Multiscale kinetic modeling in catalysis ⇒ from microkinetics to computational fluid dynamics and process simulations

Problem statement

We envision multiscale modeling as critical enablers of reaction understanding, catalyst and reactor design, scale-up, and process optimization. The framework includes predicting the molecular reaction mechanism at the molecular level to the process optimization stage. As catalytic processes occur at the multiscale, we address these issues individually and collectively.

At the microkinetic level, our models resolve the rates of the individual elementary steps, rate-determining step (RDS), adsorption, and desorption mechanisms. We use quantum chemical calculations (density functional theory, DFT) to support our assumed kinetic pathways, original parameter estimations, and adsorption-desorption energies.

We incorporate thermodynamic constraints into our models. Once developed, the microkinetic model could guide the catalyst and reactor design. We also have experience developing Langmuir-Hinshelwood and Eley-Rideal types of kinetic models.

At the macrokineitc level, we develop lump-based and empirical models which, in some cases, are very robust and, together with other models, can be used to extract information such as mechanism change, optimize conditions, or for reactor pre-design.

We couple hydrodynamics, heat transfer, and reaction kinetics at the reactor level in computational fluid dynamic (CFD) simulations. Together with optimization algorithms, we aim to improve operating scenarios, develop innovative reactor prototypes, and predict process behaviors at the industrial scale.

Goals

  • Microkinetics I ⇒ key thermodynamic relationships
  • Microkinetics II ⇒ fitting, training, and optimization
  • Microkinetics III ⇒ ab initio kinetic modeling
  • Macrokinetics ⇒ complex reaction networks and population balances
  • CPFD ⇒ reactor modeling and scale-up
  • CFD ⇒ reactor modeling and optimization
  • CFD II ⇒ modeling operando reactors
  • Process system engineering ⇒ gPROMS

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Effect of Space Velocity on the Hydrocracking of Light Cycle Oil over a Pt-Pd/HY Zeolite Catalyst
Fuel Process. Technol. Year: 2012
Authors: Gutierrez, Arandes, Castaño, Olazar, Barona, Bilbao
  • HPC
  • MKM
  • W2C
Pathways of Coke Formation on an MFI Catalyst during the Cracking of Waste Polyolefins
Catal. Sci. Technol. Year: 2012
Authors: Castaño, Elordi, Ibanez, Olazar, Bilbao
  • FCC
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Effect of Temperature in the Hydrocracking of LCO on Noble-Metal Supported Catalyst for Fuel Production
Chem. Eng. Technol. Year: 2012
Authors: Gutierrez, Arandes, Castaño, Olazar, Barona, Bilbao
  • HPC
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Modeling Product Distribution of Pyrolysis Gasoline Hydroprocessing on a Pt-Pd/HZSM-5 Catalyst
Chem. Eng. J. Year: 2011
Authors: Gutierrez, Castaño, Azkoiti, Bilbao, Arandes
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Transients Behaviour and Stability in Miniaturized Packed-Bed Reactors
Ind. Eng. Chem. Res. Year: 2010
Authors: Marquez, Castaño, Makkee, Moulijn, Kreutzer
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Effect of Hydrogen on the Cracking Mechanisms of Cycloalkanes over Zeolites
Catal. Today Year: 2010
Authors: Castaño, Arandes, Olazar, Bilbao, Pawelec, Sedran
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Volatile Tracer Dispersion in Multi-Phase Packed Beds
Chem. Eng. Sci. Year: 2010
Authors: Marquez, Castaño, Makkee, Moulijn, Kreutzer
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Kinetic and Deactivation Modelling of Biphenyl Liquid-Phase Hydrogenation over Bimetallic Pt-Pd Catalyst
Appl. Catal. B: Environ. Year: 2009
Authors: Castaño, Van Herk, Kreutzer, Moulijn, Makkee
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Kinetic Modelling for Assessing Product Distribution in Toluene Hydrocracking on a Pt/HZSM-5 Catalyst
Ind. Eng. Chem. Res. Year: 2008
Authors: Castaño, Arandes, Pawelec, Olazar, Bilbao
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Kinetic Modelling of Methylcyclohexane Ring-Opening over a HZSM-5 Zeolite Catalyst
Chem. Eng. J. Year: 2008
Authors: Castaño, Gayubo, Pawelec, Fierro, Arandes
  • FCC
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