Multiphase catalytic reactors: a perspective on current knowledge and future trends

MP Duduković, F Larachi, PL Mills - Catalysis reviews, 2002 - Taylor & Francis
Conventional and emerging processes that require the application of multiphase reactors
are reviewed with an emphasis on catalytic processes. In the past, catalyst discovery and …

Performance analysis and modeling of catalytic trickle-bed reactors: A comprehensive review

A Azarpour, N Rezaei, S Zendehboudi - Journal of Industrial and …, 2021 - Elsevier
Trickle-bed reactors (TBRs) are extensively used in industry. There have been great
progresses in design and control of the TBRs. However, more improvements are required in …

Reactions, hydrodynamics and mass transfer in micro-packed beds—Overview and new mass transfer data

A Faridkhou, JN Tourvieille, F Larachi - Chemical Engineering and …, 2016 - Elsevier
Studies on micro-packed beds were reviewed pointing out major contributions with their key
findings. Negligible mass transfer resistance and temperature gradients in micro-packed …

Gas–liquid interfacial mass transfer in trickle-bed reactors: state-of-the-art correlations

I Iliuta, F Larachi, BPA Grandjean, G Wild - Chemical Engineering Science, 1999 - Elsevier
The state-of-the-art of the gas-liquid mass transfer characteristics in trickle-bed reactors was
summarized and its quantification methods were reevaluated based on a wide-ranging data …

Determination of liquid hold-up and flow distribution inside modular catalytic structured packings

A Viva, S Aferka, D Toye, P Marchot, M Crine… - … Research and Design, 2011 - Elsevier
This paper presents the results of a study carried out to examine liquid hold-up and flow
distribution in a 0.1 m internal diameter column filled with catalytic structured packing …

Effect of coalescence and breakup on bubble size distributions in a two-dimensional packed bed

D Jo, ST Revankar - Chemical engineering science, 2010 - Elsevier
Bubble size distributions in a two-dimensional packed bed are investigated as a function of
axial direction by using image processing techniques with a large number of bubble …

Hydrodynamics and pressure loss of concurrent gas–liquid downward flow through sieve plate packing

W Shi, W Huang, Y Zhou, H Chen, D Pan - Chemical Engineering Science, 2016 - Elsevier
Gas–liquid concurrent downward flow through a new structured packing was investigated by
experiment systematically. The experimental packing consisted of 21 sieve plates. Each …

Bubbly flow through fixed beds: Microscale experiments in the dilute regime and modeling

ML Bordas, A Cartellier, P Séchet, C Boyer - AIChE journal, 2006 - Wiley Online Library
In order to predict the pressure drop and the mean void fraction for bubbly flows in packed
beds, a new one‐dimensional (1‐D) model is proposed. The balance equations for both …

A simple model for pressure drop and liquid hold-up in packed-bed bubble reactors

A Attou, G Ferschneider - Chemical engineering science, 1999 - Elsevier
A simple hydrodynamic model for cocurrent gas–liquid bubbly flow through a packed-bed
reactor is developed. The model involves the momentum balance equations for the …

Bubble flow mechanisms in trickle beds—an experimental study using image processing

K Benkrid, S Rode, MN Pons, P Pitiot… - Chemical engineering …, 2002 - Elsevier
The mechanisms of bubble motion in concurrent gas–liquid down flow through trickle beds
are investigated. The laboratory reactor is a structured quasi-two-dimensional porous …