source: branches/newlanguage/sample/mixers_splitters/sample_splitter.mso @ 137

Last change on this file since 137 was 80, checked in by Paula Bettio Staudt, 16 years ago

Updated mixers_splitters sample files header and to use with VRTherm DEMO

  • Property svn:eol-style set to native
  • Property svn:keywords set to Id
File size: 1.6 KB
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1#*-------------------------------------------------------------------
2* EMSO Model Library (EML) Copyright (C) 2004 - 2007 ALSOC.
3*
4* This LIBRARY is free software; you can distribute it and/or modify
5* it under the therms of the ALSOC FREE LICENSE as available at
6* http://www.enq.ufrgs.br/alsoc.
7*
8* EMSO Copyright (C) 2004 - 2007 ALSOC, original code
9* from http://www.rps.eng.br Copyright (C) 2002-2004.
10* All rights reserved.
11*
12* EMSO is distributed under the therms of the ALSOC LICENSE as
13* available at http://www.enq.ufrgs.br/alsoc.
14*
15*--------------------------------------------------------------------
16* Sample file for model splitter_n
17*--------------------------------------------------------------------
18*
19* This sample file needs VRTherm DEMO (www.vrtech.com.br) to run.
20*
21*----------------------------------------------------------------------
22* Author: Maurício Carvalho Maciel
23* $Id: sample_splitter.mso 80 2006-12-08 19:46:22Z paula $
24*--------------------------------------------------------------------*#
25
26using "mixers_splitters/splitter";
27
28FlowSheet TestSplitter
29        PARAMETERS
30        PP      as CalcObject(Brief="Physical Properties",File="vrpp");
31        NComp   as Integer;
32        NOutlet as Integer;
33       
34        DEVICES
35        stream as stream_therm;
36        splitter as splitter_n;
37       
38        CONNECTIONS
39        stream to splitter.Inlet;
40       
41        SET
42        PP.Components = [ "isobutane", "benzene"];
43        PP.LiquidModel = "PR";
44        PP.VapourModel = "PR";
45        NComp = PP.NumberOfComponents;
46        splitter.NOutlet = 3;
47
48        SPECIFY
49        stream.F = 153 * "kmol/h";
50        stream.P = 150 * "kPa";
51        stream.T = 298.6 * "K";
52        stream.z = [0.6, 0.4];
53        stream.v = 0;
54        splitter.frac(1) = 0.4;
55        splitter.frac(2) = 0.1;
56
57        OPTIONS
58        relativeAccuracy = 1e-7;
59       
60end
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