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Similar to Hafiz aspen 1 (20)
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