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sample_tray.mso @ 791

Last change on this file since 791 was 521, checked in by Argimiro Resende Secchi, 15 years ago
merging tray versions.
Property svn:eol-style set to `native` Property svn:keywords set to `Id`
File size: 6.2 KB

Rev	Line
[86]	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	* Sample file for model tray
	17	*--------------------------------------------------------------------
	18	*
	19	* This sample file needs VRTherm DEMO (www.vrtech.com.br) to run.
	20	*
	21	*----------------------------------------------------------------------
	22	* Author: Paula B. Staudt
	23	* $Id: sample_tray.mso 521 2008-05-21 23:20:47Z arge $
	24	--------------------------------------------------------------------#
[1]	25	using "stage_separators/tray";
	26
	27	FlowSheet tray_Test
	28	PARAMETERS
[213]	29	PP as Plugin(Brief="Physical Properties",
	30	Type="PP",
	31	Components = [ "n-pentane", "benzene"],
	32	LiquidModel = "PR",
	33	VapourModel = "PR"
	34	);
[1]	35	NComp as Integer;
	36
	37	SET
	38	NComp = PP.NumberOfComponents;
	39
	40	DEVICES
	41	t1 as tray;
[202]	42	feed as source;
	43	inL as liquid_stream;
	44	inV as vapour_stream;
[1]	45
	46	CONNECTIONS
[208]	47	feed.Outlet to t1.Inlet;
[1]	48	inL to t1.InletL;
	49	inV to t1.InletV;
	50
	51	SPECIFY
[202]	52	feed.Outlet.F = 113.4 * 'kmol/h';
	53	feed.Outlet.T = 291 * 'K';
	54	feed.Outlet.P = 1.66 * 'atm';
	55	feed.Outlet.z = [0.5, 0.5];
[1]	56
[202]	57	inL.P = 165 * 'kPa';
	58	inL.T = 310 * 'K';
	59	inL.F = 61.99 * 'kmol/h';
[1]	60	inL.z = [0.1641, 0.8359];
	61
[202]	62	inV.P = 150 * 'kPa';
	63	inV.T = 321 * 'K';
[1]	64	inV.z = [0.0584, 0.9416];
[202]	65
[1]	66	t1.Emv = 1;
[202]	67	t1.OutletV.F = 147.1 * 'kmol/h';
[1]	68
	69	SET
[202]	70	t1.V = 4 * 'ft^3';
	71	t1.Ah = 0.394 * 'ft^2';
	72	t1.lw = 20.94 * 'in';
	73	t1.hw = 0.125 * 'ft';
	74	t1.Q = 0 * 'kW';
[521]	75	t1.beta = 1;
[1]	76	t1.alfa = 4;
[202]	77	t1.Ap = 3.94 * 'ft^2';
[1]	78
[521]	79	t1.VapourFlowModel = "Feehery_Fv"; #"Roffel_Fv" "Klingberg" "Wang_Fv" "Elgue" or "Reepmeyer"-> default
	80	t1.w = 0.5 * '1/m^4';
	81
	82	t1.LiquidFlowModel = "Wang_Fl"; # "Feehery_Fl" "Roffel_Fl" "Olsen" or "default"
	83
[1]	84	INITIAL
[202]	85	t1.OutletL.T = 290 *'K';
[1]	86	t1.Level = 0.9 * t1.hw;
	87	t1.OutletL.z(1) = 0.5;
	88
	89	OPTIONS
[202]	90	TimeEnd = 100;
[1]	91	end
[498]	92
	93	FlowSheet packedStage_Test_1
	94	PARAMETERS
	95	PP as Plugin(Brief="Physical Properties",
	96	Type="PP",
	97	Components = [ "n-pentane", "benzene"],
	98	LiquidModel = "PR",
	99	VapourModel = "PR"
	100	);
	101	NComp as Integer;
	102
	103	SET
	104	NComp = PP.NumberOfComponents;
	105
	106	DEVICES
	107	t1 as packedStage;
	108	feed as source;
	109	inL as liquid_stream;
	110	inV as vapour_stream;
	111
	112	CONNECTIONS
	113	feed.Outlet to t1.Inlet;
	114	inL to t1.InletL;
	115	inV to t1.InletV;
	116
	117	SPECIFY
	118	feed.Outlet.F = 113.4 * 'kmol/h';
	119	feed.Outlet.T = 291 * 'K';
	120	feed.Outlet.P = 1.66 * 'atm';
	121	feed.Outlet.z = [0.5, 0.5];
	122
	123	inL.P = 165 * 'kPa';
	124	inL.T = 315 * 'K';
	125	inL.F = 61.99 * 'kmol/h';
	126	inL.z = [0.1641, 0.8359];
	127
	128	inV.F = 201.25 * 'kmol/h';
	129	inV.P = 150 * 'kPa';
	130	inV.T = 315 * 'K';
	131	inV.z = [0.0584, 0.9416];
	132
	133	t1.OutletV.P = 145 * 'kPa';
	134
	135	SET
	136	#Metal Pall Ring - nominal packing size 50 mm - Billet and Schultes, 1999.
	137	t1.Q = 0 * 'kW';
	138	t1.V = 0.8 * 'm^2' * 0.4 * 'm';
	139	t1.d = 1.009 * 'm';
	140	t1.Cpo = 0.763;
	141	t1.e = 0.951;
	142	t1.a = 112.6 * 'm^2/m^3';
	143	t1.hs = 0.4 * 'm';
	144	t1.Qsil = 10;
	145
	146	INITIAL
	147	t1.OutletL.T = 315 *'K';
	148	t1.ML = 0.25 * 'kmol';
	149	t1.OutletL.z(1) = 0.1641;
	150
	151	OPTIONS
	152	DAESolver(File="sundials");
	153	TimeStep = 0.001;
	154	TimeEnd = 0.1;
	155	end
	156
	157	FlowSheet packedStage_Test_2
	158	PARAMETERS
	159	PP as Plugin(Brief="Physical Properties",
	160	Type="PP",
	161	Components = [ "isobutane", "n-pentane", "propylene",
	162	"benzene", "isobutene" ],
	163	LiquidModel = "PR",
	164	VapourModel = "PR"
	165	);
	166	NComp as Integer;
	167
	168	SET
	169	NComp = PP.NumberOfComponents;
	170
	171	DEVICES
	172	t1 as packedStage;
	173	feed as source;
	174	inL as liquid_stream;
	175	inV as vapour_stream;
	176
	177	CONNECTIONS
	178	feed.Outlet to t1.Inlet;
	179	inL to t1.InletL;
	180	inV to t1.InletV;
	181
	182	SPECIFY
	183	feed.Outlet.F = 0 * 'kmol/h';
	184	feed.Outlet.T = 300 * 'K';
	185	feed.Outlet.P = 1.66 * 'atm';
	186	feed.Outlet.z = [0.226, 0.425, 0.035, 0.025, 0.289];
	187
	188	inL.F = 71.21 * 'kmol/h';
	189	inL.P = 2.22 * 'atm';
	190	inL.T = 297.6 * 'K';
	191	inL.z = [0.226, 0.425, 0.035, 0.025, 0.289];
	192
	193	inV.F = 175.3 * 'kmol/h';
	194	inV.P = 2.3062 * 'atm';
	195	inV.T = 308.3 * 'K';
	196	inV.z = [0.265, 0.233, 0.150, 0.014, 0.338];
	197
	198	t1.deltaP = 0.01 * 'atm';
	199
	200	SET
	201	#Metal Pall Ring - nominal packing size 50 mm - Billet and Schultes, 1999.
	202	t1.Q = 0 * 'kW';
	203	t1.Cpo = 0.763;
	204	t1.e = 0.951;
	205	t1.a = 112.6 * 'm^2/m^3';
	206
	207	t1.V = 4 * 'ft^2' * 1 * 'ft';
	208	t1.hs = 1 * 'ft';
	209	t1.d = 2.26 * 'ft';
	210	t1.Qsil = 10;
	211
	212	INITIAL
	213	t1.OutletL.T = 290 *'K';
	214	t1.ML = 0.02 * 'kmol';
	215	t1.OutletL.z([1:4]) = [0.226, 0.425, 0.035, 0.025];
	216
	217	OPTIONS
	218	DAESolver(File="sundials");
	219	TimeStep = 10;
	220	TimeEnd = 100;
	221	end
[506]	222
	223	FlowSheet trayRate_Test
	224	PARAMETERS
	225	PP as Plugin(Brief="Physical Properties",
	226	Type="PP",
	227	Components = [ "n-pentane", "benzene"],
	228	LiquidModel = "PR",
	229	VapourModel = "PR"
	230	);
	231	NComp as Integer;
	232
	233	SET
	234	NComp = PP.NumberOfComponents;
	235
	236	DEVICES
	237	t1 as trayRate;
	238	feed as source;
	239	feedV as source;
	240	inL as liquid_stream;
	241	inV as vapour_stream;
	242
	243	CONNECTIONS
	244	feed.Outlet to t1.Inlet;
	245	feedV.Outlet to t1.InletFV;
	246	inL to t1.InletL;
	247	inV to t1.InletV;
	248
	249	SPECIFY
[517]	250	feed.Outlet.F = 116 * 'kmol/h';
	251	feed.Outlet.T = 280 * 'K';
	252	feed.Outlet.P = 150 * 'kPa';
[506]	253	feed.Outlet.z = [0.5, 0.5];
[517]	254
[506]	255	feedV.Outlet.F = 0 * 'kmol/h';
[517]	256	feedV.Outlet.T = 280 * 'K';
	257	feedV.Outlet.P = 150 * 'atm';
[506]	258	feedV.Outlet.z = [0.5, 0.5];
[517]	259
	260	inL.P = 150 * 'kPa';
	261	inL.T = 290 * 'K';
[519]	262	inL.F = 90 * 'kmol/h';
[506]	263	inL.z = [0.1641, 0.8359];
	264
	265	inV.P = 150 * 'kPa';
[519]	266	inV.T = 500 * 'K';
[506]	267	inV.z = [0.0584, 0.9416];
[517]	268	# inV.F = 62 * 'kmol/h';
[506]	269
[517]	270	t1.OutletV.F = 120 * 'kmol/h';
	271	# t1.OutletL.F = 120 * 'kmol/h';
[519]	272	t1.interf.a = 40 * 'm^2';
[517]	273	t1.interf.htL = 10.01 * 'kW/m^2/K';
	274	t1.interf.htV = 0.025 * 'kW/m^2/K';
	275	t1.interf.kL = 0.00933 * 'm/s';
	276	t1.interf.kV = 0.000236 * 'm/s';
	277
[506]	278	SET
	279	t1.V = 4 * 'ft^3';
[517]	280	t1.Ah = 0.394 * 'ft^2';
[506]	281	t1.lw = 20.94 * 'in';
	282	t1.hw = 0.125 * 'ft';
	283	t1.beta = 0.6;
[517]	284	t1.alfa = 4;
[506]	285	t1.Ap = 3.94 * 'ft^2';
	286	t1.Q = 0 * 'kW';
[517]	287
[506]	288	INITIAL
[517]	289	t1.OutletL.T = 295 *'K';
[506]	290	t1.OutletV.T = 290 *'K';
[517]	291	t1.Level = 0.9 * t1.hw;
[506]	292	t1.OutletL.z(1) = 0.5;
[517]	293	t1.OutletV.z(1) = 0.6;
	294	t1.MV = 1.0*'mol' ;
	295
[506]	296	OPTIONS
[507]	297	TimeStep = 0.1;
[517]	298	TimeEnd = 10;
[507]	299	TimeUnit = 's';
[517]	300	GuessFile = "trayRate_Test.rlt";
[506]	301	end

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