Zobrazeno 1 - 8
of 8
pro vyhledávání: '"Lassaad Ben Mansour"'
Autor:
Maroua Mejri, Lassaad ben Mansour
Publikováno v:
Heat and Mass Transfer. 59:131-139
Autor:
Lassaad Ben Mansour, Maroua Mejri
Publikováno v:
Heat and Mass Transfer. 57:1205-1210
The effects of bubble size, solids particle (impurities) and the respective physical mechanisms on gas–liquid columns have received little attention. Therefore, the objective of this work is to study the effect of solid concentration and the ratio
Publikováno v:
Russian Journal of Electrochemistry. 55:358-363
Electroflotation column is preferred in many chemicals, electrochemical and biochemical wastewater process treatment due to their simplicity in design, operation and maintenance. Indeed, it is very important to have a tool to determine and optimize t
Autor:
Lassaad Ben Mansour, Maroua Mejri
Publikováno v:
Heat and Mass Transfer. 55:2235-2245
This work aims to experimentally study the bubble size distribution and the oxygen transfer on the electroflotation process. The distribution of bubbles was measured using a high-speed camera. The measurements were conducted in a three-phase electrof
Autor:
Lassaad Ben Mansour, Maroua Mejri
Publikováno v:
Recent Advances in Environmental Science from the Euro-Mediterranean and Surrounding Regions (2nd Edition) ISBN: 9783030512095
The effects of solids (impurities) on gas–liquid columns and the respective physical mechanisms have received little attention. Therefore, in this study, the effect of the solids concentration on the mass transfer characteristics in a three-phase e
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::fe4c69c3b71a3f66720c0cf4e5c709df
https://doi.org/10.1007/978-3-030-51210-1_32
https://doi.org/10.1007/978-3-030-51210-1_32
Publikováno v:
DESALINATION AND WATER TREATMENT. 132:150-156
Publikováno v:
DESALINATION AND WATER TREATMENT. 98:176-181
Publikováno v:
Journal of Hydrodynamics. 25:747-754
In this work, the effects of the presence of surfactants in the liquid phase and the hydrodynamic regime of the bubble flow on the oxygen transfer rate were investigated in an electroflotation process in batch mode. The volumetric mass transfer coeff