source: branches/newlanguage/sample/pressure_changers/sample_compressor.mso @ 196

Last change on this file since 196 was 196, checked in by Rafael de Pelegrini Soares, 16 years ago

Adapted pressure changers models, UOM problems with some equations

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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 centrifugal_compressor
17*--------------------------------------------------------------------
18*
19* This sample file needs VRTherm (www.vrtech.com.br) to run.
20*
21*----------------------------------------------------------------------
22* Author: Marcos L. Alencastro, Estefane da S. Horn
23* $Id: sample_compressor.mso 196 2007-03-07 20:43:43Z rafael $
24*--------------------------------------------------------------------*#
25
26using "pressure_changers/compressor";
27
28FlowSheet compressor_C1
29
30        DEVICES
31        S1 as source;
32        C1 as centrifugal_compressor;
33       
34        CONNECTIONS
35        S1.Outlet to C1.Inlet;
36       
37        PARAMETERS
38        PP              as Plugin       (Brief="External Physical Properties", File="vrpp");
39        NComp   as Integer              (Default= 1);
40       
41        SET
42        PP.Components = ["nitrogen", "oxygen"];
43        PP.LiquidModel = "IdealLiquid";
44        PP.VapourModel = "Ideal";
45        NComp = PP.NumberOfComponents;
46        C1.Effs = 0.75;
47        PP.Derivatives = 0;
48       
49
50        SPECIFY
51        S1.Outlet.F = 41.05             * 'kmol/h';
52        S1.Outlet.P = 1                 * 'atm';
53        S1.Outlet.T = 298                       * 'K' ;
54        S1.Outlet.z = [0.79,0.21];
55       
56        C1.Outlet.P = 3 * 'atm';
57end             
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