapour.P -
2238	CONDENSER.OutletLiquid.P + 1e-8 * 'atm') / (alfa*TRAYS(1).rhoV));
2239	when CONDENSER.InletVapour.F < 1e-6 * 'kmol/h' switchto "off";
2240
2241	case "off":
2242	CONDENSER.InletVapour.F = 0 * 'mol/s';
2243	when TRAYS(1).OutletVapour.P > CONDENSER.OutletLiquid.P + 1e-1 * 'atm' switchto "on";
2244
2245	end
2246
2247	CONNECTIONS
2248	#vapor
2249	TRAYS(1).OutletVapour to CONDENSER.InletVapour;
2250
2251	#liquid
2252	CONDENSER.OutletLiquid to ACCUMULATOR.Inlet;
2253	ACCUMULATOR.Outlet to SPLITTER.Inlet;
2254	SPLITTER.Outlet2 to PUMP.Inlet;
2255	PUMP.Outlet to TRAYS(1).InletLiquid;
2256
2257	#Connectors
2258	VapourConnector to TRAYS(NumberOfTrays).InletVapour;
2259	ConnectorHeatCondenser to CONDENSER.InletQ;
2260	SPLITTER.Outlet1 to ConnectorSplitterTop;
2261	ConnectorHeatAccumulator to ACCUMULATOR.InletQ;
2262
2263	end
2264
2265	Model Reboiled_Stripping_kettle as Section_ColumnBasicX
2266
2267	ATTRIBUTES
2268	Pallete = true;
2269	Icon = "icon/ReboiledKettle";
2270	Brief = "Model of a reboiled stripping column with dynamic reboiler.";
2271	Info =
2272	"== Specify ==
2273	* the feed stream of each tray (Inlet);
2274	* the Murphree eficiency for each tray Emv;
2275	* the vapour flow leaving the top of the column;
2276	* the InletLiquidiquid stream of the top tray;
2277	* the heat supllied in the reboiler;
2278	* the reboiler liquid outlet flow (OutletLiquid.F);
2279
2280	== Initial Conditions ==
2281	* the TRAYS temperature (OutletLiquid.T);
2282	* the TRAYS liquid level (Level) OR the TRAYS liquid flow (OutletLiquid.F);
2283	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions for each tray;
2284
2285	* the reboiler temperature (OutletLiquid.T);
2286	* the reboiler liquid level (Level);
2287	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions.
2288	";
2289
2290	VARIABLES
2291	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2292	# Column Vapour and Liquid Draw Sides
2293	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2294	out VapourDrawOff as vapour_stream (Brief="Vapour Outlet in the section", PosX=1, PosY=0.28,Protected = true);
2295	out LiquidDrawOff as liquid_stream (Brief="Liquid Outlet in the section", PosX=1, PosY=0.33,Protected = true);
2296	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2297	# Column Devices
2298	#+++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2299	REBOILER as reboiler (Brief="Kettle Reboiler");
2300	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2301	# Heat Port
2302	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2303	in HeatToReboiler as power (Brief="Heat supplied to Reboiler",PosX=1, PosY=0.865,Protected=true);
2304	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2305	# Column Top Outlets
2306	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2307	in LiquidInlet as stream (Brief="Liquid Inlet in the section", PosX=0.30, PosY=0);
2308	out VapourOutlet as vapour_stream (Brief="Vapour Outlet in the section", PosX=0.07, PosY=0);
2309	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2310	# Column Bottom Product
2311	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2312	out BottomProduct as liquid_stream (Brief="Liquid outlet stream From Reboiler", PosX=0.68, PosY=1);
2313	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2314	# Column Connectors
2315	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2316	in ConnectorReboilerLout as stream (Brief="Connector for Liquid outlet stream From Reboiler", Hidden=true);
2317	LiquidConnector as stream (Brief="Liquid connection at the middle TRAYS", PosX=0.75, PosY=1,Hidden=true);
2318	ConnectorHeatReboiler as power (Brief="Connector for Heat supplied to Reboiler", Hidden=true);
2319
2320	CONNECTIONS
2321	#vapor
2322	REBOILER.OutletVapour to TRAYS(NumberOfTrays).InletVapour;
2323
2324	#liquid
2325	TRAYS(NumberOfTrays).OutletLiquid to REBOILER.InletLiquid;
2326
2327	#Connectors
2328	REBOILER.OutletLiquid to ConnectorReboilerLout;
2329	LiquidConnector to TRAYS(1).InletLiquid;
2330	ConnectorHeatReboiler to REBOILER.InletQ;
2331
2332	EQUATIONS
2333	#Heat Connectors
2334	HeatToReboiler = ConnectorHeatReboiler;
2335
2336	LiquidConnector.F= LiquidInlet.F;
2337	LiquidConnector.T = LiquidInlet.T;
2338	LiquidConnector.P = LiquidInlet.P;
2339	LiquidConnector.z = LiquidInlet.z;
2340	LiquidConnector.v = LiquidInlet.v;
2341	LiquidConnector.h = LiquidInlet.h;
2342
2343	VapourOutlet.F= TRAYS(1).OutletVapour.F;
2344	VapourOutlet.T = TRAYS(1).OutletVapour.T;
2345	VapourOutlet.P = TRAYS(1).OutletVapour.P;
2346	VapourOutlet.z = TRAYS(1).OutletVapour.z;
2347
2348	# Reboiler Connector Equations
2349	ConnectorReboilerLout.T = BottomProduct.T;
2350	ConnectorReboilerLout.P = BottomProduct.P;
2351	ConnectorReboilerLout.F = BottomProduct.F;
2352	ConnectorReboilerLout.z = BottomProduct.z;
2353
2354	VapourDrawOff.F*VapSideTrayIndex= TRAYS.VapourSideStream.F;
2355	VapourDrawOff.T = TRAYS(VapourSideStreamLocation).VapourSideStream.T;
2356	VapourDrawOff.P = TRAYS(VapourSideStreamLocation).VapourSideStream.P;
2357	VapourDrawOff.z = TRAYS(VapourSideStreamLocation).VapourSideStream.z;
2358
2359	LiquidDrawOff.F*LiqSideTrayIndex= TRAYS.LiquidSideStream.F;
2360	LiquidDrawOff.T = TRAYS(LiquidSideStreamLocation).LiquidSideStream.T;
2361	LiquidDrawOff.P = TRAYS(LiquidSideStreamLocation).LiquidSideStream.P;
2362	LiquidDrawOff.z = TRAYS(LiquidSideStreamLocation).LiquidSideStream.z;
2363
2364	VapourDrawOffFlow = VapourDrawOff.F;
2365	LiquidDrawOffFlow = LiquidDrawOff.F;
2366
2367	end
2368
2369	Model Reboiled_Stripping_thermosyphon as Section_ColumnBasicX
2370
2371	ATTRIBUTES
2372	Pallete = true;
2373	Icon = "icon/ReboiledThermosyphon";
2374	Brief = "Model of a reboiled stripping column with steady reboiler.";
2375	Info =
2376	"== Specify ==
2377	* the feed stream of each tray (Inlet);
2378	* the Murphree eficiency for each tray (Emv);
2379	* the vapour flow leaving the top of the column;
2380	* the InletLiquidiquid stream of the top tray;
2381	* the heat supllied in bottom tank;
2382	* the heat supllied in the reboiler;
2383	* the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product;
2384
2385	== Initial Conditions ==
2386	* the TRAYS temperature (OutletLiquid.T);
2387	* the TRAYS liquid level (Level) OR the TRAYS liquid flow (OutletLiquid.F);
2388	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions for each tray;
2389
2390	* the bottom tank temperature (OutletLiquid.T);
2391	* the bottom tank liquid level (Level);
2392	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions.
2393	";
2394
2395	VARIABLES
2396	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2397	# Column Vapour and Liquid Draw Sides
2398	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2399	out VapourDrawOff as vapour_stream (Brief="Vapour Outlet in the section", PosX=1, PosY=0.28,Protected = true);
2400	out LiquidDrawOff as liquid_stream (Brief="Liquid Outlet in the section", PosX=1, PosY=0.33,Protected = true);
2401	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2402	# Column Devices
2403	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2404	REBOILER as reboilerSteady (Brief="steady state reboiler (thermosyphon)");
2405	SPLITTER as splitter2 (Brief="splitter which separate the bottom product and the stream to reboiler");
2406	ACCUMULATOR as tank (Brief="vessel in the bottom of column");
2407	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2408	# Heat Ports
2409	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2410	in HeatToReboiler as power (Brief="Heat supplied to Reboiler",PosX=1, PosY=0.84,Protected=true);
2411	in HeatToAccumulator as power (Brief="Heat supplied to Bottom Vessel",PosX=0, PosY=0.91,Protected=true);
2412	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2413	# Column Top Outlets
2414	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2415	in LiquidInlet as stream (Brief="Liquid Inlet in the section", PosX=0.32, PosY=0);
2416	out VapourOutlet as vapour_stream (Brief="Vapour Outlet in the section", PosX=0.07, PosY=0);
2417	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2418	# Column Bottom Product
2419	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2420	out BottomProduct as liquid_stream (Brief="Liquid outlet stream From Reboiler", PosX=0.19, PosY=1);
2421	LiquidConnector as stream (Brief="Liquid connection at the middle TRAYS", PosX=0.75, PosY=1,Hidden=true);
2422	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2423	# Column Connectors
2424	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2425	in ConnectorSplitterBottom as stream (Brief="Connector for Liquid outlet stream From Reboiler", Hidden=true);
2426	ConnectorHeatReboiler as power (Brief="Connector for Heat supplied to Reboiler", Hidden=true);
2427	ConnectorHeatAccumulator as power (Brief="Connector for Heat supplied to Bottom Accumulator", Hidden=true);
2428
2429	CONNECTIONS
2430	#vapor
2431	REBOILER.OutletVapour to TRAYS(NumberOfTrays).InletVapour;
2432
2433	#liquid
2434	TRAYS(NumberOfTrays).OutletLiquid to ACCUMULATOR.Inlet;
2435	ACCUMULATOR.Outlet to SPLITTER.Inlet;
2436	SPLITTER.Outlet2 to REBOILER.InletLiquid;
2437
2438	#Connectors
2439	LiquidConnector to TRAYS(1).InletLiquid;
2440	ConnectorHeatReboiler to REBOILER.InletQ;
2441	ConnectorHeatAccumulator to ACCUMULATOR.InletQ;
2442	SPLITTER.Outlet1 to ConnectorSplitterBottom;
2443
2444	EQUATIONS
2445	#Heat Connectors
2446	HeatToReboiler = ConnectorHeatReboiler;
2447	HeatToAccumulator = ConnectorHeatAccumulator;
2448
2449	ConnectorSplitterBottom.T = BottomProduct.T;
2450	ConnectorSplitterBottom.P = BottomProduct.P;
2451	ConnectorSplitterBottom.F = BottomProduct.F;
2452	ConnectorSplitterBottom.z = BottomProduct.z;
2453
2454	LiquidConnector.F= LiquidInlet.F;
2455	LiquidConnector.T = LiquidInlet.T;
2456	LiquidConnector.P = LiquidInlet.P;
2457	LiquidConnector.z = LiquidInlet.z;
2458	LiquidConnector.v = LiquidInlet.v;
2459	LiquidConnector.h = LiquidInlet.h;
2460
2461	VapourOutlet.F= TRAYS(1).OutletVapour.F;
2462	VapourOutlet.T = TRAYS(1).OutletVapour.T;
2463	VapourOutlet.P = TRAYS(1).OutletVapour.P;
2464	VapourOutlet.z = TRAYS(1).OutletVapour.z;
2465
2466	VapourDrawOff.F*VapSideTrayIndex= TRAYS.VapourSideStream.F;
2467	VapourDrawOff.T = TRAYS(VapourSideStreamLocation).VapourSideStream.T;
2468	VapourDrawOff.P = TRAYS(VapourSideStreamLocation).VapourSideStream.P;
2469	VapourDrawOff.z = TRAYS(VapourSideStreamLocation).VapourSideStream.z;
2470
2471	LiquidDrawOff.F*LiqSideTrayIndex= TRAYS.LiquidSideStream.F;
2472	LiquidDrawOff.T = TRAYS(LiquidSideStreamLocation).LiquidSideStream.T;
2473	LiquidDrawOff.P = TRAYS(LiquidSideStreamLocation).LiquidSideStream.P;
2474	LiquidDrawOff.z = TRAYS(LiquidSideStreamLocation).LiquidSideStream.z;
2475
2476	VapourDrawOffFlow = VapourDrawOff.F;
2477	LiquidDrawOffFlow = LiquidDrawOff.F;
2478
2479	end
2480
2481	Model ReactiveDistillation
2482
2483	ATTRIBUTES
2484	Pallete = true;
2485	Icon = "icon/DistillationReac";
2486	Brief = "Model of a reactive distillation column with dynamic condenser and reboiler.";
2487	Info =
2488	"== Specify ==
2489	* the reaction related variables for each tray, condenser and reboiler;
2490	* the feed stream of each tray (Inlet);
2491	* the Murphree eficiency for each tray Emv;
2492	* the pump pressure difference;
2493	* the heat supllied in reboiler and condenser;
2494	* the condenser vapor outlet flow (OutletVapour.F);
2495	* the reboiler liquid outlet flow (OutletLiquid.F);
2496	* both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
2497
2498	== Initial Conditions ==
2499	* the TRAYS temperature (OutletLiquid.T);
2500	* the TRAYS liquid level (Level) OR the TRAYS liquid flow (OutletLiquid.F);
2501	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions for each tray;
2502
2503	* the condenser temperature (OutletLiquid.T);
2504	* the condenser liquid level (Level);
2505	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions;
2506
2507	* the reboiler temperature (OutletLiquid.T);
2508	* the reboiler liquid level (Level);
2509	* (NoComps - 1) OutletLiquid (OR OutletVapour) compositions.
2510	";
2511
2512	PARAMETERS
2513	outer PP as Plugin (Type="PP");
2514	outer NComp as Integer (Brief="Number of Components");
2515	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2516	# Section Column Feed Tray - Side Streams Location and Numbering
2517	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2518	NumberOfTrays as Integer (Brief="Number of TRAYS", Default=2);
2519	FeedTrayIndex(NumberOfTrays) as Integer (Brief="Feed Tray Index", Default=0,Hidden=true);
2520	LiqSideTrayIndex(NumberOfTrays) as Integer (Brief="Liquid Side Tray Index", Default=0,Hidden=true);
2521	VapSideTrayIndex(NumberOfTrays) as Integer (Brief="Vapour Side Tray Index", Default=0,Hidden=true);
2522	FeedTrayLocation as Integer (Brief="Feed tray Location", Default=2);
2523	LiquidSideStreamLocation as Integer (Brief="Liquid Side Stream Location", Default=2);
2524	VapourSideStreamLocation as Integer (Brief="Vapour Side Stream Location", Default=2);
2525	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2526	# Section Column Flow Model for Liquid and Vapour
2527	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2528	VapourFlow as Switcher (Valid = ["on", "off"], Default = "off",Hidden=true);
2529	TrayVapourFlow as Switcher (Valid = ["on", "off"], Default = "off",Hidden=true);
2530	TrayLiquidFlow as Switcher (Valid = ["on", "off"], Default = "off",Hidden=true);
2531	alfacond as Real;
2532	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2533	# Section Column Tray Geometry and Auxiliar Parameters
2534	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2535	V as volume (Brief="Total Volume of the tray",Hidden=true);
2536	Q as power (Brief="Rate of heat supply",Hidden=true);
2537	Ap as area (Brief="Plate area = Atray - Adowncomer",Hidden=true);
2538	Ah as area (Brief="Total holes area",Hidden=true);
2539	lw as length (Brief="Weir length",Hidden=true);
2540	g as acceleration (Brief="Gravity Acceleration",Default=9.81,Hidden=true);
2541	hw as length (Brief="Weir height",Hidden=true);
2542	beta as fraction (Brief="Aeration fraction");
2543	alfa as fraction (Brief="Dry pressure drop coefficient");
2544
2545	VolumeOfTray as volume (Brief="Total Volume of the tray");
2546	HeatSupply as heat_rate (Brief="Rate of heat supply");
2547	PlateArea as area (Brief="Plate area = Atray - Adowncomer");
2548	HolesArea as area (Brief="Total holes area");
2549	WeirLength as length (Brief="Weir length");
2550	WeirHeight as length (Brief="Weir height");
2551
2552	stoic(NComp) as Real(Brief="Stoichiometric matrix");
2553	Hr as energy_mol;
2554
2555	SET
2556
2557	FeedTrayIndex(FeedTrayLocation) =1;
2558	VapSideTrayIndex(FeedTrayLocation) =1;
2559	LiqSideTrayIndex(FeedTrayLocation) =1;
2560
2561	V=VolumeOfTray;
2562	Q=HeatSupply;
2563	Ap=PlateArea;
2564	Ah=HolesArea;
2565	lw=WeirLength;
2566	hw=WeirHeight ;
2567
2568	VARIABLES
2569	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2570	# Tray Initialization For the Whole Column Section
2571	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2572	INITIALIZATION as InitializeSection (Brief = "Column Model Initialization");
2573	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2574	# Column Feed - Side Stream Flow and Murphree Efficiency
2575	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2576	in FeedTray as stream (Brief="Feed stream", PosX=0, PosY=0.55);
2577	VapourDrawOffFlow as flow_mol (Brief = "Stream Molar Flow Rate");
2578	LiquidDrawOffFlow as flow_mol (Brief = "Stream Molar Flow Rate");
2579	MurphreeEff as Real (Brief = "Murphree efficiency");
2580	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2581	# Column Vapour and Liquid Draw Sides
2582	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2583	out VapourDrawOff as vapour_stream (Brief="Vapour Outlet in the section", PosX=1, PosY=0.395,Protected = true);
2584	out LiquidDrawOff as liquid_stream (Brief="Liquid Outlet in the section", PosX=1, PosY=0.44,Protected = true);
2585	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2586	# Heat Ports
2587	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2588	in HeatToReboiler as power (Brief="Heat supplied to Reboiler", PosX=1, PosY=0.89);
2589	in HeatToCondenser as power (Brief="Heat supplied to Condenser", PosX=1, PosY=0.07);
2590	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2591	# Column Devices
2592	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2593	TRAYS(NumberOfTrays) as trayReac;
2594	CONDENSER as condenserReact;
2595	REBOILER as reboilerReact;
2596	SPLITTER as splitter2;
2597	PUMP as pump;
2598	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2599	# Column Outlets
2600	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2601	out VapourDistillate as vapour_stream (Brief="Vapour outlet stream From Condenser", PosX=0.59, PosY=0);
2602	out LiquidDistillate as liquid_stream (Brief="Liquid outlet stream From Splitter", PosX=1, PosY=0.23);
2603	out BottomProduct as liquid_stream (Brief="Liquid outlet stream From Reboiler", PosX=0.67, PosY=1);
2604	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2605	# Column Connectors
2606	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2607	in ConnectorCondenserVout as stream (Brief="Connector for Vapour outlet stream From Top Condenser", Hidden=true);
2608	in ConnectorSplitterOut as stream (Brief="Connector for Liquid outlet stream From Top Splitter", Hidden=true);
2609	in ConnectorReboilerLout as stream (Brief="Connector for Liquid outlet stream From Reboiler", Hidden=true);
2610	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2611	# Column Control Ports
2612	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2613	out TRI as control_signal (Brief="Temperature of Reboiler Indicator", PosX=1, PosY=0.83);
2614	out LRI as control_signal (Brief="Level of Reboiler Indicator", PosX=1, PosY=0.855);
2615	out TCI as control_signal (Brief="Temperature of Condenser Indicator", PosX=1, PosY=0.01);
2616	out LCI as control_signal (Brief="Level of Condenser Indicator", PosX=1, PosY=0.04);
2617
2618	CONNECTIONS
2619	#vapor
2620	REBOILER.OutletVapour to TRAYS(NumberOfTrays).InletVapour;
2621	TRAYS(1).OutletVapour to CONDENSER.InletVapour;
2622	TRAYS([2:NumberOfTrays]).OutletVapour to TRAYS([1:NumberOfTrays-1]).InletVapour;
2623
2624	#liquid
2625	CONDENSER.OutletLiquid to SPLITTER.Inlet;
2626	SPLITTER.Outlet2 to PUMP.Inlet;
2627	PUMP.Outlet to TRAYS(1).InletLiquid;
2628	TRAYS([1:NumberOfTrays-1]).OutletLiquid to TRAYS([2:NumberOfTrays]).InletLiquid;
2629	TRAYS(NumberOfTrays).OutletLiquid to REBOILER.InletLiquid;
2630
2631	#Connectors
2632	CONDENSER.OutletVapour to ConnectorCondenserVout;
2633	SPLITTER.Outlet1 to ConnectorSplitterOut;
2634	REBOILER.OutletLiquid to ConnectorReboilerLout;
2635
2636	INITIAL
2637	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2638	# Tray Initialization
2639	#++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
2640	for i in 1:NumberOfTrays do
2641
2642	"The initial temperature of the TRAYS"
2643	TRAYS(i).OutletLiquid.T = INITIALIZATION.TopTemperature+(INITIALIZATION.BottomTemperature-INITIALIZATION.TopTemperature)*((i-1)/(NumberOfTrays-1));
2644
2645	"The initial Level of the TRAYS"
2646	TRAYS(i).Level = INITIALIZATION.LevelFraction*hw;
2647	end
2648
2649	for i in 1:NComp-1 do
2650
2651	for j in 1:NumberOfTrays do
2652
2653	"The initial composition of the TRAYS - Normalized"
2654	TRAYS(j).OutletLiquid.z(i) = INITIALIZATION.TopComposition(i)/sum(INITIALIZATION.TopComposition) +(INITIALIZATION.BottomComposition(i)/sum(INITIALIZATION.BottomComposition)-INITIALIZATION.TopComposition(i)/sum(INITIALIZATION.TopComposition) )*((j-1)/(NumberOfTrays-1));
2655	end
2656
2657	end
2658
2659	EQUATIONS
2660
2661	for i in [1:NumberOfTrays] do
2662
2663	"Murphree Efficiency"
2664	TRAYS(i).OutletVapour.z = MurphreeEff * (TRAYS(i).yideal - TRAYS(i).InletVapour.z) + TRAYS(i).InletVapour.z;
2665
2666	"Energy Holdup"
2667	TRAYS(i).E = TRAYS(i).MLTRAYS(i).OutletLiquid.h + TRAYS(i).MVTRAYS(i).OutletVapour.h - TRAYS(i).OutletLiquid.P*V;
2668
2669	"Component Molar Balance"
2670	diff(TRAYS(i).M)=TRAYS(i).Inlet.FTRAYS(i).Inlet.z + TRAYS(i).InletLiquid.FTRAYS(i).InletLiquid.z + TRAYS(i).InletVapour.FTRAYS(i).InletVapour.z- TRAYS(i).OutletLiquid.FTRAYS(i).OutletLiquid.z - TRAYS(i).OutletVapour.F*TRAYS(i).OutletVapour.z-
2671	TRAYS(i).LiquidSideStream.FTRAYS(i).LiquidSideStream.z-TRAYS(i).VapourSideStream.FTRAYS(i).VapourSideStream.z + stoicTRAYS(i).r3TRAYS(i).ML*TRAYS(i).vL;
2672
2673	"Energy Balance"
2674	diff(TRAYS(i).E) = ( TRAYS(i).Inlet.FTRAYS(i).Inlet.h + TRAYS(i).InletLiquid.FTRAYS(i).InletLiquid.h + TRAYS(i).InletVapour.FTRAYS(i).InletVapour.h- TRAYS(i).OutletLiquid.FTRAYS(i).OutletLiquid.h - TRAYS(i).OutletVapour.F*TRAYS(i).OutletVapour.h
2675	-TRAYS(i).VapourSideStream.FTRAYS(i).VapourSideStream.h - TRAYS(i).LiquidSideStream.FTRAYS(i).LiquidSideStream.h + Q ) + Hr * TRAYS(i).r3 TRAYS(i). vLTRAYS(i).ML;
2676
2677	"Level of clear liquid over the weir"
2678	TRAYS(i).Level = TRAYS(i).ML*TRAYS(i).vL/Ap;
2679
2680	"Geometry Constraint"
2681	V = TRAYS(i).ML* TRAYS(i).vL + TRAYS(i).MV*TRAYS(i).vV;
2682
2683	end
2684
2685	switch VapourFlow
2686	case "on":
2687	"Pressure Drop through the condenser"
2688	CONDENSER.InletVapour.F*TRAYS(1).vV / 'm^2' =
2689	sqrt((TRAYS(1).OutletVapour.P - CONDENSER.OutletLiquid.P + 1e-8 * 'atm')/(TRAYS(1).rhoV*alfacond));
2690	when TRAYS(1).OutletVapour.P < CONDENSER.OutletLiquid.P switchto "off";
2691
2692	case "off":
2693	"Prato selado"
2694	CONDENSER.InletVapour.F = 0.0 * 'mol/s';
2695	when TRAYS(1).OutletVapour.P > CONDENSER.OutletLiquid.P + 1e-3 * 'atm' switchto "on";
2696	end
2697
2698	for i in [1:NumberOfTrays] do
2699
2700	switch TrayLiquidFlow
2701	case "on":
2702	"Francis Equation"
2703	TRAYS(i).OutletLiquid.FTRAYS(i).vL = 1.84'1/s'lw((TRAYS(i).Level-(betahw)+1e-6'm')/(beta))^2;
2704	when TRAYS(i).Level < (beta * hw) switchto "off";
2705
2706	case "off":
2707	"Low level"
2708	TRAYS(i).OutletLiquid.F = 0 * 'mol/h';
2709	when TRAYS(i).Level > (beta * hw) + 1e-6*'m' switchto "on";
2710	end
2711
2712	switch TrayVapourFlow
2713	case "on":
2714	TRAYS(i).InletVapour.FTRAYS(i).vV = sqrt((TRAYS(i).InletVapour.P - TRAYS(i).OutletVapour.P - TRAYS(i).LevelgTRAYS(i).rhoL + 1e-8 'atm')/(TRAYS(i).rhoValfa))Ah;
2715	when TRAYS(i).InletVapour.P < TRAYS(i).OutletVapour.P + TRAYS(i).LevelgTRAYS(i).rhoL switchto "off";
2716
2717	case "off":
2718	TRAYS(i).InletVapour.F = 0 * 'mol/s';
2719	when TRAYS(i).InletVapour.P > TRAYS(i).OutletVapour.P + TRAYS(i).LevelgTRAYS(i).rhoL + 3e-2 * 'atm' switchto "on";
2720	end
2721
2722	end
2723
2724	# Connecting Trays
2725	FeedTray.F*FeedTrayIndex= TRAYS.Inlet.F;
2726	FeedTray.T = TRAYS.Inlet.T;
2727	FeedTray.P = TRAYS.Inlet.P;
2728	FeedTray.z = TRAYS.Inlet.z;
2729	FeedTray.v = TRAYS.Inlet.v;
2730	FeedTray.h = TRAYS.Inlet.h;
2731
2732	HeatToReboiler = REBOILER.InletQ;
2733	HeatToCondenser = CONDENSER.InletQ;
2734
2735	"Reboiler Temperature indicator"
2736	TRI * 'K' = REBOILER.OutletLiquid.T;
2737
2738	"Reboiler Level indicator"
2739	LRIREBOILER.V = REBOILER.LevelREBOILER.Across;
2740
2741	"Condenser Temperature indicator"
2742	TCI * 'K' = CONDENSER.OutletLiquid.T;
2743
2744	"Condenser Level indicator"
2745	LCICONDENSER.V = CONDENSER.LevelCONDENSER.Across;
2746
2747	# Condenser Connector Equations
2748	ConnectorCondenserVout.T = VapourDistillate.T;
2749	ConnectorCondenserVout.P = VapourDistillate.P;
2750	ConnectorCondenserVout.F = VapourDistillate.F;
2751	ConnectorCondenserVout.z = VapourDistillate.z;
2752
2753	# Splitter Connector Equations
2754	ConnectorSplitterOut.T = LiquidDistillate.T;
2755	ConnectorSplitterOut.P = LiquidDistillate.P;
2756	ConnectorSplitterOut.F = LiquidDistillate.F;
2757	ConnectorSplitterOut.z = LiquidDistillate.z;
2758
2759	# Reboiler Connector Equations
2760	ConnectorReboilerLout.T = BottomProduct.T;
2761	ConnectorReboilerLout.P = BottomProduct.P;
2762	ConnectorReboilerLout.F = BottomProduct.F;
2763	ConnectorReboilerLout.z = BottomProduct.z;
2764
2765	VapourDrawOff.F*VapSideTrayIndex= TRAYS.VapourSideStream.F;
2766	VapourDrawOff.T = TRAYS(VapourSideStreamLocation).VapourSideStream.T;
2767	VapourDrawOff.P = TRAYS(VapourSideStreamLocation).VapourSideStream.P;
2768	VapourDrawOff.z = TRAYS(VapourSideStreamLocation).VapourSideStream.z;
2769
2770	LiquidDrawOff.F*LiqSideTrayIndex= TRAYS.LiquidSideStream.F;
2771	LiquidDrawOff.T = TRAYS(LiquidSideStreamLocation).LiquidSideStream.T;
2772	LiquidDrawOff.P = TRAYS(LiquidSideStreamLocation).LiquidSideStream.P;
2773	LiquidDrawOff.z = TRAYS(LiquidSideStreamLocation).LiquidSideStream.z;
2774
2775	VapourDrawOffFlow = VapourDrawOff.F;
2776	LiquidDrawOffFlow = LiquidDrawOff.F;
2777
2778	end
2779
2780	*#

Note: See TracBrowser for help on using the repository browser.

Download in other formats:

Original Format