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Montrant les résultats 72 à 91 de 185
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Date de publication
Titre
Auteur(s)
2012-09-01
Enhancement of Sedimentation Velocity of Heavy Metals Loaded Hydroxyapatite Using Chitosan Extracted from Shrimp Waste
Lounici, Hakim
1999-02
Enhancement of ultrafiltration flux by coupling static turbulence promoter and electric field
Lounici, Hakim
2000-02
Enzymatic saccharification of olive mill solid residue in a membrane reactor
Lounici, Hakim
2000-01
Enzymatic saccharification of solid residue of olive mill in a batch reactor
Lounici, Hakim
2010-02
Equilibrium, kinetic and thermodynamic studies on aluminum biosorption by a mycelial biomass (Streptomyces rimosus)
Lounici, Hakim
2012
Etude de l'adsorption du Nickel par des biosorbants
Lounici, Hakim
2011-04-01
Evaluating removal of metribuzin pesticide from contaminated groundwater using an electrochemical reactor combined with ultraviolet oxidation Desalination
Lounici, Hakim
2011-06
Evaluation of crude chitinases extracted from marine biomass (stomach of fishes) on the feed insect: Callosobruchus maculatus (Coléoptera: Bruchidae)
Lounici, Hakim
2018
Evaluation of the robustness of the enzymatic hydrolysis in batch and continuous mode by a central composite design Authors N Abdi, O Kitous, H Grib, M Drouiche, H Lounici, N Drouiche, N Mameri Publication date 2018/1 Journal Journal of Food Processing and Preservation Volume 42 Issue 1 Pages e13330 Description The main purpose of this work is to study the ability of the enzymatic reaction. For the performance of the experiment, it is desirable to control variations so that they are minimized to the maximum extend and therefore an optimum operating point can be maintained. To achieve this target, the central composite design takes into account all interaction effects that may be useful for creating a mathematical model in agreement with the validity criteria. The model showed to be more suitable for the saccharification experiments in batch mode than in continuous mode. In batch mode, a correlation coefficient close to unity (R2 = .98) was obtained. Moreover, the resulting mathematical model was satisfactory in accordance with the validation criteria. For continuous mode, the coefficient value obtained was R2 = .83 indicating that the model to study the ability of the enzymatic reaction was inferior than the batch mode …
Lounici, Hakim
2016
Evaluation of Trivalent and Hexavalent Chromium Retention on Ain Oussera Soil by the Batch Method and Radiotracer Technique.
Lounici, Hakim
2019-09-01
Experimental versus theoretical study of reverse osmosis pilot scaling: The case of Algerian brackish water desalination
Lounici, Hakim
2003-01
Filtration of zinc ions utilising pretreated Streptomyces rimosus biomass.
Lounici, Hakim
2016
First results on biostimulation of denitrifying activated sludge using low frequency ultrasound
Lounici, Hakim
2012
Fish protein hydrolysate production from sardine solid waste by crude pepsin enzymatic hydrolysis in a bioreactor coupled to an ultrafiltration unit
Lounici, Hakim
2000-10
Flocculation of Latex P articles of Varying Surface Charge Densities by Chitosans
Lounici, Hakim
2012-01-01
Fluoride removal from pretreated photovoltaic wastewater by electrocoagulation:
Lounici, Hakim
2004
Fluoride removal with electro-activated alumina
Lounici, Hakim
2004-03-01
Fluoride removal with electro-activated alumina,
Lounici, Hakim
2011-01-02
GOOSEN Development of an empirical model for fluoride removal from photovoltaic wastewater by a bipolar electrocoagulation process, Desalination and water treatment Desalination and Water Treatment
Lounici, Hakim
2018
Green hydrogen production by Rhodobacter sphaeroides
Lounici, Hakim