0,10,0,

{Kondensor}//From TurbinT2= 45,87 [C]P2= 0,1 [bar]X2 = 0,847ms_2 = 376910*convert(kg/h;kg/s)mg_2 = 1885 *convert(kg/h;kg/s)

//To GRST3 = 29 [C]P3=P2ms_3 = 736*convert(kg/h;kg/s){mg_3 =1885 *convert(kg/h;kg/s)}{ma_3 = 120 *convert(kg/h;kg/s)}

//From CTT4= 27 [C]P4=P2mw_4 = 11800000*convert(kg/h;kg/s)

//To CTT5 = 42,7596[C]P5 = P2 {mw_5 = 12488135 *convert(kg/h;kg/s)}

//From Inter CondensorT6 = 50 [C]P6 = 0,41 [bar]mw_6 = 156419 *convert(kg/h;kg/s)

//From After CondensorT7 = 50 [C]P7 = 0,95 [bar]mw_7 = 155542 *convert(kg/h;kg/s)

{Kesetimbangan Massa}ms_2+mw_4+mw_6+mw_7= ms_3+mw_5mg_2=mg_3

{Kesetimbangan Energi}ms_2*h2+mg_2*hg_2+mw_4*hw_4+mw_6*hw_6+mw_7*hw_7 = ms_3*h3+mg_3*hg_3+ma_3*ha_3+mw_5*hw_5

h2 = Enthalpy (steam;P=P2;X=X2)hg_2 = Enthalpy (CarbonDioxide;T=T2;P=P2)h3 = Enthalpy (Steam;P=P3;T=T3)hg_3 = Enthalpy (CarbonDioxide;T=T3;P=P3)ha_3 =Enthalpy (Air_ha;T=T3;P=P3)hw_4 =Enthalpy (Water;T=T4;P=P4)hw_5 = Enthalpy (Water; T=T5;P=P5)hw_6 =Enthalpy (Water;T=T6;P=P6)hw_7 = Enthalpy(water;T=T7;P=P7)