Reconciliation of HP HCR Reactor Model

Hypothetical raactor Feed eum of real reactore Hydrogen quench = sum of real reactors Effluent products from the real process Catalyst loading sum of real reactors Temperature average of real reactors Pressure - average of real reactors 

Delumpingofthe Reactor Model Effluent and Fractionator Model Development 

Delumping the reactor model effluent is an essential step to integrate the reactor model with the fractionator model, because kinetic lumps used in the reactor model are based on the structure and carbon number and cannot represent accurate thermodynamic behavior of the fractionator model. Because boiling point (volatility) is the most important property for distillation operation, process modelers typically use pseudocomponents based on the true boiling point (TBP) curve to represent the feed oil to the HCR fractionators. We present five steps to develop pseudocomponents based on boiling-point ranges to represent the petroleum fraction [32, 34]  

2 Asiuoee rci AST14-I088 17) TBP(F) TBPfd TBPrCI TBP (F) ASTM-D86 CF) MlMDSerC) 

13 jflSTM-D2887(C) Urt%AM% AS1U 0288717) TBP(F) TBP(C) TBPCCI TBP (F) ASTW-D2S87(F) ASTM 02887(d 

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