Mass transfer to volumetric electrodes with two-phase flow

Coppola, L. ; Cavatorta, O. N. ; Böhm, U.
Springer
Published 1989
ISSN:
1572-8838
Source:
Springer Online Journal Archives 1860-2000
Topics:
Chemistry and Pharmacology
Electrical Engineering, Measurement and Control Technology
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.
Type of Medium:
Electronic Resource
URL:
_version_ 1798296400464707585
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
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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
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