Brahim Arhoun

Brahim Arhoun

*This is an algorithmically generated author record based on publicly available information.

Current Organizations / Institutes

The organizations/institutes from the scholar's latest article

Previous Organizations / Institutes

The organizations / institutes from the scholar's other articles in the past ten years


Brahim Arhoun has a total of 17 co-authors. Here are the top co-authors by number of shared publications:


Latest Publications

  • Open Access

    Electrochemical treatment of landfill leachate

    by Brahim Arhoun, Maria Villen-Guzman, Jose Miguel Rodriguez-Maroto, Juan Manuel Paz-Garcia

    A significant municipal solid waste is managed by disposition in a landfill. This kind of management system makes producing leachate with toxic characteristics


  • Open Access

    Separation treatment of landfill leachate

    by Brahim Arhoun, Juan Manuel Paz-Garcia, Jose Miguel Rodriguez-Maroto, Maria Villen-Guzman

    Landfilling municipal waste is the most common way to manage waste in the world. An important problem associated with landfills is the production of leachates. Landfill leachate is heterogeneous wastewater and often possesses potential pollution with high concentrations of organic and inorganic contaminants. The generated leachate must be appropriately collected and treated before being discharged into the environment. Several technologies have been used for leachate treatment which can be classified as biological, chemical, and physical processes. Among physical processes, membrane separation including microfiltration, ultrafiltration, nanofiltration, and reverse osmosis has been used for landfill leachate treatment. However, single-membrane processes are not very effective unless they are combined with biological and physicochemical treatment processes. This is because membrane separation presents two main drawbacks: membrane concentrates (MCs) and fouling. Here, we briefly review the main processes currently used for MC treatment. Finally, the fouling membrane is also discussed.


  • Effect of pretreatment and co‐substrate addition on biogas production from pig slurry

    by Brahim Arhoun, Irene Malpartida García, Maria Villen‐Guzman, Roberto Teofilo Abdala Diaz, Francisco Garcia‐Herruzo, Jose Miguel Rodriguez‐Maroto

    The anaerobic digestion of pig slurry samples collected from different points of a farm and raw pig slurry pretreated by centrifugation and decantation was first studied. The specific methane production of raw pig slurry and after centrifugation and decantation pretreatment was 158, 24 and 42.34 L kgVS−1, respectively. Second, the anaerobic digestion of the mixture of raw pig slurry and decanted solid fraction at different organic loading rate (1.364–3.41 gVS·L−1·d−1) results in a specific methane production of 249 ± 37·L kgVS −1. The concentration of ammonium ion in the digester increased to 2500 mg L−1 without inhibition. Lastly, the co‐digestion of pear waste and raw pig slurry was also analysed, which enhanced the specific methane production (243 L kgVS−1). This work deals with the integral management of pig slurry and points out the possibility of revalorization of other wastes in the same digester.


  • Open Access

    Chemical Reduction of Nitrate by Zero-Valent Iron: Shrinking-Core versus Surface Kinetics Models

    by Maria Villen-Guzman, Juan Manuel Paz-Garcia, Brahim Arhoun, Maria del Mar Cerrillo-Gonzalez, Jose Miguel Rodriguez-Maroto, Carlos Vereda-Alonso, Cesar Gomez-Lahoz

    Zero valent iron (ZVI) is being used in permeable reactive barriers (PRB) for the removal of oxidant contaminants, from nitrate to chlorinated organics. A sound design of these barriers requires a good understanding of kinetics. Here we present a study of the kinetics of nitrate reduction under relatively low values of pH, from 2 to 4.5. We use a particle size of 0.42 mm, which is within the recommended size for PRBs (0.2 mm to 2.0 mm). In order to avoid possible mass-transfer limitations, a well-stirred reactor coupled with a fluidized bed reactor was used. The experiments were performed at constant pH values using a pH controller that allows to accurately track the amount of acid added. Since the reduction of H + to H 2 by the oxidation of ZVI will always be present for these pH values, blank experiments (without nitrate) were performed and the rate of this H + reduction obtained. This rate of reduction was studied using three kinetic models: a regular empirical one, the Shrinking-Core Model (SCM), and the Surface Kinetics Model (SKM). The best performance was obtained from the SKM model. Therefore, this model was also used to study the results for the nitrate reduction, also with satisfactory results. In both cases, some assumptions are introduced to maintain a moderate number of fitting parameters.


  • Anaerobic co-digestion of municipal sewage sludge and fruit/vegetable waste: effect of different mixtures on digester stability and methane yield

    by Brahim Arhoun, Maria D. Villen-Guzman, Carlos Vereda-Alonso, José Miguel Rodriguez-Maroto, Francisco Garcia-Herruzo, César Gómez-Lahoz

    The anaerobic co-digestion of fruit and vegetable waste (FVW) and municipal sewage sludge (MSS) is investigated under mesophilic conditions. This was done at a constant hydraulic retention time (HRT) similar to that typically used at waste water treatment plant digesters, 20 days. The effects on digester performance of the FVW:MSS ratio and the organic loading rate (OLR) were examined. Initially the digester was fed with MSS from wastewater treatment plants (WWTP) with an average OLR of 1.03 kgVS (m3 d)−1. The co-digestion of MSS and FVW was performed at various ratios of FVW in the mixture, while increasing the OLRs, from 1.03 to 4.78 kgVS (m3 d)−1. The experimental specific methane production (SMP) was 0.303 m3 (kgVS)−1 for MSS and 0.403 m3 (kgVS)−1 for FVW as single substrate. This value varied for co-digestion with a maximum of 0.445 m3 (kgVS)−1 for a FVW:MSS ratio of 40:60. Alkalinity and pH values remain relatively constant regardless the different FVW:MSS ratios fed. As this ratio increases, the removal of the volatile solids (VS) increased from 38.7% to 82%. The average methane content of digester biogas was about 62–64%.


  • Open Access

    Electrodialytic processes in solid matrices. New insights into battery recycling. A review

    by Maria Villen‐Guzman, Brahim Arhoun, Carlos Vereda‐Alonso, Cesar Gomez‐Lahoz, Jose M. Rodriguez‐Maroto, Juan M. Paz‐Garcia

    Electrodialytic remediation has been widely applied to the recovery of different contaminants from numerous solid matrices, solving emerging issues of environmental concern. Results and conclusions reported in studies about real contaminated matrices are summarized in this work. The influence of pH value on the treatment effectiveness has been widely proved, highlighting the phenomenon of ‘water splitting’ in the membrane surface. This dissociation of water molecules is related to the ‘limiting current’ which it is desirable to exceed at the anion exchange membrane in order to produce the entering of protons toward the solid matrix. Other important parameters for the optimization of the technique, such as the current density and the liquid/solid ratio, are also discussed through the revision of studies using real solid matrices.This work also focuses on the pioneer proposal of electrokinetic technologies for the recycling of lithium ion batteries, considering the relevance of waste properties in the design and optimization of the technique. From a thorough literature revision, it could be concluded that further experimental results are needed to allow an optimal application of the technique to the rising problem of residues from batteries. The main aim of this work is to take the first steps in the recovery of valuable metals such as Li and Co from spent batteries, incorporating principles of green chemistry. © 2019 Society of Chemical Industry


  • Immobilization of Brown Seaweeds Sargassum vulgare for Fe3+ Removal in Batch and Fixed-Bed Column

    by Souad Benaisa, Brahim Arhoun, Maria Villen-Guzman, Rachad El Mail, Jose Miguel Rodriguez-Maroto


  • Production of biogas from co-digestion of livestock and agricultural residues: A case study

    by Brahim Arhoun, Cesar Gomez-Lahoz, Roberto Teofilo Abdala-Diaz, Jose Miguel Rodriguez-Maroto, Francisco Garcia-Herruzo, Carlos Vereda-Alonso

    This study was undertaken to determine the possible changes in the digester yield and performance for the anaerobic co-digestion under mesophilic conditions of strawberry residues (SRs) together with pig manure (PM). The first part of this paper deals with the digestion of SR as a single substrate. For organic loading rates (OLRs) of 4.4 (g L−1 d−1) or less, the experimental specific biogas and methane productions are 0.588 and 0.231 L g−1, respectively. When higher OLRs (5.5 g L−1 d−1) are used the digester fails due to acidification. In the second part, the co-digestion of both residues is explored using a wide variety of SR:PM ratios and OLRs of 5.5 g L−1 d−1 with good stability. Therefore, it is demonstrated that co-digestion allows the improvement of the treatment capacity as compared with SR as a single residue. The methane and biogas productions increase as the SR:PM ratio increases. It may be concluded that, when a digester works with a certain OLR, the performance for co-digestion is always better than for single substrates because the presence of PM provides a better stability and the presence of SR improves the biogas and methane production.