Wet air oxidation (WAO) as a precursor to biological treatment of substituted phenols: refractory nature of the WAO intermediates.
Suárez-Ojeda M.E., Carrera J., Metcalfe I.S., Font J.
Chemical Engineering Journal (2008) doi: 10.1016/j.cej.2008.01.022.

Mixing and hydrodynamics investigation using CFD in a square-sectioned torus reactor in batch and continuous regimes.
Pramparo L., Pruvost J., Stüber F., Font J., Fortuny A., Fabregat A., Legentilhomme P., Legrand J., Bengoa C.
Chemical Engineering Journal (2008) 137, 386-395.

Recovery of iron (III) from aqueous streams by ultrafiltration.
Bernat X., Fortuny A., Stüber F., Bengoa C., Fabregat A., Font J.
Desalination (2008) 221, 413-418.

Catalytic and non-catalytic wet air oxidation of sodium dodecylbenzene sulfonate: Kinetics and biodegradability enhancement.
Suárez-Ojeda M.E., Kim J., Carrera J., Metcalfe I.S., Font J.
Journal of Hazardous Materials (2007) 144, 655-662.

Integrated catalytic wet air oxidation and aerobic biological treatment in a municipal WWTP of a high-strength o-cresol wastewater.
Suárez-Ojeda M.E., Guisasola A., Baeza J.A., Fabregat A., Stüber F., Fortuny A., Font J., Carrera J.
Chemosphere (2007) 66, 2096-2105.

Catalytic wet air oxidation of substituted phenols: Temperature and pressure effect on the pollutant removal, the catalyst preservation and the biodegradability enhancement.
Suárez-Ojeda M.E., Fabregat A., Stüber F., Fortuny A., Carrera J., Font J.
Chemical Engineering Journal (2007) 132, 105-115.

Gas feed composition modulation in phenol CWAO over active carbon.
Larruy B., Ayude A., Font J., Fortuny A., Bengoa C., Fabregat A., Stüber F.
Chemical Engineering Science (2007) 62, 5564-5566.

Effective anaerobic decolorization of azo dye acid orange 7 in continuous upflow packed-bed reactor using biological activated carbon system.
Mezohegyi G., Kolodkin A., Castro U.I., Bengoa C., Stüber F., Font J., Fabregat A., Fortuny A.
Industrial & Engineering Chemistry Research (2007) 46, 6788-6792.

Phenol wastewater remediation: advanced oxidation processes coupled to a biological treatment.
Rubalcaba A., Suárez-Ojeda M.E., Stüber F., Fortuny A., Bengoa C., Metcalfe I., Font J., Carrera J., Fabregat A.
Water Science and Technology (2007) 55, 221-227.

Biodegradability enhancement of phenolic compounds by Hydrogen Peroxide Promoted Catalytic Wet Air Oxidation.
Rubalcaba A., Suárez-Ojeda M.E., Carrera J., Font J., Stüber F., Bengoa C., Fortuny A., Fabregat A.
Catalysis Today (2007) 124, 191-197.

Effect of gas feed flow and gas composition modulation on activated carbon performance in phenol wet air oxidation.
Ayude A., Rodriguez T., Font J., Fortuny A., Bengoa C., Fabregat A., Stüber F.
Chemical Engineering Science (2007) 62, 7352-7358.

Elimination of phenol and aromatic compounds by zero valent iron and EDTA at low temperature and atmospheric pressure.
Sánchez I., Stüber F., Font J., Fortuny A., Fabregat A., Bengoa C.
Chemosphere (2007) 68, 338-344.

Catalytic wet air oxidation of phenol over active carbon catalyst - Global kinetic modelling using simulated annealing.
Eftaxias A., Font J., Fortuny A., Fabregat A., Stüber F.
Applied Catalysis B-Environmental (2006) 67, 12-23.

Carbon materials and catalytic wet air oxidation of organic pollutants in wastewater.
Stüber F., Font J., Fortuny A., Bengoa C., Eftaxias A., Fabregat A.
Topics in Catalysis (2005) 33, 3-50.

Chemical wet oxidation for the abatement of refractory non-biodegradable organic wastewater pollutants.
Stüber F., Font J., Eftaxias A., Paradowska M., Suarez M.E., Fortuny A., Bengoa C., Fabregat A.
Process Safety and Environmental Protection (2005) 83 (B4), 371-380.

Scale-up and modeling of fixed-bed reactors for catalytic phenol oxidation over adsorptive active carbon.
Suwanprasop S., Eftaxias A., Stüber F., Polaert I., Julcour-Lebigue C., Delmas, H.
Industrial & Engineering Chemistry Research (2005) 44 (25), 9513-9523.

Kinetics of phenol oxidation in a trickle bed reactor over active carbon catalyst.
Eftaxias A., Font J., Fortuny A., Fabregat A., Stüber, F.
Journal of Chemical Technology and Biotechnology (2005) 80 (6), 677-687.

Casein hydrolysis by immobilized enzymes in a torus reactor.
Benkhelifa H., Bengoa C., Larre C., Guibal E., Popineau Y., Legrand J.
Process Biochemistry (2005) 40, 461-467.

Processing of black liquors by UF/NF ceramic membranes.
Dafinov A., Font J., Garcia-Valls R.
Desalination (2005) 173, 83-90.

Modified activated carbons for catalytic wet air oxidation of phenol.
Santiago M., Stüber F., Fortuny A., Fabregat A., Font J.
Carbon (2005) 43, 2134-2145.

Catalytic Wet Air Oxidation of Substituted Phenols using Activated Carbon as Catalyst.
Suárez M.E., Stüber F., Fortuny A., Fabregat A., Carrera J., Font J.
Applied Catalysis B-Environmental (2005) 58, 105-114.

Partial hydrogenation in an upflow fixed-bed reactor: a multistage operation for experimental optimization of selectivty.
Stüber F., Delmas H.
Industrial & Engineering Chemistry Research (2003) 42 (1), 6-13.

Unit operations laboratory using ill-posed problems.
Jiménez L., Font J., Farriol X.
International Journal Of Engineering Education (2003) 19 (5), 717-720.

Modelling of trickle bed reactor for the catalytic wet air oxidation of phenol.
Eftaxias A., Larachi F., Stüber F.
Canadian Journal of Chemical Engineering (2003) 81 (3-4), 784-794.

Nonlinear Kinetic Parameter Estimation using Simulated Annealing.
Eftaxias A., Font J., Fortuny A., Fabregat A., Stüber F.
Computers & Chemical Engineering (2002) 26, 1725-1733.

Modification of Ceramic Membranes by Alcohol Adsorption.
Dafinov A., Garcia-Valls R., Font J.
Journal of Membrane Science (2002) 196, 69-77.

A Holistic Unit Operations Laboratory.
Jiménez L., Font J., Bonet J., Farriol, X.
Chemical Engineering Education (2002) 36 (2), 150-154.

Solvent screening for the supercritical hydrogenation of polyunsaturated hydrocarbons using VLE calculations.
DeJong A., Eftaxias A., Trabelsi F., Recasens F., Sueiras J., Stüber F.
Industrial & Engineering Chemistry Research (2001) 40 (14), 3225-3229.

Kinetic modelling of catalytic wet air oxidation of phenol by simulated annealing.
Eftaxias A., Font J., Fortuny A., Giralt J., Fabregat A., Stüber F.
Applied Catalysis B: Environmental (2001) 33, 175-190.

Catalytic wet air oxidation of phenol using active carbon. performance of discontinuous and continuous reactor type.
Stüber F., Polaert I., Delmas H., Font J., Fortuny A., Fabregat A.
Journal of Chemical Technology and Biotechnology (2001) 76 (7), 743-751.

Coking and ex situ catalyst reactivation using supercritical CO2: A preliminary study.
Trabelsi F., Stüber F., Abaroudi K., Larrayoz M.A., Recasens F., Sueiras J.E.
Industrial & Engineering Chemistry Research (2000) 39 (10), 3666-3670.

Characterization and modeling of the hydrodynamic behavior in the filter-press-type FM01-LC electrochemical cell by direct flow visualization and residence time distribution.
Bengoa C., Montillet A., Legentilhomme P., Legrand J.
Industrial & Engineering Chemistry Research (2000) 39, 2199-2206.

Water pollution bbatement by catalytic wet air oxidation in trickle bed reactor.
Fortuny A., Bengoa C., Font J.; Castells F., Fabregat A.
Catalysis Today (1999) 53, 107-114.

Three phase reactors for environmental remediation: catalytic wet oxidation of phenol using active carbon.
Fortuny A., Miró C., Font J., Fabregat A.
Catalysis Today (1999) 48, 323-328.

Bimetallic catalysts for continuous catalytic wet air oxidation of phenol.
Fortuny A., Bengoa C., Font J., Fabregat A.
Journal of Hazardous Materials (1999) 64-2, 181-193.

Aqueous phase catalytic oxidation of phenol in a trickle bed reactor.
Alejandre A., Miró C., Fortuny A., Bengoa C., Font J., Fabregat A.
Water Research (1999) 33 (4), 1005-1013.

Local measurement for the study of external loop airlift hydrodynamics.
Utiger M., Stüber F., Duquenne A.M., Delmas H., Guy C.
Canadian Journal of Chemical Engineering (1999) 77, 3755-382.

Dynamics of a three phase upflow fixed bed reactor.
Julcour C., Stüber F., Lelann J.M., Wilhelm A.M., Delmas H.
Chemical Engineering Science (1998) 54 (13-14), 2391-2400.

Wet air oxidation of phenol using active carbon as catalyst.
Fortuny A., Font J., Fabregat A.
Applied Catalysis B-Environmental (1998) 19 (3-4), 165-173.

Characterization and activity of copper and nickel catalysts for the oxidation of phenol aqueuous solutions.
Alejandre A., Medina F., Fortuny A., Fabregat A., Salagre P., Sueiras J.E.
Applied Catalysis B-Environmental (1998) 18, 307-315.

Testing a predictor-corrector integral method for estimating parameters in complex kinetic systems described by ordinary differential equations.
Font J., Fabregat A.
Computers & Chemical Engineering (1997) 21 (7), 719-731.

Influence des catalyseurs heterogenes sur le coprocesing d'un lignite du Bergueda avec un residu de distillation sous vide.
Bengoa C., Font J., Moros A., Fabregat A., Giralt F.
Revue de l'Institut Francais du Petrole (1997) 52 (1), 61-71.

Internal mass transfer in sintered metallic pellets filled with supercritical fluid.
Stüber F., Julien S., Recasens F.
Chemical Engineering Science (1997) 52 (20), 3527-3542.

Flow visualization and modelling of a filter-press type electrochemical reactor.
Bengoa C., Montillet A., Legentilhomme P., Legrand J.
Journal of Applied Electrochemistry (1997) 27, 1313-1322.

Influence of type of vacuum residue on the catalytic coprocessing of a demineralized Catalan lignite.
Bengoa C., Font J., Moros A., Fortuny A., Fabregat A., Giralt F.
Fuel (1996) 75 (11), 1327-1330.

Performance of different catalysts on the coprocessing of a demineralized catalan lignite.
Bengoa C., Font J., Moros A., Fortuny A., Fabregat A., Giralt F.
Energy & Fuels (1996) 10 (3), 679-683.

Hydraulic Permeability Loss in Ceramic Membranes.
Font J., Castro R.P., Cohen Y.
Journal of Colloid and Interface Science (1996) 181, 347-350.

Modeling of a three phase catalytic upflow reactor: a significant chemical determination of liquid-solid and gas-liquid mass transfer coefficients.
Stüber F., Wilhelm A.M., Delmas H.
Chemical Engineering Science (1996) 51 (10), 2161-2167.

Supercritical fluid extraction of packed beds: External mass transfer in upflow and dowflow operation.
Stüber F., Vazquez A.M., Larrayoz M.A., Recasens F.
Industrial & Engineering Chemistry Research (1996) 35 (10), 3618-3628.

Catalytic removal of phenol from aqueus phase using molecular oxigen or air as oxidant.
Fortuny A., Ferrer C., Bengoa C., Font J., Fabregat A.
Catalysis Today (1995) 24 (1-2), 79-83.

Coprocessing of a bergueda lignite with vacuum residue under increasing hydrogen pressure. Comparison with hydrotreating.
Bengoa C., Font J., Moros A., Fabregat A., Giralt F.
Fuel (1995) 74 (11), 1704-1708.

Partial Hydrogenation of 1,5,9-Cyclododecatriene in three phase catalytic reactors.
Stüber F., Benaissa M., Delmas H.
Catalysis Today (1995) 24 (1-2), 95-101.

Influence of Fe and FeMo high loading supported catalysts on the coprocessing of two spanish lignites with a vacuum residue.
Font J., Moros A., Fabregat A., Salvadó J., Giralt F.
Fuel Processing Technology (1994) 37 (2), 163-173.

Influence of temperature, catalysts and partial pressure of hydrogen on thecoprocessing of spanish lignites.
Fabregat A., Salvado J., Giralt J., Moros A., Font J., Giralt F.
International Journal of Energy Research (1994) 18, 317-328.

A holistic approach to ChE education. Part II: approach at the introductoryLevel.
Giralt F., Fabregat A., Farriol X., Grau F.X., Giralt J., Medir M., Thier H.
Chemical Engineering Education (1994) 28 (3), 204-209.

Influence of temperature and hydrogen pressure on the coprocessing of two spanish lignites with a vacuum residue.
Font J., Fabregat A., Salvado J., Moros A., Bengoa C., Giralt F.
Fuel (1992) 71 (11), 1169-1175.

Catalytic hydroliquefaction of Bergueda lignite with fuel oil and anthracene oil under various reactive atmospheres.
Salvado J., Giralt J., Fabregat A., Giralt F.
Fuel (1990) 69 (6), 743-746.

Kinetics of the solvolysis of a catalan lignite with tetralin and anthracene oil.
Giralt J., Fabregat A., Giralt F.
Industrial & Engineering Chemistry Research (1988) 27, 1110-1114.

Solvolysis of a catalan lignite with solvents of low hydrogen donor capacity.
Fabregat A., Giralt J., Giralt F.
Fuel (1987) 66 (6), 835-839.