The document describes a process involving streams S1 through S5. Stream S1 and S3 are fed into a pre-heater and mixer before entering reactor S4. S4 then flows to S5. The streams are described with properties such as temperature, pressure, flow rates, compositions and phase properties. The heat duty of the reactor is also provided for a given flow rate in stream S1.

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