Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
Само за регистроване кориснике
2017
Аутори
Živković, Nikola V.Živković, Emila
Šerbanović, Slobodan P.
Majstorović, Divna
Kijevčanin, Mirjana
Чланак у часопису (Објављена верзија)
Метаподаци
Приказ свих података о документуАпстракт
Desulphurization processes (FGD) of flue gases from the thermal power and industrial plants, based on organic liquid solvents with mechanism of physical absorption (tetraethylene glycol dimethyl ether) or combination of physical and chemical absorption (N-methyl-2-pyrrolidone), recently gained its significance. The research results presented in this paper include density and dynamic viscosity measurements of following binary systems at atmospheric pressure: polyethylene glycol 200 + tetraethylene glycol dimethyl ether, polyethylene glycol 400 + tetraethylene glycol dimethyl ether, in temperature range from 288.15 to 333.15 K, and binary systems polyethylene glycol 200 + N-methyl-2-pyrrolidone and polyethylene glycol 400 + N-methyl-2-pyrrolidone, in temperature range from 288.15 to 323.15 K. In order to analyze and comment intermolecular interactions, calculated values of excess molar volumes and viscosity deviations were used. Strong, physical interactions of dipole-dipole type or form...ation of intermolecular hydrogen bonds lead and contribute to negative V-E values that occur in these systems. Calculated values of excess and deviation properties were interpolated using the Redlich-Kister polynomial equation. Viscosity modeling has been performed, using predictive, group contribution models (UNIFAC - VISCO and ASOG- VISCO) as well as correlative models (McAlister, Eyring - UNIQUAC and Eyring - NRTL). For simultaneous modeling of excess molar volumes and viscosities, model based on the equation of state was used. For investigated systems, correlative McAllister models gave the best results and can be used for viscosity calculations.
Кључне речи:
Flue gas desulphurization / Density / Viscosity / Gibbs energy / Molecular interactions / Viscosity modelingИзвор:
Journal of Chemical Thermodynamics, 2017, 108, 162-180Издавач:
- Academic Press Ltd- Elsevier Science Ltd, London
Финансирање / пројекти:
- Research Fund of Ministry of Science and Environmental Protection, Serbia
- Нови индустријски и еколошки аспекти примене хемијске термодинамике на унапређење хемијских процеса са вишефазним и вишекомпонентним системима (RS-172063)
DOI: 10.1016/j.jct.2017.01.018
ISSN: 0021-9614
WoS: 000395614400018
Scopus: 2-s2.0-85011552143
Институција/група
Tehnološko-metalurški fakultetTY - JOUR AU - Živković, Nikola V. AU - Živković, Emila AU - Šerbanović, Slobodan P. AU - Majstorović, Divna AU - Kijevčanin, Mirjana PY - 2017 UR - http://TechnoRep.tmf.bg.ac.rs/handle/123456789/3697 AB - Desulphurization processes (FGD) of flue gases from the thermal power and industrial plants, based on organic liquid solvents with mechanism of physical absorption (tetraethylene glycol dimethyl ether) or combination of physical and chemical absorption (N-methyl-2-pyrrolidone), recently gained its significance. The research results presented in this paper include density and dynamic viscosity measurements of following binary systems at atmospheric pressure: polyethylene glycol 200 + tetraethylene glycol dimethyl ether, polyethylene glycol 400 + tetraethylene glycol dimethyl ether, in temperature range from 288.15 to 333.15 K, and binary systems polyethylene glycol 200 + N-methyl-2-pyrrolidone and polyethylene glycol 400 + N-methyl-2-pyrrolidone, in temperature range from 288.15 to 323.15 K. In order to analyze and comment intermolecular interactions, calculated values of excess molar volumes and viscosity deviations were used. Strong, physical interactions of dipole-dipole type or formation of intermolecular hydrogen bonds lead and contribute to negative V-E values that occur in these systems. Calculated values of excess and deviation properties were interpolated using the Redlich-Kister polynomial equation. Viscosity modeling has been performed, using predictive, group contribution models (UNIFAC - VISCO and ASOG- VISCO) as well as correlative models (McAlister, Eyring - UNIQUAC and Eyring - NRTL). For simultaneous modeling of excess molar volumes and viscosities, model based on the equation of state was used. For investigated systems, correlative McAllister models gave the best results and can be used for viscosity calculations. PB - Academic Press Ltd- Elsevier Science Ltd, London T2 - Journal of Chemical Thermodynamics T1 - Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes EP - 180 SP - 162 VL - 108 DO - 10.1016/j.jct.2017.01.018 ER -
@article{ author = "Živković, Nikola V. and Živković, Emila and Šerbanović, Slobodan P. and Majstorović, Divna and Kijevčanin, Mirjana", year = "2017", abstract = "Desulphurization processes (FGD) of flue gases from the thermal power and industrial plants, based on organic liquid solvents with mechanism of physical absorption (tetraethylene glycol dimethyl ether) or combination of physical and chemical absorption (N-methyl-2-pyrrolidone), recently gained its significance. The research results presented in this paper include density and dynamic viscosity measurements of following binary systems at atmospheric pressure: polyethylene glycol 200 + tetraethylene glycol dimethyl ether, polyethylene glycol 400 + tetraethylene glycol dimethyl ether, in temperature range from 288.15 to 333.15 K, and binary systems polyethylene glycol 200 + N-methyl-2-pyrrolidone and polyethylene glycol 400 + N-methyl-2-pyrrolidone, in temperature range from 288.15 to 323.15 K. In order to analyze and comment intermolecular interactions, calculated values of excess molar volumes and viscosity deviations were used. Strong, physical interactions of dipole-dipole type or formation of intermolecular hydrogen bonds lead and contribute to negative V-E values that occur in these systems. Calculated values of excess and deviation properties were interpolated using the Redlich-Kister polynomial equation. Viscosity modeling has been performed, using predictive, group contribution models (UNIFAC - VISCO and ASOG- VISCO) as well as correlative models (McAlister, Eyring - UNIQUAC and Eyring - NRTL). For simultaneous modeling of excess molar volumes and viscosities, model based on the equation of state was used. For investigated systems, correlative McAllister models gave the best results and can be used for viscosity calculations.", publisher = "Academic Press Ltd- Elsevier Science Ltd, London", journal = "Journal of Chemical Thermodynamics", title = "Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes", pages = "180-162", volume = "108", doi = "10.1016/j.jct.2017.01.018" }
Živković, N. V., Živković, E., Šerbanović, S. P., Majstorović, D.,& Kijevčanin, M.. (2017). Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes. in Journal of Chemical Thermodynamics Academic Press Ltd- Elsevier Science Ltd, London., 108, 162-180. https://doi.org/10.1016/j.jct.2017.01.018
Živković NV, Živković E, Šerbanović SP, Majstorović D, Kijevčanin M. Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes. in Journal of Chemical Thermodynamics. 2017;108:162-180. doi:10.1016/j.jct.2017.01.018 .
Živković, Nikola V., Živković, Emila, Šerbanović, Slobodan P., Majstorović, Divna, Kijevčanin, Mirjana, "Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes" in Journal of Chemical Thermodynamics, 108 (2017):162-180, https://doi.org/10.1016/j.jct.2017.01.018 . .