source: branches/newlanguage/sample/pressure_changers/sample_turbine.mso @ 137

Last change on this file since 137 was 81, checked in by Paula Bettio Staudt, 16 years ago

Updated pressure_changers sample files header and to use it with VRTherm DEMO

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File size: 1.7 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 Hidraulic turbine
17*--------------------------------------------------------------------
18*
19* This sample file needs VRTherm DEMO (www.vrtech.com.br) to run.
20*
21*----------------------------------------------------------------------
22* Author: Andrey Copat, Estefane S. Horn, Marcos L. Alencastro
23* $Id: sample_turbine.mso 81 2006-12-08 19:57:14Z paula $
24*--------------------------------------------------------------------*#
25
26using "pressure_changers/turbine";
27
28FlowSheet HTurbine_HT1
29       
30        DEVICES
31        S1 as streamTP;
32        HT1 as Hidraulic_Turbine;
33       
34        CONNECTIONS
35        S1 to HT1.Inlet;
36       
37        PARAMETERS
38        PP              as CalcObject   (Brief="External Physical Properties", File="vrpp");
39        Mw              as positive     (Brief = "Molar Mass", Unit = "kg/kmol");
40        NComp   as Integer              (Default= 1);
41       
42        SET
43        PP.Components = ["water", "benzene"];   
44        PP.LiquidModel = "PR";
45        PP.VapourModel = "PR";
46        PP.Derivatives = 0;
47        NComp = PP.NumberOfComponents;
48        HT1.Beta = 425e-6       * "1/K";
49        HT1.Meff = 0.95;
50        HT1.Eff = 0.72;
51       
52        SPECIFY
53        S1.F = 1000                     * "kmol/h";
54        S1.P = 5                        * "atm" ;
55        S1.T = 298                      * "K" ;
56        S1.z = [1];
57        #HT1.Pdiff = 100        * "kPa";
58        HT1.Outlet.P = 1        * "atm";
59       
60end
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