source: mso/sample/stage_separators/sample_condenser.mso @ 100

Last change on this file since 100 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: 2.5 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 condenser and condenserSteady
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_condenser.mso 86 2006-12-08 20:58:15Z paula $
24*--------------------------------------------------------------------*#
25using "stage_separators/condenser";
26using "mixers_splitters/splitter";
27
28# condenser with splitter dividing liquid outlet
29FlowSheet condenser_Test
30        PARAMETERS
31        PP      as CalcObject(Brief="Physical Properties",File="vrpp");
32        NComp   as Integer;
33
34        VARIABLES
35        Q       as heat_rate (Brief="Heat supplied");
36       
37        SET
38        PP.Components = [ "isobutane", "benzene"];
39        PP.LiquidModel = "PR";
40        PP.VapourModel = "PR";
41        NComp = PP.NumberOfComponents;
42       
43        DEVICES
44        c1 as condenser;
45        sp as splitter;
46        s1 as stream_therm;
47       
48        CONNECTIONS
49        s1 to c1.InletV;
50        c1.OutletL to sp.Inlet;
51        Q to c1.Q;
52       
53        SPECIFY
54        s1.P = 152 * "kPa";
55        s1.T = 298.6 * "K";
56        s1.F = 153 * "kmol/h";
57        s1.z = [0.664, 0.336];
58        s1.v = 1.0;
59       
60        sp.frac = 0.444445;
61        c1.OutletV.F = 0 * "kmol/h";
62        c1.OutletL.F = 153 * "kmol/h";
63
64        Q = -3.71e6 * "kJ/h";
65
66        SET
67        c1.V = 2 * "m^3";
68        c1.Across = 1 * "m^2";
69
70        INITIAL
71        c1.OutletL.T = 280 *"K";
72        c1.Level = 1 * "m";
73        c1.OutletL.z(1) = 0.65;
74       
75        OPTIONS
76        time = [0:20:1000];
77end
78
79FlowSheet condenserSteady_Test
80        PARAMETERS
81        PP      as CalcObject(Brief="Physical Properties",File="vrpp");
82        NComp   as Integer;
83
84        VARIABLES
85        Q       as heat_rate (Brief="Heat supplied");
86       
87        SET
88        PP.Components = [ "isobutane", "benzene"];
89        PP.LiquidModel = "PR";
90        PP.VapourModel = "PR";
91        NComp = PP.NumberOfComponents;
92       
93        DEVICES
94        c1 as condenserSteady;
95        s1 as stream_therm;
96       
97        CONNECTIONS
98        s1 to c1.InletV;
99        Q to c1.Q;
100       
101        SPECIFY
102        s1.P = 152 * "kPa";
103        s1.T = 298.6 * "K";
104        s1.F = 153 * "kmol/h";
105        s1.z = [0.664, 0.336];
106        s1.v = 1.0;
107        Q = 3.71e6 * "kJ/h";
108        c1.DP = 100 * "kPa";
109
110        OPTIONS
111        mode = "steady";
112        time = [0:20:1000];
113end
Note: See TracBrowser for help on using the repository browser.