2004
DOI: 10.1002/aic.10057
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New approach to refinery process simulation with adaptive composition representation

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Cited by 31 publications
(20 citation statements)
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“…The concept brings back simplicity into the description of a mixture and the number of pseudo-components usually employed to describe a crude is in the order of dozens. There are a number of empirical ways to perform this mapping, and no consensus of an optimal procedure exits 4 . Related approaches map the behaviour of a crude to a mixture of real components 5 or characterize pseudo-components based on 13 C NMR and other analytical data subsequently applying group contribution methods 6,7 to obtain the corresponding equation of state (EoS) parameters.…”
Section: Introductionmentioning
confidence: 99%
“…The concept brings back simplicity into the description of a mixture and the number of pseudo-components usually employed to describe a crude is in the order of dozens. There are a number of empirical ways to perform this mapping, and no consensus of an optimal procedure exits 4 . Related approaches map the behaviour of a crude to a mixture of real components 5 or characterize pseudo-components based on 13 C NMR and other analytical data subsequently applying group contribution methods 6,7 to obtain the corresponding equation of state (EoS) parameters.…”
Section: Introductionmentioning
confidence: 99%
“…The pseudo-components approach based on distillation curves is widely used to represent the complex composition of petroleum fractions (Briesen and Marquardt, 2004), although it is not effective in LLE modeling because chemical structure has much bigger effect than boiling temperature. For that reason, the "molecules-type" approach should be more convenient since it makes difference according to chemical nature of compounds (Vakili-Nezhaad et al, 1999).…”
Section: Introductionmentioning
confidence: 99%
“…(1)Physical property data In order to build mechanistic model with actual physical property for each component involved, real component method is needed, which is more accurate than pseudo-component method in the modeling and simulation [11], and higher accuracy can be expected in industrial practice [11][12][13].…”
Section: Accepted Manuscriptmentioning
confidence: 99%
“…Comparison of converted and calculated TBP distillation curves with and without HDS for refined diesel ○: converted value; ▼: calculated value by real components with HDS; △: calculated value by real components without HDSEOS models are usually used to calculate the properties for hydrocarbon mixtures[11], among equations of state, e.g. Peng-Robinson and Soave-Redlich-Kwong (SRK), are used frequently.…”
mentioning
confidence: 99%