Coupling VOF interfacial mass transfer model with RSM approach in LLE systems: Developing the new correlations for mass transfer, aspect ratio and terminal velocity. (April 2021)
- Record Type:
- Journal Article
- Title:
- Coupling VOF interfacial mass transfer model with RSM approach in LLE systems: Developing the new correlations for mass transfer, aspect ratio and terminal velocity. (April 2021)
- Main Title:
- Coupling VOF interfacial mass transfer model with RSM approach in LLE systems: Developing the new correlations for mass transfer, aspect ratio and terminal velocity
- Authors:
- Roshdi, Sepideh
Kasiri, Norollah - Abstract:
- Abstract: The performance of liquid-liquid extraction (LLE) systems is determined by terminal velocity and extraction fraction. Several parameters and their interactive effects influence the performance. In the present study, the response surface methodology(RSM) approach has been used to investigate the parameters' effects and their complicated interactions in hydrodynamics and mass transfer. Hydrodynamic and mass transfer simulations of a single droplet system have been carried out using the VOF method and close agreements have been attained in comparison with experimental data. Subsequently, the RSM and central composite design methods were employed in terminal velocity, aspect ratio, and extraction fraction modeling. The drop diameter, density ratio, and viscosity ratio have been chosen as the effective hydrodynamic parameters in the terminal velocity and aspect ratio. The mentioned hydrodynamic parameters, partition coefficient, and diffusivity ratio have been chosen as the mass transfer variables. The suggested quadratic models of terminal velocity(R 2 = 0.99) gives accurate predictions in high Re numbers, while the previous correlations could not. The new general quadratic model of aspect ratio having included the viscosity ratio as an effective parameter, can be used in the wide range of material properties with high accuracy (R 2 = 0.95), while the previous correlations have not included the viscosity ratio. The new quadratic model of mass transfer with highAbstract: The performance of liquid-liquid extraction (LLE) systems is determined by terminal velocity and extraction fraction. Several parameters and their interactive effects influence the performance. In the present study, the response surface methodology(RSM) approach has been used to investigate the parameters' effects and their complicated interactions in hydrodynamics and mass transfer. Hydrodynamic and mass transfer simulations of a single droplet system have been carried out using the VOF method and close agreements have been attained in comparison with experimental data. Subsequently, the RSM and central composite design methods were employed in terminal velocity, aspect ratio, and extraction fraction modeling. The drop diameter, density ratio, and viscosity ratio have been chosen as the effective hydrodynamic parameters in the terminal velocity and aspect ratio. The mentioned hydrodynamic parameters, partition coefficient, and diffusivity ratio have been chosen as the mass transfer variables. The suggested quadratic models of terminal velocity(R 2 = 0.99) gives accurate predictions in high Re numbers, while the previous correlations could not. The new general quadratic model of aspect ratio having included the viscosity ratio as an effective parameter, can be used in the wide range of material properties with high accuracy (R 2 = 0.95), while the previous correlations have not included the viscosity ratio. The new quadratic model of mass transfer with high accuracy (R 2 = 0.99), includes partition coefficient and its interactive effects with diffusivity ratio and hydrodynamic parameters which have not been considered yet. More additionally, the developed model could be applied in every LLE system regardless of the mass transfer resistance existence in the drop/continuous phase or both. Finally, the ANOVA showed that the partition coefficient and viscosity ratio are the most effective parameters in mass transfer, hence the reduction in the partition coefficient along with the reduction in viscosity ratio would help to reach the better mass transfer performance. At the final stage, the optimized conditions have been presented. Highlights: Coupling the RSM with CFD simulations to investigate the independent variables and their interactive effects on the hydrodynamics and mass transfer of LLE Presenting the regression model for terminal velocity with high accuracy in large Re numbers Presenting the regression model for aspect ratio including viscosity ratio in the wide range of material properties Presenting the regression model for extraction fraction, considering the interactive effects of partition coefficient with hydrodynamic variables and diffusivity ratio ANOVA showed that PC and viscosity ratio are the most effective parameters in mass transfer, and the optimized condition for LLE has been presented. Optimized condition for LLE in terms of hydrodynamics and mass transfer has been presented. … (more)
- Is Part Of:
- International communications in heat and mass transfer. Volume 123(2021)
- Journal:
- International communications in heat and mass transfer
- Issue:
- Volume 123(2021)
- Issue Display:
- Volume 123, Issue 2021 (2021)
- Year:
- 2021
- Volume:
- 123
- Issue:
- 2021
- Issue Sort Value:
- 2021-0123-2021-0000
- Page Start:
- Page End:
- Publication Date:
- 2021-04
- Subjects:
- Heat -- Transmission -- Periodicals
Mass transfer -- Periodicals
Chaleur -- Transmission -- Périodiques
Transfert de masse -- Périodiques
Heat -- Transmission
Mass transfer
Periodicals
621.4022 - Journal URLs:
- http://www.sciencedirect.com/science/journal/07351933 ↗
http://www.elsevier.com/journals ↗ - DOI:
- 10.1016/j.icheatmasstransfer.2021.105216 ↗
- Languages:
- English
- ISSNs:
- 0735-1933
- Deposit Type:
- Legaldeposit
- View Content:
- Available online (eLD content is only available in our Reading Rooms) ↗
- Physical Locations:
- British Library DSC - 4538.722800
British Library DSC - BLDSS-3PM
British Library HMNTS - ELD Digital store - Ingest File:
- 16098.xml