FSD100MbP?h㈵>d  dfffffr@м@`y}fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 173.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 193.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene $(last 2 messages repeated 2 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene  (last message repeated 1 time) message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 173.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 163.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 183.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene $(last 2 messages repeated 4 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 163.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 153.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 173.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 193.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 193.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene $(last 2 messages repeated 2 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 153.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 143.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 163.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 183.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 183.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene $(last 2 messages repeated 3 times) message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 143.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 133.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 153.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 173.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 173.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene $(last 2 messages repeated 2 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 133.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 123.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 143.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 183.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 183.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene $(last 2 messages repeated 3 times) message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 123.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 113.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 133.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 173.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 173.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene $(last 2 messages repeated 2 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 113.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 113.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 133.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 173.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 173.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene $(last 2 messages repeated 2 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 113.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 103.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 123.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 163.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 163.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene $(last 2 messages repeated 2 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 123.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 113.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 133.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 173.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 173.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene $(last 2 messages repeated 2 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 113.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 103.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 123.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 163.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 163.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene $(last 2 messages repeated 2 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 103.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 93.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 113.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 153.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 153.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 193.33 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene #(last 2 messages repeated 1 time) message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 93.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene !(last message repeated 3 times) message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 83.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 103.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 143.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 143.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 183.33 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene #(last 2 messages repeated 1 time) message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 83.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 93.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 113.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 153.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 153.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 193.33 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene #(last 2 messages repeated 1 time) message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 93.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 83.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 103.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 143.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 143.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene $(last 2 messages repeated 2 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 103.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 73.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 93.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 133.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 133.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene $(last 2 messages repeated 2 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 113.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 63.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 83.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 123.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 123.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene $(last 2 messages repeated 2 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 123.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA CalcProp error when calculating logFugacityCoefficient/logFugacityCoefficient.Dtemperature/logFugacityCoefficient.Dpressure for Vapor phase, calcType pure: Property evaluation using equation of state failed: zero or negative pressure message: TEA CalcProp error when calculating logFugacityCoefficient/logFugacityCoefficient.Dmolfraction/logFugacityCoefficient.Dtemperature for Liquid phase, calcType Mixture: Property evaluation using equation of state failed: zero or negative pressure warning: Material object error in CalcProp: CalcProp failed: Property evaluation using equation of state failed: zero or negative pressure message: TEA CalcProp error when calculating logFugacityCoefficient for Vapor phase, calcType pure: Property evaluation using equation of state failed: zero or negative pressure message: TEA CalcProp error when calculating logFugacityCoefficient for Liquid phase, calcType Mixture: Property evaluation using equation of state failed: zero or negative pressure warning: Material object error in CalcProp: CalcProp failed: Property evaluation using equation of state failed: zero or negative pressure *error: calculate failed for unit C-101: run failed: CalcProp() failed on COSE material for calculation of property logFugacityCoefficient in the Liquid phase: CalcProp failed: Property evaluation using equation of state failed: zero or negative pressure (for more info, see full output in report) ?failed to solve unit C-101: calculate failed for unit C-101: run failed: CalcProp() failed on COSE material for calculation of property logFugacityCoefficient in the Liquid phase: CalcProp failed: Property evaluation using equation of state failed: zero or negative pressure (for more info, see full output in report) Solve failed solving C-101 message: TEA warning: Temperature out of correlation range for CP for compound Benzene in enthalpy calculations (T = 101325 K, range = [50.00 - 1000.00] K) message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 101325 K, range = [200.00 - 1500.00] K) message: TEA warning: Temperature out of correlation range for CP for compound P-xylene in enthalpy calculations (T = 101325 K, range = [50.00 - 1000.00] K) $(last 3 messages repeated 2 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene !(last message repeated 3 times) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene !(last message repeated 2 times) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene $(last 2 messages repeated 2 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene $(last 2 messages repeated 2 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene %(last 2 messages repeated 19 times) message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 193.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene $(last 2 messages repeated 5 times) message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 193.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene $(last 2 messages repeated 3 times) message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 193.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 183.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene $(last 2 messages repeated 3 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene  (last message repeated 1 time) message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 183.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 173.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 193.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene $(last 2 messages repeated 2 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene  (last message repeated 1 time) message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 173.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 163.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 183.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene $(last 2 messages repeated 4 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 163.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 153.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 173.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 193.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 193.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene $(last 2 messages repeated 2 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 153.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 143.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 163.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 183.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 183.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene $(last 2 messages repeated 3 times) message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 143.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 133.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 153.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 173.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 173.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene $(last 2 messages repeated 2 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 133.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 123.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 143.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 183.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 183.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene $(last 2 messages repeated 3 times) message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 123.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 113.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 133.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 173.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 173.34 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene $(last 2 messages repeated 2 times) gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene message: TEA warning: Temperature out of correlation range for CP for compound Toluene in enthalpy calculations (T = 113.38 K, range = [200.00 - 1500.00] K)  (last message repeated 1 time) fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Benzene fmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for Toluene gmessage: TEA warning: temperature out of range for CorE relation of heat of vaporization for P-xylene 4error: calculate failed for unit C-101: no results Saved CScasebook_BTX_112.fsd Restoring flowsheet from file Loaded CScasebook_BTX_112.fsd Starting solve solving C-101 solving C-102 Solve finished in 3s, 438ms inserted stream 10 Econnected stream 10 to unit C-101 as INLET at port Column heat duty Starting solve solving C-101 solving C-102 Solve finished in 547ms inserted stream 11 Hconnected stream 11 to unit C-101 as OUTLET at port Reboiler heat duty Starting solve solving C-101 solving C-102 Solve finished in 531ms Restoring flowsheet from file Loaded CScasebook_BTX_112.fsd Starting solve solving C-101 solving C-102 Solve finished in 8s, 734ms Restoring flowsheet from file Loaded CScasebook_BTX_113.fsd Starting solve solving C-101 solving C-102 Solve finished in 2s, 984ms Starting solve solving C-101 solving C-102 Solve finished in 500ms Starting solve solving C-101 solving C-102 Solve finished in 1s, 672ms Starting solve solving C-101 solving C-102 Solve finished in 515ms Starting solve solving C-101 solving C-102 Solve finished in 468ms Saved CScasebook_BTX_113.fsd Starting solve solving C-101 solving C-102 Solve finished in 547ms Starting solve solving C-101 solving C-102 Solve finished in 500ms Restoring flowsheet from file Loaded CScasebook_BTX_113.fsd Starting solve solving C-101 solving C-102 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 1: -1.5332e+015 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 2: -1.59971e+015 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 3: -1.58068e+015 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 4: -1.59011e+015 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 5: -1.55689e+015 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 6: -1.44435e+015 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 7: -1.64702e+015 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 8: -1.51407e+015 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 9: -1.30803e+015 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 1: -6.65588e+015 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 2: -6.96152e+015 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 3: -6.89692e+015 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 4: -6.90935e+015 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 5: -6.7889e+015 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 6: -6.32292e+015 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 7: -7.16281e+015 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 8: -6.61628e+015 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 9: -5.74893e+015 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 1: -2.7456e+016 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 2: -2.87385e+016 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 3: -2.85007e+016 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 4: -2.85078e+016 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 5: -2.80496e+016 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 6: -2.61689e+016 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 7: -2.95595e+016 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 8: -2.73608e+016 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 9: -2.38371e+016 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 1: -1.11486e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 2: -1.16721e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 3: -1.15813e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 4: -1.15757e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 5: -1.13977e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 6: -1.06441e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 7: -1.20028e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 8: -1.11233e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 9: -9.70689e+016 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 1: -4.50264e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 2: -4.71438e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 3: -4.67923e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 4: -4.67482e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 5: -4.60513e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 6: -4.30384e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 7: -4.847e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 8: -4.49588e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 9: -3.92846e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 1: -1.8147e+018 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 2: -1.90005e+018 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 3: -1.88636e+018 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 4: -1.88393e+018 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 5: -1.85655e+018 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 6: -1.73619e+018 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 7: -1.95316e+018 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 8: -1.81305e+018 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 9: -1.58602e+018 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 1: -7.30163e+018 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 2: -7.6447e+018 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 3: -7.59113e+018 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 4: -7.57939e+018 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 5: -7.47151e+018 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 6: -6.99096e+018 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 7: -7.85715e+018 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 8: -7.29831e+018 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 9: -6.39079e+018 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 1: -2.94619e+019 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 2: -3.0848e+019 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 3: -3.06406e+019 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 4: -3.05809e+019 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 5: -3.01582e+019 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 6: -2.8237e+019 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 7: -3.16999e+019 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 8: -2.94684e+019 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 9: -2.58334e+019 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 1: -1.18018e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 2: -1.23549e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 3: -1.22724e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 4: -1.22481e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 5: -1.20802e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 6: -1.13144e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 7: -1.26945e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 8: -1.18055e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 9: -1.03563e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 1: -4.75033e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 2: -4.97294e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 3: -4.94077e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 4: -4.92962e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 5: -4.86352e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 6: -4.55759e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 7: -5.10891e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 8: -4.75409e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 9: -4.1744e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 1: -1.90384e+021 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 2: -1.99278e+021 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 3: -1.98002e+021 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 4: -1.97544e+021 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 5: -1.94919e+021 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 6: -1.82718e+021 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 7: -2.04703e+021 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 8: -1.9056e+021 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 9: -1.67435e+021 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 1: -7.64382e+021 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 2: -8.00029e+021 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 3: -7.95005e+021 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 4: -7.93045e+021 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 5: -7.82663e+021 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 6: -7.33963e+021 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 7: -8.21709e+021 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 8: -7.65297e+021 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 9: -6.72921e+021 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 1: -3.04916e+022 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 2: -3.19046e+022 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 3: -3.17016e+022 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 4: -3.16291e+022 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 5: -3.12128e+022 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 6: -2.92739e+022 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 7: -3.27666e+022 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 8: -3.0521e+022 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 9: -2.68462e+022 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 1: -1.20771e+023 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 2: -1.26305e+023 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 3: -1.25463e+023 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 4: -1.25242e+023 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 5: -1.23549e+023 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 6: -1.15852e+023 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 7: -1.29713e+023 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 8: -1.20793e+023 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 9: -1.06242e+023 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 1: -4.61407e+023 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 2: -4.81755e+023 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 3: -4.77859e+023 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 4: -4.78124e+023 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 5: -4.70808e+023 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 6: -4.40733e+023 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 7: -4.9484e+023 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 8: -4.59861e+023 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 9: -4.03606e+023 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 1: -1.43954e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 2: -1.50219e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 3: -1.4895e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 4: -1.49125e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 5: -1.46779e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 6: -1.37365e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 7: -1.54296e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 8: -1.43339e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 9: -1.2578e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 1: -5.76446e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 2: -6.00691e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 3: -5.95693e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 4: -5.96476e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 5: -5.8737e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 6: -5.50777e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 7: -6.16505e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 8: -5.74049e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 9: -5.05862e+020 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 1: -2.12363e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 2: -2.29083e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 3: -2.35233e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 4: -2.22794e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 5: -2.29315e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 6: -2.25166e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 7: -2.33226e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 8: -2.29546e+017 message: TEA warning: Suspect value for property activityCoefficient.DmolFraction (phase Liquid, calctype mixture, basis ), index 9: -2.15098e+017 4error: calculate failed for unit C-102: no results Ifailed to solve unit C-102: calculate failed for unit C-102: no results Solve failed Starting solve solving C-101 solving C-102 umessage: TEA warning: temperature above TC for determining Racket liquid density for compound Benzene; using TR=1.0 umessage: TEA warning: temperature above TC for determining Racket liquid density for compound Toluene; using TR=1.0 vmessage: TEA warning: temperature above TC for determining Racket liquid density for compound P-xylene; using TR=1.0 #(last 3 messages repeated 1 time) message: TEA Material error: Invalid value for property logFugacityCoefficient (phase Liquid, calctype mixture, basis ), index 1: non-finite value 1.#QNAN `message: TEA CalcProp error when calculating logFugacityCoefficient/logFugacityCoefficient.Dtemperature for Liquid phase, calcType Mixture: Failed to set property logFugacityCoefficient, calctype mixture, phase Liquid: Invalid value for property logFugacityCoefficient (phase Liquid, calctype mixture, basis ), index 1: non-finite value 1.#QNAN {message: TEA warning: PVF inside-out flash failed: failed to obtain logFugacityCoefficient or one of its derivatives from a calculation material for the Liquid phase: Failed to set property logFugacityCoefficient, calctype mixture, phase Liquid: Invalid value for property logFugacityCoefficient (phase Liquid, calctype mixture, basis ), index 1: non-finite value 1.#QNAN twarning: Material object error in CalcEquilibrium: Total phase fraction is not unity after equilibrium calculation error: calculate failed for unit C-102: run failed: Flash calculation failed: Total phase fraction is not unity after equilibrium calculation (for more info, see full output in report) failed to solve unit C-102: calculate failed for unit C-102: run failed: Flash calculation failed: Total phase fraction is not unity after equilibrium calculation (for more info, see full output in report) Solve failed Starting solve solving C-101 solving C-102 umessage: TEA warning: temperature above TC for determining Racket liquid density for compound Benzene; using TR=1.0 umessage: TEA warning: temperature above TC for determining Racket liquid density for compound Toluene; using TR=1.0 vmessage: TEA warning: temperature above TC for determining Racket liquid density for compound P-xylene; using TR=1.0 #(last 3 messages repeated 1 time) message: TEA Material error: Invalid value for property logFugacityCoefficient (phase Liquid, calctype mixture, basis ), index 1: non-finite value 1.#QNAN `message: TEA CalcProp error when calculating logFugacityCoefficient/logFugacityCoefficient.Dtemperature for Liquid phase, calcType Mixture: Failed to set property logFugacityCoefficient, calctype mixture, phase Liquid: Invalid value for property logFugacityCoefficient (phase Liquid, calctype mixture, basis ), index 1: non-finite value 1.#QNAN {message: TEA warning: PVF inside-out flash failed: failed to obtain logFugacityCoefficient or one of its derivatives from a calculation material for the Liquid phase: Failed to set property logFugacityCoefficient, calctype mixture, phase Liquid: Invalid value for property logFugacityCoefficient (phase Liquid, calctype mixture, basis ), index 1: non-finite value 1.#QNAN twarning: Material object error in CalcEquilibrium: Total phase fraction is not unity after equilibrium calculation error: calculate failed for unit C-102: run failed: Flash calculation failed: Total phase fraction is not unity after equilibrium calculation (for more info, see full output in report) failed to solve unit C-102: calculate failed for unit C-102: run failed: Flash calculation failed: Total phase fraction is not unity after equilibrium calculation (for more info, see full output in report) Solve failed Starting solve solving C-101 solving C-102 Solve finished in 500ms Starting solve solving C-101 solving C-102 4error: calculate failed for unit C-102: no results Ifailed to solve unit C-102: calculate failed for unit C-102: no results Solve failed Restoring flowsheet from file Loaded CScasebook_BTX_114.fsd Starting solve solving C-101 solving C-102 Solve finished in 3s, 422ms Restoring flowsheet from file Loaded CScasebook_BTX_114.fsd Starting solve solving C-101 solving C-102 Solve finished in 13s, 46ms Starting solve solving C-101 solving C-102 Solve finished in 406ms Starting solve solving C-101 solving C-102 Solve finished in 546ms Starting solve solving C-101 solving C-102 Solve finished in 422ms Starting solve solving C-101 solving C-102 Solve finished in 562ms Restoring flowsheet from file Loaded CScasebook_BTX_114.fsd Starting solve solving C-101 solving C-102 Solve finished in 2s, 719ms Starting solve solving C-101 solving C-102 Solve finished in 547ms Saved CScasebook_BTX_114.fsd Restoring flowsheet from file Loaded CScasebook_BTX_114.fsd Starting solve solving C-101 solving C-102 Solve finished in 2s, 735ms Starting solve solving C-101 solving C-102 Solve finished in 453ms Restoring flowsheet from file Loaded CScasebook_BTX_114.fsd Starting solve solving C-101 solving C-102 Solve finished in 2s, 687ms Starting solve solving C-101 solving C-102 Solve finished in 438ms ]=x temperaturepressure compositionflow 0@V@B@33333sI@@Fpressure temperatureflow compositionBTX-Antoine-UNIFACڐ@'t+""BTX-Antoine-UNIFAC$Benzene / Toluene / p-Xylene exampleư>MbP?MbP?MbP?K2C:\Program Files\COCO\data\DefaultComponentLib.pcdiBenzene-CHCHCHCHCHCH-C6H671-43-2c1ccccc13`f@FRAMb?&?v@@jq@@jq@`8@KS@? ?`=C@Ǩ?A“A(AoAbbATS}Ar]@5*@6 8 8 8q@q@?@?`f@`? 8q@`f@i@V@`8C $@">@q@G@e@FA?п??q@`f@j@ '_)h@-2`*o?D@@3kq@d@6@@3$f6@ f`6f>@jq@@@ B@)@`)+`3j>i@p@h?)k2L@Qq@@h)8@ [@aվ@@jq@@e`>? @ A 8q@@@f-]?@ ?f`?;~o>q@y@H>:?zDc@@ 8@o@@@f@5^jTwx`IC>q@`f@@@@`I C?.Z@>I@@@d 8 8 8 8 8 8 8@35@B@D 8 8 u@`f@ `&5> 8 8@jq@@ |?5.[@@W;?Cl,f"-ܾ@@ @@33@@33@C?1L@ ? 8 8 8Y?h? 8j?@j>?Wʢ?pV@?&@ t@` A??xToluene (C6H5)CH3C7H8108-88-3 c1ccccc1(C)3~@pWOA X9?@`?w@Ef@Ef@U?  W@ [?@`?=@V9@x?ADA"AxAxPYAA@ #@`:? 8 8 8IW@Ef@U??~@.4? 8@3cd@`fn@i X@n&@i>@Ef@@3@eA@?෯?S@+0?Ef@ρ@j2Û@v^0 ?D@Ef@d@`H@%@@`?g|>@3Cf@@@ @̮E)@@)7>tUb@p@S:?dk`F@=o@@h@c @t6@.}@Ef@zw@e Z>_?=s@`f@ 8Ef@@@f +'7uqZ[`>Ef@}@`Xo> a?@ g@`@ 8zw@@@f43@mV 7|ϾEf@ρ@OV܂@ٿ \? 8i@p@ 8 8 8 8 8 8 8 /4@`f@N 8 85v@t@ N@]"? 8 8Ef@zw@ x#4@@33333ξ =DQOI?Zb#>@a@v@v@ ?w@>W? 8 8 8f?@? 84?f?E?`[@ [?"@-s@K\y?4?Z?P-xylene CH3(C6H4)CH3C8H10106-42-3c1(C)ccc(C)cc1 A@lJA&1?t?zy@`q@`q@C@ Z@`๿?ज़?S=}@ ?bXA1qAA~A?QpA A`E$/@ ?S?A@ T? 8`q@A@i VX@ d&s>@ׯq@A@ew܊A/L? !?&kv?`q@A@jK̎@ @#MG? ~a)3@`q@d@vuA*@k`g>`fq@@w@L *@y>MRi@p@o@z d9@W`f.u@p@h7@3o@@@@Ͼ@`q@y@eOZ>`?`V"@ 8`fq@@fbE?)^@zn FY>`q@y@`>`C?@V|F@ 8t@@@f )l@5P@ `^?ټܾq@A@@p^@` l?.Vʢ>I@@@d 8 8 8 8 8 8 8 5@@`I 8 8@3#w@H@ kZa> 8 8`q@y@ e@ffffiFtϺF?J +6:vj$Ť@ף@Q @Q @h?„@v? 8 8 8@?? 8KP?ç??`@`๿?M@-ms@@ё?`I?activityCoefficientactivityCoefficientDdensitydensity enthalpyenthalpyentropyentropy:: excessEnthalpyexcessEnthalpy heatCapacityheatCapacityCpKK heatOfVaporizationheatOfVaporizationO logFugacityCoefficientlogFugacityCoefficientsurfaceTensionsurfaceTensionsurfaceTension (pure)surfaceTension (pure)thermalConductivitythermalConductivity04thermalConductivity (pure)thermalConductivity (pure))1 vaporPressure vaporPressureN viscosity viscosity& viscosity (pure)viscosity (pure)" volumevolumeVapor Vapor phaseLiquid Liquid phase   ACHACCH2ACHqh??K7 *@ACCH3B?`"?%C ;@d@YbACHACCH2ACHqh??K7 *@ACCH3B?`"?%C ;@d@Yb V瞯<BTX-Antoine-UNIFAC71-43-2BenzeneKS@v@C6H6BTX-Antoine-UNIFACBenzene108-88-3Toluene  W@w@C7H8BTX-Antoine-UNIFACToluene106-42-3P-xylene Z@zy@C8H10BTX-Antoine-UNIFACP-xylene excessEnthalpy.Dpressure?thermalConductivity.Dmoles? / molviscosity.Dtemperature??thermalConductivity.Dpressure?activityCoefficient thermalConductivity.Dtemperature?heatCapacity.DmolFraction?density.Dpressure?@enthalpy.Dmoles?heatOfVaporization?#logFugacityCoefficient.DmolFractionentropy.Dtemperature?viscosity.Dmoles?? / mol volume.Dmoles@@enthalpy?vaporPressure.Dtemperature?volume.Dpressure@@excessEnthalpy.Dtemperature?surfaceTension.DmolFraction?heatOfVaporization.DmolFraction? activityCoefficient.DtemperatureheatOfVaporization.Dpressure?activityCoefficient.Dmoles / molenthalpy.DmolFraction?enthalpy.Dpressure?logFugacityCoefficientvolume.DmolFraction@@density?@thermalConductivity?surfaceTension.Dtemperature?surfaceTension?density.DmolFraction?@heatCapacity.Dtemperature?#logFugacityCoefficient.DtemperatureexcessEnthalpy?viscosity.DmolFraction??surfaceTension.Dmoles? / molenthalpy.Dtemperature?entropy.Dpressure?density.Dmoles?@ / mol thermalConductivity.DmolFraction?logFugacityCoefficient.Dmoles / molheatOfVaporization.Dtemperature?surfaceTension.Dpressure?entropy.DmolFraction?volume@@entropy?heatCapacity.Dpressure? logFugacityCoefficient.Dpressureviscosity.Dpressure? heatCapacity?entropy.Dmoles?activityCoefficient.Dpressure activityCoefficient.DmolFraction viscosity??heatOfVaporization.Dmoles?excessEnthalpy.Dmoles?volume.Dtemperature@@density.Dtemperature?@heatCapacity.Dmoles?excessEnthalpy.DmolFraction?@&{71F5AC07-65A1-4357-8F1B-A8CD58148763}Temperature profile?Pressure profile?Vapour Flow profile?Liquid Flow profile?Vapour Density profile@?Vapour Viscosity profile??Vapour Heat capacity profile?#Vapour Thermal conductivity profile?Liquid Density profile@?Liquid Viscosity profile??Liquid Heat capacity profile?Liquid Thermal cond. profile?Surface tension profile?RelativePerturbationTemperature?RelativePerturbationPressure?PerturbationComposition?TotalMassBalancePropertiesFraction? TotalFlowMass? streamParamswork?BactivityCoefficientactivityCoefficient.Dmoles activityCoefficient.DmolFractionactivityCoefficient.Dpressure activityCoefficient.Dtemperaturedensitydensity.Dmolesdensity.DmolFractiondensity.Dpressuredensity.Dtemperatureenthalpyenthalpy.Dmolesenthalpy.DmolFractionenthalpy.Dpressureenthalpy.Dtemperatureentropyentropy.Dmolesentropy.DmolFractionentropy.Dpressureentropy.DtemperatureexcessEnthalpyexcessEnthalpy.DmolesexcessEnthalpy.DmolFractionexcessEnthalpy.DpressureexcessEnthalpy.Dtemperature heatCapacityheatCapacity.DmolesheatCapacity.DmolFractionheatCapacity.DpressureheatCapacity.DtemperatureheatOfVaporizationheatOfVaporization.DmolesheatOfVaporization.DmolFractionheatOfVaporization.DpressureheatOfVaporization.DtemperaturelogFugacityCoefficientlogFugacityCoefficient.Dmoles#logFugacityCoefficient.DmolFraction logFugacityCoefficient.Dpressure#logFugacityCoefficient.DtemperaturesurfaceTensionsurfaceTension.DmolessurfaceTension.DmolFractionsurfaceTension.DpressuresurfaceTension.DtemperaturethermalConductivitythermalConductivity.Dmoles thermalConductivity.DmolFractionthermalConductivity.Dpressure thermalConductivity.Dtemperature vaporPressurevaporPressure.Dtemperature viscosityviscosity.Dmolesviscosity.DmolFractionviscosity.Dpressureviscosity.Dtemperaturevolume volume.Dmolesvolume.DmolFractionvolume.Dpressurevolume.DtemperaturebubblePointTemperaturebubblePointPressuredewPointTemperaturedewPointPressureVaporBTX-Antoine-UNIFACVaporLiquidBTX-Antoine-UNIFACLiquid VaporLiquiddefaultdefault material templateBTX-Antoine-UNIFAC 1 Gat least one compound needs to be present for materials of type default defaultм@fffffr@$@Kh/? 1ZGU?I?1ZGU?)pGJU?KqU?nД??1ZGU?I?1ZGU?)pGJU?KqU?nД?1ZGU?I?1ZGU?)pGJU?KqU?nД?fffffr@м@$@Kh/?22,40,4,4 =_=_defaultм@zNVv@7! @~?T?dː6?K<`?5?k >sX|F>r}?;?5 ,?z?V%Z5>Av>?T?6?j<`?%|?k >N|F>23,92,9,229  defaultм@Ҧx@$@9?zұ^_?܀?`l*T?f8(?vo?m>(?fHc¦?K ?J~&?iI?_/l?ߎy??۱^_?⯁܀?T*T?n8(?o??nm>(?24GRLGRGR ԑ`defaultм@S" b4w@$ @a1Y?^_? /R,?#{N?G g?\a&J?8N?<0Fp?]F?_T(??sD*6?=)/9??m^_?q4,?A{N?S g?ْha&J?,މ8N?25GRLGRGR defaultм@$r]y@$ @g?f(=8yc=+I?h"E NF?CF[? }l?xnt>@ZE7=Y^yZ?7 V?f)?v9>??f(=*yc=S,I?W F NF?!\?B_}l?26E S!K!E S!E E!S!  , 384.11work heat duty|a@?temperatureLowlower temperature for heat duty+Zo]y@?temperatureHighupper temperature for heat duty+Zo]y@?27,50,5,5 , 360.73work heat duty,CA@?temperatureLowlower temperature for heat dutyrĵuv@?temperatureHighupper temperature for heat dutyrĵuv@?210  work heat dutyj@j@@?temperatureLowlower temperature for heat dutyfffff}@fffff}@?temperatureHighupper temperature for heat dutyfffff}@fffff}@?211* 3"-"* 3"* *"3"  tagework heat duty1w@?temperatureLowlower temperature for heat dutyyIx@?temperatureHighupper temperature for heat dutyyIx@?2C-101ChemSep Unit OperationqeWCXcnCSUO5Y[ChemSep] Version=6.31 Name=C:\DOCUME~1\Harry\LOCALS~1\Temp\CS350.sep Title=ChemSep CO Unit Operation "C-101" in COFE Flowsheet User=Harry Date=2009-04-12 Time=11:00:55 [Cape-Open] unitname=C-101 CO_ID=CS350 3 components Benzene 71-43-2 78.1139984131 Mw Toluene 108-88-3 92.1409988403 Mw P-xylene 106-42-3 106.166999817 Mw 1 thermo exe=C:\PROGRA~1\ChemSepL\bin\co-col2.exe mode=COFE NoWarnings=FALSE WilsonEstimate=TRUE Status= 0 only K-values and ethalpies 0 use only perturbed derivative 0 use only perturbed mole derivative 0.001 relative T perturbation 0.001 relative P perturbation 0.001 X perturbation 0 write all values to log 1 use initial guess 0 inlet reflash 0 outlet reflash 1 expose energy ports 0 clear log 0 update icon [Paths] Device drivers path=c:\progra~1\chemsepl\bin\ Help and Info path=c:\progra~1\chemsepl\help\ Component data path=c:\progra~1\chemsepl\pcd\ Property data path=c:\progra~1\chemsepl\ipd\ Section data path=c:\progra~1\chemsepl\ild\ Executables path=C:\PROGRA~1\ChemSepL\bin\ Temporary path=WINTMPDIR Scripts path=c:\progra~1\chemsepl\bin\ [Units] Temperature=C Flow=mol/s Mass flow=kg/s Pressure=bar Heat=MW Enthalpy=kJ/kmol Entropy=J/kmol/K Fraction= Length=m 1/Length=1/m Area=m Volume=m3 Mass=kg Angle=rad Velocity=m/s Surface tension=N/m Density=kg/m3 Molar density=kmol/m3 Viscosity=N/m2.s Molecular weight=kg/kmol Heat capacity=J/kmol/K Thermal conductivity=J/s/m/K Diffusivity=1e-8 m/s Interaction parameter=J/mol Time=s [Components] 3 125 501 Library Offset, Index DT=2009-03-26,23:59:44 CHK=55335 CAS=71-43-2 CID=Benzene Name=Benzene Lib=c:\program files\chemsepl\pcd\chemsep1.pcd 140 502 Library Offset, Index DT=2009-03-26,23:59:44 CHK=60854 CAS=108-88-3 CID=Toluene Name=Toluene Lib=c:\program files\chemsepl\pcd\chemsep1.pcd 152 507 Library Offset, Index DT=2009-03-26,23:59:44 CHK=62355 CAS=106-42-3 CID=P-xylene Name=P-xylene Lib=c:\program files\chemsepl\pcd\chemsep1.pcd [Operation] 2 Operation Column 1 Operation kind Simple Distillation 1 Condenser Total (Liquid product) 1 Reboiler Partial (Liquid product) 20 Stages 1 Feed stages 0 Sidestream stages F=10 S= 0 Pumparound stages P= [Properties] [Thermodynamics] 3 K model Gamma-Phi 11 Activity coefficient Modified UNIFAC (D) * Wilson model * * UNIQUAC model * 3 Equation of State Cubic 5 Cubic EOS Peng-Robinson * Virial EOS * 1 Vapour pressure Antoine [Enthalpy] 3 Enthalpy Excess 1 Enthalpy reference state Vapour 298.15 Enthalpy reference temperature 1 Formation enthalpies Excluded 298.15 Exergy surroundings temperature [Physical property models] 0 No Check T range * Cubic EOS * * Virial EOS * * Vapour model * * Liquid mixture density * * Liquid component density * * Vapour mixture viscosity * * Vapour mixture viscosity pressure correction * * Vapour component viscosity * * Liquid mixture viscosity * * Liquid component viscosity * Vapour mixture Cp * Vapour component Cp * Liquid mixture Cp * Liquid component Cp * Vapour mixture conductivity * * Vapour component conductivity * * Liquid mixture conductivity * * Liquid component conductivity * Mixture surface tension * * Component surface tension * * Vignes MS D-model * * D mixture model * * Vapour Diffusion Coefficients * [Property Data] [Peng-Robinson Data] i j kij Component Component 1 2 * Benzene/Toluene 1 3 * Benzene/P-xylene 2 3 * Toluene/P-xylene [Reaction data] 0 Number of reactions [Specifications] Top Bottom [Heaters/Coolers] 0 Number 100000 Column duty Qcolumn 2 First stage 19 Last stage [Efficiencies] 1 Default efficiency 0 Number [Pressures] 1 Column pressure Constant pressure 101325 Condenser pressure 101325 Top pressure * Pressure Drop * Bottom pressure [Feeds] 1 Number 1 Feed state T & p 10 Stage Feed1{split} 298.15 Temperature 101325 Pressure 0 Vapour fraction 3 componentflows 0.0033496439031 Component 1 flow 0.0033496439031 Component 2 flow 0.00334974439342 Component 3 flow [Condenser] 1 Type Reflux ratio 2 Value Qcondenser * Type * * Initialization guess [Reboiler] 9 Type Fraction of combined feeds recovered 0.666667 Value Qreboiler * Type * * Initialization guess [Solve options] 3 Initialization Old Results 1 Method Newton's method 0.2 Flow Step limit 10 Temperature Step limit 1 Composition Step limit 1 Flux Step limit 0.000001 Accuracy 30 Maximum iterations 1 Iteration count & function vector 0 T/V/L profiles 0 X/Y profiles 0 Variable and function vectors 0 Jacobian 1 History Screen History file= 1 Feeds type Stage below 1 Interactive 0 Log thermodynamics 0 Log enthalpy/entropy 0 Log physical properties 0 Log timing 0 CO numeric differencing 0 Log from iteration 0 CS K-value 0 CS enthalpy 0 CS entropy 0 CS flash 0 CS activity coefficient 0 CS vapor pressuure 0 CS density 0 CS viscosity 0 CS thermal conductivity 0 CS heat capacity 0 CS surface tension 0 CS diffusivity [Programs] Temporary file=SCRATCH.TMP User program= 8 DOS extender NT 1 Show windows Hidden [FlowSheet] [CoCo] [Settings] -1 -1 -1 0 Graph settings 1 Auto colors 1 Auto points 0.2 StringGrid5 2 8 Title Labels Stages Axis color Commands Box Labels box Import data StringGrid4 5 9 Title Start End Tic interval Small tics Grid Logarithmic Scientific notation x1 y1 x2 y2 StringGrid3 1 14 Label Plot X Plot Y X axis Y axis Units X Units Y Color Points Thickness Style 1st stage Last stage 0 Graph settings -1 -1 StringGrid7 16 2 StringGrid11 5 3 -1 -1 -1 0.95 0.95 1.2 1 0 Use old results 1 Automatic 0 Keep sep-files 1 Restore original StringGrid1 1 6 StringGrid2 4 1 StringGrid3 1 1 None -1 -1 -1 21 Binary Phase Diagram T p x -1 -1 StringGrid1 3 5 -1 -1 -1 0 21 Ternary Phase Diagram T 0 1 1 StringGrid1 3 5 0 0 -1 -1 -1 21 Binary Property Diagram StringGrid1 13 4 Axis Left Right X/Y Property -click to select- -click to select- x Title x Units - Minimum 0 Maximum 1 Interval 0.2 Grid Off Off Off Log Off Off Off Color Blue Red Black Line Normal Normal Style Solid Solid Point None None -1 -1 [End Settings] [End of Input] [Results] 1 Converged 0 Iterations [Profiles] Stage Temperature Pressure Vapour Flow Liquid Flow 1 353.7162378 1.013250000E+05 3.349674050E-03 6.699348100E-03 2 354.2888036 1.013250000E+05 1.004902215E-02 6.484402314E-03 3 355.1493975 1.013250000E+05 9.834076365E-03 6.257873683E-03 4 356.3562960 1.013250000E+05 9.607547733E-03 6.021131678E-03 5 357.9112424 1.013250000E+05 9.370805729E-03 5.778637609E-03 6 359.7396944 1.013250000E+05 9.128311660E-03 5.535247869E-03 7 361.7452222 1.013250000E+05 8.884921919E-03 5.290375257E-03 8 363.9577845 1.013250000E+05 8.640049307E-03 5.033542891E-03 9 366.6832968 1.013250000E+05 8.383216941E-03 4.750237155E-03 10 370.3907147 1.013250000E+05 8.099911205E-03 1.865393080E-02 11 371.6276300 1.013250000E+05 1.195457265E-02 1.844741352E-02 12 373.3645484 1.013250000E+05 1.174805537E-02 1.823952814E-02 13 375.6468216 1.013250000E+05 1.154016999E-02 1.804164374E-02 14 378.3652917 1.013250000E+05 1.134228559E-02 1.786669078E-02 15 381.2435987 1.013250000E+05 1.116733263E-02 1.771884993E-02 16 383.9647608 1.013250000E+05 1.101949178E-02 1.758690127E-02 17 386.3710060 1.013250000E+05 1.088754312E-02 1.744827265E-02 18 388.6052142 1.013250000E+05 1.074891450E-02 1.727670484E-02 19 391.1669722 1.013250000E+05 1.057734669E-02 1.704829991E-02 20 394.8675969 1.013250000E+05 1.034894176E-02 6.699358149E-03 [Enthalpies/Entropies] Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy 1 -0.2577221E+08 -0.2577221E+08 0.1545705E+05 -0.7017025E+05 2 0.4879220E+07 -0.2576445E+08 0.1609433E+05 -0.6921572E+05 3 0.4989363E+07 -0.2574853E+08 0.1695444E+05 -0.6804602E+05 4 0.5146604E+07 -0.2571787E+08 0.1805915E+05 -0.6668561E+05 5 0.5353976E+07 -0.2566482E+08 0.1937953E+05 -0.6520203E+05 6 0.5604375E+07 -0.2558492E+08 0.2083479E+05 -0.6365559E+05 7 0.5885450E+07 -0.2547999E+08 0.2234292E+05 -0.6201792E+05 8 0.6198616E+07 -0.2535184E+08 0.2391781E+05 -0.6012093E+05 9 0.6583384E+07 -0.2518461E+08 0.2573558E+05 -0.5775464E+05 10 0.7112558E+07 -0.2493190E+08 0.2802326E+05 -0.5499213E+05 11 0.7318516E+07 -0.2480160E+08 0.2892282E+05 -0.5425418E+05 12 0.7617160E+07 -0.2460729E+08 0.3015493E+05 -0.5326679E+05 13 0.8026848E+07 -0.2433358E+08 0.3170633E+05 -0.5204643E+05 14 0.8541778E+07 -0.2398280E+08 0.3342803E+05 -0.5069381E+05 15 0.9120549E+07 -0.2358536E+08 0.3505337E+05 -0.4936919E+05 16 0.9699581E+07 -0.2318914E+08 0.3634404E+05 -0.4820309E+05 17 0.1023272E+08 -0.2282854E+08 0.3727011E+05 -0.4719477E+05 18 0.1073227E+08 -0.2249601E+08 0.3808608E+05 -0.4615842E+05 19 0.1129456E+08 -0.2212817E+08 0.3930354E+05 -0.4474416E+05 20 0.1210946E+08 -0.2160458E+08 0.4155050E+05 -0.4263778E+05 [Vapour Properties] Stage Moleweight Density Viscosity Heat capacity Thermal conductivity 1 0.7823633E+02 0.2777197E+01 0.9018876E-05 0.9883828E+05 0.1509275E-01 2 0.7840697E+02 0.2778781E+01 0.9024091E-05 0.9932349E+05 0.1511953E-01 3 0.7866886E+02 0.2781354E+01 0.9031622E-05 0.1000644E+06 0.1515907E-01 4 0.7904687E+02 0.2785343E+01 0.9041564E-05 0.1011265E+06 0.1521313E-01 5 0.7955112E+02 0.2791084E+01 0.9053340E-05 0.1025322E+06 0.1528071E-01 6 0.8016331E+02 0.2798485E+01 0.9065857E-05 0.1042283E+06 0.1535846E-01 7 0.8084018E+02 0.2806713E+01 0.9078472E-05 0.1061052E+06 0.1544591E-01 8 0.8155018E+02 0.2814332E+01 0.9092264E-05 0.1081083E+06 0.1555541E-01 9 0.8233191E+02 0.2820202E+01 0.9109950E-05 0.1103933E+06 0.1572142E-01 10 0.8331689E+02 0.2825211E+01 0.9131860E-05 0.1133402E+06 0.1599228E-01 11 0.8384872E+02 0.2834166E+01 0.9132284E-05 0.1147385E+06 0.1604088E-01 12 0.8463080E+02 0.2847908E+01 0.9131066E-05 0.1167774E+06 0.1610546E-01 13 0.8572016E+02 0.2867978E+01 0.9126287E-05 0.1195890E+06 0.1618442E-01 14 0.8711001E+02 0.2894852E+01 0.9115895E-05 0.1231374E+06 0.1627042E-01 15 0.8869052E+02 0.2926752E+01 0.9099392E-05 0.1271312E+06 0.1635350E-01 16 0.9027745E+02 0.2959753E+01 0.9078898E-05 0.1311102E+06 0.1830832E-01 17 0.9171887E+02 0.2989913E+01 0.9057682E-05 0.1347149E+06 0.1859375E-01 18 0.9300586E+02 0.3015830E+01 0.9037124E-05 0.1379541E+06 0.1882728E-01 19 0.9433365E+02 0.3040104E+01 0.9013927E-05 0.1413475E+06 0.1903116E-01 20 0.9613292E+02 0.3070573E+01 0.8976527E-05 0.1459741E+06 0.1924418E-01 [Liquid Properties] Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension 1 0.7840697E+02 0.8121001E+03 0.3152610E-03 0.1500853E+06 0.1234895E+00 0.2107935E-01 2 0.7880415E+02 0.8115006E+03 0.3135074E-03 0.1508997E+06 0.1231209E+00 0.2101745E-01 3 0.7938940E+02 0.8105982E+03 0.3109065E-03 0.1521100E+06 0.1225774E+00 0.2092506E-01 4 0.8018763E+02 0.8093304E+03 0.3073276E-03 0.1537817E+06 0.1218358E+00 0.2079675E-01 5 0.8118140E+02 0.8076938E+03 0.3028342E-03 0.1558993E+06 0.1209149E+00 0.2063361E-01 6 0.8231264E+02 0.8057663E+03 0.2977354E-03 0.1583638E+06 0.1198798E+00 0.2044506E-01 7 0.8354034E+02 0.8036490E+03 0.2924451E-03 0.1611075E+06 0.1188030E+00 0.2024315E-01 8 0.8494385E+02 0.8013094E+03 0.2871483E-03 0.1643256E+06 0.1176855E+00 0.2002814E-01 9 0.8677916E+02 0.7984237E+03 0.2815112E-03 0.1686348E+06 0.1164034E+00 0.1977489E-01 10 0.8929291E+02 0.7945041E+03 0.2749059E-03 0.1746903E+06 0.1147907E+00 0.1944312E-01 11 0.8985192E+02 0.7932087E+03 0.2719879E-03 0.1761124E+06 0.1142581E+00 0.1932539E-01 12 0.9060066E+02 0.7913929E+03 0.2679183E-03 0.1780574E+06 0.1135310E+00 0.1916098E-01 13 0.9152795E+02 0.7890125E+03 0.2626263E-03 0.1805356E+06 0.1126098E+00 0.1894658E-01 14 0.9255909E+02 0.7861850E+03 0.2564064E-03 0.1833906E+06 0.1115590E+00 0.1869354E-01 15 0.9357829E+02 0.7831998E+03 0.2499298E-03 0.1863241E+06 0.1104956E+00 0.1842835E-01 16 0.9449540E+02 0.7803845E+03 0.2519510E-03 0.1890554E+06 0.1095318E+00 0.1818050E-01 17 0.9531030E+02 0.7779001E+03 0.2489675E-03 0.1915209E+06 0.1087103E+00 0.1796475E-01 18 0.9614610E+02 0.7755978E+03 0.2464330E-03 0.1940094E+06 0.1079716E+00 0.1776964E-01 19 0.9726261E+02 0.7729654E+03 0.2437259E-03 0.1972242E+06 0.1071497E+00 0.1755401E-01 20 0.9900771E+02 0.7691802E+03 0.2397632E-03 0.2021724E+06 0.1059968E+00 0.1725146E-01 [Vapour phase compositions] Component Mole fractions on stages: 1 to 5 1 0.991279544E+00 0.979119349E+00 0.960467868E+00 0.933590998E+00 0.897898910E+00 2 0.871952471E-02 0.208749193E-01 0.395073597E-01 0.663122928E-01 0.101748532E+00 3 0.931731288E-06 0.573184087E-05 0.247721900E-04 0.967095008E-04 0.352557335E-03 Component Mole fractions on stages: 6 to 10 1 0.855099572E+00 0.809407539E+00 0.765858144E+00 0.727567205E+00 0.694327999E+00 2 0.143702866E+00 0.186832457E+00 0.223314144E+00 0.244163761E+00 0.240419846E+00 3 0.119756165E-02 0.376000458E-02 0.108277118E-01 0.282690339E-01 0.652521545E-01 Component Mole fractions on stages: 11 to 15 1 0.660909923E+00 0.611627155E+00 0.542923689E+00 0.455392632E+00 0.356403683E+00 2 0.269340863E+00 0.312150401E+00 0.371895178E+00 0.447872598E+00 0.533173223E+00 3 0.697492148E-01 0.762224435E-01 0.851811334E-01 0.967347700E-01 0.110423093E+00 Component Mole fractions on stages: 16 to 20 1 0.258617395E+00 0.173998010E+00 0.108557202E+00 0.619950368E-01 0.306524777E-01 2 0.615610621E+00 0.682087431E+00 0.721216937E+00 0.719678078E+00 0.654083905E+00 3 0.125771985E+00 0.143914558E+00 0.170225861E+00 0.218326885E+00 0.315263617E+00 [Liquid phase compositions] Component Mole fractions on stages: 1 to 5 1 0.979119349E+00 0.950832997E+00 0.909220877E+00 0.852714382E+00 0.783209647E+00 2 0.208749193E-01 0.491323951E-01 0.906337155E-01 0.146740115E+00 0.214901930E+00 3 0.573184087E-05 0.346079405E-04 0.145407433E-03 0.545503182E-03 0.188842369E-02 Component Mole fractions on stages: 6 to 10 1 0.706705861E+00 0.630828871E+00 0.560166686E+00 0.493504722E+00 0.427299157E+00 2 0.287262224E+00 0.351491331E+00 0.392755887E+00 0.395234000E+00 0.348429224E+00 3 0.603191548E-02 0.176797976E-01 0.470774263E-01 0.111261278E+00 0.224271618E+00 Component Mole fractions on stages: 11 to 15 1 0.393298654E+00 0.347341490E+00 0.290167936E+00 0.226678335E+00 0.164781885E+00 2 0.376577449E+00 0.415112345E+00 0.463351276E+00 0.516818843E+00 0.567950851E+00 3 0.230123897E+00 0.237546165E+00 0.246480789E+00 0.256502822E+00 0.267267264E+00 Component Mole fractions on stages: 16 to 20 1 0.111692449E+00 0.708829657E-01 0.420020040E-01 0.227080669E-01 0.104358099E-01 2 0.608747151E+00 0.632269975E+00 0.630444542E+00 0.589430971E+00 0.489557306E+00 3 0.279560400E+00 0.296847059E+00 0.327553454E+00 0.387860962E+00 0.500006884E+00 [Reaction rates] Component reaction rates on stages: 1 to 5 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 6 to 10 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 11 to 15 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 16 to 20 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 [Condenser Heat Duty] -3.080169026E+05 [Reboiler Heat Duty] 3.578309194E+05 [K-values] Component K-values on stages: 1 to 5 1 0.101241949E+01 0.102974902E+01 0.105636363E+01 0.109484618E+01 0.114643501E+01 2 0.417703389E+00 0.424870785E+00 0.435901359E+00 0.451902990E+00 0.473464970E+00 3 0.162553584E+00 0.165622131E+00 0.170363987E+00 0.177284949E+00 0.186693983E+00 Component K-values on stages: 6 to 10 1 0.120997958E+01 0.128308586E+01 0.136719705E+01 0.147428637E+01 0.162492263E+01 2 0.500249819E+00 0.531542174E+00 0.568582595E+00 0.617770179E+00 0.690010611E+00 3 0.198537546E+00 0.212672384E+00 0.229997966E+00 0.254077929E+00 0.290951471E+00 Component K-values on stages: 11 to 15 1 0.168042776E+01 0.176088147E+01 0.187106732E+01 0.200898175E+01 0.216288146E+01 2 0.715233686E+00 0.751966108E+00 0.802620434E+00 0.866594952E+00 0.938766484E+00 3 0.303094194E+00 0.320874242E+00 0.345589355E+00 0.377129458E+00 0.413156073E+00 Component K-values on stages: 16 to 20 1 0.231544187E+01 0.245472247E+01 0.258457191E+01 0.273008882E+01 0.293723995E+01 2 0.101127469E+01 0.107879142E+01 0.114398155E+01 0.122097096E+01 0.133607220E+01 3 0.449891973E+00 0.484810456E+00 0.519688792E+00 0.562899881E+00 0.630518555E+00 [Molecular weights] 1 78.114 2 92.141 3 106.167 [Feed stream 1] 10 Stage Number 1.0049032199620E-02 Flow rate 2.9815000000000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -3.7901619293392E+07 Enthalpy [J/kmol] -1.1611696433490E+05 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 3.3333000000007E-01 Mole fraction of component 1 3.3333000000007E-01 Mole fraction of component 2 3.3333999999987E-01 Mole fraction of component 3 1.0049032199620E-02 Flow rate 3.3333000000007E-01 Mole fraction of component 1 3.3333000000007E-01 Mole fraction of component 2 3.3333999999987E-01 Mole fraction of component 3 9.2140805953443E+01 Molar mass 8.6455346607154E+02 Density 5.8636921825020E-04 Viscosity 1.3298139619436E-01 Thermal conductivity 1.5830793828504E+05 Heat capacity 2.7981923535285E-02 Surface tension [Top product] 1 Stage Number 3.3496740500000E-03 Flow rate 3.5371623780000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.5772209946428E+07 Enthalpy [J/kmol] -7.0170247785488E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 9.7911934900000E-01 Mole fraction of component 1 2.0874919300000E-02 Mole fraction of component 2 5.7318408700000E-06 Mole fraction of component 3 3.3496740500000E-03 Flow rate 9.7911934900000E-01 Mole fraction of component 1 2.0874919300000E-02 Mole fraction of component 2 5.7318408700000E-06 Mole fraction of component 3 7.8406971721370E+01 Molar mass 8.1210012399860E+02 Density 3.1526097336988E-04 Viscosity 1.2348946094370E-01 Thermal conductivity 1.5008529264155E+05 Heat capacity 2.1079345558550E-02 Surface tension [Bottom product] 20 Stage Number 6.6993581490000E-03 Flow rate 3.9486759690000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.1604577314079E+07 Enthalpy [J/kmol] -4.2637776048634E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 1.0435809900000E-02 Mole fraction of component 1 4.8955730600000E-01 Mole fraction of component 2 5.0000688400000E-01 Mole fraction of component 3 6.6993581490000E-03 Flow rate 1.0435809900000E-02 Mole fraction of component 1 4.8955730600000E-01 Mole fraction of component 2 5.0000688400000E-01 Mole fraction of component 3 9.9007712764464E+01 Molar mass 7.6918023133782E+02 Density 2.3976317153705E-04 Viscosity 1.0599681805380E-01 Thermal conductivity 2.0217241577353E+05 Heat capacity 1.7251462039965E-02 Surface tension [End of Results] GUIArguments /kpldUseCOSEThermo:UseCOSEDiffusionCoefficients8UsePerturbedDerivativesOnly"UsePerturbed_ddX"SuppressWarnings@RelativePerturbationTemperatureMbP?:RelativePerturbationPressureMbP?0PerturbationCompositionMbP?InletReflash<none>OutletFlash AutoDUseOnlyKValuesAndEnthalpyFromCOSE*RestartDataAvailable,OmitStageFromPortNameWilsonEstimate"LogPropertyCallsEnergyPorts UseInitialGuess(Temperature profile4Temperature at each stagerĵuv@y$v@ c2v@!;ocEv@+r^v@{v@ nv@Sv@bv@^@&w@? :w@0Uw@%aYzw@<إw@w@hGow@%x@2Ix@u rx@yIx@"Pressure profile.Pressure at each stageм@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@(Vapour Flow profile4Vapour Flow at each stage7! @(fn$@G #@7#@r?ڽ"@{A"@<[|!@G!@5 @9'3 @'@~ '@J2)'@W@&@ZU&@H &@.aD l%@q%@@'%@?ю~$@(Liquid Flow profile4Liquid Flow at each stage7!@g)@ @犣@\h-S@Mor$@LJ!X)@nOY"@W3+>@Gh2@10Dr2@WQ=2@b* 2@@kr1@1@`)?1@pr1@q F1@b] 1@$@4Vapour Moleweight profile@Vapour Moleweight at each stageD S@ S@f,ΪS@wJS@ ҌES@Gɫs T@6U5T@s,&6cT@p>T@|GT@ݰmQT@F_(U@nU@bg U@Nz1,V@V@QV@`@W@ޓZW@>X@.Vapour Density profile:Vapour Density at each staged7@+m:@Oʤ6@@#)aH@e##T@ŊLc@{%t@~@ Ə@Ie9@){K9_@W"P@.s@V*(@Oi@2@ǁW@]zk @ "R@Iط@2Vapour Viscosity profile>Vapour Viscosity at each stage*>6ꁟ>>4~ '>4y>1>Cذ >V?_>K>*fH&>F&>0'4&>U#>L>2>0xc=2 >U>Km>P>z<>:Vapour Heat capacity profileFVapour Heat capacity at each stage9(aX@QfX@1w-!Y@ktHY@Y@QkwZ@ǘZ@ c[@a+[@Y8U\@%C\@D1]@V-]@^)^@ Oe_@&†c`@"u`@#>a@Qa@a+?b@HVapour Thermal conductivity profileTVapour Thermal conductivity at each stage@? ?) ?u(?Nb-~K?VUAt?t?Ƀۏ?ęF?)ZG`? ;m?}?=k ?^2+g1?V?,j? ףp= ?}_uG?C8|??4Liquid Moleweight profile@Liquid Moleweight at each stage S@ŏ1wS@CS@oB! T@߾KT@3KT@.9T@ hLiquid Viscosity at each stage3H34?Jȋ4? ?%`4?$4?003?L+3?=#j*3?$2?ɿer2?7'2?"31?$V1?^#61?v<0?L:Q a0?9!N 0?50EP0?u&0?>/? %4m/?:Liquid Heat capacity profileFLiquid Heat capacity at each stage)Ǻb@ÆWb@Qc@鷯9c@^)|c@?c@> ףp#d@|Pkd@HPe@e@Aǘf@KY8Af@w#f@*:f@G_Jg@Y8šg@z6g@:M@h@mxz,h@:MEi@:Liquid Thermal cond. profileFLiquid Thermal cond. at each stage>??ل?Č:;a?$d{0?M_eG?vsLq?i?衶 ?-$̽?b^b?Η@?} ^?5Ӽ?p!?ZpI?;<ߪF ?m=/pԻ?D?ǵF)n? {5"?0Surface tension profile<Surface tension at each stage{;ӕ?͔1?Qwam?WsDK? ?OB?DA̞?2A?#Sg?? ?a9!ʓ?bU֙?SZuf?.;f$?EFޒ?S 蝒?[Ye?Z42?}bt?As]?, not all ports are connectedFeed1{split}_stage10Column heat duty TopProduct BottomProductReboiler heat dutyCondenser heat duty @ @0@@ @ @ @(@ @(@$@,@@@@@@@@$@@(@@(@ @(@ @ @ @,@$@@@$@@(@ @,@ @ @,@ @$@0@,@4@@0@@2@@2@$@2@(@0@(@(@(@(@ @(@$@4@,@0@@ 4@,@0@ 4@,@0@4@,@0@ 4@,@0@ 4@,@0@ ,@0@  ,@0@@:@solving C-101 C-102ChemSep Unit OperationqeWCXc8CSUOo[ChemSep] Version=6.31 Name=C:\DOCUME~1\Harry\LOCALS~1\Temp\CS351.sep Title=ChemSep CO Unit Operation "C-102" in COFE Flowsheet User=Harry Date=2009-04-12 Time=11:00:56 [Cape-Open] unitname=C-102 CO_ID=CS351 3 components Benzene 71-43-2 78.1139984131 Mw Toluene 108-88-3 92.1409988403 Mw P-xylene 106-42-3 106.166999817 Mw 0 thermo exe=C:\PROGRA~1\ChemSepL\bin\co-col2.exe mode=COFE NoWarnings=FALSE WilsonEstimate=TRUE Status= 0 only K-values and ethalpies 0 use only perturbed derivative 0 use only perturbed mole derivative 0.001 relative T perturbation 0.001 relative P perturbation 0.001 X perturbation 0 write all values to log 1 use initial guess 0 inlet reflash 0 outlet reflash 1 expose energy ports 0 clear log 0 update icon [Paths] Device drivers path=c:\progra~1\chemsepl\bin\ Help and Info path=c:\progra~1\chemsepl\help\ Component data path=c:\progra~1\chemsepl\pcd\ Property data path=c:\progra~1\chemsepl\ipd\ Section data path=c:\progra~1\chemsepl\ild\ Executables path=C:\PROGRA~1\ChemSepL\bin\ Temporary path=WINTMPDIR Scripts path=c:\progra~1\chemsepl\bin\ [Units] Temperature=C Flow=mol/s Mass flow=kg/s Pressure=bar Heat=MW Enthalpy=kJ/kmol Entropy=J/kmol/K Fraction= Length=m 1/Length=1/m Area=m Volume=m3 Mass=kg Angle=rad Velocity=m/s Surface tension=N/m Density=kg/m3 Molar density=kmol/m3 Viscosity=N/m2.s Molecular weight=kg/kmol Heat capacity=J/kmol/K Thermal conductivity=J/s/m/K Diffusivity=1e-8 m/s Interaction parameter=J/mol Time=s [Components] 3 125 501 Library Offset, Index DT=2009-03-26,23:59:44 CHK=55335 CAS=71-43-2 CID=Benzene Name=Benzene Lib=c:\program files\chemsepl\pcd\chemsep1.pcd 140 502 Library Offset, Index DT=2009-03-26,23:59:44 CHK=60854 CAS=108-88-3 CID=Toluene Name=Toluene Lib=c:\program files\chemsepl\pcd\chemsep1.pcd 152 507 Library Offset, Index DT=2009-03-26,23:59:44 CHK=62355 CAS=106-42-3 CID=P-xylene Name=P-xylene Lib=c:\program files\chemsepl\pcd\chemsep1.pcd [Operation] 2 Operation Column 1 Operation kind Simple Distillation 1 Condenser Total (Liquid product) 1 Reboiler Partial (Liquid product) 30 Stages 1 Feed stages 0 Sidestream stages F=15 S= 0 Pumparound stages P= [Properties] [Thermodynamics] 1 K model Raoult's law * Activity coefficient * * Wilson model * * UNIQUAC model * * Equation of State * * Cubic EOS * * Virial EOS * 1 Vapour pressure Antoine [Enthalpy] 2 Enthalpy Ideal 1 Enthalpy reference state Vapour 298.15 Enthalpy reference temperature 1 Formation enthalpies Excluded 298.15 Exergy surroundings temperature [Physical property models] 0 No Check T range * Cubic EOS * * Virial EOS * * Vapour model * * Liquid mixture density * * Liquid component density * * Vapour mixture viscosity * * Vapour mixture viscosity pressure correction * * Vapour component viscosity * * Liquid mixture viscosity * * Liquid component viscosity * Vapour mixture Cp * Vapour component Cp * Liquid mixture Cp * Liquid component Cp * Vapour mixture conductivity * * Vapour component conductivity * * Liquid mixture conductivity * * Liquid component conductivity * Mixture surface tension * * Component surface tension * * Vignes MS D-model * * D mixture model * * Vapour Diffusion Coefficients * [Reaction data] 0 Number of reactions [Specifications] Top Bottom [Heaters/Coolers] 0 Number 0 Column duty Qcolumn 2 First stage 29 Last stage [Efficiencies] 1 Default efficiency 0 Number [Pressures] 1 Column pressure Constant pressure 101325 Condenser pressure 101325 Top pressure * Pressure Drop * Bottom pressure [Feeds] 1 Number 1 Feed state T & p 15 Stage Feed1{split} 394.426471263 Temperature 101325 Pressure 0 Vapour fraction 3 componentflows 6.9913228095e-005 Component 1 flow 0.00327971972735 Component 2 flow 0.00334972519288 Component 3 flow [Condenser] 1 Type Reflux ratio 3 Value Qcondenser * Type * * Initialization guess [Reboiler] 9 Type Fraction of combined feeds recovered 0.5 Value Qreboiler * Type * * Initialization guess [Solve options] 3 Initialization Old Results 1 Method Newton's method 0.2 Flow Step limit 10 Temperature Step limit 1 Composition Step limit 1 Flux Step limit 0.000001 Accuracy 30 Maximum iterations 1 Iteration count & function vector 0 T/V/L profiles 0 X/Y profiles 0 Variable and function vectors 0 Jacobian 1 History Screen History file= 1 Feeds type Stage below 1 Interactive 0 Log thermodynamics 0 Log enthalpy/entropy 0 Log physical properties 0 Log timing 0 CO numeric differencing 0 Log from iteration 0 CS K-value 0 CS enthalpy 0 CS entropy 0 CS flash 0 CS activity coefficient 0 CS vapor pressuure 0 CS density 0 CS viscosity 0 CS thermal conductivity 0 CS heat capacity 0 CS surface tension 0 CS diffusivity [Programs] Temporary file=SCRATCH.TMP User program= 8 DOS extender NT 1 Show windows Hidden [FlowSheet] [CoCo] [Settings] -1 -1 -1 0 Graph settings 1 Auto colors 1 Auto points 0.2 StringGrid5 2 8 Title Labels Stages Axis color Commands Box Labels box Import data StringGrid4 5 9 Title Start End Tic interval Small tics Grid Logarithmic Scientific notation x1 y1 x2 y2 StringGrid3 1 14 Label Plot X Plot Y X axis Y axis Units X Units Y Color Points Thickness Style 1st stage Last stage 0 Graph settings -1 -1 StringGrid7 16 2 StringGrid11 5 3 -1 -1 -1 0.95 0.95 1.2 1 0 Use old results 1 Automatic 0 Keep sep-files 1 Restore original StringGrid1 1 6 StringGrid2 4 1 StringGrid3 1 1 None -1 -1 -1 21 Binary Phase Diagram T p x -1 -1 StringGrid1 3 5 -1 -1 -1 0 21 Ternary Phase Diagram T 0 1 1 StringGrid1 3 5 0 0 -1 -1 -1 21 Binary Property Diagram StringGrid1 13 4 Axis Left Right X/Y Property -click to select- -click to select- x Title x Units - Minimum 0 Maximum 1 Interval 0.2 Grid Off Off Off Log Off Off Off Color Blue Red Black Line Normal Normal Style Solid Solid Point None None -1 -1 [End Settings] [End of Input] [Results] 1 Converged 0 Iterations [Profiles] Stage Temperature Pressure Vapour Flow Liquid Flow 1 382.5752888 1.013250000E+05 3.349679075E-03 1.004903722E-02 2 383.0883485 1.013250000E+05 1.339871630E-02 1.005222277E-02 3 383.2918430 1.013250000E+05 1.340190185E-02 1.005050567E-02 4 383.4095360 1.013250000E+05 1.340018474E-02 1.004499316E-02 5 383.5328331 1.013250000E+05 1.339467223E-02 1.003477854E-02 6 383.7160187 1.013250000E+05 1.338445762E-02 1.001744112E-02 7 384.0140447 1.013250000E+05 1.336712020E-02 9.989118669E-03 8 384.4990376 1.013250000E+05 1.333879774E-02 9.944772979E-03 9 385.2639533 1.013250000E+05 1.329445205E-02 9.879511448E-03 10 386.4068445 1.013250000E+05 1.322919052E-02 9.791685814E-03 11 387.9852813 1.013250000E+05 1.314136489E-02 9.686823379E-03 12 389.9508225 1.013250000E+05 1.303650245E-02 9.578479872E-03 13 392.1166110 1.013250000E+05 1.292815895E-02 9.482628065E-03 14 394.2152735 1.013250000E+05 1.283230714E-02 9.409308548E-03 15 396.0188674 1.013250000E+05 1.275898762E-02 1.604565379E-02 16 398.0943928 1.013250000E+05 1.269597471E-02 1.597835066E-02 17 400.4768623 1.013250000E+05 1.262867159E-02 1.592280353E-02 18 402.9507278 1.013250000E+05 1.257312446E-02 1.589001242E-02 19 405.2415278 1.013250000E+05 1.254033335E-02 1.588047240E-02 20 407.1447907 1.013250000E+05 1.253079332E-02 1.588649495E-02 21 408.5886036 1.013250000E+05 1.253681587E-02 1.589893294E-02 22 409.6102879 1.013250000E+05 1.254925387E-02 1.591163473E-02 23 410.2982810 1.013250000E+05 1.256195566E-02 1.592194885E-02 24 410.7462566 1.013250000E+05 1.257226978E-02 1.592941014E-02 25 411.0316037 1.013250000E+05 1.257973106E-02 1.593446509E-02 26 411.2108243 1.013250000E+05 1.258478602E-02 1.593775928E-02 27 411.3223972 1.013250000E+05 1.258808020E-02 1.593985630E-02 28 411.3914742 1.013250000E+05 1.259017722E-02 1.594117233E-02 29 411.4340952 1.013250000E+05 1.259149326E-02 1.594199108E-02 30 411.4603371 1.013250000E+05 1.259231201E-02 3.349679075E-03 [Enthalpies/Entropies] Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy 1 -0.2315894E+08 -0.2315894E+08 0.3091318E+05 -0.6134155E+05 2 0.1011066E+08 -0.2308556E+08 0.3057250E+05 -0.6142670E+05 3 0.1015780E+08 -0.2305826E+08 0.3045249E+05 -0.6138934E+05 4 0.1018253E+08 -0.2304537E+08 0.3047874E+05 -0.6124253E+05 5 0.1020588E+08 -0.2303474E+08 0.3060935E+05 -0.6097793E+05 6 0.1023923E+08 -0.2302036E+08 0.3084803E+05 -0.6055848E+05 7 0.1029316E+08 -0.2299706E+08 0.3123125E+05 -0.5992382E+05 8 0.1038134E+08 -0.2295805E+08 0.3181911E+05 -0.5900053E+05 9 0.1052187E+08 -0.2289336E+08 0.3268548E+05 -0.5772420E+05 10 0.1073534E+08 -0.2278968E+08 0.3389531E+05 -0.5608008E+05 11 0.1103734E+08 -0.2263335E+08 0.3546179E+05 -0.5415039E+05 12 0.1142559E+08 -0.2241882E+08 0.3729723E+05 -0.5212681E+05 13 0.1186996E+08 -0.2215891E+08 0.3920496E+05 -0.5024898E+05 14 0.1231815E+08 -0.2188538E+08 0.4095044E+05 -0.4869958E+05 15 0.1271799E+08 -0.2163452E+08 0.4236842E+05 -0.4754239E+05 16 0.1320192E+08 -0.2132593E+08 0.4374710E+05 -0.4644264E+05 17 0.1377801E+08 -0.2095369E+08 0.4528361E+05 -0.4532756E+05 18 0.1440452E+08 -0.2054635E+08 0.4670531E+05 -0.4436572E+05 19 0.1501312E+08 -0.2015107E+08 0.4777039E+05 -0.4366887E+05 20 0.1554113E+08 -0.1981015E+08 0.4838293E+05 -0.4325392E+05 21 0.1595600E+08 -0.1954431E+08 0.4860241E+05 -0.4306549E+05 22 0.1625734E+08 -0.1935258E+08 0.4856465E+05 -0.4302363E+05 23 0.1646400E+08 -0.1922183E+08 0.4840078E+05 -0.4305880E+05 24 0.1660021E+08 -0.1913599E+08 0.4820073E+05 -0.4312413E+05 25 0.1668766E+08 -0.1908103E+08 0.4801263E+05 -0.4319350E+05 26 0.1674286E+08 -0.1904639E+08 0.4785584E+05 -0.4325495E+05 27 0.1677733E+08 -0.1902479E+08 0.4773380E+05 -0.4330464E+05 28 0.1679872E+08 -0.1901140E+08 0.4764277E+05 -0.4334271E+05 29 0.1681193E+08 -0.1900313E+08 0.4757669E+05 -0.4337092E+05 30 0.1682007E+08 -0.1899804E+08 0.4752948E+05 -0.4339142E+05 [Vapour Properties] Stage Moleweight Density Viscosity Heat capacity Thermal conductivity 1 0.9150166E+02 0.2914701E+01 0.8978592E-05 0.1333778E+06 0.1869378E-01 2 0.9185943E+02 0.2922178E+01 0.8972417E-05 0.1342539E+06 0.1876932E-01 3 0.9199152E+02 0.2924827E+01 0.8970245E-05 0.1345809E+06 0.1879664E-01 4 0.9205157E+02 0.2925838E+01 0.8969486E-05 0.1347355E+06 0.1880830E-01 5 0.9209801E+02 0.2926373E+01 0.8969191E-05 0.1348629E+06 0.1881638E-01 6 0.9215826E+02 0.2926889E+01 0.8969010E-05 0.1350335E+06 0.1882610E-01 7 0.9225368E+02 0.2927646E+01 0.8968761E-05 0.1353056E+06 0.1884102E-01 8 0.9240998E+02 0.2928907E+01 0.8968230E-05 0.1357500E+06 0.1886486E-01 9 0.9266161E+02 0.2931051E+01 0.8967000E-05 0.1364607E+06 0.1890203E-01 10 0.9305015E+02 0.2934636E+01 0.8964234E-05 0.1375468E+06 0.1895674E-01 11 0.9361226E+02 0.2940353E+01 0.8958561E-05 0.1390962E+06 0.1903072E-01 12 0.9435480E+02 0.2948737E+01 0.8948447E-05 0.1411089E+06 0.1912032E-01 13 0.9522963E+02 0.2959639E+01 0.8933320E-05 0.1434383E+06 0.1921581E-01 14 0.9613621E+02 0.2971909E+01 0.8914612E-05 0.1458126E+06 0.1930511E-01 15 0.9696339E+02 0.2983828E+01 0.8895303E-05 0.1479497E+06 0.1937931E-01 16 0.9800422E+02 0.3000134E+01 0.8868429E-05 0.1505938E+06 0.1947011E-01 17 0.9925357E+02 0.3020304E+01 0.8833283E-05 0.1537380E+06 0.1956437E-01 18 0.1006341E+03 0.3043513E+01 0.8791353E-05 0.1571737E+06 0.1965548E-01 19 0.1019968E+03 0.3067287E+01 0.8747408E-05 0.1605306E+06 0.1973491E-01 20 0.1031944E+03 0.3088797E+01 0.8707104E-05 0.1634573E+06 0.1979759E-01 21 0.1041444E+03 0.3106214E+01 0.8674223E-05 0.1657651E+06 0.1984317E-01 22 0.1048388E+03 0.3119126E+01 0.8649752E-05 0.1674455E+06 0.1987442E-01 23 0.1053169E+03 0.3128099E+01 0.8632712E-05 0.1685997E+06 0.1989499E-01 24 0.1056330E+03 0.3134063E+01 0.8621374E-05 0.1693612E+06 0.1990818E-01 25 0.1058362E+03 0.3137912E+01 0.8614052E-05 0.1698504E+06 0.1991649E-01 26 0.1059646E+03 0.3140350E+01 0.8609414E-05 0.1701593E+06 0.1992168E-01 27 0.1060448E+03 0.3141876E+01 0.8606511E-05 0.1703522E+06 0.1992490E-01 28 0.1060946E+03 0.3142823E+01 0.8604708E-05 0.1704719E+06 0.1992689E-01 29 0.1061254E+03 0.3143409E+01 0.8603593E-05 0.1705459E+06 0.1992811E-01 30 0.1061443E+03 0.3143770E+01 0.8602906E-05 0.1705915E+06 0.1992886E-01 [Liquid Properties] Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension 1 0.9185943E+02 0.7807640E+03 0.2387458E-03 0.1945505E+06 0.1121610E+00 0.1822998E-01 2 0.9203554E+02 0.7802157E+03 0.2375160E-03 0.1950968E+06 0.1119725E+00 0.1818382E-01 3 0.9211561E+02 0.7800005E+03 0.2370705E-03 0.1953306E+06 0.1118986E+00 0.1816590E-01 4 0.9217757E+02 0.7798792E+03 0.2368750E-03 0.1954920E+06 0.1118565E+00 0.1815610E-01 5 0.9225802E+02 0.7797553E+03 0.2367323E-03 0.1956870E+06 0.1118131E+00 0.1814636E-01 6 0.9238552E+02 0.7795731E+03 0.2365544E-03 0.1959901E+06 0.1117491E+00 0.1813218E-01 7 0.9259460E+02 0.7792779E+03 0.2362785E-03 0.1964862E+06 0.1116454E+00 0.1810921E-01 8 0.9293181E+02 0.7787991E+03 0.2358361E-03 0.1972890E+06 0.1114774E+00 0.1807181E-01 9 0.9345387E+02 0.7780474E+03 0.2351459E-03 0.1985401E+06 0.1112143E+00 0.1801270E-01 10 0.9421190E+02 0.7769317E+03 0.2341306E-03 0.2003757E+06 0.1108250E+00 0.1792409E-01 11 0.9521770E+02 0.7754038E+03 0.2327627E-03 0.2028486E+06 0.1102946E+00 0.1780118E-01 12 0.9640822E+02 0.7735195E+03 0.2311211E-03 0.2058350E+06 0.1096451E+00 0.1764734E-01 13 0.9764695E+02 0.7714630E+03 0.2294003E-03 0.2090175E+06 0.1089425E+00 0.1747693E-01 14 0.9878038E+02 0.7694865E+03 0.2278288E-03 0.2120036E+06 0.1082738E+00 0.1731100E-01 15 0.9970598E+02 0.7677983E+03 0.2265589E-03 0.2145001E+06 0.1077079E+00 0.1716782E-01 16 0.1007006E+03 0.7658585E+03 0.2250805E-03 0.2172664E+06 0.1070653E+00 0.1700189E-01 17 0.1017957E+03 0.7636469E+03 0.2236023E-03 0.2203811E+06 0.1063401E+00 0.1681122E-01 18 0.1028735E+03 0.7613607E+03 0.2222579E-03 0.2235348E+06 0.1055995E+00 0.1661271E-01 19 0.1038191E+03 0.7592497E+03 0.2211741E-03 0.2263838E+06 0.1049243E+00 0.1642839E-01 20 0.1045685E+03 0.7574984E+03 0.2203904E-03 0.2287020E+06 0.1043705E+00 0.1627491E-01 21 0.1051163E+03 0.7561709E+03 0.2198673E-03 0.2304330E+06 0.1039546E+00 0.1615830E-01 22 0.1054936E+03 0.7552318E+03 0.2195347E-03 0.2316442E+06 0.1036623E+00 0.1607570E-01 23 0.1057430E+03 0.7545994E+03 0.2193284E-03 0.2324537E+06 0.1034665E+00 0.1602004E-01 24 0.1059034E+03 0.7541876E+03 0.2192019E-03 0.2329783E+06 0.1033394E+00 0.1598379E-01 25 0.1060048E+03 0.7539253E+03 0.2191244E-03 0.2333113E+06 0.1032586E+00 0.1596069E-01 26 0.1060682E+03 0.7537606E+03 0.2190771E-03 0.2335201E+06 0.1032079E+00 0.1594618E-01 27 0.1061075E+03 0.7536580E+03 0.2190481E-03 0.2336499E+06 0.1031764E+00 0.1593714E-01 28 0.1061318E+03 0.7535945E+03 0.2190303E-03 0.2337302E+06 0.1031569E+00 0.1593155E-01 29 0.1061468E+03 0.7535554E+03 0.2190194E-03 0.2337797E+06 0.1031448E+00 0.1592810E-01 30 0.1061560E+03 0.7535312E+03 0.2190127E-03 0.2338102E+06 0.1031374E+00 0.1592597E-01 [Vapour phase compositions] Component Mole fractions on stages: 1 to 5 1 0.459175539E-01 0.208716197E-01 0.122444053E-01 0.931986461E-02 0.833305193E-02 2 0.953744209E+00 0.978330387E+00 0.986167505E+00 0.987735613E+00 0.986398258E+00 3 0.338237407E-03 0.797993681E-03 0.158808948E-02 0.294452234E-02 0.526868978E-02 Component Mole fractions on stages: 6 to 10 1 0.799872809E-02 0.788183580E-02 0.783459384E-02 0.780531002E-02 0.777384386E-02 2 0.982771042E+00 0.976201695E+00 0.965152791E+00 0.947271317E+00 0.919632489E+00 3 0.923022981E-02 0.159164695E-01 0.270126155E-01 0.449233728E-01 0.725936668E-01 Component Mole fractions on stages: 11 to 15 1 0.773037493E-02 0.766982044E-02 0.759231584E-02 0.750440289E-02 0.741693197E-02 2 0.879643110E+00 0.826823967E+00 0.764607334E+00 0.700147696E+00 0.641347824E+00 3 0.112626515E+00 0.165506212E+00 0.227800350E+00 0.292347901E+00 0.351235244E+00 Component Mole fractions on stages: 16 to 20 1 0.315592278E-02 0.128569570E-02 0.498381612E-03 0.183504604E-03 0.644345982E-04 2 0.575663062E+00 0.490329533E+00 0.393478172E+00 0.296955027E+00 0.211803338E+00 3 0.421181015E+00 0.508384771E+00 0.606023447E+00 0.702861469E+00 0.788132228E+00 Component Mole fractions on stages: 21 to 25 1 0.217532970E-04 0.712891279E-05 0.228773609E-05 0.723849845E-06 0.226911953E-06 2 0.144162935E+00 0.946841310E-01 0.606008839E-01 0.380739380E-01 0.235866000E-01 3 0.855815312E+00 0.905308740E+00 0.939396828E+00 0.961925338E+00 0.976413173E+00 Component Mole fractions on stages: 26 to 30 1 0.706916020E-07 0.219158826E-07 0.675221032E-08 0.205063951E-08 0.595313411E-09 2 0.144321265E-01 0.871145470E-02 0.516135507E-02 0.296774550E-02 0.161592342E-02 3 0.985567803E+00 0.991288523E+00 0.994838638E+00 0.997032252E+00 0.998384076E+00 [Liquid phase compositions] Component Mole fractions on stages: 1 to 5 1 0.208716197E-01 0.936957852E-02 0.546984217E-02 0.415184669E-02 0.370166708E-02 2 0.978330387E+00 0.988779050E+00 0.990870230E+00 0.989088632E+00 0.984253364E+00 3 0.797993681E-03 0.185137128E-02 0.365992735E-02 0.675952177E-02 0.120449690E-01 Component Mole fractions on stages: 6 to 10 1 0.353825077E-02 0.346285153E-02 0.340420965E-02 0.333300224E-02 0.323483111E-02 2 0.975489893E+00 0.960733911E+00 0.936809750E+00 0.899730785E+00 0.845882763E+00 3 0.209718566E-01 0.358032378E-01 0.597860408E-01 0.969362130E-01 0.150882406E+00 Component Mole fractions on stages: 11 to 15 1 0.310467158E-02 0.294842591E-02 0.278251713E-02 0.262711286E-02 0.249709466E-02 2 0.774433430E+00 0.689866493E+00 0.601881400E+00 0.521383277E+00 0.455651772E+00 3 0.222461899E+00 0.307185081E+00 0.395336083E+00 0.475989610E+00 0.541851133E+00 Component Mole fractions on stages: 16 to 20 1 0.101616429E-02 0.393537137E-03 0.144821120E-03 0.508433943E-04 0.171666290E-04 2 0.387701940E+00 0.310867173E+00 0.234521020E+00 0.167292930E+00 0.113931429E+00 3 0.611281896E+00 0.688739289E+00 0.765334158E+00 0.832656227E+00 0.886051404E+00 Component Mole fractions on stages: 21 to 25 1 0.562698286E-05 0.180615798E-05 0.571595997E-06 0.179226852E-06 0.558616418E-07 2 0.749007562E-01 0.480084249E-01 0.302288827E-01 0.187916555E-01 0.115631197E-01 3 0.925093617E+00 0.951989769E+00 0.969770546E+00 0.981208165E+00 0.988436824E+00 Component Mole fractions on stages: 26 to 30 1 0.173403035E-07 0.536380121E-08 0.165027445E-08 0.500757278E-09 0.145296264E-09 2 0.704536891E-02 0.424152371E-02 0.250892782E-02 0.144116974E-02 0.784225376E-03 3 0.992954614E+00 0.995758471E+00 0.997491071E+00 0.998558830E+00 0.999215774E+00 [Reaction rates] Component reaction rates on stages: 1 to 5 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 6 to 10 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 11 to 15 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 16 to 20 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 21 to 25 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 26 to 30 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 [Condenser Heat Duty] -4.457700321E+05 [Reboiler Heat Duty] 4.511139242E+05 [K-values] Component K-values on stages: 1 to 5 1 0.219999955E+01 0.222759430E+01 0.223852992E+01 0.224475163E+01 0.225116191E+01 2 0.974869248E+00 0.989432763E+00 0.995253945E+00 0.998632057E+00 0.100217921E+01 3 0.423859757E+00 0.431028443E+00 0.433912842E+00 0.435611045E+00 0.437418291E+00 Component K-values on stages: 6 to 10 1 0.226064477E+01 0.227611138E+01 0.230144282E+01 0.234182562E+01 0.240316839E+01 2 0.100746409E+01 0.101609997E+01 0.103025485E+01 0.105283862E+01 0.108718670E+01 3 0.440124591E+00 0.444553914E+00 0.451821447E+00 0.463432307E+00 0.481127448E+00 Component K-values on stages: 11 to 15 1 0.248991712E+01 0.260132717E+01 0.272857830E+01 0.285652094E+01 0.297022460E+01 2 0.113585374E+01 0.119852750E+01 0.127036212E+01 0.134286566E+01 0.140753940E+01 3 0.506273281E+00 0.538783367E+00 0.576219476E+00 0.614189668E+00 0.648213545E+00 Component K-values on stages: 16 to 20 1 0.310572102E+01 0.326702510E+01 0.344136002E+01 0.360921229E+01 0.375347997E+01 2 0.148480831E+01 0.157729595E+01 0.167779490E+01 0.177506023E+01 0.185904222E+01 3 0.689012742E+00 0.738138188E+00 0.791841628E+00 0.844119633E+00 0.889488154E+00 Component K-values on stages: 21 to 25 1 0.386589003E+01 0.394700402E+01 0.400236548E+01 0.403873547E+01 0.406203515E+01 2 0.192471935E+01 0.197223990E+01 0.200473450E+01 0.202610877E+01 0.203981284E+01 3 0.925112113E+00 0.950964779E+00 0.968679480E+00 0.980347874E+00 0.987835690E+00 Component K-values on stages: 26 to 30 1 0.407672230E+01 0.408588643E+01 0.409156811E+01 0.409507679E+01 0.409723826E+01 2 0.204845575E+01 0.205385029E+01 0.205719552E+01 0.205926159E+01 0.206053446E+01 3 0.992560777E+00 0.995511012E+00 0.997340895E+00 0.998471220E+00 0.999167648E+00 [Molecular weights] 1 78.114 2 92.141 3 106.167 [Feed stream 1] 15 Stage Number 6.6993581483250E-03 Flow rate 3.9442647126300E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.1876161997475E+07 Enthalpy [J/kmol] -4.8209725860445E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 1.0435809901054E-02 Mole fraction of component 1 4.8955730604879E-01 Mole fraction of component 2 5.0000688405016E-01 Mole fraction of component 3 6.6993581483250E-03 Flow rate 1.0435809901054E-02 Mole fraction of component 1 4.8955730604879E-01 Mole fraction of component 2 5.0000688405016E-01 Mole fraction of component 3 9.9007712774367E+01 Molar mass 7.6932520393503E+02 Density 2.2830176015549E-04 Viscosity 1.0821204212469E-01 Thermal conductivity 2.1249914438075E+05 Heat capacity 1.7297868167950E-02 Surface tension [Top product] 1 Stage Number 3.3496790750000E-03 Flow rate 3.8257528880000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.3158944056546E+07 Enthalpy [J/kmol] -6.1341548849842E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 2.0871619700000E-02 Mole fraction of component 1 9.7833038700000E-01 Mole fraction of component 2 7.9799368100000E-04 Mole fraction of component 3 3.3496790750000E-03 Flow rate 2.0871619700000E-02 Mole fraction of component 1 9.7833038700000E-01 Mole fraction of component 2 7.9799368100000E-04 Mole fraction of component 3 9.1859425317138E+01 Molar mass 7.8076399049648E+02 Density 2.3874577705319E-04 Viscosity 1.1216102768628E-01 Thermal conductivity 1.9455046512769E+05 Heat capacity 1.8229976901582E-02 Surface tension [Bottom product] 30 Stage Number 3.3496790750000E-03 Flow rate 4.1146033710000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -1.8998035334249E+07 Enthalpy [J/kmol] -4.3391423714141E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 1.4529626400000E-10 Mole fraction of component 1 7.8422537600000E-04 Mole fraction of component 2 9.9921577400000E-01 Mole fraction of component 3 3.3496790750000E-03 Flow rate 1.4529626400000E-10 Mole fraction of component 1 7.8422537600000E-04 Mole fraction of component 2 9.9921577400000E-01 Mole fraction of component 3 1.0615600021611E+02 Molar mass 7.5353123219065E+02 Density 2.1901273891886E-04 Viscosity 1.0313742313356E-01 Thermal conductivity 2.3381022785276E+05 Heat capacity 1.5925970026475E-02 Surface tension [End of Results] GUIArguments /kpldUseCOSEThermo:UseCOSEDiffusionCoefficients8UsePerturbedDerivativesOnly"UsePerturbed_ddX"SuppressWarnings@RelativePerturbationTemperatureMbP?:RelativePerturbationPressureMbP?0PerturbationCompositionMbP?InletReflash<none>OutletFlash AutoDUseOnlyKValuesAndEnthalpyFromCOSE*RestartDataAvailable,OmitStageFromPortNameWilsonEstimate"LogPropertyCallsEnergyPorts UseInitialGuess(Temperature profile4Temperature at each stage\b4w@iiw@ɐcw@uw@+|w@1=tw@r9x@x@r'9x@`o&x@ S?x@\6_x@~݁x@!#qx@^GMx@Ox@ \:y@^Z.6/y@2!ALSy@= Qry@ějy@P>Ùy@J@LŤy@ɶªy@ry@<M_y@'e(y@cszCy@ y@+Zo]y@"Pressure profile.Pressure at each stageм@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@(Vapour Flow profile4Vapour Flow at each stage$ @$*@_K*@Q*@z*@,2*@f-*@vv*@Ik–*@uXu*@`H*@r*@z_7)@ U)$)@{)@Vd)@>A)@yp%)@R`)@\$)@a?)@7)@)@-k%)@Yn()@i+)@-)@}e+.)@D_4.)@C/)@(Liquid Flow profile4Liquid Flow at each stage_h$@Xb$@<$@|W $@&'~$@ $@om#@$H#@7<SO#@W#@]P_#@D.(#@"@9D"@ ~ 0@p`/@{Ky/@9/@FG/@h/@15@/@~/@l /@׽W/@}Q5r/@=!/@N4/@V/@rL/@$ @4Vapour Moleweight profile@Vapour Moleweight at each stagem2V@̯V@UMuV@ALW@+EW@ W@ K<W@=W@8-xW*W@>yX5CW@)D/gW@' W@ BW@%X@҇.=X@N#EX@O}:X@1*(Y@):Y@ꕲ qY@b= Z@15Z@HTZ@nhZ@:MuZ@/n}Z@ނZ@( Z@ǺZ@46Vapour Viscosity at each stageIX>C>>t>bz9L>Y3>k&3 >XL%>2C>>p?>A}0)>\& >>K">Ǚ3>++U>[o>:X>BB>!0>+#>+$>>=J>$>iݕ >% >߱i >οe >:Vapour Heat capacity profileFVapour Heat capacity at each stage`@`@ǘ`@K7`@u`@Pn`@ y`@`@( a@}b1a@ca@Q|a@Ǻa@Y:b@\ Ac~b@hb@V-7c@jMc@?٬d@3nd@n{d@K7Ad@) 0e@jM+e@z6;e@HPEe@48EKe@p_Oe@]FxQe@rhRe@HVapour Thermal conductivity profileTVapour Thermal conductivity at each stageXVv$?fEC8?WzL(m?? ̒{B?jD?>/&G?rK?%wROQ?|H [?ZIei?|?)1[F?.O?aē?Uz+ؓ?O?rD?& ?s(dc5?w[E?Z˘Q?/7Y?-Z_?1nXb? d?TSPYf?g1g?7qg?eh?G';h?4Liquid Moleweight profile@Liquid Moleweight at each stage̯V@lIFW@E|'fW@ N] W@mQfW@ \W@( &W@}iƢ;W@4 ]W@oŏW@W@dF X@l giX@X@S.X@a,Y@W[rY@ClY@ h"lY@Mb$Z@!uqGZ@St$_Z@d;OoZ@6;NyZ@UNZ@ec]Z@{GZ@8gDioZ@a+eZ@DlZ@.Liquid Density profile:Liquid Density at each stage'1f@a@/$`@%u_@Z ^@s\@x#9Z@qdV@N@aP@w-!tG@~:;@-',@bX9@Z @-Cb@|?5@B>,݇@V}ʇ@}b@#@^@Yڙ@):˔@m4@鷯g@s@%C@K7@!uq@?@2Liquid Viscosity profile>Liquid Viscosity at each stage]J/?А!/?1/?\4 /?Q j/?>r/?uI0.?ZfX.?f6/.?<.?8S^8.?!#K.?Շe.?|}-?/!-? r-?!N-?ĄҼ!-?'m _,?,?չ,?\\,?3p,?1,?yuC,?,?,?"^o,?]R,?ش,?:Liquid Heat capacity profileFLiquid Heat capacity at each stageV-Qh@HPch@؁sFjh@9voh@Dluh@1h@jMh@i|?h@;Hh@o i@W/'[i@Qi@(\ j@H}j@Yj@JY(k@.1k@Ӽk@HLl@X9vl@`"l@QIl@@ܵm@5;Nm@j+)m@T0m@t4m@Bc]7m@jM8m@(9m@:Liquid Thermal cond. profileFLiquid Thermal cond. at each stageR?%:?wb?~SX?@Çȟ?ŀɖ?೿ʔ?|<>kȉ?XUx?tF_?SD??Yӂ8?շj?"q?6qQZ?Ȉx:?D$?O#x?q?Bp?h?fl6?{?LҐ?ȸ^?,_<(͋? %v?g?C ^?PIW?ob2T?]\Q?8\P?YtO?mr:N?9G not all ports are connectedFeed1{split}_stage15 TopProduct BottomProductReboiler heat duty @ @0@@ @ @ @(@ @(@$@,@@@@@@@@$@@(@@(@ @(@ @ @ @,@$@@@$@@(@ @,@ @ @,@ @$@0@,@4@@0@@2@@2@$@2@(@0@(@(@(@(@ @(@$@4@,@0@@ 4@,@0@ 4@,@0@4@,@0@ 4@,@0@ 4@,@0@ ,@0@  ,@0@@:@solving C-102 MS Sans-C6?-C6?h㈵>-C6?E#