Mass transfer and liquid mixing in an airlift reactor with a net draft tube
Abstract Mass transfer and liquid mixing in an airlift reactor with a net draft tube were experimentally investigated. Four different column diameters were considered. The mass transfer was measured using the volumetric gas-liquid mass transfer coefficient which was determined by the dynamic method....
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Hsiun, D. -Y. [verfasserIn] |
|---|
| Format: |
Artikel |
|---|---|
| Sprache: |
Englisch |
| Erschienen: |
1995 |
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| Schlagwörter: |
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| Anmerkung: |
© Springer-Verlag 1995 |
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| Übergeordnetes Werk: |
Enthalten in: Bioprocess engineering - Springer-Verlag, 1986, 12(1995), 5 vom: Apr., Seite 221-225 |
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| Übergeordnetes Werk: |
volume:12 ; year:1995 ; number:5 ; month:04 ; pages:221-225 |
| Links: |
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| DOI / URN: |
10.1007/BF00369494 |
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OLC2106599013 |
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| 520 | |a Abstract Mass transfer and liquid mixing in an airlift reactor with a net draft tube were experimentally investigated. Four different column diameters were considered. The mass transfer was measured using the volumetric gas-liquid mass transfer coefficient which was determined by the dynamic method. The mass transfer coefficients in the airlift reactors with different column diameters were not always higher than those in the bubble columns. The liquid mixing was measured using mixing time which was determined by a pulse technique. Under the same superficial gas velocity, the mixing times of the airlift reactors with a net draft tube were always less than those of the bubble columns. | ||
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10.1007/BF00369494 doi (DE-627)OLC2106599013 (DE-He213)BF00369494-p DE-627 ger DE-627 rakwb eng 570 690 540 VZ 12 ssgn Hsiun, D. -Y. verfasserin aut Mass transfer and liquid mixing in an airlift reactor with a net draft tube 1995 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Springer-Verlag 1995 Abstract Mass transfer and liquid mixing in an airlift reactor with a net draft tube were experimentally investigated. Four different column diameters were considered. The mass transfer was measured using the volumetric gas-liquid mass transfer coefficient which was determined by the dynamic method. The mass transfer coefficients in the airlift reactors with different column diameters were not always higher than those in the bubble columns. The liquid mixing was measured using mixing time which was determined by a pulse technique. Under the same superficial gas velocity, the mixing times of the airlift reactors with a net draft tube were always less than those of the bubble columns. Waste Water Mass Transfer Water Management Water Pollution Mass Transfer Coefficient Wu, W. -T. aut Enthalten in Bioprocess engineering Springer-Verlag, 1986 12(1995), 5 vom: Apr., Seite 221-225 (DE-627)129208922 (DE-600)55154-5 (DE-576)01445761X 0178-515X nnns volume:12 year:1995 number:5 month:04 pages:221-225 https://doi.org/10.1007/BF00369494 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-CHE GBV_ILN_11 GBV_ILN_23 GBV_ILN_32 GBV_ILN_40 GBV_ILN_65 GBV_ILN_70 GBV_ILN_2006 GBV_ILN_2018 GBV_ILN_4046 GBV_ILN_4277 GBV_ILN_4307 GBV_ILN_4310 GBV_ILN_4328 AR 12 1995 5 04 221-225 |
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10.1007/BF00369494 doi (DE-627)OLC2106599013 (DE-He213)BF00369494-p DE-627 ger DE-627 rakwb eng 570 690 540 VZ 12 ssgn Hsiun, D. -Y. verfasserin aut Mass transfer and liquid mixing in an airlift reactor with a net draft tube 1995 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Springer-Verlag 1995 Abstract Mass transfer and liquid mixing in an airlift reactor with a net draft tube were experimentally investigated. Four different column diameters were considered. The mass transfer was measured using the volumetric gas-liquid mass transfer coefficient which was determined by the dynamic method. The mass transfer coefficients in the airlift reactors with different column diameters were not always higher than those in the bubble columns. The liquid mixing was measured using mixing time which was determined by a pulse technique. Under the same superficial gas velocity, the mixing times of the airlift reactors with a net draft tube were always less than those of the bubble columns. Waste Water Mass Transfer Water Management Water Pollution Mass Transfer Coefficient Wu, W. -T. aut Enthalten in Bioprocess engineering Springer-Verlag, 1986 12(1995), 5 vom: Apr., Seite 221-225 (DE-627)129208922 (DE-600)55154-5 (DE-576)01445761X 0178-515X nnns volume:12 year:1995 number:5 month:04 pages:221-225 https://doi.org/10.1007/BF00369494 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-CHE GBV_ILN_11 GBV_ILN_23 GBV_ILN_32 GBV_ILN_40 GBV_ILN_65 GBV_ILN_70 GBV_ILN_2006 GBV_ILN_2018 GBV_ILN_4046 GBV_ILN_4277 GBV_ILN_4307 GBV_ILN_4310 GBV_ILN_4328 AR 12 1995 5 04 221-225 |
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10.1007/BF00369494 doi (DE-627)OLC2106599013 (DE-He213)BF00369494-p DE-627 ger DE-627 rakwb eng 570 690 540 VZ 12 ssgn Hsiun, D. -Y. verfasserin aut Mass transfer and liquid mixing in an airlift reactor with a net draft tube 1995 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Springer-Verlag 1995 Abstract Mass transfer and liquid mixing in an airlift reactor with a net draft tube were experimentally investigated. Four different column diameters were considered. The mass transfer was measured using the volumetric gas-liquid mass transfer coefficient which was determined by the dynamic method. The mass transfer coefficients in the airlift reactors with different column diameters were not always higher than those in the bubble columns. The liquid mixing was measured using mixing time which was determined by a pulse technique. Under the same superficial gas velocity, the mixing times of the airlift reactors with a net draft tube were always less than those of the bubble columns. Waste Water Mass Transfer Water Management Water Pollution Mass Transfer Coefficient Wu, W. -T. aut Enthalten in Bioprocess engineering Springer-Verlag, 1986 12(1995), 5 vom: Apr., Seite 221-225 (DE-627)129208922 (DE-600)55154-5 (DE-576)01445761X 0178-515X nnns volume:12 year:1995 number:5 month:04 pages:221-225 https://doi.org/10.1007/BF00369494 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-CHE GBV_ILN_11 GBV_ILN_23 GBV_ILN_32 GBV_ILN_40 GBV_ILN_65 GBV_ILN_70 GBV_ILN_2006 GBV_ILN_2018 GBV_ILN_4046 GBV_ILN_4277 GBV_ILN_4307 GBV_ILN_4310 GBV_ILN_4328 AR 12 1995 5 04 221-225 |
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10.1007/BF00369494 doi (DE-627)OLC2106599013 (DE-He213)BF00369494-p DE-627 ger DE-627 rakwb eng 570 690 540 VZ 12 ssgn Hsiun, D. -Y. verfasserin aut Mass transfer and liquid mixing in an airlift reactor with a net draft tube 1995 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Springer-Verlag 1995 Abstract Mass transfer and liquid mixing in an airlift reactor with a net draft tube were experimentally investigated. Four different column diameters were considered. The mass transfer was measured using the volumetric gas-liquid mass transfer coefficient which was determined by the dynamic method. The mass transfer coefficients in the airlift reactors with different column diameters were not always higher than those in the bubble columns. The liquid mixing was measured using mixing time which was determined by a pulse technique. Under the same superficial gas velocity, the mixing times of the airlift reactors with a net draft tube were always less than those of the bubble columns. Waste Water Mass Transfer Water Management Water Pollution Mass Transfer Coefficient Wu, W. -T. aut Enthalten in Bioprocess engineering Springer-Verlag, 1986 12(1995), 5 vom: Apr., Seite 221-225 (DE-627)129208922 (DE-600)55154-5 (DE-576)01445761X 0178-515X nnns volume:12 year:1995 number:5 month:04 pages:221-225 https://doi.org/10.1007/BF00369494 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-CHE GBV_ILN_11 GBV_ILN_23 GBV_ILN_32 GBV_ILN_40 GBV_ILN_65 GBV_ILN_70 GBV_ILN_2006 GBV_ILN_2018 GBV_ILN_4046 GBV_ILN_4277 GBV_ILN_4307 GBV_ILN_4310 GBV_ILN_4328 AR 12 1995 5 04 221-225 |
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Mass transfer and liquid mixing in an airlift reactor with a net draft tube |
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Abstract Mass transfer and liquid mixing in an airlift reactor with a net draft tube were experimentally investigated. Four different column diameters were considered. The mass transfer was measured using the volumetric gas-liquid mass transfer coefficient which was determined by the dynamic method. The mass transfer coefficients in the airlift reactors with different column diameters were not always higher than those in the bubble columns. The liquid mixing was measured using mixing time which was determined by a pulse technique. Under the same superficial gas velocity, the mixing times of the airlift reactors with a net draft tube were always less than those of the bubble columns. © Springer-Verlag 1995 |
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Abstract Mass transfer and liquid mixing in an airlift reactor with a net draft tube were experimentally investigated. Four different column diameters were considered. The mass transfer was measured using the volumetric gas-liquid mass transfer coefficient which was determined by the dynamic method. The mass transfer coefficients in the airlift reactors with different column diameters were not always higher than those in the bubble columns. The liquid mixing was measured using mixing time which was determined by a pulse technique. Under the same superficial gas velocity, the mixing times of the airlift reactors with a net draft tube were always less than those of the bubble columns. © Springer-Verlag 1995 |
| abstract_unstemmed |
Abstract Mass transfer and liquid mixing in an airlift reactor with a net draft tube were experimentally investigated. Four different column diameters were considered. The mass transfer was measured using the volumetric gas-liquid mass transfer coefficient which was determined by the dynamic method. The mass transfer coefficients in the airlift reactors with different column diameters were not always higher than those in the bubble columns. The liquid mixing was measured using mixing time which was determined by a pulse technique. Under the same superficial gas velocity, the mixing times of the airlift reactors with a net draft tube were always less than those of the bubble columns. © Springer-Verlag 1995 |
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Mass transfer and liquid mixing in an airlift reactor with a net draft tube |
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