source: trunk/template/flowsheet.mso @ 1006

Last change on this file since 1006 was 936, checked in by Rafael de Pelegrini Soares, 11 years ago

Fixed flowsheet template for the new models

  • Property svn:eol-style set to native
  • Property svn:keywords set to Id
File size: 2.4 KB
Line 
1#*
2 * EMSO template file for new flowsheets.
3 *
4 * The user should edit the contents of this file in order
5 * to develop a new flowsheet.
6 *
7 * $Id: flowsheet.mso 936 2011-07-08 16:34:23Z rafael $
8 *#
9
10#*
11 * The using command makes available entities declared in another files.
12 *
13 * With this command the user can make use of the EML models
14 *#
15using "stage_separators/flash";
16
17#*
18 * A new flowsheet is declared with the FlowSheet keyword and a name.
19 * A flowhseet can have several sections presented above:
20 *#
21FlowSheet MyFlowSheet
22        #*
23         * In the PARAMETERS section we can define the constants of the
24         * FlowSheet. When the model requires thermodynamic calculations
25         * we should create an special parameter called PP and select
26         * the model and components of the mixture, as follows:
27         *#
28        PARAMETERS
29        PP      as Plugin(Brief="Physical Properties",
30                Type="PP",
31                Components = ["1,3-butadiene", "isobutene", "n-pentane", "1-pentene"],
32                LiquidModel = "PR",
33                VapourModel = "PR"
34        );
35        NComp   as Integer;
36        SET
37        NComp = PP.NumberOfComponents;
38       
39        #*
40         * In the DEVICES section the components of the process are declared.
41         * Each device is based in a previously defined mathematical model, coming
42         * from the EML or developed by the user.
43         *#
44        DEVICES
45        STR101   as source;
46        FLASH101 as flash;
47        Q101     as energy_source;
48
49        #*
50         * Once the devices of the process were declared we can connect them
51         * in the CONNECTIONS section
52         *#
53        CONNECTIONS
54        STR101.Outlet     to   FLASH101.Inlet;
55        Q101.OutletQ       to   FLASH101.InletQ;
56
57        #*
58         * In order to simulate the process the user should specify some variables
59         *#
60        SPECIFY
61        STR101.Outlet.F = 496.3 * 'kmol/h';
62        STR101.Outlet.T = 338 * 'K';
63        STR101.Outlet.P = 507.1 * 'kPa';
64        STR101.Outlet.z = [0.2379, 0.3082, 0.09959, 0.35431];
65
66        FLASH101.OutletVapour.F = 68.5 * 'kmol/h';
67        FLASH101.OutletLiquid.F = 400*sqrt(FLASH101.Level/'m') * 'kmol/h';
68        FLASH101.InletQ = 1 * 'kJ/h';
69       
70        #*
71         * We can adjust the parameters of the devices in any point after
72         * its declaration.
73         *#
74        SET
75        FLASH101.Lenght = 2 * 'm';
76        FLASH101.Orientation = "vertical";
77        FLASH101.Diameter = 1 * 'm';
78         
79        #*
80         * Besides the usual specifications, dynamic models require the specification
81         * of initial conditions.
82         *#
83        INITIAL
84        FLASH101.OutletLiquid.T = 330 *'K';
85        FLASH101.Level = 1 * 'm';
86        FLASH101.OutletLiquid.z(1) = 0.1;
87        FLASH101.OutletLiquid.z(2) = 0.1;
88        FLASH101.OutletLiquid.z(3) = 0.1;
89end
90# The end keyword informs that the flowsheet declaration have ended.
91
92
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