source: branches/newlanguage/sample/mixers_splitters/sample_sepComp.mso @ 115

Last change on this file since 115 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: 2.2 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 sepComp_n and sepComp
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_sepComp.mso 80 2006-12-08 19:46:22Z paula $
24*--------------------------------------------------------------------*#
25
26using "mixers_splitters/sepComp";
27
28FlowSheet Sample_sepComp_n
29        PARAMETERS
30        PP      as CalcObject(Brief="Physical Properties",File="vrpp");
31        NComp as Integer;
32       
33        DEVICES
34        stream as stream_therm;
35        sep as sepComp_n;
36       
37        CONNECTIONS
38        stream to sep.Inlet;
39       
40        SET
41        PP.Components = [ "isobutane", "benzene"];
42        PP.LiquidModel = "PR";
43        PP.VapourModel = "PR";
44        NComp = PP.NumberOfComponents;
45        sep.mainComp = 1;
46        sep.NOutlet = 3;
47
48        SPECIFY
49        stream.F = 30 * "kmol/h";
50        stream.P = 120 * "kPa";
51        stream.T = 290 * "K";
52        stream.z = [0.6, 0.4];
53        stream.v = 0;
54        sep.Outlet(1).z(1) = 0.7;
55        sep.Outlet(2).z(1) = 0.1;
56        sep.frac(1) = 0.4;
57        sep.frac(2) = 0.2;
58#       sep.recovery(1) = 0.533333;
59#       sep.recovery(2) = 0.033333;
60
61        OPTIONS
62        relativeAccuracy = 1e-7;
63       
64end
65
66
67FlowSheet Sample_sepComp
68        PARAMETERS
69        PP      as CalcObject(Brief="Physical Properties",File="vrpp");
70        NComp as Integer;
71       
72        DEVICES
73        stream as streamTP;
74        sep as sepComp;
75       
76        CONNECTIONS
77        stream to sep.Inlet;
78       
79        SET
80        PP.Components = [ "isobutane", "benzene"];
81        PP.LiquidModel = "PR";
82        PP.VapourModel = "PR";
83        NComp = PP.NumberOfComponents;
84        sep.mainComp = 1;
85
86        SPECIFY
87        stream.F = 30 * "kmol/h";
88        stream.P = 120 * "kPa";
89        stream.T = 290 * "K";
90        stream.z = [0.6, 0.4];
91        sep.Outlet1.z(1) = 0.7;
92        sep.frac = 0.4;
93#       sep.recovery = 0.533333;
94
95        OPTIONS
96        relativeAccuracy = 1e-7;
97       
98end
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