source: trunk/BioModel/economic_assumptions.mso @ 1008

#*-------------------------------------------------------------------
* Biorrefinaria Petrobras
*--------------------------------------------------------------------
* Nome do arquivo: economic_assumptions.mso
* Projeto: producao de etanol 1G e 2G
* Conteudo: Valores dos principais parametros ambientais de processo 
*--------------------------------------------------------------------*#

#*-------------------------------------------------------------------
*
* Data:    08/2019
* Autores:   Andrew Milli Elias
* Versao: 2.1
*--------------------------------------------------------------------
*Descricao: simulacao da producao de E1G e E2G
*--------------------------------------------------------------------*#

using "types";

Model EconomicParameters
        VARIABLES
        #TODO: Retirar esse acrescimo de 10% no preco do etanol
        EthanolPrice            as positive (Brief = "media em valor presente dos 10 anos 2007-2017 acrescida de 10%", Unit ='US$/m^3');
        
        PARAMETERS
        WorkedHours                     as time_h (Brief = "Media de horas trabalhadas das usinas do estado de Sao Paulo"); 
        
        ExchangeRate            as positive (Brief = "Taxa de cambio utilizada na conversao dolar x real - 2017",Default = 3.144);
        EnzymeCost                      as positive (Brief = " Preco enzima de acordo com Klein-Marcuschamer et al 2012", Unit = 'US$ / kg');
        
        #media em valor presente dos 10 anos 2007-2017
        EnergyPrice      as Real (Brief = "Energy price", Unit = 'US$/MW/h');
        #preco da cana de acucar - contabiliza transporte - na porta da usina
        SugarcaneCost as  Real (Brief = "Sugarcane Costs", Unit = 'US$ / t', Default = 69.256/3.144); #contabiliza transporte - na porta da usina
        #Danta (2013)30,00 reais/tonn seca
        StrawCost as  Real (Brief = "Straw Costs", Unit = 'US$ / t', Default = 30/3.144); #Danta (2013)30,00 reais/tonn seca
        #com base na ref1
        
        Ethanol1GProduction as flow_vol (Brief = "Anhydrous Ethanol Volumetric Production in 1G plant(ref1)", Default = 74.8409);
        Extraction1GCost    as positive (Unit = 'US$ / m^3');
        Treatment1GCost     as positive (Unit = 'US$ / m^3');
        EECost                          as Real (Brief = "Electric Energy production Cost", Unit = 'US$/MW', Default = 148/3.144);

        WaterCost                       as Real (Brief = "Water Costs", Unit = 'US$ / t');
        FosfCost                        as Real (Brief = "KH2PO4 (98%) Costs", Unit = 'US$ / kg');
        CalCost                         as Real (Brief = "Calcium Costs", Unit = 'US$ / kg');
        PolCost                         as Real (Brief = "Polymer Costs", Unit = 'US$ / kg');
        SulfCost                        as Real (Brief = "Ac Sulfuric Cost", Unit = 'US$ / kg');
        AmmoniaCost             as Real (Brief = "Ammonia Cost", Unit = 'US$ / kg');
        InoxCost                        as Real (Unit = 'US$/kg');
        CarbonSteelCost         as Real (Unit = 'US$/kg');
        PumpCost                        as Real;
        HighPumpCost            as Real  (Unit = 'US$/m^3*h');
        pHmetroCost             as Real (Default = 15000);

        ConcreteCost            as Real (Brief = "Cost of m3 of concrete", Unit = 'US$/m^3');
        ConveyorBeltCost        as Real (Brief = "Cost per metre of conveyor belt", Unit = 'US$/m');
        
        PretreatmentInstalationFactor   as positive (Default = 1.3);
        HydrolysisInstalationFactor             as positive (Default = 1.3);
        C5InstalationFactor                             as positive (Default = 1.3);


        ProjTime        as Integer (Brief = "lifetime", Default = 25);
        r                       as fraction (Brief = "Minimum Attractiveness Rate", Default = 0.11);
        
        SPECIFY
        EthanolPrice = 470.835 * 1.1 * 'US$/m^3'; #dolares
        
        SET
        EnergyPrice = 80.8 * 'US$/MW/h'; #dolares
        SugarcaneCost = 69.256 * 'US$ / t';#reais
        StrawCost = 30 * 'US$ / t';#reais
        Ethanol1GProduction = 74.8409 * 'm^3/h';#com base na ref1
        Extraction1GCost = 21.87 * 'US$/m^3';
        Treatment1GCost = 7.87 * 'US$/m^3';
        EECost = (122.86/ExchangeRate) * 'US$/MW';#com base na relatorio - custos industriais pecege 2015
        
        WorkedHours     = 240*21 * 'h'; #240*24*0.875
        #234 dias * 20h/d - media do ano de 2016 para os estados sudeste (Relatorio Conab 2019)
        #240 dias * 21h/d - essa eh a media de SP para o ano de 2016 (Relatorio Conab 2019)
        
        ExchangeRate  = 3.144;
        EnzymeCost    = 10.14 *  'US$ / kg';
        
        PumpCost        = 4468.96 / ExchangeRate; 
        HighPumpCost= 134.42 / ExchangeRate * 'US$/m^3*h';
        WaterCost       = (0.05 / ExchangeRate) * 'US$ / t'; #0.05 reais por m^3
        FosfCost        = 0.400 * 'US$ / kg';
        CalCost         = 0.100 * 'US$ / kg';
        PolCost         = 0.100 * 'US$ / kg';
        SulfCost        = (0.92 /ExchangeRate) * 'US$ / kg';
        AmmoniaCost = 0.100 * 'US$ / kg';
        InoxCost        = (25/ExchangeRate) *'US$/kg';
        CarbonSteelCost         = (13.5 /ExchangeRate) *'US$/kg';
        ConcreteCost            = (1300/ExchangeRate) * 'US$/m^3';
        ConveyorBeltCost        = (10000/ExchangeRate) * 'US$/m';
        pHmetroCost = 15000; #Valor em reais
        
        PretreatmentInstalationFactor   = 1.3;
        HydrolysisInstalationFactor     = 1.3;
        C5InstalationFactor                     = 1.3;
        
        r  = 0.11;
        ProjTime = 25;
        
        #utilities
        #custo da agua tratada 0.05 reais/m^3 - preco que a usina paga em 2019
        #custo da agua desmi 2.44 reais/m^3
end