Zobrazeno 1 - 4
of 4
pro vyhledávání: '"Tariq Allie-Ebrahim"'
Autor:
Tariq, Allie-Ebrahim, Vincenzo, Russo, Ornella, Ortona, Luigi, Paduano, Riccardo, Tesser, Martino, Di Serio, Pranav, Singh, Qingyu, Zhu, Geoff D, Moggridge, Carmine, D'Agostino
Publikováno v:
Physical chemistry chemical physics : PCCP. 20(27)
Diffusion plays a central part in many unit operations. The Maxwell-Stefan model is the dominant model for both gaseous and liquid diffusion. However, it was developed from the kinetic theory of gases, raising the question of whether it can be extend
Publikováno v:
Physical Chemistry Chemical Physics. 21:12704-12705
Correction for ‘Maxwell–Stefan diffusion coefficient estimation for ternary systems: an ideal ternary alcohol system’ by Tariq Allie-Ebrahim et al., Phys. Chem. Chem. Phys., 2017, 19, 16071–16077.
Maxwell-Stefan diffusion coefficient estimation for ternary systems: an ideal ternary alcohol system
Publikováno v:
Allie-Ebrahim, T, Zhu, Q, Brauer, P, Moggridge, G D & D'Agostino, C 2017, ' Maxwell-Stefan diffusion coefficient estimation for ternary systems: an ideal ternary alcohol system ', Physical Chemistry Chemical Physics, vol. 19, no. 24, pp. 16071-16077 . https://doi.org/10.1039/c7cp02582c
The Maxwell–Stefan model is a popular diffusion model originally developed to model diffusion of gases, which can be considered thermodynamically ideal mixtures, although its application has been extended to model diffusion in non-ideal liquid mixt
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::0729d7c63afff0fa5ed4427f14afba76
https://doi.org/10.1039/c7cp02582c
https://doi.org/10.1039/c7cp02582c
Publikováno v:
D'Agostino, C, Allie-Ebrahim, T, Zhu, Q & Moggridge, G D 2017, ' Liquid-liquid equilibrium for the ternary system ethanol/toluene/n-decane: a correction to the existing coexistence curve and NRTL parameters ', PHYSICS AND CHEMISTRY OF LIQUIDS, vol. 55, no. 5, pp. 669-673 . https://doi.org/10.1080/00319104.2016.1262367
A correction to the reported liquid–liquid equilibrium parameters using the non-random two liquid (NRTL) thermodynamic model for the ethanol/toluene/n-decane system at 298 K is reported. The parameters were calculated by minimising the residual bet
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::ba6af68076fa57b1e56b683369cc92ea
https://www.repository.cam.ac.uk/handle/1810/262413
https://www.repository.cam.ac.uk/handle/1810/262413