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Identification of Mass Transfer Limitations by Kinetic Modeling of a Technical-Scale Trickle Bed Reactor for the Hydrogenation of Viscous Aromatics

Industrial & engineering chemistry research, 2024-01, Vol.63 (1), p.147-162

2024

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Kinetic Modeling of the Partial Oxidation of Propylene to Acrolein: A Systematic Procedure for Parameter Estimation Based on Non-isothermal Data

Industrial & engineering chemistry research, 2019-02, Vol.58 (5), p.1857-1874

2019

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Assessment of Periodic Open Cellular Structures for Enhanced Heat Conduction in Catalytic Fixed-Bed Reactors

Advanced engineering materials, 2016-04, Vol.18 (4), p.608-614

2016

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Packed Periodic Open Cellular Structures – an Option for the Intensification of Non-Adiabatic Catalytic Processes

Chemical engineering and processing, 2020-09, Vol.155, p.108057, Article 108057

2020

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An appraisal of the heat transfer properties of metallic open-cell foams for strongly exo-/endo-thermic catalytic processes in tubular reactors

Chemical engineering journal (Lausanne, Switzerland : 1996), 2012-08, Vol.198-199, p.512-528

2012

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Numerical simulation of heat transfer in the near-wall region of tubular reactors packed with metal open-cell foams

Chemical engineering journal (Lausanne, Switzerland : 1996), 2015-03, Vol.264, p.268-279

2015

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Simultaneous design of the optimal reaction and process concept for multiphase systems

Chemical engineering science, 2014-08, Vol.115, p.69-87

2014

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Comparative evaluation of heat transfer correlations with different fluid property considerations for fixed-bed reactor modeling

International journal of heat and mass transfer, 2020-02, Vol.148, p.119099, Article 119099

2020

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Analysis and optimal design of an ethylene oxide reactor

Chemical engineering science, 2011-12, Vol.66 (24), p.6453-6469

2011

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Design of optimal multiphase reactors exemplified on the hydroformylation of long chain alkenes

Chemical engineering journal (Lausanne, Switzerland : 1996), 2012-04, Vol.188, p.126-141

2012

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A New Process for Azeotropic Mixture Separation by Phase Behavior Tuning Using Pressurized Carbon Dioxide

Industrial & engineering chemistry research, 2013-10, Vol.52 (43), p.15154-15164

2013

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An Overview of Mutual Solubility of Ionic Liquids and Water Predicted by COSMO-RS

Industrial & engineering chemistry research, 2012-05, Vol.51 (17), p.6256-6264

2012

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Model-based prediction of optimal conditions for 1-octene hydroformylation

Chemical engineering science, 2014-08, Vol.115, p.58-68

2014

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Chemische Reaktionstechnik

7. Auflage 2024, 2024

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Evaluation of the ionic liquids 1-alkyl-3-methylimidazolium hexafluorophosphate as a solvent for the extraction of benzene from cyclohexane: (Liquid+liquid) equilibria

The Journal of chemical thermodynamics, 2012-05, Vol.48, p.145-149

2012

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Modelling (vapour + liquid) and (vapour + liquid + liquid) equilibria of {water (H 2O) + methanol (MeOH) + dimethyl ether (DME) + carbon dioxide (CO 2)} quaternary system using the Peng–Robinson EoS with Wong–Sandler mixing rule

The Journal of chemical thermodynamics, 2011-12, Vol.43 (12), p.2002-2014

2011

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Predicting the Specific Surface Area and Pressure Drop of Reticulated Ceramic Foams Used as Catalyst Support

Advanced engineering materials, 2011-11, Vol.13 (11), p.990-995

2011

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Dynamic Carbon Dioxide Methanation in a Wall-Cooled Fixed Bed Reactor: Comparative Evaluation of Reactor Models

Industrial & engineering chemistry research, 2019-10, Vol.58 (42), p.19406-19420

2019

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Methodology for the Design of Optimal Chemical Reactors Based on the Concept of Elementary Process Functions

Industrial & engineering chemistry research, 2010-11, Vol.49 (21), p.10535-10548

2010

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Identification of Reaction Pathways and Kinetic Modeling of Olefin Interconversion over an H‑ZSM‑5 Catalyst

Industrial & engineering chemistry research, 2020-07, Vol.59 (28), p.12696-12709

2020

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Systematic Experimental Investigations and Modeling of the Heat Transfer in Additively Manufactured Periodic Open Cellular Structures with Diamond Unit Cell

Industrial & engineering chemistry research, 2021-05, Vol.60 (18), p.6753-6766

2021

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Multiscale Chemical Process Design Exemplified for a PEM Fuel Cell Process

Chemie ingenieur technik, 2014-12, Vol.86 (12), p.2075-2088

2014

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Sugar acid production on gold nanoparticles in slurry reactor: Kinetics, solubility and modelling

Chemical engineering science, 2022-10, Vol.260, p.117948, Article 117948

2022

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Dynamics of liquid–liquid systems based on linear thermodynamics of irreversible processes

Computers & chemical engineering, 2011-04, Vol.35 (4), p.630-637

2011

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Heat transfer properties of metal foam supports for structured catalysts: Wall heat transfer coefficient

Catalysis today, 2013-11, Vol.216, p.121-134

2013

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Identification of Mass Transfer Limitations by Kinetic Modeling of a Technical-Scale Trickle Bed Reactor for the Hydrogenation of Viscous Aromatics

Kinetic Modeling of the Partial Oxidation of Propylene to Acrolein: A Systematic Procedure for Parameter Estimation Based on Non-isothermal Data

Assessment of Periodic Open Cellular Structures for Enhanced Heat Conduction in Catalytic Fixed-Bed Reactors

Packed Periodic Open Cellular Structures – an Option for the Intensification of Non-Adiabatic Catalytic Processes

An appraisal of the heat transfer properties of metallic open-cell foams for strongly exo-/endo-thermic catalytic processes in tubular reactors

Numerical simulation of heat transfer in the near-wall region of tubular reactors packed with metal open-cell foams

Simultaneous design of the optimal reaction and process concept for multiphase systems

Comparative evaluation of heat transfer correlations with different fluid property considerations for fixed-bed reactor modeling

Analysis and optimal design of an ethylene oxide reactor

Design of optimal multiphase reactors exemplified on the hydroformylation of long chain alkenes

A New Process for Azeotropic Mixture Separation by Phase Behavior Tuning Using Pressurized Carbon Dioxide

An Overview of Mutual Solubility of Ionic Liquids and Water Predicted by COSMO-RS

Model-based prediction of optimal conditions for 1-octene hydroformylation

Chemische Reaktionstechnik

Evaluation of the ionic liquids 1-alkyl-3-methylimidazolium hexafluorophosphate as a solvent for the extraction of benzene from cyclohexane: (Liquid+liquid) equilibria

Modelling (vapour + liquid) and (vapour + liquid + liquid) equilibria of {water (H 2O) + methanol (MeOH) + dimethyl ether (DME) + carbon dioxide (CO 2)} quaternary system using the Peng–Robinson EoS with Wong–Sandler mixing rule

Predicting the Specific Surface Area and Pressure Drop of Reticulated Ceramic Foams Used as Catalyst Support

Dynamic Carbon Dioxide Methanation in a Wall-Cooled Fixed Bed Reactor: Comparative Evaluation of Reactor Models

Methodology for the Design of Optimal Chemical Reactors Based on the Concept of Elementary Process Functions

Identification of Reaction Pathways and Kinetic Modeling of Olefin Interconversion over an H‑ZSM‑5 Catalyst

Systematic Experimental Investigations and Modeling of the Heat Transfer in Additively Manufactured Periodic Open Cellular Structures with Diamond Unit Cell

Multiscale Chemical Process Design Exemplified for a PEM Fuel Cell Process

Sugar acid production on gold nanoparticles in slurry reactor: Kinetics, solubility and modelling

Dynamics of liquid–liquid systems based on linear thermodynamics of irreversible processes

Heat transfer properties of metal foam supports for structured catalysts: Wall heat transfer coefficient

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