Performance study of ionic liquid in extraction based on single-drop experiments
Experiments of single-drop sedimentation and mass transfer on a laboratory scale for the extraction of acetone from a water + acetone mixture by means of the ionic liquid 1-hexyl-3-methylimidazolium hexafluorophosphate (HMIMPF 6 ) were performed at a temperature of 298.2 K and ambient pressure. Stud...
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Published in | Solvent extraction and ion exchange Vol. 35; no. 7; pp. 563 - 572 |
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Main Authors | , , , |
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Language | English |
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10.11.2017
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Abstract | Experiments of single-drop sedimentation and mass transfer on a laboratory scale for the extraction of acetone from a water + acetone mixture by means of the ionic liquid 1-hexyl-3-methylimidazolium hexafluorophosphate (HMIMPF
6
) were performed at a temperature of 298.2 K and ambient pressure. Study of the system equilibrium conditions in a previous work (Saien et al., 2015) showed that HMIMPF
6
, as a green solvent for the extraction of acetone from aqueous solutions, has suitable capability. The single-drop experiments with this system show that the mass transfer is not as slow as expected despite the relatively high viscosity of the system. The Henschke model is applied to the obtained data for the challenging system involving an ionic liquid by determining appropriate values for the corresponding material-specific model parameters. This model describes the experimental data with very good accuracy. |
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AbstractList | Experiments of single-drop sedimentation and mass transfer on a laboratory scale for the extraction of acetone from a water + acetone mixture by means of the ionic liquid 1-hexyl-3-methylimidazolium hexafluorophosphate (HMIMPF
6
) were performed at a temperature of 298.2 K and ambient pressure. Study of the system equilibrium conditions in a previous work (Saien et al., 2015) showed that HMIMPF
6
, as a green solvent for the extraction of acetone from aqueous solutions, has suitable capability. The single-drop experiments with this system show that the mass transfer is not as slow as expected despite the relatively high viscosity of the system. The Henschke model is applied to the obtained data for the challenging system involving an ionic liquid by determining appropriate values for the corresponding material-specific model parameters. This model describes the experimental data with very good accuracy. Experiments of single-drop sedimentation and mass transfer on a laboratory scale for the extraction of acetone from a water + acetone mixture by means of the ionic liquid 1-hexyl-3-methylimidazolium hexafluorophosphate (HMIMPF6) were performed at a temperature of 298.2 K and ambient pressure. Study of the system equilibriumconditions in a previous work (Saien et al., 2015) showed that HMIMPF6, as a green solvent for the extraction of acetone from aqueous solutions, has suitable capability. The single-drop experimentswith this systemshow that the mass transfer is not as slow as expected despite the relatively high viscosity of the system. The Henschke model is applied to the obtained data for the challenging system involving an ionic liquid by determining appropriate values for the corresponding material-specific model parameters. This model describes the experimental data with very good accuracy. |
Author | Badieh, Marjan Mohammadi Sarab Quaresima, Maria Chiara Saien, Javad Pfennig, Andreas |
Author_xml | – sequence: 1 givenname: Marjan Mohammadi Sarab surname: Badieh fullname: Badieh, Marjan Mohammadi Sarab organization: Department of Applied Chemistry, Bu-Ali Sina University – sequence: 2 givenname: Maria Chiara surname: Quaresima fullname: Quaresima, Maria Chiara organization: Department of Chemical Engineering, University of Liège – sequence: 3 givenname: Andreas surname: Pfennig fullname: Pfennig, Andreas email: andreas.pfennig@ulg.ac.be organization: Department of Chemical Engineering, University of Liège – sequence: 4 givenname: Javad surname: Saien fullname: Saien, Javad organization: Department of Applied Chemistry, Bu-Ali Sina University |
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CitedBy_id | crossref_primary_10_1016_j_ijheatmasstransfer_2019_118603 crossref_primary_10_1021_acs_iecr_0c02787 crossref_primary_10_1016_j_cherd_2020_12_014 crossref_primary_10_1016_j_cjche_2019_03_025 |
Cites_doi | 10.1002/1522-2640(200011)72:11<1376::AID-CITE1376>3.0.CO;2-C 10.1021/i160021a012 10.5772/24160 10.1016/j.ces.2012.07.035 10.1002/aic.11976 10.1039/b513079d 10.1002/aic.v58.5 10.1002/(ISSN)1547-5905 10.1021/ie000710d 10.1016/j.ces.2009.11.043 10.1039/C4GC00236A 10.1002/cite.330580407 10.1016/j.jct.2015.08.027 10.1016/j.seppur.2016.05.047 10.1016/j.procbio.2010.03.030 |
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SubjectTerms | Chemical engineering Engineering, computing & technology Ingénierie chimique Ingénierie, informatique & technologie mass transfer Room-temperature ionic liquids sedimentation velocity singe-drop experiments |
Title | Performance study of ionic liquid in extraction based on single-drop experiments |
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