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Table 6 Validation results

From: Exergy analysis and performance study for sour water stripper units, amine regenerator units and a Sulphur recovery unit of a refining plant

  Design Simulation Dev % Design Simulation Dev %
Stream name AAG to SRU SWS AG to SRU
Temperature 55 55 0.00 92 92 0.00
Pressure 0.75 0.75 0.00 0.77 0.77 0.00
Mass 11,975 12,263.52 − 2.41 3674 3762.59 − 2.41
Component Mole fraction Mole fraction
 H2O 0.100 0.091 8.94 0.338 0.343 − 1.54
 NH3 0.000 0.000 0.00 0.337 0.315 6.42
 H2S 0.900 0.909 − 0.99 0.325 0.341 − 5.02