source: trunk/BioModel/separators/cleaning.mso @ 1008

Last change on this file since 1008 was 1008, checked in by Argimiro Resende Secchi, 21 months ago

Adding BioModel? to the MSO library.
File size: 9.7 KB
Line 
1#*-------------------------------------------------------------------
2* Biorrefinaria Petrobras
3*--------------------------------------------------------------------
4* Nome do arquivo: cleaning.mso
5* Projeto: Modelo integrado de producao de etanol 1G/2G
6* Conteudo: lavadora
7*--------------------------------------------------------------------*#
8
9#*-------------------------------------------------------------------
10*
11* Versao 2.2
12* Data:    03/2016
13* Autores:   Anderson R. A. Lino e Gabriel C. Fonseca
14*
15*--------------------------------------------------------------------
16*Descricao: modelo da lavadora que sera empregado
17*na biorrefinaria.
18*--------------------------------------------------------------------
19
20*--------------------------------------------------------------------
21*Notas: Foi feito o flowsheet teste para averiguar o modelo
22*--------------------------------------------------------------------*#
23
24using "main_stream";
25using "assumptions";
26
27Model cleaning
28       
29        ATTRIBUTES
30        Pallete         = true;
31        Icon            = "icon/cleaning";
32        Brief           = "Model of a Washer";
33        Info =
34"== GENERAL ==
35        Model of a simplified sugarcane washer where water is used to
36        decrease the amount of impurities (dirt) in the sugarcane stream.
37       
38== ASSUMPTIONS ==
39* Steady-state;
40* No water is absorbed by the sugarcane;
41* Adiabatic.
42
43== SPECIFY ==
44* The CrudeCane stream:
45  flow rate
46  temperature
47  pressure;
48  stream composition;
49* The Water stream (Except the fluid flow);
50  flow rate
51  temperature
52  pressure
53  stream composition;
54* The water stream (Except the fluid flow);
55* The cleaning efficiency (Efficiency);
56* The fraction of sugar lost (SugarLosses);
57* The fraction of solids kept in the main stream (Separation).
58
59== SET ==
60* Number of stream components(Ncomp/NcompS);
61* Basic composition (mass or molar).
62";
63
64#*-------------------------------------------------------------------
65* Declaracao de variaveis
66*--------------------------------------------------------------------*#
67       
68        VARIABLES
69in      CrudeCane                       as main_stream          (Brief = "Inlet Cane", PosX=0.0, PosY=0.5, Symbol="_{Cane}", Protected = false);
70in      Water                           as main_stream          (Brief = "Inlet Water", PosX=0.5, PosY=0.0, Symbol="_{Water}", Protected = false);
71out     SugarCane                       as main_stream_eq       (Brief = "SugarCane Stream", PosX=1.0, PosY=0.5, Symbol="_{Sugar}", Protected = false);
72out     Dirt                            as main_stream_eq       (Brief = "Dirt Stream", PosX=0.5, PosY=1.0, Symbol="_{Dirt}", Protected = false );
73        Separation              as fraction                     (Brief = "Separation Efficiency");
74        Efficiency              as fraction                     (Brief = "Cleaning Efficiency");
75        SugarLosses             as fraction                     (Brief = "Fraction of Sugar Lost in the Sludge");
76        humidity                        as fraction                     (Brief = "Fraction of Water in the SugarCane");
77        impurity                        as fraction                     (Brief = "Fraction of Solids in the Sludge");
78        WFPTC                           as positive                     (Brief = "Ton of Water Per Ton of Cane");
79        Fiber                   as fraction                     (Brief = "Amount of Fiber in the Inlet Sugarcane", Default = 0.12, Protected = true);
80       
81#*-------------------------------------------------------------------
82#Parametros
83*--------------------------------------------------------------------*#
84
85        PARAMETERS
86       
87outer   PP                              as Plugin               (Brief = "External Physical Properties (Fluid Phase)", Type="PP");
88outer   PPS                     as Plugin               (Brief = "External Physical Properties (Solid Phase)", Type="PP");
89outer   NComp                   as Integer              (Brief = "Number of Chemical Components for the Fluid Phase", Lower = 1);
90outer   NCompS                  as Integer              (Brief = "Number of Chemical Components for the Solid Phase", Lower = 1);
91                M(NComp)                as molweight    (Brief = "Component Mol Weight (Fluid Phase), Vector Size = NComp", Protected=true);
92                MS(NCompS)      as molweight    (Brief = "Component Mol Weight (Solid Phase), Vector Size = NCompS", Protected=true);
93outer   flu as ConstituentFluid(Symbol = " ", Protected = true);
94outer   sol as ConstituentSolid(Symbol = " ", Protected = true);       
95
96#*-------------------------------------------------------------------
97* Define o valor dos parametros declarados no modelo
98*--------------------------------------------------------------------*#
99
100        SET
101       
102        M    = PP.MolecularWeight();
103        MS   = PPS.MolecularWeight();
104       
105        SugarCane.Phase = "Liquid";
106        Dirt.Phase = "Liquid";
107       
108#*-------------------------------------------------------------------
109* Equacoes do modelo
110*--------------------------------------------------------------------*#
111       
112        EQUATIONS
113        "Water Flow per Flow of Fiber"
114        Water.Fluid.Fw = (CrudeCane.Fluid.Fw + CrudeCane.Solid.Fw) * WFPTC;
115       
116        "Global Molar Balance (Fluid Phase)"
117        CrudeCane.Fluid.F + Water.Fluid.F = SugarCane.Fluid.F + Dirt.Fluid.F;
118       
119        "Sum of Molar Fractions (Fluid Phase)"
120        sum(SugarCane.Fluid.z) = sum(Dirt.Fluid.z);
121       
122        for i in [1 : NComp] do
123                if i equal flu.Water then
124                        "Component Molar Balance (Fluid Phase) 1"
125                        CrudeCane.Fluid.F * CrudeCane.Fluid.z(i) = SugarCane.Fluid.F * SugarCane.Fluid.z(i);
126                               
127                        "Component Molar Balance (Fluid Phase) 2"
128                        Water.Fluid.F * Water.Fluid.z(i) = Dirt.Fluid.F * Dirt.Fluid.z(i);
129
130                else
131                        "Component Molar Balance (Fluid Phase) 1"
132                        CrudeCane.Fluid.F * CrudeCane.Fluid.z(i) * (1 - SugarLosses) = SugarCane.Fluid.F * SugarCane.Fluid.z(i);
133                               
134                        "Component Molar Balance (Fluid Phase) 2"
135                        CrudeCane.Fluid.F * CrudeCane.Fluid.z(i) * SugarLosses = Dirt.Fluid.F * Dirt.Fluid.z(i);
136                end
137        end
138       
139        for i in [1 : NCompS] do
140                if i equal sol.Impurities then
141                        "Component Molar Balance (Solid Phase) 1"
142                        SugarCane.Solid.F * SugarCane.Solid.z(i) = (CrudeCane.Solid.F * CrudeCane.Solid.z(i) + Water.Solid.F * Water.Solid.z(i)) * (1-Efficiency);
143               
144                        "Component Molar Balance (Solid Phase) 2"
145                        Dirt.Solid.F * Dirt.Solid.z(i) = (CrudeCane.Solid.F * CrudeCane.Solid.z(i) + Water.Solid.F * Water.Solid.z(i)) * Efficiency;
146                else
147                        "Component Molar Balance (Solid Phase) 1"
148                        SugarCane.Solid.F * SugarCane.Solid.z(i) = (CrudeCane.Solid.F * CrudeCane.Solid.z(i) + Water.Solid.F * Water.Solid.z(i)) * Separation;
149               
150                        "Component Molar Balance (Solid Phase) 2"
151                        Dirt.Solid.F * Dirt.Solid.z(i) = (CrudeCane.Solid.F * CrudeCane.Solid.z(i) + Water.Solid.F * Water.Solid.z(i)) * (1-Separation);
152                end
153        end
154       
155        "Global Molar Balance (Solid Phase)"
156        CrudeCane.Solid.F + Water.Solid.F = Dirt.Solid.F + SugarCane.Solid.F;
157       
158        "Sum of Molar Fractions (Solid Phase)"
159        sum(SugarCane.Solid.z) = sum(Dirt.Solid.z);
160       
161        "Solid Humidty"
162        Dirt.Total.zw(flu.Water) = humidity;
163       
164        "SugarCane Stream Impurities"
165        SugarCane.Fluid.Fw = impurity * (SugarCane.Fluid.Fw + SugarCane.Solid.Fw);
166       
167        "Thermal Equilibrium 1"
168        Dirt.T = CrudeCane.T;
169       
170        "Thermal Equilibrium 2"
171        SugarCane.T = CrudeCane.T;
172       
173        "Mechanical Equilibrium 1"
174        Dirt.P = CrudeCane.P;
175       
176        "Mechanical Equilibrium 2"
177        SugarCane.P = CrudeCane.P;
178       
179        "Calculation of Fiber"
180        Fiber * (CrudeCane.Solid.Fw + CrudeCane.Fluid.Fw) =
181                CrudeCane.Solid.Fw * (CrudeCane.Solid.z(sol.Cellulose) + CrudeCane.Solid.z(sol.Hemicell) + CrudeCane.Solid.z(sol.Lignin));
182       
183end
184
185
186FlowSheet teste_cleaning
187       
188#*-------------------------------------------------------------------
189* Declaracao de dispositivos (ou blocos contendo o modelo)
190*--------------------------------------------------------------------*#
191       
192        DEVICES
193        C101 as cleaning;
194        S101 as main_sourceR;
195        S102 as main_sourceR;
196       
197#*-------------------------------------------------------------------
198* Especifica as conexoes entre os modelos
199*--------------------------------------------------------------------*#
200       
201        CONNECTIONS
202        S101.Outlet to C101.CrudeCane;
203        S102.Outlet to C101.Water;
204       
205#*-------------------------------------------------------------------
206#Parametros
207*--------------------------------------------------------------------*#
208       
209        PARAMETERS
210        PP as Plugin    (Brief = "External Physical Properties",
211                Type="PP",
212                Project = "../Flowsheets/v2_2/Fluid_v2_2.vrtherm"
213        );
214        PPS as Plugin   (Brief = "External Physical Properties",
215                Type="PP",
216                Project = "../Flowsheets/v2_2/Solid_v2_2.vrtherm"
217        );
218       
219        NComp   as Integer (Brief = "Number of chemical components in the fluid phase");
220        NCompS  as Integer (Brief = "Number of chemical components in the solid phase");
221        flu as ConstituentFluid(Symbol = " ", Protected = true);
222        sol as ConstituentSolid(Symbol = " ", Protected = true);
223
224#*-------------------------------------------------------------------
225* Especifica variaveis definidas no modelo
226*--------------------------------------------------------------------*#
227
228        SPECIFY
229        # CrudeCane
230        S101.CompositionOfFluid(1:3) = [0.8, 0.16, 0.04];
231        S101.CompositionOfFluid(4:NComp) = 0;
232        S101.CompositionOfSolid = [0.57, 0.193, 0.193, 0, 0.044, 0, 0, 0, 0];
233        S101.Fluid.Fw = 442.78 * 't/h';
234        S101.Solid.Fw = 57.2 * 't/h';
235        S101.T = 300.318 * 'K';
236        S101.P = 1 * 'atm';
237       
238        # Water
239        S102.CompositionOfFluid = [1, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0];
240        S102.CompositionOfSolid = [0.57, 0.193, 0.193, 0, 0.044, 0, 0, 0, 0];
241        S102.Fluid.Fw = 1100 * 't/h';
242        S102.Solid.Fw = 0 * 'kg/h';
243        S102.T = 300.318 * 'K';
244        S102.P = 1 * 'atm';
245       
246        C101.Efficiency = 0.9; 
247        C101.Separation = 0.99;
248        C101.SugarLosses = 0.02;
249       
250#*-------------------------------------------------------------------
251* Define o valor dos parametros declarados no modelo
252*--------------------------------------------------------------------*#
253
254        SET
255        NComp = PP.NumberOfComponents();
256        NCompS = PPS.NumberOfComponents();
257        S101.CompositionBasis = "Molar";
258        S102.CompositionBasis = "Molar";
259       
260#*-------------------------------------------------------------------
261* Condicoes iniciais e opcoes de Solver
262*--------------------------------------------------------------------*#
263       
264        OPTIONS
265        Dynamic = false;
266       
267end
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