[article]
Titre : |
Dynamic simulation of rosemary essential oil extraction in an industrial steam distillation unit |
Type de document : |
texte imprimé |
Auteurs : |
Rafael B. Sartor, Auteur ; Argimiro R. Secchi, Auteur ; Rafael de P. Soares, Auteur |
Année de publication : |
2011 |
Article en page(s) : |
pp. 3955-3959 |
Note générale : |
Chimie industrielle |
Langues : |
Anglais (eng) |
Mots-clés : |
Modeling Steam distillation Essential oil Dynamic model |
Résumé : |
This work presents the dynamic simulation of rosemary essential oil extraction by steam-distillation. Experimental data acquired in an industrial steam-distillation unit were used to estimate the model parameters. Two distinct climatic conditions (summer and winter) were used to verify the model flexibility. In winter condition, two time-dependent experimental data curves were used together to verify the parameter estimation strategy, whereas in summer condition, two time-dependent curves were used for parameter estimation and a third one for model validation with respect to prediction. The mathematical model fitted satisfactorily both set of industrial data, resulting, for the summer and winter, in global mass transfer coefficient of 8.64 x 10―4s―1 and 9.10 × 10―4 s ―1, and equilibrium constant 2.72 x 10―4 m3/kg and 1.07 x 10―2m3/kg, respectively. |
DEWEY : |
660 |
ISSN : |
0888-5885 |
En ligne : |
http://cat.inist.fr/?aModele=afficheN&cpsidt=24027641 |
in Industrial & engineering chemistry research > Vol. 50 N° 7 (Avril 2011) . - pp. 3955-3959
[article] Dynamic simulation of rosemary essential oil extraction in an industrial steam distillation unit [texte imprimé] / Rafael B. Sartor, Auteur ; Argimiro R. Secchi, Auteur ; Rafael de P. Soares, Auteur . - 2011 . - pp. 3955-3959. Chimie industrielle Langues : Anglais ( eng) in Industrial & engineering chemistry research > Vol. 50 N° 7 (Avril 2011) . - pp. 3955-3959
Mots-clés : |
Modeling Steam distillation Essential oil Dynamic model |
Résumé : |
This work presents the dynamic simulation of rosemary essential oil extraction by steam-distillation. Experimental data acquired in an industrial steam-distillation unit were used to estimate the model parameters. Two distinct climatic conditions (summer and winter) were used to verify the model flexibility. In winter condition, two time-dependent experimental data curves were used together to verify the parameter estimation strategy, whereas in summer condition, two time-dependent curves were used for parameter estimation and a third one for model validation with respect to prediction. The mathematical model fitted satisfactorily both set of industrial data, resulting, for the summer and winter, in global mass transfer coefficient of 8.64 x 10―4s―1 and 9.10 × 10―4 s ―1, and equilibrium constant 2.72 x 10―4 m3/kg and 1.07 x 10―2m3/kg, respectively. |
DEWEY : |
660 |
ISSN : |
0888-5885 |
En ligne : |
http://cat.inist.fr/?aModele=afficheN&cpsidt=24027641 |
|