Separation of mercury and arsenic from produced water via hollow fiber contactor: Kinetic and mass transfer analysis
Abstract The separation of Hg(II) and As(V) from produced water by hollow fiber contactors was investigated. Two identical hollow fiber modules were employed. The first module was used for extraction, while the second module was used for stripping. The optimum conditions achieved were 14% (v/v) of A...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Sribudda, Dolapop [verfasserIn] |
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| Format: |
Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2015 |
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| Schlagwörter: |
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| Anmerkung: |
© Korean Institute of Chemical Engineers, Seoul, Korea 2016 |
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| Übergeordnetes Werk: |
Enthalten in: The Korean journal of chemical engineering - Springer US, 1984, 33(2015), 1 vom: 14. Sept., Seite 197-206 |
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| Übergeordnetes Werk: |
volume:33 ; year:2015 ; number:1 ; day:14 ; month:09 ; pages:197-206 |
| Links: |
|---|
| DOI / URN: |
10.1007/s11814-015-0130-y |
|---|
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OLC2063033536 |
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| 520 | |a Abstract The separation of Hg(II) and As(V) from produced water by hollow fiber contactors was investigated. Two identical hollow fiber modules were employed. The first module was used for extraction, while the second module was used for stripping. The optimum conditions achieved were 14% (v/v) of Aliquat336, 0.07 M thiourea, volumetric flow rate of 100 mL/min for aqueous solution and 0.02 M HCl of stripping solution. At such conditions, the maximum extraction of Hg(II) and As(V) attained 100% and 78.78%, respectively. Concurrently, the maximum stripping of Hg(II) and As(V) reached 47.88% and 6.66%, respectively. The overall mass transfer coefficients of Hg(II) and As(V) extraction were 2.31×$ 10^{−6} $ and 1.15×$ 10^{−6} $m/s, while the Hg(II) and As(V) stripping exhibited the overall mass transfer coefficients of 8.37×$ 10^{−7} $ m/s and 9.05×$ 10^{−7} $ m/s, respectively. Mass transfer coefficients of the organic layer diffusion ($ k_{0} $) had the most effect on the overall mass transfer coefficients. | ||
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10.1007/s11814-015-0130-y doi (DE-627)OLC2063033536 (DE-He213)s11814-015-0130-y-p DE-627 ger DE-627 rakwb eng 660 VZ 58.00 bkl Sribudda, Dolapop verfasserin aut Separation of mercury and arsenic from produced water via hollow fiber contactor: Kinetic and mass transfer analysis 2015 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Korean Institute of Chemical Engineers, Seoul, Korea 2016 Abstract The separation of Hg(II) and As(V) from produced water by hollow fiber contactors was investigated. Two identical hollow fiber modules were employed. The first module was used for extraction, while the second module was used for stripping. The optimum conditions achieved were 14% (v/v) of Aliquat336, 0.07 M thiourea, volumetric flow rate of 100 mL/min for aqueous solution and 0.02 M HCl of stripping solution. At such conditions, the maximum extraction of Hg(II) and As(V) attained 100% and 78.78%, respectively. Concurrently, the maximum stripping of Hg(II) and As(V) reached 47.88% and 6.66%, respectively. The overall mass transfer coefficients of Hg(II) and As(V) extraction were 2.31×$ 10^{−6} $ and 1.15×$ 10^{−6} $m/s, while the Hg(II) and As(V) stripping exhibited the overall mass transfer coefficients of 8.37×$ 10^{−7} $ m/s and 9.05×$ 10^{−7} $ m/s, respectively. Mass transfer coefficients of the organic layer diffusion ($ k_{0} $) had the most effect on the overall mass transfer coefficients. Hg(II) As(V) Hollow Fiber Contactor Mass Transfer Coefficients Kinetic Wannachod, Thanaporn aut Ramakul, Prakorn aut Pancharoen, Ura aut Phatanasri, Suphot aut Enthalten in The Korean journal of chemical engineering Springer US, 1984 33(2015), 1 vom: 14. Sept., Seite 197-206 (DE-627)129165409 (DE-600)50398-8 (DE-576)099445263 0256-1115 nnns volume:33 year:2015 number:1 day:14 month:09 pages:197-206 https://doi.org/10.1007/s11814-015-0130-y lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 58.00 VZ AR 33 2015 1 14 09 197-206 |
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10.1007/s11814-015-0130-y doi (DE-627)OLC2063033536 (DE-He213)s11814-015-0130-y-p DE-627 ger DE-627 rakwb eng 660 VZ 58.00 bkl Sribudda, Dolapop verfasserin aut Separation of mercury and arsenic from produced water via hollow fiber contactor: Kinetic and mass transfer analysis 2015 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Korean Institute of Chemical Engineers, Seoul, Korea 2016 Abstract The separation of Hg(II) and As(V) from produced water by hollow fiber contactors was investigated. Two identical hollow fiber modules were employed. The first module was used for extraction, while the second module was used for stripping. The optimum conditions achieved were 14% (v/v) of Aliquat336, 0.07 M thiourea, volumetric flow rate of 100 mL/min for aqueous solution and 0.02 M HCl of stripping solution. At such conditions, the maximum extraction of Hg(II) and As(V) attained 100% and 78.78%, respectively. Concurrently, the maximum stripping of Hg(II) and As(V) reached 47.88% and 6.66%, respectively. The overall mass transfer coefficients of Hg(II) and As(V) extraction were 2.31×$ 10^{−6} $ and 1.15×$ 10^{−6} $m/s, while the Hg(II) and As(V) stripping exhibited the overall mass transfer coefficients of 8.37×$ 10^{−7} $ m/s and 9.05×$ 10^{−7} $ m/s, respectively. Mass transfer coefficients of the organic layer diffusion ($ k_{0} $) had the most effect on the overall mass transfer coefficients. Hg(II) As(V) Hollow Fiber Contactor Mass Transfer Coefficients Kinetic Wannachod, Thanaporn aut Ramakul, Prakorn aut Pancharoen, Ura aut Phatanasri, Suphot aut Enthalten in The Korean journal of chemical engineering Springer US, 1984 33(2015), 1 vom: 14. Sept., Seite 197-206 (DE-627)129165409 (DE-600)50398-8 (DE-576)099445263 0256-1115 nnns volume:33 year:2015 number:1 day:14 month:09 pages:197-206 https://doi.org/10.1007/s11814-015-0130-y lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 58.00 VZ AR 33 2015 1 14 09 197-206 |
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10.1007/s11814-015-0130-y doi (DE-627)OLC2063033536 (DE-He213)s11814-015-0130-y-p DE-627 ger DE-627 rakwb eng 660 VZ 58.00 bkl Sribudda, Dolapop verfasserin aut Separation of mercury and arsenic from produced water via hollow fiber contactor: Kinetic and mass transfer analysis 2015 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Korean Institute of Chemical Engineers, Seoul, Korea 2016 Abstract The separation of Hg(II) and As(V) from produced water by hollow fiber contactors was investigated. Two identical hollow fiber modules were employed. The first module was used for extraction, while the second module was used for stripping. The optimum conditions achieved were 14% (v/v) of Aliquat336, 0.07 M thiourea, volumetric flow rate of 100 mL/min for aqueous solution and 0.02 M HCl of stripping solution. At such conditions, the maximum extraction of Hg(II) and As(V) attained 100% and 78.78%, respectively. Concurrently, the maximum stripping of Hg(II) and As(V) reached 47.88% and 6.66%, respectively. The overall mass transfer coefficients of Hg(II) and As(V) extraction were 2.31×$ 10^{−6} $ and 1.15×$ 10^{−6} $m/s, while the Hg(II) and As(V) stripping exhibited the overall mass transfer coefficients of 8.37×$ 10^{−7} $ m/s and 9.05×$ 10^{−7} $ m/s, respectively. Mass transfer coefficients of the organic layer diffusion ($ k_{0} $) had the most effect on the overall mass transfer coefficients. Hg(II) As(V) Hollow Fiber Contactor Mass Transfer Coefficients Kinetic Wannachod, Thanaporn aut Ramakul, Prakorn aut Pancharoen, Ura aut Phatanasri, Suphot aut Enthalten in The Korean journal of chemical engineering Springer US, 1984 33(2015), 1 vom: 14. Sept., Seite 197-206 (DE-627)129165409 (DE-600)50398-8 (DE-576)099445263 0256-1115 nnns volume:33 year:2015 number:1 day:14 month:09 pages:197-206 https://doi.org/10.1007/s11814-015-0130-y lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 58.00 VZ AR 33 2015 1 14 09 197-206 |
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10.1007/s11814-015-0130-y doi (DE-627)OLC2063033536 (DE-He213)s11814-015-0130-y-p DE-627 ger DE-627 rakwb eng 660 VZ 58.00 bkl Sribudda, Dolapop verfasserin aut Separation of mercury and arsenic from produced water via hollow fiber contactor: Kinetic and mass transfer analysis 2015 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Korean Institute of Chemical Engineers, Seoul, Korea 2016 Abstract The separation of Hg(II) and As(V) from produced water by hollow fiber contactors was investigated. Two identical hollow fiber modules were employed. The first module was used for extraction, while the second module was used for stripping. The optimum conditions achieved were 14% (v/v) of Aliquat336, 0.07 M thiourea, volumetric flow rate of 100 mL/min for aqueous solution and 0.02 M HCl of stripping solution. At such conditions, the maximum extraction of Hg(II) and As(V) attained 100% and 78.78%, respectively. Concurrently, the maximum stripping of Hg(II) and As(V) reached 47.88% and 6.66%, respectively. The overall mass transfer coefficients of Hg(II) and As(V) extraction were 2.31×$ 10^{−6} $ and 1.15×$ 10^{−6} $m/s, while the Hg(II) and As(V) stripping exhibited the overall mass transfer coefficients of 8.37×$ 10^{−7} $ m/s and 9.05×$ 10^{−7} $ m/s, respectively. Mass transfer coefficients of the organic layer diffusion ($ k_{0} $) had the most effect on the overall mass transfer coefficients. Hg(II) As(V) Hollow Fiber Contactor Mass Transfer Coefficients Kinetic Wannachod, Thanaporn aut Ramakul, Prakorn aut Pancharoen, Ura aut Phatanasri, Suphot aut Enthalten in The Korean journal of chemical engineering Springer US, 1984 33(2015), 1 vom: 14. Sept., Seite 197-206 (DE-627)129165409 (DE-600)50398-8 (DE-576)099445263 0256-1115 nnns volume:33 year:2015 number:1 day:14 month:09 pages:197-206 https://doi.org/10.1007/s11814-015-0130-y lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 58.00 VZ AR 33 2015 1 14 09 197-206 |
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10.1007/s11814-015-0130-y doi (DE-627)OLC2063033536 (DE-He213)s11814-015-0130-y-p DE-627 ger DE-627 rakwb eng 660 VZ 58.00 bkl Sribudda, Dolapop verfasserin aut Separation of mercury and arsenic from produced water via hollow fiber contactor: Kinetic and mass transfer analysis 2015 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Korean Institute of Chemical Engineers, Seoul, Korea 2016 Abstract The separation of Hg(II) and As(V) from produced water by hollow fiber contactors was investigated. Two identical hollow fiber modules were employed. The first module was used for extraction, while the second module was used for stripping. The optimum conditions achieved were 14% (v/v) of Aliquat336, 0.07 M thiourea, volumetric flow rate of 100 mL/min for aqueous solution and 0.02 M HCl of stripping solution. At such conditions, the maximum extraction of Hg(II) and As(V) attained 100% and 78.78%, respectively. Concurrently, the maximum stripping of Hg(II) and As(V) reached 47.88% and 6.66%, respectively. The overall mass transfer coefficients of Hg(II) and As(V) extraction were 2.31×$ 10^{−6} $ and 1.15×$ 10^{−6} $m/s, while the Hg(II) and As(V) stripping exhibited the overall mass transfer coefficients of 8.37×$ 10^{−7} $ m/s and 9.05×$ 10^{−7} $ m/s, respectively. Mass transfer coefficients of the organic layer diffusion ($ k_{0} $) had the most effect on the overall mass transfer coefficients. Hg(II) As(V) Hollow Fiber Contactor Mass Transfer Coefficients Kinetic Wannachod, Thanaporn aut Ramakul, Prakorn aut Pancharoen, Ura aut Phatanasri, Suphot aut Enthalten in The Korean journal of chemical engineering Springer US, 1984 33(2015), 1 vom: 14. Sept., Seite 197-206 (DE-627)129165409 (DE-600)50398-8 (DE-576)099445263 0256-1115 nnns volume:33 year:2015 number:1 day:14 month:09 pages:197-206 https://doi.org/10.1007/s11814-015-0130-y lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 58.00 VZ AR 33 2015 1 14 09 197-206 |
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Separation of mercury and arsenic from produced water via hollow fiber contactor: Kinetic and mass transfer analysis |
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Separation of mercury and arsenic from produced water via hollow fiber contactor: Kinetic and mass transfer analysis |
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Sribudda, Dolapop |
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The Korean journal of chemical engineering |
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Sribudda, Dolapop Wannachod, Thanaporn Ramakul, Prakorn Pancharoen, Ura Phatanasri, Suphot |
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separation of mercury and arsenic from produced water via hollow fiber contactor: kinetic and mass transfer analysis |
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Separation of mercury and arsenic from produced water via hollow fiber contactor: Kinetic and mass transfer analysis |
| abstract |
Abstract The separation of Hg(II) and As(V) from produced water by hollow fiber contactors was investigated. Two identical hollow fiber modules were employed. The first module was used for extraction, while the second module was used for stripping. The optimum conditions achieved were 14% (v/v) of Aliquat336, 0.07 M thiourea, volumetric flow rate of 100 mL/min for aqueous solution and 0.02 M HCl of stripping solution. At such conditions, the maximum extraction of Hg(II) and As(V) attained 100% and 78.78%, respectively. Concurrently, the maximum stripping of Hg(II) and As(V) reached 47.88% and 6.66%, respectively. The overall mass transfer coefficients of Hg(II) and As(V) extraction were 2.31×$ 10^{−6} $ and 1.15×$ 10^{−6} $m/s, while the Hg(II) and As(V) stripping exhibited the overall mass transfer coefficients of 8.37×$ 10^{−7} $ m/s and 9.05×$ 10^{−7} $ m/s, respectively. Mass transfer coefficients of the organic layer diffusion ($ k_{0} $) had the most effect on the overall mass transfer coefficients. © Korean Institute of Chemical Engineers, Seoul, Korea 2016 |
| abstractGer |
Abstract The separation of Hg(II) and As(V) from produced water by hollow fiber contactors was investigated. Two identical hollow fiber modules were employed. The first module was used for extraction, while the second module was used for stripping. The optimum conditions achieved were 14% (v/v) of Aliquat336, 0.07 M thiourea, volumetric flow rate of 100 mL/min for aqueous solution and 0.02 M HCl of stripping solution. At such conditions, the maximum extraction of Hg(II) and As(V) attained 100% and 78.78%, respectively. Concurrently, the maximum stripping of Hg(II) and As(V) reached 47.88% and 6.66%, respectively. The overall mass transfer coefficients of Hg(II) and As(V) extraction were 2.31×$ 10^{−6} $ and 1.15×$ 10^{−6} $m/s, while the Hg(II) and As(V) stripping exhibited the overall mass transfer coefficients of 8.37×$ 10^{−7} $ m/s and 9.05×$ 10^{−7} $ m/s, respectively. Mass transfer coefficients of the organic layer diffusion ($ k_{0} $) had the most effect on the overall mass transfer coefficients. © Korean Institute of Chemical Engineers, Seoul, Korea 2016 |
| abstract_unstemmed |
Abstract The separation of Hg(II) and As(V) from produced water by hollow fiber contactors was investigated. Two identical hollow fiber modules were employed. The first module was used for extraction, while the second module was used for stripping. The optimum conditions achieved were 14% (v/v) of Aliquat336, 0.07 M thiourea, volumetric flow rate of 100 mL/min for aqueous solution and 0.02 M HCl of stripping solution. At such conditions, the maximum extraction of Hg(II) and As(V) attained 100% and 78.78%, respectively. Concurrently, the maximum stripping of Hg(II) and As(V) reached 47.88% and 6.66%, respectively. The overall mass transfer coefficients of Hg(II) and As(V) extraction were 2.31×$ 10^{−6} $ and 1.15×$ 10^{−6} $m/s, while the Hg(II) and As(V) stripping exhibited the overall mass transfer coefficients of 8.37×$ 10^{−7} $ m/s and 9.05×$ 10^{−7} $ m/s, respectively. Mass transfer coefficients of the organic layer diffusion ($ k_{0} $) had the most effect on the overall mass transfer coefficients. © Korean Institute of Chemical Engineers, Seoul, Korea 2016 |
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