source: branches/newlanguage/sample/stage_separators/sample_tray.mso @ 125

Last change on this file since 125 was 86, checked in by Paula Bettio Staudt, 16 years ago

Updated stage_separators sample files header

  • Property svn:eol-style set to native
  • Property svn:keywords set to Id
File size: 2.1 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 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 86 2006-12-08 20:58:15Z paula $
24*--------------------------------------------------------------------*#
25using "stage_separators/tray";
26
27FlowSheet tray_Test
28        PARAMETERS
29        PP      as CalcObject(Brief="Physical Properties",File="vrpp");
30        NComp   as Integer;
31
32        SET
33        PP.Components = [ "n-pentane", "benzene"];
34        PP.LiquidModel = "PR";
35        PP.VapourModel = "PR";
36        NComp = PP.NumberOfComponents;
37       
38        DEVICES
39        t1 as tray;
40        feed as stream_therm;
41        inL as stream_therm;
42        inV as stream_therm;
43       
44        CONNECTIONS
45        feed to t1.Inlet;
46        inL to t1.InletL;
47        inV to t1.InletV;
48       
49        SPECIFY
50        feed.F = 113.4 * "kmol/h";
51        feed.T = 291 * "K";
52        feed.P = 1.66 * "atm";
53        feed.z = [0.5, 0.5];
54        feed.v = 0;
55       
56        inL.P = 165 * "kPa";
57        inL.T = 310 * "K";
58        inL.F = 61.99 * "kmol/h";
59        inL.z = [0.1641, 0.8359];
60        inL.v = 0.0;
61
62        inV.F = 147.1 * "kmol/h";
63        inV.v = 1.0;
64        inV.P = 150 * "kPa";
65        inV.T = 321 * "K";
66        inV.z = [0.0584, 0.9416];
67       
68        t1.Emv = 1;
69        t1.OutletV.F = 147.1 * "kmol/h";
70
71        SET
72        t1.V = 4 * "ft^3";
73        t1.Ah = 0.394 * "ft^2";
74        t1.lw = 20.94 * "in";
75        t1.hw = 0.125 * "ft";
76        t1.Q = 0 * "kW";
77        t1.beta = 0.6;
78        t1.alfa = 4;
79        t1.Ap = 3.94 * "ft^2";
80       
81        INITIAL
82        t1.OutletL.T = 290 *"K";
83        t1.Level = 0.9 * t1.hw;
84        t1.OutletL.z(1) = 0.5;
85       
86        OPTIONS
87        relativeAccuracy = 1e-6;
88        time = [0:1:100];
89end
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