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70 Model Details 54 T_Ex1 ( rqst . objectId) 55 M_Egr ( rqst . objectId) 56 57 M_Ex ( rqst . objectId) 58 59 W_Egr ( rqst . objectId) 60 61 W_Ex ( rqst . objectId) 62 63 T_Evapin(rqst.objectId) 64 T_Ex2 ( rqst . objectId) 65 T_Egr2(rqst.objectId) 66 oid = rqst . objectId ; = 0; = 0; = 0; = 0; = 0; = 0; = 0; = 0; % Exhaust HX - FlueGas inlet temperature % Mass flow rate % in EGR HX % Mass flow rate % in Exhaust HX % Mass flow rate % in the EGR HX % Mass flow rate % in the Exhaust HX % Evaporator inlet temperature-WF side % Exhaust HX exit tempetaure-FlueGas side % EGR HX Exit temperature-FlueGas side 67 P_atm(rqst.objectId) = 1.01325; % Pressure on fluegas side in bar 68 69 check = zeros (1 , rqst . objectId) ; 70 for i=1:10 71 if ( ins ( i ) . value==−1) 72 73 74 75 76 77 78 79 80 81 82 83 84 end 85 end check(rqst.objectId) = −1; T_PinchEx( rqst . objectId) = −1; T_PinchEGR( rqst . objectId) = −1; h_WF1(rqst.objectId)=−1; h_WFsat1( rqst . objectId)=−1; h_Ex2(rqst.objectId)=−1; h_Egr2(rqst.objectId)=−1; dh_Ex(rqst.objectId) = −1; dh_Egr ( rqst . objectId) = −1; T_ExY(rqst.objectId)=−1; T_EgrY(rqst.objectId)=−1; break; 86 %% For 87 if(check(rqst.objectId)== 0) 88 P_Evap(rqst.objectId) = ins(1).value; 89 DELTL(rqst.objectId) = ins(2).value; 90 T_Egr1(rqst.objectId) = ins(3).value; 91 T_Ex1(rqst.objectId) = ins(4).value; 92 M_Egr(rqst.objectId) = ins(5).value; 93 M_Ex (rqst.objectId) = ins(6).value; 94 W_Egr(rqst.objectId) = ins(7).value; 95 W_Ex (rqst.objectId) = ins(8).value; 96 T_Evapin(rqst.objectId) = ins(9).value; 97 aid (rqst.objectId) = ins(10).value; 98 x (rqst.objectId) = ins(11).value; 99 T_Evap (rqst.objectId)= ins(12).value; 100 fluid = strcat(’DORC_’ ,num2str(oid)) ; 101 T_Ex2(rqst.objectId) = T_Evapin(rqst.objectId)+ DELTL(rqst.objectId); 102 T_Egr2(rqst.objectId)= T_Evapin(rqst.objectId)+ DELTL(rqst.objectId); 103 % Saturated temperature is fixed to be 5 K lower than 104 % evaporator outlet temperature 105 T_sat(rqst.objectId) = T_Evap(rqst.objectId)− 5; 106 if(P_Evap(rqst.objectId) > x(rqst.objectId)) Akshay Hattiangadi Master of Science Thesis valid inputs of working fluid of working fluid of flue gas of flue gasPDF Image | Working Fluid Design for Organic Rankine Cycle
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