2021
DOI: 10.1016/j.fuproc.2021.106879
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Evaluating refinery configurations for deriving sustainable aviation fuel from ethanol or syncrude

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Cited by 24 publications
(17 citation statements)
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“…All pumps, turbines and compressors were modelled as isentropic units [39]. Finally, distillation processes were modelled using the RADFRAC model Aspen Plus ® , which facilitates rigorous energy and mass balance calculations and can be used to facilitate the separation of highly non-ideal liquid mixtures [40].…”
Section: Methodsmentioning
confidence: 99%
See 1 more Smart Citation
“…All pumps, turbines and compressors were modelled as isentropic units [39]. Finally, distillation processes were modelled using the RADFRAC model Aspen Plus ® , which facilitates rigorous energy and mass balance calculations and can be used to facilitate the separation of highly non-ideal liquid mixtures [40].…”
Section: Methodsmentioning
confidence: 99%
“…To determine the column design specifications, the design parameters (i.e., number of stages, reboiler duty, reflux ratio, etc.) were initially estimated using the Fenske-Underwood-Gilliland correlation model in Aspen Plus ® [39,41].…”
Section: Methodsmentioning
confidence: 99%
“…T, R and yi represent the temperature in K, the universal gas constant (8.314 J/mol•K), the mole fraction vapour of the ith specie respectively. Furthermore, all pumps, turbines and compressors were modelled as isentropic units [41]. Finally, distillation processes were modelled using the RADFRAC model Aspen Plus®, which facilitates rigorous energy and mass balance calculations and can be used to facilitate the separation of highly nonideal liquid mixtures [42].…”
Section: Methodsmentioning
confidence: 99%
“…number of stages, reboiler duty, reflux ratio etc.) were estimated using the Fenske-Underwood-Gilliland correlation model in Aspen Plus® [41,43].…”
Section: Methodsmentioning
confidence: 99%
See 1 more Smart Citation