Mass transfer to volumetric electrodes with two-phase flow
ISSN: |
1572-8838
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Source: |
Springer Online Journal Archives 1860-2000
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Topics: |
Chemistry and Pharmacology
Electrical Engineering, Measurement and Control Technology
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Notes: |
Abstract Experimental studies of mass transfer were conducted in stacked screens with a gas-liquid mixture flowing through the bed. Depending on the gas and liquid flow rates and on the geometric characteristics of the screens, different flow regimes are obtained. In the heterogeneous flow regime the gas phase controls mass transfer, meanwhile in the transition and bubbling flow regimes the influence of the liquid flow prevails. Appropriate dimensionless groups correlate the mass transfer coefficients with the pertinent variables for the different regimes.
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Type of Medium: |
Electronic Resource
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URL: |
_version_ | 1798296400464707585 |
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autor | Coppola, L. Cavatorta, O. N. Böhm, U. |
autorsonst | Coppola, L. Cavatorta, O. N. Böhm, U. |
book_url | http://dx.doi.org/10.1007/BF01039397 |
datenlieferant | nat_lic_papers |
hauptsatz | hsatz_simple |
identnr | NLM193295490 |
issn | 1572-8838 |
journal_name | Journal of applied electrochemistry |
materialart | 1 |
notes | Abstract Experimental studies of mass transfer were conducted in stacked screens with a gas-liquid mixture flowing through the bed. Depending on the gas and liquid flow rates and on the geometric characteristics of the screens, different flow regimes are obtained. In the heterogeneous flow regime the gas phase controls mass transfer, meanwhile in the transition and bubbling flow regimes the influence of the liquid flow prevails. Appropriate dimensionless groups correlate the mass transfer coefficients with the pertinent variables for the different regimes. |
package_name | Springer |
publikationsjahr_anzeige | 1989 |
publikationsjahr_facette | 1989 |
publikationsjahr_intervall | 8014:1985-1989 |
publikationsjahr_sort | 1989 |
publisher | Springer |
reference | 19 (1989), S. 100-104 |
search_space | articles |
shingle_author_1 | Coppola, L. Cavatorta, O. N. Böhm, U. |
shingle_author_2 | Coppola, L. Cavatorta, O. N. Böhm, U. |
shingle_author_3 | Coppola, L. Cavatorta, O. N. Böhm, U. |
shingle_author_4 | Coppola, L. Cavatorta, O. N. Böhm, U. |
shingle_catch_all_1 | Coppola, L. Cavatorta, O. N. Böhm, U. Mass transfer to volumetric electrodes with two-phase flow Abstract Experimental studies of mass transfer were conducted in stacked screens with a gas-liquid mixture flowing through the bed. Depending on the gas and liquid flow rates and on the geometric characteristics of the screens, different flow regimes are obtained. In the heterogeneous flow regime the gas phase controls mass transfer, meanwhile in the transition and bubbling flow regimes the influence of the liquid flow prevails. Appropriate dimensionless groups correlate the mass transfer coefficients with the pertinent variables for the different regimes. 1572-8838 15728838 Springer |
shingle_catch_all_2 | Coppola, L. Cavatorta, O. N. Böhm, U. Mass transfer to volumetric electrodes with two-phase flow Abstract Experimental studies of mass transfer were conducted in stacked screens with a gas-liquid mixture flowing through the bed. Depending on the gas and liquid flow rates and on the geometric characteristics of the screens, different flow regimes are obtained. In the heterogeneous flow regime the gas phase controls mass transfer, meanwhile in the transition and bubbling flow regimes the influence of the liquid flow prevails. Appropriate dimensionless groups correlate the mass transfer coefficients with the pertinent variables for the different regimes. 1572-8838 15728838 Springer |
shingle_catch_all_3 | Coppola, L. Cavatorta, O. N. Böhm, U. Mass transfer to volumetric electrodes with two-phase flow Abstract Experimental studies of mass transfer were conducted in stacked screens with a gas-liquid mixture flowing through the bed. Depending on the gas and liquid flow rates and on the geometric characteristics of the screens, different flow regimes are obtained. In the heterogeneous flow regime the gas phase controls mass transfer, meanwhile in the transition and bubbling flow regimes the influence of the liquid flow prevails. Appropriate dimensionless groups correlate the mass transfer coefficients with the pertinent variables for the different regimes. 1572-8838 15728838 Springer |
shingle_catch_all_4 | Coppola, L. Cavatorta, O. N. Böhm, U. Mass transfer to volumetric electrodes with two-phase flow Abstract Experimental studies of mass transfer were conducted in stacked screens with a gas-liquid mixture flowing through the bed. Depending on the gas and liquid flow rates and on the geometric characteristics of the screens, different flow regimes are obtained. In the heterogeneous flow regime the gas phase controls mass transfer, meanwhile in the transition and bubbling flow regimes the influence of the liquid flow prevails. Appropriate dimensionless groups correlate the mass transfer coefficients with the pertinent variables for the different regimes. 1572-8838 15728838 Springer |
shingle_title_1 | Mass transfer to volumetric electrodes with two-phase flow |
shingle_title_2 | Mass transfer to volumetric electrodes with two-phase flow |
shingle_title_3 | Mass transfer to volumetric electrodes with two-phase flow |
shingle_title_4 | Mass transfer to volumetric electrodes with two-phase flow |
sigel_instance_filter | dkfz geomar wilbert ipn albert fhp |
source_archive | Springer Online Journal Archives 1860-2000 |
timestamp | 2024-05-06T09:51:30.196Z |
titel | Mass transfer to volumetric electrodes with two-phase flow |
titel_suche | Mass transfer to volumetric electrodes with two-phase flow |
topic | V ZN |
uid | nat_lic_papers_NLM193295490 |