Faı̈çal Larachi

ORCID: 0000-0002-0127-4738
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About
Contact & Profiles
Research Areas
  • Heat and Mass Transfer in Porous Media
  • Lattice Boltzmann Simulation Studies
  • Granular flow and fluidized beds
  • Fluid Dynamics and Mixing
  • Minerals Flotation and Separation Techniques
  • Enhanced Oil Recovery Techniques
  • Carbon Dioxide Capture Technologies
  • Catalytic Processes in Materials Science
  • Groundwater flow and contamination studies
  • Metal Extraction and Bioleaching
  • Catalysts for Methane Reforming
  • CO2 Sequestration and Geologic Interactions
  • Mineral Processing and Grinding
  • Extraction and Separation Processes
  • Innovative Microfluidic and Catalytic Techniques Innovation
  • Catalysis and Hydrodesulfurization Studies
  • Industrial Gas Emission Control
  • Cyclone Separators and Fluid Dynamics
  • Characterization and Applications of Magnetic Nanoparticles
  • Membrane Separation and Gas Transport
  • Thermochemical Biomass Conversion Processes
  • Ionic liquids properties and applications
  • Advanced oxidation water treatment
  • Rheology and Fluid Dynamics Studies
  • Carbon dioxide utilization in catalysis

Université Laval
2015-2024

Indian Institute of Technology Delhi
2008-2013

Université de Sherbrooke
2004-2013

IFP Énergies nouvelles
2013

Centre National de la Recherche Scientifique
1991-2008

Total (France)
2008

Natural Resources Canada
2008

Polytechnique Montréal
1993-2001

Université Savoie Mont Blanc
2000

Universitatea Națională de Știință și Tehnologie Politehnica București
1999

10.1016/j.cep.2010.03.008 article EN Chemical Engineering and Processing - Process Intensification 2010-03-17

ABSTRACT Conventional and emerging processes that require the application of multiphase reactors are reviewed with an emphasis on catalytic processes. In past, catalyst discovery development preceded drove selection appropriate reactor type. This sequential approach is increasingly being replaced by a parallel to selection. Either requires quantitative models for flow patterns, phase contacting, transport in various types. review focuses these physical parameters reactors. First, fixed-bed...

10.1081/cr-120001460 article EN Catalysis Reviews 2002-08-04

10.1016/s0009-2509(98)00367-4 article EN Chemical Engineering Science 1999-07-01

A condensed review of recent advances accomplished in the development and applications noninvasive tomographic velocimetric measurement techniques to multiphase flows systems is presented. In years utilization such has become widespread many engineering disciplines that deal with involving two immiscible phases or more. Tomography provides concentration, holdup, 2D 3D density distribution at least one component system, whereas velocimetry dynamic features phase interest as flow pattern,...

10.1021/ie970210t article EN Industrial & Engineering Chemistry Research 1997-11-01

Mineral carbonation of ultramafic rocks provides an environmentally safe and permanent solution for CO2 sequestration. In order to assess the potential waste material produced by industrial processing, we designed a laboratory-scale method, using modified eudiometer, measure continuous consumption in samples at atmospheric pressure near ambient temperature. The eudiometer allows monitoring partial during mineral reactions. maximum amount reaction rate different were measured range...

10.1021/es203063a article EN Environmental Science & Technology 2011-10-04

The potential and limits of in situ removal water under dimethyl ether (DME) synthesis conditions a fixed-bed membrane reactor were studied numerically. motivation for H2O during DME by means hydrophilic membranes is to displace the water−gas shift equilibrium enhance conversion CO2 into methanol improve productivity. In CO-rich feeds, yield/selectivity increases/decreases slowly with increasing permeance because only small amounts are removed from system. Methanol dehydration not inhibited...

10.1021/ie901726u article EN Industrial & Engineering Chemistry Research 2010-02-08

Abstract Calcium carbonate nanoparticles (CCNP) were synthesised by precipitation from saturated sodium and calcium nitrate aqueous solutions. The effect of agitation rate, mixing time, calcium/carbonate ions concentration temperature on particle size morphology investigated. Particles characterised using X‐ray diffraction (XRD), transmission electron microscopy (TEM) thermogravimetric analysis (TGA). Increasing the time 30 to 180 min resulted in a decrease particles size. Mixing rate...

10.1002/cjce.20673 article EN The Canadian Journal of Chemical Engineering 2011-11-15
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