source: trunk/sample/pressure_changers/sample_valve.mso @ 233

Last change on this file since 233 was 213, checked in by Rafael de Pelegrini Soares, 17 years ago

Adapted some samples to the new Plugin mechanism

  • Property svn:eol-style set to native
  • Property svn:keywords set to Id
File size: 2.8 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 models valve_simplified and valve
17*--------------------------------------------------------------------
18*
19* This sample file needs VRTherm DEMO (www.vrtech.com.br) to run.
20*
21*----------------------------------------------------------------------
22* Author: Paula B. Staudt, Estefane Horn, Núbia do Carmo Ferreira
23* $Id: sample_valve.mso 213 2007-03-15 19:40:55Z rafael $
24*--------------------------------------------------------------------*#
25
26using "pressure_changers/valve";
27
28FlowSheet valve_Test_V
29# with vapour conditions
30        PARAMETERS
31        PP      as Plugin(Brief="Physical Properties",
32                Type="PP",
33                Components = [ "isobutane", "benzene"],
34                LiquidModel = "PR",
35                VapourModel = "PR"
36        );
37        NComp   as Integer;
38
39        SET
40        NComp = PP.NumberOfComponents;
41       
42        DEVICES
43        v1 as valve_simplified;
44        s1 as source;
45       
46        CONNECTIONS
47        s1.Outlet to v1.Inlet;
48
49        SPECIFY
50        s1.Outlet.P = 150 * 'kPa';
51        s1.Outlet.T = 281.75 * 'K';
52        s1.Outlet.z = [0.664, 0.336];
53
54        v1.x = 0.866;
55        v1.Outlet.P = 148 * 'kPa';
56
57        SET
58        v1.k = 20 * 'gal/min/psi^0.5';
59       
60        OPTIONS
61        RelativeAccuracy = 1e-6;
62        Dynamic = false;
63end
64
65FlowSheet valve_Test_L
66#with liquid conditions
67        PARAMETERS
68        PP      as Plugin(Brief="Physical Properties",
69                Type="PP",
70                Components = [ "isobutane", "benzene"],
71                LiquidModel = "PR",
72                VapourModel = "PR"
73        );
74        NComp   as Integer;
75
76        SET
77        NComp = PP.NumberOfComponents;
78       
79        DEVICES
80        v1 as valve_simplified;
81        s1 as source;
82       
83        CONNECTIONS
84        s1.Outlet to v1.Inlet;
85
86        SPECIFY
87        s1.Outlet.P = 185 * 'kPa';
88        s1.Outlet.T = 328.12 * 'K';
89        s1.Outlet.z = [0.001848, 0.9982];
90
91        v1.x = 0.3363;
92        v1.Outlet.P = 183 * 'kPa';
93
94        SET
95        v1.k = 20 * 'gal/min/psi^0.5';
96       
97        OPTIONS
98        RelativeAccuracy = 1e-6;
99        Dynamic = false;
100end
101
102FlowSheet valve_linear_Test
103       
104        DEVICES
105        S1 as source;
106        V1 as valve;
107
108        CONNECTIONS
109        S1.Outlet to V1.Inlet;
110       
111        PARAMETERS
112        PP      as Plugin(Brief="Physical Properties",
113                Type="PP",
114                Components = [ "isobutane", "benzene"],
115                LiquidModel = "PR",
116                VapourModel = "PR"
117        );
118        NComp   as Integer              (Default= 1);
119       
120        SET
121        NComp = PP.NumberOfComponents;
122        V1.valve_type = "linear"; #"parabolic", "equal", "quick", "hyperbolic"
123
124        SPECIFY
125        S1.Outlet.P = 2169.78                   * 'kPa';
126        S1.Outlet.T = 394.26                    * 'K' ;
127        S1.Outlet.z = [1];
128       
129        V1.Qv = 113.56                  * 'm^3/h';
130        V1.x = 0.5;
131        V1.cv = 10                              * 'm^3/h/kPa^0.5';
132       
133        OPTIONS
134        RelativeAccuracy = 1e-6;
135        Dynamic = false;
136end
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