1981
DOI: 10.1021/i200013a024
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Abstract: Froment, G. F., Ed.; Elsevier: Amsterdam, 1980 p 91. Mlron, S.; Lee, R. J. Dev. 1062, 7, 102. 1964. Process Des. Dev. 1066, 5, 193. Ozawa, Y.; Blschoff, K. Ind. fng. Chem. Process Des. Dev. 1068r, 7 , 72. Ozawa, Y.; Blschoff, K. Ind. Eng. Chem. Process Des. Dev. 1068b, 7, 67. Pachovsky, R. A.; Best, D.; Wojciechowskl, B. W. Ind. fng. Chem. Process Poutsma, M. L.A UNIFAC groupinteraction parameter table especially suited for prediction of liquid-liquid equilibria at temperatures between 10 and 40 O C has been d… Show more

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Cited by 795 publications
(600 citation statements)
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“…The equilibrium data for the ternary mixture were also predicted by the UNIFAC method (Fredenslund et al, 1975(Fredenslund et al, , 1977 using the parameters obtained by Magnussen et al (1981). The values of the UNIFAC parameters for LLE prediction are summarized in Table 7 The root mean square deviations (RMSD) were calculated from the difference between the experimental data and the predictions of the UNIFAC method at each temperature according to the following formula:…”
Section: Prediction Of Equilibria By the Unifac Methodsmentioning
confidence: 99%
“…The equilibrium data for the ternary mixture were also predicted by the UNIFAC method (Fredenslund et al, 1975(Fredenslund et al, , 1977 using the parameters obtained by Magnussen et al (1981). The values of the UNIFAC parameters for LLE prediction are summarized in Table 7 The root mean square deviations (RMSD) were calculated from the difference between the experimental data and the predictions of the UNIFAC method at each temperature according to the following formula:…”
Section: Prediction Of Equilibria By the Unifac Methodsmentioning
confidence: 99%
“…Two models were used in our calculations: UNIQUAC (Abrams and Prausnitz, 1975) and UNIFAC (Fredenslund et al, 1975). The data, equations, parameters and programs were taken from Sørensen and Arlt (1980) and Magnussen et al (1981).…”
Section: Models and Methodsmentioning
confidence: 99%
“…They were computed from bond angle and bond distance and were estimated by group-contribution method using tabulated S g and Q g values from [28] and [29]. v g(i) is the number of functional group g for compound i, is the mole fraction of compound i.…”
Section: E Thermodynamic Modelingmentioning
confidence: 99%