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Date de publicationTitreAuteur(s)
2012-09-01Enhancement of Sedimentation Velocity of Heavy Metals Loaded Hydroxyapatite Using Chitosan Extracted from Shrimp WasteLounici, Hakim
1999-02Enhancement of ultrafiltration flux by coupling static turbulence promoter and electric fieldLounici, Hakim
2000-02Enzymatic saccharification of olive mill solid residue in a membrane reactorLounici, Hakim
2000-01Enzymatic saccharification of solid residue of olive mill in a batch reactorLounici, Hakim
2010-02Equilibrium, kinetic and thermodynamic studies on aluminum biosorption by a mycelial biomass (Streptomyces rimosus)Lounici, Hakim
2012Etude de l'adsorption du Nickel par des biosorbantsLounici, Hakim
2011-04-01Evaluating removal of metribuzin pesticide from contaminated groundwater using an electrochemical reactor combined with ultraviolet oxidation DesalinationLounici, Hakim
2011-06Evaluation of crude chitinases extracted from marine biomass (stomach of fishes) on the feed insect: Callosobruchus maculatus (Coléoptera: Bruchidae)Lounici, Hakim
2018Evaluation 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
2016Evaluation of Trivalent and Hexavalent Chromium Retention on Ain Oussera Soil by the Batch Method and Radiotracer Technique.Lounici, Hakim
2019-09-01Experimental versus theoretical study of reverse osmosis pilot scaling: The case of Algerian brackish water desalinationLounici, Hakim
2003-01Filtration of zinc ions utilising pretreated Streptomyces rimosus biomass.Lounici, Hakim
2016First results on biostimulation of denitrifying activated sludge using low frequency ultrasoundLounici, Hakim
2012Fish protein hydrolysate production from sardine solid waste by crude pepsin enzymatic hydrolysis in a bioreactor coupled to an ultrafiltration unitLounici, Hakim
2000-10Flocculation of Latex P articles of Varying Surface Charge Densities by ChitosansLounici, Hakim
2012-01-01Fluoride removal from pretreated photovoltaic wastewater by electrocoagulation:Lounici, Hakim
2004Fluoride removal with electro-activated aluminaLounici, Hakim
2004-03-01Fluoride removal with electro-activated alumina,Lounici, Hakim
2011-01-02GOOSEN Development of an empirical model for fluoride removal from photovoltaic wastewater by a bipolar electrocoagulation process, Desalination and water treatment Desalination and Water TreatmentLounici, Hakim
2018Green hydrogen production by Rhodobacter sphaeroidesLounici, Hakim
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