source: branches/newlanguage/eml/streams.mso @ 125

Last change on this file since 125 was 125, checked in by Rafael de Pelegrini Soares, 16 years ago

Updated some models for the new language proposal

  • Property svn:eol-style set to native
  • Property svn:keywords set to Id
File size: 3.9 KB
RevLine 
[79]1#*-------------------------------------------------------------------
2* EMSO Model Library (EML) Copyright (C) 2004 - 2007 ALSOC.
[1]3*
[79]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* Model of basic streams
[1]17*----------------------------------------------------------------------
[79]18* Author: Paula B. Staudt and Rafael de P. Soares
[1]19* $Id: streams.mso 125 2007-01-22 19:57:16Z rafael $
20*---------------------------------------------------------------------*#
21
22using "types";
23
24Model stream
[117]25        ATTRIBUTES
26        Pallete = false;
27        Brief = "General Material Stream";
[123]28        Info =
[117]29        "This is the basic building block for the EML models.
30        Every model should have input and output streams derived
31        from this model.";
32       
[1]33        PARAMETERS
[117]34        outer NComp as Integer (Brief = "Number of chemical components", Lower = 1);
[1]35
36        VARIABLES
37        F as flow_mol;
38        T as temperature;
39        P as pressure;
[117]40        z(NComp) as fraction(Brief = "Overall Molar Fraction");
[1]41        h as enth_mol;
[117]42        v as fraction(Brief = "Vapourisation fraction");
[1]43end
44
[117]45Model liquid_stream as stream
46        ATTRIBUTES
47        Pallete = false;
48        Brief = "Liquid Material Stream";
[123]49        Info =
[117]50        "Model for liquid material streams.
51        This model should be used only when the phase of the stream
52        is known ''a priori''.";
53
[1]54        PARAMETERS
[117]55        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
[1]56       
57        EQUATIONS
[117]58        "Liquid Enthalpy"
59        h = PP.LiquidEnthalpy(T, P, z);
60        "Liquid stream"
61        v = 0;
[1]62end
63
[117]64Model vapour_stream as stream
65        ATTRIBUTES
66        Pallete = false;
67        Brief = "Vapour Material Stream";
[123]68        Info =
[117]69        "Model for vapour material streams.
70        This model should be used only when the phase of the stream
71        is known ''a priori''.";
72
[1]73        PARAMETERS
[117]74        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
[1]75       
76        EQUATIONS
[117]77        "Vapour Enthalpy"
78        h = PP.VapourEnthalpy(T, P, z);
79        "Vapour stream"
80        v = 1;
[1]81end
82
[125]83Model streamPH as stream
84        PARAMETERS
85        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
86        outer NComp as Integer (Brief = "Number of chemical components", Lower = 1);
87       
88        VARIABLES
89        x(NComp) as fraction(Brief = "Liquid Molar Fraction");
90        y(NComp) as fraction(Brief = "Vapour Molar Fraction");
91       
92        EQUATIONS
93        "Flash Calculation"
94        [v, x, y] = PP.FlashPH(P, h, z);
95        "Enthalpy"
96        h = (1-v)*PP.LiquidEnthalpy(T, P, x) +
97                v*PP.VapourEnthalpy(T, P, y);
98end
99
[117]100Model source
101        ATTRIBUTES
[123]102        Info =
[117]103        "Material stream source.
104        This model should be used for boundary streams.
105        Usually these streams are known and come from another process
106        units.";
107
108        PARAMETERS
109        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
110        outer NComp as Integer (Brief = "Number of chemical components", Lower = 1);
111       
112        VARIABLES
113        out Outlet as stream;
114        x(NComp) as fraction(Brief = "Liquid Molar Fraction");
115        y(NComp) as fraction(Brief = "Vapour Molar Fraction");
[123]116        hl as enth_mol;
117        hv as enth_mol;
[117]118       
119        EQUATIONS
120        "Flash Calculation"
121        [Outlet.v, x, y] = PP.Flash(Outlet.T, Outlet.P, Outlet.z);
122        "Overall Enthalpy"
123        Outlet.h = (1-Outlet.v)*PP.LiquidEnthalpy(Outlet.T, Outlet.P, x) +
124                Outlet.v*PP.VapourEnthalpy(Outlet.T, Outlet.P, y);
[123]125       
126        hl = PP.LiquidEnthalpy(Outlet.T, Outlet.P, x);
127        hv = PP.VapourEnthalpy(Outlet.T, Outlet.P, y);
[117]128end
129
130Model sink
131        ATTRIBUTES
[123]132        Info =
[117]133        "Material stream sink.
134        This model should be used for boundary streams.";
135
136        PARAMETERS
137        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
138        outer NComp as Integer (Brief = "Number of chemical components", Lower = 1);
139       
140        VARIABLES
141        in Inlet as stream;
142        v as fraction;
143        x(NComp) as fraction(Brief = "Liquid Molar Fraction");
144        y(NComp) as fraction(Brief = "Vapour Molar Fraction");
145       
146        EQUATIONS
147        "Flash Calculation"
[123]148        [v, x, y] = PP.FlashPH(Inlet.P, Inlet.h, Inlet.z);
[117]149end
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