2001
DOI: 10.1080/00986440108912837
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CALCULATING DISTILLATION EFFICIENCIES OF MULTICOMPONENT i-BUTANE/ n-BUTANE COLUMN

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Cited by 3 publications
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“…In this model, the CDC system is simulated as an equilibrium-based RadFrac ® column with the Soave-Redlich-Kwong (SRK) property package using Aspen Plus ® (Version 9.0). Stage efficiencies are adjusted to reproduce the reported data of column duties and stage temperatures [38,39] and product compositions and flow rates (Table 1). Using the predicted stage efficiency of 137.9%, the number of theoretical stages in the conventional column is calculated to be 104.…”
Section: Exergy Analysis Of the Conventional Distillation Columnmentioning
confidence: 99%
“…In this model, the CDC system is simulated as an equilibrium-based RadFrac ® column with the Soave-Redlich-Kwong (SRK) property package using Aspen Plus ® (Version 9.0). Stage efficiencies are adjusted to reproduce the reported data of column duties and stage temperatures [38,39] and product compositions and flow rates (Table 1). Using the predicted stage efficiency of 137.9%, the number of theoretical stages in the conventional column is calculated to be 104.…”
Section: Exergy Analysis Of the Conventional Distillation Columnmentioning
confidence: 99%