source: trunk/BioModel/assumptions.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: 7.1 KB
Line 
1#*-------------------------------------------------------------------
2* Biorrefinaria Petrobras
3*--------------------------------------------------------------------
4* Nome do arquivo: assumptions.mso
5* Projeto: producao de etanol 1G e 2G
6* Conteudo: Modelos com os indices dos componentes nos vetores usados
7*                       nas simulacoes e tambem os valores gerais dos principais
8*                       parametros de processo.
9*--------------------------------------------------------------------*#
10
11#*-------------------------------------------------------------------
12*
13* Data:    03/2016
14* Autores:   Anderson R. A. Lino e Gabriel C. Fonseca
15* Versao: 2.1
16*--------------------------------------------------------------------
17*Descricao: simulacao da producao de E1G e E2G
18*--------------------------------------------------------------------*#
19
20using "types";
21
22Model ConstituentFluid
23        PARAMETERS
24        Water                           as Integer (Brief = "Water", Default = 1);
25        Sucrose                         as Integer (Brief = "Sucrose", Default = 2);
26        Glucose                         as Integer (Brief = "Glucose", Default = 3);
27        Xylose                          as Integer (Brief = "Xylose", Default = 4);
28        Ethanol                         as Integer (Brief = "Ethanol", Default = 5);
29        CO2                             as Integer (Brief = "Carbon Dioxide", Default = 6);
30        CO                                      as Integer (Brief = "Carbon Monoxide", Default = 7);
31        O2                                      as Integer (Brief = "Oxygen", Default = 8);
32        N2                                      as Integer (Brief = "Nitrogen", Default = 9);
33        H2                                      as Integer (Brief = "Hydrogen", Default = 10);
34        CH4                             as Integer (Brief = "Methane", Default = 11);
35        Ammonia                         as Integer (Brief = "Ammonia", Default = 12);
36        Lignin                          as Integer (Brief = "Soluble Lignin", Default = 13);
37        Xylan                           as Integer (Brief = "Xylooligomers", Default = 14);
38        AceticAcid                      as Integer (Brief = "Acetic Acid", Default = 15);
39        Furfural                        as Integer (Brief = "Furfural", Default = 16);
40        HMF                             as Integer (Brief = "Hydroxymethylfurfural", Default = 17);
41        Glycerol                        as Integer (Brief = "Glycerol", Default = 18);
42        Solunkn                         as Integer (Brief = "Unknown sugars", Default = 19);
43        MEG                             as Integer (Brief = "Ethylene Glycol", Default = 20);
44        H2SO4                           as Integer (Brief = "Sulfuric Acid", Default = 21);
45        PhosphoricAcid          as Integer (Brief = "Phosphoric Acid", Default = 22);
46        Impurities                      as Integer (Brief = "Impurities", Default = 23);
47        Cellobiose                      as Integer (Brief = "Cellobiose", Default = 24);
48        AmmoniumHydroxide       as Integer (Brief = "Ammonium Hydroxide", Default = 25);
49end
50
51Model ConstituentSolid
52        PARAMETERS
53        Cellulose                       as Integer (Brief = "Cellulose", Default = 1);
54        Hemicell                        as Integer (Brief = "Hemicellulose", Default = 2);
55        Lignin                          as Integer (Brief = "Lignin", Default = 3);
56        Ash                             as Integer (Brief = "Ashes", Default = 4);
57        Enzyme                          as Integer (Brief = "Enzyme", Default = 5);
58        Yeast                           as Integer (Brief = "Yeast", Default = 6);
59        CaOH2                           as Integer (Brief = "Calcium Hydroxide", Default = 7);
60        Calciumphosphate        as Integer (Brief = "Calcium Phosphate", Default = 8);
61        Impurities                      as Integer (Brief = "Impurities", Default = 9);
62       
63end
64
65Model Assumptions
66        PARAMETERS
67       
68        roomT   as temperature          (Brief = "Room Temperature", Default = 303.15);
69        U               as heat_trans_coeff (Brief = "General Heat Transfer Coefficient for the Plant", Default = 0.69445);
70
71        SugarcaneComposition(25)                as fraction     (Brief = "Sugarcane Base Composition (Fluid Phase)");
72        SugarcaneCompositionSolid(9)    as fraction     (Brief = "Sugarcane Base Composition (Solid Phase)");
73        SugarcaneFiber                                  as fraction     (Brief = "Sugarcane Fiber Fraction");
74        SugarcaneFlow                                   as flow_mass    (Brief = "Sugarcane Mass Flow", Default = 833333);
75       
76        StrawComposition(25)                    as fraction (Brief = "Straw Base Composition (Fluid Phase)");
77        StrawCompositionSolid(9)                as fraction (Brief = "Straw Base Composition (Solid Phase)");
78        StrawComposition_baled(25)              as fraction (Brief = "Base Composition for the Baled Straw (Fluid Phase)");
79        StrawCompositionSolid_baled(9)  as fraction (Brief = "Base Composition for the Baled Straw (Solid Phase)");
80        DryCleaning_effVeg                              as fraction (Default = 0.65);
81        DryCleaning_effMin                              as fraction (Default = 0.70);
82        DryCleaningDuty                                 as positive (Brief = "Actual Duty (per Ton of CrudeCane)", Default=5, Unit = 'kW*h/t');
83        humidity_straw                                  as fraction     (Brief = "Fraction of Water in the OutletStraw", Default = 0.280135);
84        humidity_baled_straw                    as fraction     (Brief = "Fraction of Water in the Baled Straw", Default = 0.15);
85       
86        MillDuty                        as positive (Brief = "Actual Duty (per Ton of Fiber)", Default=3.2, Unit = 'W*h/kg');
87       
88        SugarRecovery           as fraction     (Brief = "Overall sugar recovery", Default = 0.962);
89       
90        SoakingWater            as positive (Brief = "Amount of soaking water - in relation to the inlet of Sugarcane Flow", Default = 0.2683);
91       
92        Pith_proportion         as positive (Brief = "Amount of pith - in relation to the inlet of Sugarcane Flow", Default = 6, Unit = 'kg/t');
93       
94        Water_filter            as positive (Brief = "Amount of water for the filter - in relation to the inlet of Sugarcane Flow", Default = 30, Unit = 'kg/t');
95       
96        PolymerFraction         as fraction  (Brief = "Mass fraction of polymer in decanter", Default = 0.003);
97       
98        PumpEff                         as fraction (Brief = "Pump Efficiency", Default = 0.7);
99       
100        yeastConcTreatment      as fraction (Brief = "Yeast Concentration in the Treatment Reactor - %v/v", Default = 0.25);
101        yeastConcFermenter      as fraction (Brief = "Yeast Concentration in the Fermenter - %v/v", Default = 0.098);
102        #SulfurAcTreatment      as fraction (Brief = "Ratio of Sulfuric Acid Added in the Yeast Treatment", Default = 0.00057);
103        SulfurAcTreatment       as fraction (Brief = "Ratio of Sulfuric Acid Added in the Yeast Treatment- liter acid / m^3 solution", Default = 0.001);
104        SulfurAcDensity         as positive (Brief = "Sulfuric Acid density @ 20 C", Unit = 'g/cm^3', Default = 1.8356);
105
106        TurbineEff                      as fraction (Brief = "Turbine Isoentropic Efficiency", Default = 0.80);
107        MechanicalEff           as fraction (Brief = "Turbine Mechanical Efficiency", Default = 0.982);
108       
109        HydrEthDens             as dens_mass (Brief = "Hydrous Ethanol Density @ 20 C", Default = 808.44);
110        AnhyEthDens             as dens_mass (Brief = "Anhydrous Ethanol Density @ 20 C", Default = 789.34);
111        density_solution        as dens_mass (Brief = "Solution Density", Default = 1000);
112        pi                                      as Real (Brief = "pi constant", Default = 3.141592654);
113       
114        SET
115        #Capacidade de moagem da planta 1G_2G
116        SugarcaneFlow = 833.333 * 't/h';
117
118        #Dados da cana-de-acucar
119        SugarcaneComposition = [0.809107, 0.162519, 0.01509, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0.013284, 0, 0];
120        SugarcaneCompositionSolid = [0.4348, 0.2563, 0.2324, 0.0294, 0, 0, 0, 0, 0.0481];
121        SugarcaneFiber = 0.13653; #Observacao--> os dados foram ponderados para representar as fracoes adequadamente
122       
123        #Dados da palha
124        StrawComposition = [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];
125        StrawCompositionSolid = [0.4605, 0.2720, 0.2467, 0.0208, 0, 0, 0, 0, 0];
126        humidity_straw = 0.5; #Observacao--> os dados foram ponderados para representar as fracoes adequadamente
127       
128        #Dados da palha enfardada
129        StrawComposition_baled = [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];
130        StrawCompositionSolid_baled = [0.4605, 0.2720, 0.2467, 0.0208, 0, 0, 0, 0, 0];
131        humidity_baled_straw = 0.15; #Observacao--> os dados foram ponderados para representar as fracoes adequadamente
132       
133        pi = 3.141592654;
134       
135end
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