Advances in Multi-Scale Methods in Fluid Mechanics for Bubble Columns and Fluidized Beds

A special issue of Processes (ISSN 2227-9717). This special issue belongs to the section "Chemical Processes and Systems".

Deadline for manuscript submissions: closed (20 November 2023) | Viewed by 1148

Special Issue Editors


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Guest Editor
Institute of Chemical Engineering, Polish Academy of Sciences, 44-100 Gliwice, Poland
Interests: mass transfer; hydrodynamics; mixing; turbulence; nonlinear chaos theory; information entropy theory
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Guest Editor
Department of Chemical and Biochemical Engineering, Western University, London, ON N6A 3K7, Canada
Interests: multiphase reactor engineering; gas-liquid transport phenomena; CO2 and bio-oil upgrading (hydrogenation, thermal cracking); gas-liquid-solid fluidized beds (ebullated beds, slurry bubble columns); particle agglomeration phenomena; reactor fouling

Special Issue Information

Dear Colleagues,

The multiphase reactors are the most important units in the chemical, biochemical, and petrochemical industries. Numerous research groups in different parts of the world are dealing with multiphase reactors. Especially in the field of bubble column reactors, there are over 500 papers in the open literature about different aspects of hydrodynamics, mixing, and mass and heat transfer. These facilities are simple but very effective gas–liquid contactors. They are characterized with a complicated hydrodynamics, which implies the formation of various flow regimes. This issue has rendered the successful design and scale-up of bubble columns a very difficult multi-parameter task.

Since the analogous description of the hydrodynamics of both bubble columns and fluidized beds is feasible, these multiphase reactors should be simultaneously investigated and their performance compared, with some analogies extracted. In both reactor types, advanced measurement techniques and new approaches for CFD simulations are frequently applied.

In this Special Issue, manuscripts are solicited that focus on the advances on multi-scale methods in fluid mechanics of both reactor types. Especially welcome are articles that focus on the various modifications of both bubble columns (including slurry bubble columns) and fluidized beds.

Prof. Dr. Stoyan Nedeltchev
Dr. Dominic Pjontek
Guest Editors

Manuscript Submission Information

Manuscripts should be submitted online at www.mdpi.com by registering and logging in to this website. Once you are registered, click here to go to the submission form. Manuscripts can be submitted until the deadline. All submissions that pass pre-check are peer-reviewed. Accepted papers will be published continuously in the journal (as soon as accepted) and will be listed together on the special issue website. Research articles, review articles as well as short communications are invited. For planned papers, a title and short abstract (about 100 words) can be sent to the Editorial Office for announcement on this website.

Submitted manuscripts should not have been published previously, nor be under consideration for publication elsewhere (except conference proceedings papers). All manuscripts are thoroughly refereed through a single-blind peer-review process. A guide for authors and other relevant information for submission of manuscripts is available on the Instructions for Authors page. Processes is an international peer-reviewed open access monthly journal published by MDPI.

Please visit the Instructions for Authors page before submitting a manuscript. The Article Processing Charge (APC) for publication in this open access journal is 2400 CHF (Swiss Francs). Submitted papers should be well formatted and use good English. Authors may use MDPI's English editing service prior to publication or during author revisions.

Keywords

  • bubble columns
  • fluidized beds
  • hydrodynamic analogies
  • advanced measurement techniques
  • CFD simulations
  • mixing
  • mass and heat transfer

Published Papers (1 paper)

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Research

16 pages, 2608 KiB  
Article
Quality of Mixedness Using Information Entropy in a Counter-Current Three-Phase Bubble Column
by Ritesh Prakash, Subrata Kumar Majumder, Jinkee Lee and Stoyan Nedeltchev
Processes 2024, 12(2), 281; https://doi.org/10.3390/pr12020281 - 27 Jan 2024
Viewed by 862
Abstract
Knowledge of mixing phenomena is of great value in the mineral and other chemical and biochemical industries. This work aims to analyze the quality of mixedness (QM), the intrinsic mass transfer (MT) number, and the MT efficiency based on information entropy theory in [...] Read more.
Knowledge of mixing phenomena is of great value in the mineral and other chemical and biochemical industries. This work aims to analyze the quality of mixedness (QM), the intrinsic mass transfer (MT) number, and the MT efficiency based on information entropy theory in the counter-current microstructured slurry bubble column. A thorough analysis is conducted to assess the effects of particle loading, gas and slurry velocity, and axial variation on the QM. The range of gas velocity, slurry velocity, particle size, and particle loading was 0.011–0.075 m/s, 0.018–0.058 m/s, 242.72–408.31 μm, and 15.54–88.94 kg/m3, respectively. QM is a time-dependent parameter, and the concept of contact time has been used for scale-up purposes. The maximum QM was achieved at dimensionless times of 0.40 × 10−3, 0.15 × 10−3, and 0.85 × 10−3 for the maximum superficial gas velocity, particle loading, and axial height, respectively. The gas velocity positively influenced both the intrinsic MT number and its efficiency. In contrast, the slurry velocity and particle loading had a negative effect. The present theoretical analysis will pave the path for industrial process intensification in counter-current flow systems. Full article
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