source: trunk/sample/stage_separators/sample_stream.mso @ 247

Last change on this file since 247 was 247, checked in by Rafael de Pelegrini Soares, 16 years ago

Updated solver options for the new language

  • Property svn:eol-style set to native
  • Property svn:keywords set to Id
File size: 1.6 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* Sample file for model flash and flashSteady
17*--------------------------------------------------------------------
18*
19* This sample file needs VRTherm (www.vrtech.com.br) to run.
20*
21*----------------------------------------------------------------------
22* Author: Paula B. Staudt
23* $Id: sample_stream.mso 247 2007-04-24 13:44:18Z rafael $
24*--------------------------------------------------------------------*#
25using "streams";
26
27# exemplo baseado nos dados do artigo do Gani 1985.
28FlowSheet stream_test
29        PARAMETERS
30        PP as Plugin(Brief="Physical Properties",
31                Type="PP",
32                Components = ["1,3-butadiene", "isobutene", "n-pentane", "1-pentene", "1-hexene", "benzene"],
33                LiquidModel = "PR",
34                VapourModel = "PR"
35        );
36        NComp as Integer;
37
38        SET
39        NComp = PP.NumberOfComponents;
40       
41        DEVICES
42        s1 as source;
43        s2 as sink;
44       
45        CONNECTIONS
46        s1.Outlet to s2.Inlet;
47       
48        SPECIFY
49        s1.Outlet.F = 496.3 * 'kmol/h';
50        s1.Outlet.T = 338 * 'K';
51        #s1.Outlet.P = 507.1 * 'kPa';
52        s1.Outlet.v = 0.12;
53        s1.Outlet.z = [0.2379,0.3082,0.09958,0.1373,0.08872,0.1283];
54
55        OPTIONS
56        Dynamic = false;
57end
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