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CSTR
                                                               PRE-H
                       MIXER
                                                                            S4                                       S5
   S1                            S3


             S2




                                   Esterification KC09017
Stream ID                             S1            S2             S3            S4             S5
Temperature            C                     28.0           30.0          28.2           80.0          80.0
Pressure               bar                  1.000          1.000         1.100          1.000         1.000
Vapor Frac                                  0.000          0.000         0.000          0.000         0.000
Mole Flow              kmol/hr             36.000          3.600        39.600         39.600        39.600
Mass Flow              kg/hr           1910.189          165.849    2076.037      2076.037       2076.037
Volume Flow            cum/hr               2.476          0.226         2.703          2.858         2.712
Enthalpy               MMkcal/hr           -3.251         -0.239        -3.490         -3.422        -3.414
Mass Frac
 ETHAN-01                                   0.434          1.000         0.479          0.479         0.165
 ACETI-01                                   0.566                        0.521          0.521         0.111
 WATER                                                                                                0.123
 ETHYL-01                                                                                             0.601
Mole Flow              kmol/hr
 ETHAN-01                                  18.000          3.600        21.600         21.600         7.437
 ACETI-01                                  18.000                       18.000         18.000         3.837
 WATER                                                                                               14.163
 ETHYL-01                                                                                            14.163
*** VAPOR PHASE ***
Density
Viscosity
*** LIQUID PHASE ***
Density                kg/cum          771.376           732.737    768.150           726.488    765.553
Viscosity              cP                   0.725          0.626         0.716          0.403         0.421
Surface Ten            dyne/cm             24.297         21.681        24.058         19.236        33.608
CSTR
                                                       PRE-H
                     MIXER
                                                                 S4                                             S5
     S1                         S3


               S2




                                     Esterification KC09017
   Stream ID                             S1             S2            S3            S4            S5
   Temperature            C                     28.0           30.0          28.5          80.0          80.0
   Pressure               bar                  1.000          1.000         1.100         1.000         1.000
   Vapor Frac                                  0.000          0.000         0.000         0.000         0.000
   Mole Flow              kmol/hr             10.800          3.600        14.400        14.400        14.400
   Mass Flow              kg/hr           573.057        165.849       738.905       738.905       738.905
   Volume Flow            cum/hr               0.743          0.226         0.969         1.026         0.978
   Enthalpy               MMkcal/hr           -0.975         -0.239        -1.214        -1.189        -1.187
   Mass Frac
    ETHAN-01                                   0.434          1.000         0.561         0.561         0.269
    ACETI-01                                   0.566                        0.439         0.439         0.059
    WATER                                                                                               0.114
    ETHYL-01                                                                                            0.558
   Mole Flow              kmol/hr
    ETHAN-01                                   5.400          3.600         9.000         9.000         4.322
    ACETI-01                                   5.400                        5.400         5.400         0.722
    WATER                                                                                               4.678
    ETHYL-01                                                                                            4.678
   *** VAPOR PHASE ***
   Density
   Viscosity
   *** LIQUID PHASE ***
   Density                kg/cum          771.376        732.737       762.365       720.003       755.214
   Viscosity              cP                   0.725          0.626         0.702         0.396         0.414
   Surface Ten            dyne/cm             24.297         21.681        23.640        18.887        31.941



The heat duty of reactor for flow rate 3mol/s for Stream 1 = 3.27817123kW

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Hafiz aspen 1

  • 1. CSTR PRE-H MIXER S4 S5 S1 S3 S2 Esterification KC09017 Stream ID S1 S2 S3 S4 S5 Temperature C 28.0 30.0 28.2 80.0 80.0 Pressure bar 1.000 1.000 1.100 1.000 1.000 Vapor Frac 0.000 0.000 0.000 0.000 0.000 Mole Flow kmol/hr 36.000 3.600 39.600 39.600 39.600 Mass Flow kg/hr 1910.189 165.849 2076.037 2076.037 2076.037 Volume Flow cum/hr 2.476 0.226 2.703 2.858 2.712 Enthalpy MMkcal/hr -3.251 -0.239 -3.490 -3.422 -3.414 Mass Frac ETHAN-01 0.434 1.000 0.479 0.479 0.165 ACETI-01 0.566 0.521 0.521 0.111 WATER 0.123 ETHYL-01 0.601 Mole Flow kmol/hr ETHAN-01 18.000 3.600 21.600 21.600 7.437 ACETI-01 18.000 18.000 18.000 3.837 WATER 14.163 ETHYL-01 14.163 *** VAPOR PHASE *** Density Viscosity *** LIQUID PHASE *** Density kg/cum 771.376 732.737 768.150 726.488 765.553 Viscosity cP 0.725 0.626 0.716 0.403 0.421 Surface Ten dyne/cm 24.297 21.681 24.058 19.236 33.608
  • 2. CSTR PRE-H MIXER S4 S5 S1 S3 S2 Esterification KC09017 Stream ID S1 S2 S3 S4 S5 Temperature C 28.0 30.0 28.5 80.0 80.0 Pressure bar 1.000 1.000 1.100 1.000 1.000 Vapor Frac 0.000 0.000 0.000 0.000 0.000 Mole Flow kmol/hr 10.800 3.600 14.400 14.400 14.400 Mass Flow kg/hr 573.057 165.849 738.905 738.905 738.905 Volume Flow cum/hr 0.743 0.226 0.969 1.026 0.978 Enthalpy MMkcal/hr -0.975 -0.239 -1.214 -1.189 -1.187 Mass Frac ETHAN-01 0.434 1.000 0.561 0.561 0.269 ACETI-01 0.566 0.439 0.439 0.059 WATER 0.114 ETHYL-01 0.558 Mole Flow kmol/hr ETHAN-01 5.400 3.600 9.000 9.000 4.322 ACETI-01 5.400 5.400 5.400 0.722 WATER 4.678 ETHYL-01 4.678 *** VAPOR PHASE *** Density Viscosity *** LIQUID PHASE *** Density kg/cum 771.376 732.737 762.365 720.003 755.214 Viscosity cP 0.725 0.626 0.702 0.396 0.414 Surface Ten dyne/cm 24.297 21.681 23.640 18.887 31.941 The heat duty of reactor for flow rate 3mol/s for Stream 1 = 3.27817123kW