Standard

Kinetics of esterification and hydrolysis in the n-propanol + acetic acid + n-propyl acetate + water system in homogeneous and heterogeneous composition areas. / Tsvetov, N.S.; Pervukhin, O.K.; Toikka, A.M.

In: Theoretical Foundations of Chemical Engineering, Vol. 49, No. 3, 2015, p. 297-305.

Research output: Contribution to journal › Article

Harvard

Tsvetov, NS, Pervukhin, OK & Toikka, AM 2015, 'Kinetics of esterification and hydrolysis in the n-propanol + acetic acid + n-propyl acetate + water system in homogeneous and heterogeneous composition areas', Theoretical Foundations of Chemical Engineering, vol. 49, no. 3, pp. 297-305. https://doi.org/10.1134/S0040579515030148

APA

Tsvetov, N. S., Pervukhin, O. K., & Toikka, A. M. (2015). Kinetics of esterification and hydrolysis in the n-propanol + acetic acid + n-propyl acetate + water system in homogeneous and heterogeneous composition areas. Theoretical Foundations of Chemical Engineering, 49(3), 297-305. https://doi.org/10.1134/S0040579515030148

Vancouver

Tsvetov NS, Pervukhin OK, Toikka AM. Kinetics of esterification and hydrolysis in the n-propanol + acetic acid + n-propyl acetate + water system in homogeneous and heterogeneous composition areas. Theoretical Foundations of Chemical Engineering. 2015;49(3):297-305. https://doi.org/10.1134/S0040579515030148

Author

Tsvetov, N.S. ; Pervukhin, O.K. ; Toikka, A.M. / Kinetics of esterification and hydrolysis in the n-propanol + acetic acid + n-propyl acetate + water system in homogeneous and heterogeneous composition areas. In: Theoretical Foundations of Chemical Engineering. 2015 ; Vol. 49, No. 3. pp. 297-305.

BibTeX

@article{bd7ec07a542c4c2db8e33aaf500947ae,
title = "Kinetics of esterification and hydrolysis in the n-propanol + acetic acid + n-propyl acetate + water system in homogeneous and heterogeneous composition areas",
abstract = "The reaction kinetics of esterification-hydrolysis in the n-propanol + acetic acid + n-propyl acetate + water system is considered. The phase state of the reaction mixture-homogeneous or two-phase-can change in the course of reaction due to the occurrence of a splitting region. For the analysis of the behavior of the system under these conditions, experimental data on the reaction kinetics were obtained at 293.15 K for both the homogeneous and heterogeneous regions of compositions. The evolution of the reaction system in time with the simultaneous occurrence of a chemical process and interphase mass transfer is also considered.",
author = "N.S. Tsvetov and O.K. Pervukhin and A.M. Toikka",
year = "2015",
doi = "10.1134/S0040579515030148",
language = "English",
volume = "49",
pages = "297--305",
journal = "Theoretical Foundations of Chemical Engineering",
issn = "0040-5795",
publisher = "МАИК {"}Наука/Интерпериодика{"}",
number = "3",

}

RIS

TY - JOUR

T1 - Kinetics of esterification and hydrolysis in the n-propanol + acetic acid + n-propyl acetate + water system in homogeneous and heterogeneous composition areas

AU - Tsvetov, N.S.

AU - Pervukhin, O.K.

AU - Toikka, A.M.

PY - 2015

Y1 - 2015

N2 - The reaction kinetics of esterification-hydrolysis in the n-propanol + acetic acid + n-propyl acetate + water system is considered. The phase state of the reaction mixture-homogeneous or two-phase-can change in the course of reaction due to the occurrence of a splitting region. For the analysis of the behavior of the system under these conditions, experimental data on the reaction kinetics were obtained at 293.15 K for both the homogeneous and heterogeneous regions of compositions. The evolution of the reaction system in time with the simultaneous occurrence of a chemical process and interphase mass transfer is also considered.

AB - The reaction kinetics of esterification-hydrolysis in the n-propanol + acetic acid + n-propyl acetate + water system is considered. The phase state of the reaction mixture-homogeneous or two-phase-can change in the course of reaction due to the occurrence of a splitting region. For the analysis of the behavior of the system under these conditions, experimental data on the reaction kinetics were obtained at 293.15 K for both the homogeneous and heterogeneous regions of compositions. The evolution of the reaction system in time with the simultaneous occurrence of a chemical process and interphase mass transfer is also considered.

U2 - 10.1134/S0040579515030148

DO - 10.1134/S0040579515030148

M3 - Article

VL - 49

SP - 297

EP - 305

JO - Theoretical Foundations of Chemical Engineering

JF - Theoretical Foundations of Chemical Engineering

SN - 0040-5795

IS - 3

ER -

ID: 3937508