source: trunk/eml/pressure_changers/expander.mso @ 639

Last change on this file since 639 was 625, checked in by gerson bicca, 15 years ago

added expander model with sample diagram
File size: 4.3 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* Authors: Rafael de Pelegrini Soares
17*          Andrey Copat, Estefane S. Horn, Marcos L. Alencastro
18* $Id$
19*--------------------------------------------------------------------*#
20
21using "streams";
22
23Model expander
24       
25ATTRIBUTES
26        Pallete         = true;
27        Icon            = "icon/expander";
28        Brief           = "Model of an expansor.";
29        Info            =
30"To be documented";
31       
32PARAMETERS
33
34outer PP                        as Plugin               (Brief = "External Physical Properties", Type="PP");
35outer NComp     as Integer              (Brief = "Number of chemical components", Lower = 1);
36        Rgas                            as positive     (Brief = "Constant of Gases", Unit= 'kJ/kmol/K', Default = 8.31451,Hidden=true);
37        Mw(NComp)       as molweight (Brief = "Molar Weight");
38
39VARIABLES
40
41        IseCoeff        as positive     (Brief = "Isentropic Coefficient", Lower=0.2);
42        Pratio          as positive             (Brief = "Pressure Ratio", Symbol ="P_{ratio}");       
43        Pdrop           as press_delta  (Brief = "Pressure Drop", DisplayUnit = 'kPa', Symbol ="\Delta P");
44        Pdecrease       as press_delta  (Brief = "Pressure Decrease", DisplayUnit = 'kPa', Symbol ="P_{decr}");
45
46        Head                            as energy_mass  (Brief = "Head",Hidden=true);
47        HeadIsentropic          as energy_mass  (Brief = "Isentropic Head");
48        Tisentropic                     as temperature  (Brief = "Isentropic Temperature");
49       
50        IsentropicEff   as efficiency   (Brief = "Isentropic efficiency");
51        MechanicalEff   as efficiency   (Brief = "Mechanical efficiency");
52       
53        FluidPower      as power                (Brief = "Fluid Power");
54        BrakePower      as power                (Brief = "Brake Power");
55        PowerLoss       as power                (Brief = "Power Losses",Lower=0);
56        Mwm                     as molweight    (Brief = "Mixture Molar Weight");
57        rho                     as dens_mass    (Brief = "Mass Density");
58        Zfac_in         as fraction     (Brief = "Compressibility factor at inlet");
59        Zfac_out        as fraction     (Brief = "Compressibility factor at outlet");
60
61in      Inlet           as stream       (Brief = "Inlet stream", PosX=0.05, PosY=0.0, Symbol="_{in}");
62out     Outlet          as streamPH     (Brief = "Outlet stream", PosX=0.65, PosY=1, Symbol="_{out}");
63
64out     WorkOut         as work_stream  (Brief = "Work Outlet", PosX=1, PosY=0.46);
65
66SET
67
68        Mw = PP.MolecularWeight();
69
70        Rgas    = 8.31451*'kJ/kmol/K';
71
72EQUATIONS
73
74"Overall Molar Balance"
75        Outlet.F = Inlet.F;
76
77"Component Molar Balance"
78        Outlet.z = Inlet.z;
79
80"Average Molecular Weight"
81        Mwm = sum(Mw*Inlet.z);
82
83"Pressure Ratio"
84        Outlet.P = Inlet.P * Pratio;
85
86"Pressure Drop"
87        Outlet.P  = Inlet.P - Pdrop;
88
89"Pressure Decrease"
90        Outlet.P  = Inlet.P - Pdecrease;
91
92"Mass Density"
93        rho = PP.VapourDensity(Inlet.T, Inlet.P, Inlet.z);
94       
95"Compressibility factor at Inlet Conditions"
96        Zfac_in = PP.VapourCompressibilityFactor(Inlet.T,Inlet.P,Inlet.z);
97       
98"Compressibility factor at Outlet Conditions"
99        Zfac_out = PP.VapourCompressibilityFactor(Outlet.T,Outlet.P,Outlet.z);
100
101"Isentropic Head"
102        HeadIsentropic*Mwm = (PP.VapourEnthalpy(Tisentropic,Outlet.P,Outlet.z)-Inlet.h);
103
104"Actual Head"
105        Head*Mwm = (Outlet.h-Inlet.h);
106
107"Isentropic Coefficient"
108        HeadIsentropic = (0.5*Zfac_in+0.5*Zfac_out)*(1/Mwm)*(IseCoeff/(IseCoeff-1.001))*Rgas*Inlet.T*((Outlet.P/Inlet.P)^((IseCoeff-1.001)/IseCoeff) - 1);
109
110"Isentropic Outlet Temperature"
111        PP.VapourEntropy(Tisentropic, Outlet.P, Outlet.z) = PP.VapourEntropy(Inlet.T, Inlet.P, Inlet.z);
112
113
114if IsentropicEff equal 1
115
116        then
117"Discharge Temperature"
118        Outlet.T = Tisentropic;
119
120        else
121
122"Discharge Temperature"
123        (PP.VapourEnthalpy(Outlet.T,Outlet.P,Outlet.z)-Inlet.h)= (PP.VapourEnthalpy(Tisentropic,Outlet.P,Outlet.z)-Inlet.h)*IsentropicEff;
124
125end
126
127"Fluid Power"
128        FluidPower = IsentropicEff*HeadIsentropic*sum(Mw*Inlet.z)*Inlet.F+PowerLoss;
129
130"Brake Power"
131        BrakePower = WorkOut.Work;
132
133"Brake Power"
134        BrakePower = FluidPower*MechanicalEff;
135
136"Power Loss"
137        PowerLoss = BrakePower - FluidPower;
138
139end
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