Erratum to “Modeling and simulation of saline extractive distillation columns for the production of absolute ethanol” [Comput. Chem. Eng. 27 (2003) 527–549]

Llano‐Restrepo, Mario; Aguilar-Arias, Jaime

doi:10.1016/j.compchemeng.2004.07.001

Cited by 1 publication

(6 citation statements)

References 0 publications

Supporting

Mentioning

Contrasting

Order By: Relevance

“…A feed with a concentration of approximately 40 wt-% (20 % on a molar basis) ethanol was chosen for the simulation study reported in that paper [6]. Also, in the industry, a steam-stripping column is usually used to preconcentrate dilute solution of ethanol to a concentration greater than 30 wt-% before any azeotropic or extractive distillation step.…”

Section: Simulation Resultsmentioning

confidence: 99%

“…Detailed information on how to calculate each part of Eq. (27) is not the purpose of this work, but is given by Llano-Restrepo et al [6].…”

Section: This Model Is Formulated As Followsmentioning

confidence: 96%

“…Regarding the results obtained by Pinto et al, extractive distillation using CaCl 2 had a lower energy requirement in comparison with other salt alternatives [5]. Llano-Restrepo et al simulated saline extractive distillation columns and applied them to produce absolute ethanol using CaCl 2 to break the ethanol-water azeotrope [6]. In their work, the E-NRTL model proved to be the most accurate to correlate the experimental vapor-liquid equilibrium (VLE) data available for the ethanol-water-CaCl 2 system [6].…”

Section: Introductionmentioning

confidence: 94%

“…Llano-Restrepo et al, based on the enthalpy model discussed by Liu and Watanasiri for aqueous/salt systems [6], developed the approach for the calculation of the liquid enthalpy of mixed solvent/salt systems.…”

Section: Enthalpy Model For Mixed Solvent/salt Systemsmentioning

confidence: 99%

“…Llano-Restrepo et al simulated saline extractive distillation columns and applied them to produce absolute ethanol using CaCl 2 to break the ethanol-water azeotrope [6]. In their work, the E-NRTL model proved to be the most accurate to correlate the experimental vapor-liquid equilibrium (VLE) data available for the ethanol-water-CaCl 2 system [6]. In the process of simulation with electrolytes, suitable models are needed to predict the thermodynamic and transport properties of electrolyte solutions.…”

Section: Introductionmentioning

confidence: 99%

See 4 more Smart Citations

Application of a New Gibbs Energy Equation to Model a Distillation Tower for Production of Pure Ethanol

et al. 2011

View full text Add to dashboard Cite

A steady-state equilibrium-stage model based on MESH equations was proposed to simulate saline extractive distillation columns. The interaction parameters between each component of water-CaCl 2 and ethanol-water were obtained from mean ionic activity coefficients and vapor-liquid equilibrium (VLE) experimental data. Additionally, the interaction coefficients for the ethanol-CaCl 2 pair were fitted to experimental VLE data which were reported by Nishi for the ethanolwater-CaCl 2 system. It should be noted that adjustable parameters between each pair were considered to be temperature dependent. The results confirmed that the proposed model could accurately predict the experimental vapor-liquid equilibrium data for ethanol-CaCl 2 -water systems. Finally, the validated model was coded using MATLAB software and was solved using the Wang-Henke method, including the VLE and enthalpy models.

show abstract

Section: Simulation Resultsmentioning

confidence: 99%

“…Detailed information on how to calculate each part of Eq. (27) is not the purpose of this work, but is given by Llano-Restrepo et al [6].…”

Section: This Model Is Formulated As Followsmentioning

confidence: 96%