There is a simulation in which energy is not conserved; what should be done?

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$ Generated by PRO/II Keyword Generation System $ Generated on: Sat Feb 13 20:35:13 2016 TITLE TOLERANCE FLASH=3E-6 DIMENSION METRIC, PRES=KPA, PBASIS=101.325 SEQUENCE SIMSCI CALCULATION RECYCLE=TEAR COMPONENT DATA LIBID 1,H20/2,IPROPNOL/3,BENZENE, BANK=SIMSCI,PROCESS ASSAY FIT=ALTERNATE, CONVERSION=API94, CURVEFIT=CURRENT, & KVRECONCILE=TAILS, FORMATION=VER91 THERMODYNAMIC DATA METHOD SYSTEM=UNIQ, SET=UNIQ01, DEFAULT METHOD SYSTEM(VLLE)=UNIQ, SET=UNIQ02 STREAM DATA PROPERTY STREAM=FEED, PRESSURE=111, PHASE=L, & COMPOSITION(M,KGM/H)=1,30.22/2,63.94 PROPERTY STREAM=MAKEUP, PRESSURE=111, PHASE=L, RATE(M)=0.25, & COMPOSITION(M)=3,1 PROPERTY STREAM=RECYCLE, PRESSURE=111, PHASE=L, RATE(M)=246, & COMPOSITION(M)=1,0.1/2,0.25/3,0.65 OUTPUT FORMAT=MATERIAL, SPTPRINT=ON OUTPUT FORMAT=MATERIAL, STREAMS=IPROPNOL, SPTPRINT=ON UNIT OPERATIONS COLUMN UID=T1 PARAMETER TRAY=38,CHEMDIST=50 CVARIABLE=LOG FEED FEED,5/RECYCLE,1 PRODUCT OVHD(M)=S4, BTMS(M)=IPROPNOL,55.5, SUPERSEDE=ON DUTY 1,38,,REBOILER PSPEC PTOP=101, DPCOLUMN=3 PRINT PROPTABLE=PART ESTIMATE MODEL=CHEM SPEC ID=COL1SPEC1, STREAM=IPROPNOL,FRACTION(WT), COMP=2,WET, & VALUE=0.995 VARY DNAME=REBOILER VLLECHECK CHECK=OFF REBOILER TYPE=KETTLE FLASH UID=F1 FEED S4,S7 PRODUCT L=S5, W=S6 ISO TEMPERATURE=30 METHOD SET=UNIQ02 COLUMN UID=T2 PARAMETER TRAY=10,CHEMDIST=50 CVARIABLE=LOG FEED S6,1 PRODUCT OVHD(M)=S7, BTMS(M)=S9,30, SUPERSEDE=ON DUTY 1,10,,REBOILER PSPEC PTOP=101 PRINT PROPTABLE=PART ESTIMATE MODEL=CHEM SPEC ID=COL2SPEC1, STREAM=S7, RATE(KGM/H),TOTAL,WET, DIVIDE, & STREAM=S6, RATE(KGM/H),TOTAL,WET, VALUE=0.8 VARY DNAME=REBOILER VLLECHECK CHECK=OFF REBOILER TYPE=KETTLE CALCULATOR UID=CA1 SEQUENCE STREAM=MAKEUP DEFINE P(1) AS STREAM=IPROPNOL, RATE(KGM/H), COMP=3,WET DEFINE P(2) AS STREAM=S9, RATE(KGM/H), COMP=3,WET DEFINE P(3) AS STREAM=S7, RATE(KGM/H), COMP=3,WET PROCEDURE R(1) = P(1) + P(2) CALL SRXSTR(SMR,R(1),MAKEUP) RETURN MIXER UID=M1 FEED MAKEUP,S5 PRODUCT M=RECYCLE END