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role of catalyst activity on the steady state and transient behavior of an industrial-scale fixed bed catalytic reactor for the partial oxidation of o-xylene on V₂O₅/TiO₂ catalysts

Chemical engineering journal (Lausanne, Switzerland : 1996), 2011-12, Vol.176, p.26-32

2011

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Heat-Transfer Studies in Packed-Bed Catalytic Reactors of Low Tube/Particle Diameter Ratio

Industrial & engineering chemistry research, 2007-11, Vol.46 (23), p.7426-7435

2007

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Experimental and theoretical study of membrane-aerated biofilm reactor behavior under different modes of oxygen supply for the treatment of synthetic wastewater

Chemical engineering science, 2006-08, Vol.61 (16), p.5268-5281

2006

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The coupling of ω-transaminase and Oppenauer oxidation reactions via intra-membrane multicomponent diffusion – A process model for the synthesis of chiral amines

Chemical engineering journal (Lausanne, Switzerland : 1996), 2015-01, Vol.259, p.221-231

2015

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The Effect of Turbulence on Momentum and Heat Transport in Packed Beds with Low Tube to Particle Diameter Ratio

International journal of chemical reactor engineering, 2018-11, Vol.16 (11)

2018

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Modeling the Partial Oxidation of o-Xylene in an Industrial Packed-Bed Catalytic Reactor: The Role of Hydrodynamics and Catalyst Activity in the Heat Transport

Industrial & engineering chemistry research, 2010-08, Vol.49 (15), p.6845-6853

2010

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A heterogeneous biodiesel production kinetic model

Revista mexicana de ingeniería química, 2014-04, Vol.13 (1), p.311-322

2014

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Natural convection in a cylindrical porous cavity with internal heat source: a numerical study with Brinkman-extended Darcy model

International journal of heat and mass transfer, 1999, Vol.42 (22), p.4185-4195

1999

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5-Lump kinetic model for gas oil catalytic cracking

Applied catalysis. A, General, 1999-02, Vol.177 (2), p.227-235

1999

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Morphometric evaluation of the specific growth rate of Aspergillus niger grown in agar plates at high glucose levels

Biotechnology and bioengineering, 1997-11, Vol.56 (3), p.287-294

1997

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Robust Regulation of Temperature in Reactor−Regenerator Fluid Catalytic Cracking Units

Industrial & engineering chemistry research, 1996, Vol.35 (5), p.1652-1659

1996

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The role of catalyst activity on the steady state and transient behavior of an industrial-scale fixed bed catalytic reactor for the partial oxidation of o-xylene on V sub(2O) sub(5)/TiO sub(2 catalysts)

Chemical engineering journal (Lausanne, Switzerland : 1996), 2011-12, Vol.176-177, p.26-32

2011

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Mass transfer and growth kinetics in filamentous fungi

Chemical engineering science, 1997-08, Vol.52 (15), p.2629-2639

1997

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A Strategy for Kinetic Parameter Estimation in the Fluid Catalytic Cracking Process

Industrial & engineering chemistry research, 1997-12, Vol.36 (12), p.5170-5174

1997

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Modeling and Simulation of an Industrial Fluid Catalytic Cracking Riser Reactor Using a Lump-Kinetic Model for a Distinct Feedstock

Industrial & engineering chemistry research, 2006-01, Vol.45 (1), p.120-128

2006

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Symmetric branching model for the kinetics of mycelial growth

Biotechnology and bioengineering, 1993-06, Vol.42 (1), p.1-10

1993

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Correlations for Predicting the Effect of Feedstock Properties on Catalytic Cracking Kinetic Parameters

Industrial & engineering chemistry research, 1998-12, Vol.37 (12), p.4637-4640

1998

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The role of catalyst activity on the steady state and transient behavior of an industrial-scale fixed bed catalytic reactor for the partial oxidation of o-xylene on V2O5/TiO2 catalysts

Chemical engineering journal (1996), 2011, Vol.176-77, p.26-32

2011

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Approach to the analysis of the dynamics of industrial FCC units

Journal of process control, 1998, Vol.8 (2), p.89-100

1998

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Measurement and estimation in catalytic reactors for partial oxidation

Transactions of the Institute of Measurement and Control, 1986-07, Vol.8 (3), p.137-143

1986

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Distortion of measured temperature profiles in fixed-bed reactors [distortions introduced by the presence of temperature measurement devices]

Chemical engineering research & design, 1992-05, Vol.70, p.255-264

1992

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Dynamic modelling of an industrial fluid catalytic cracking unit

Computers & chemical engineering, 1992, Vol.16, p.S139-S148

López-Isunza, Felipe

1992

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Deactivation of fluid catalytic cracking catalysts : A modelling approach

Fluid Catalytic Cracking V, 2001, Vol.134, p.187-199

2001

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Estimation of catalyst activity profiles in fixed-bed reactors with decaying catalysts

Applied catalysis. A, General, 1993-12, Vol.106 (2), p.193-199

1993

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An strategy to regulate temperature in FCC units with poor knowledge of chemical kinetics

Computers & chemical engineering, 1996, Vol.20, p.S859-S864

1996

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role of catalyst activity on the steady state and transient behavior of an industrial-scale fixed bed catalytic reactor for the partial oxidation of o-xylene on V₂O₅/TiO₂ catalysts

Heat-Transfer Studies in Packed-Bed Catalytic Reactors of Low Tube/Particle Diameter Ratio

Experimental and theoretical study of membrane-aerated biofilm reactor behavior under different modes of oxygen supply for the treatment of synthetic wastewater

The coupling of ω-transaminase and Oppenauer oxidation reactions via intra-membrane multicomponent diffusion – A process model for the synthesis of chiral amines

The Effect of Turbulence on Momentum and Heat Transport in Packed Beds with Low Tube to Particle Diameter Ratio

Modeling the Partial Oxidation of o-Xylene in an Industrial Packed-Bed Catalytic Reactor: The Role of Hydrodynamics and Catalyst Activity in the Heat Transport

A heterogeneous biodiesel production kinetic model

Natural convection in a cylindrical porous cavity with internal heat source: a numerical study with Brinkman-extended Darcy model

5-Lump kinetic model for gas oil catalytic cracking

Morphometric evaluation of the specific growth rate of Aspergillus niger grown in agar plates at high glucose levels

Robust Regulation of Temperature in Reactor−Regenerator Fluid Catalytic Cracking Units

The role of catalyst activity on the steady state and transient behavior of an industrial-scale fixed bed catalytic reactor for the partial oxidation of o-xylene on V sub(2O) sub(5)/TiO sub(2 catalysts)

Mass transfer and growth kinetics in filamentous fungi

A Strategy for Kinetic Parameter Estimation in the Fluid Catalytic Cracking Process

Modeling and Simulation of an Industrial Fluid Catalytic Cracking Riser Reactor Using a Lump-Kinetic Model for a Distinct Feedstock

Symmetric branching model for the kinetics of mycelial growth

Correlations for Predicting the Effect of Feedstock Properties on Catalytic Cracking Kinetic Parameters

The role of catalyst activity on the steady state and transient behavior of an industrial-scale fixed bed catalytic reactor for the partial oxidation of o-xylene on V2O5/TiO2 catalysts

Approach to the analysis of the dynamics of industrial FCC units

Measurement and estimation in catalytic reactors for partial oxidation

Distortion of measured temperature profiles in fixed-bed reactors [distortions introduced by the presence of temperature measurement devices]

Dynamic modelling of an industrial fluid catalytic cracking unit

Deactivation of fluid catalytic cracking catalysts : A modelling approach

Estimation of catalyst activity profiles in fixed-bed reactors with decaying catalysts

An strategy to regulate temperature in FCC units with poor knowledge of chemical kinetics

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