CFD-aided enhancement of propylene oxide decomposition in a tubular reactor with a corrugated cooling jacket

_This research delves into the decomposition kinetics of propylene oxide within a novel reactor design characterized by a corrugated inner wall for enhanced cooling. By applying Computational Fluid Dynamics (CFD), this study aims to optimize the reactor's heat transfer capabilities to achieve precise control over the exothermic decomposition process. This approach addresses a previously unexplored area in CFD application, proposing a model that fine-tunes the decomposition efficiency of propylene oxide by considering the interplay of key parameters such as inlet mixture temperature, activation energy, flow rate, and the resulting thermal profile. The primary goal is to advance the development of more efficient and environmentally friendly chemical processing techniques in the propylene oxide industry. The study highlights the critical relationship between activation energy (74–76 kJ/mol), process temperature (29–37 °C), and cooling efficiency in optimizing the decomposition process. Significant findings indicate that higher inlet temperatures (37 °C) and lower activation energies (74 kJ/mol) lead to superior conversion rates. The study presents a clear correlation between temperature elevation, reduced activation energy, and enhanced conversion rates, demonstrating that optimizing these parameters can lead to significantly improved conversion efficiencies, potentially approaching 100 % under ideal conditions.

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Publication Details

Journal
Case Studies in Thermal Engineering
Published
2024-08-19
DOI
https://doi.org/10.1016/j.csite.2024.105004
Citations
1
Primary Topic
Catalysis and Oxidation Reactions
Type
article
Field-Weighted Citation Impact
0.11

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article

CFD-aided enhancement of propylene oxide decomposition in a tubular reactor with a corrugated cooling jacket

Ali Jawad Chamkha, Noureddine Kaid, Djelloul Bendaho, Sultan Alqahtani et al.
1 citations
Case Studies in Thermal Engineering
Catalysis and Oxidation Reactions
0.11
article

CFD-aided enhancement of propylene oxide decomposition in a tubular reactor with a corrugated cooling jacket

Ali Jawad Chamkha, Noureddine Kaid, Djelloul Bendaho, Sultan Alqahtani, Younes Menni, Badr M. Alshammari, Lioua Kolsi
article en
1 citations

Abstract

_This research delves into the decomposition kinetics of propylene oxide within a novel reactor design characterized by a corrugated inner wall for enhanced cooling. By applying Computational Fluid Dynamics (CFD), this study aims to optimize the reactor's heat transfer capabilities to achieve precise control over the exothermic decomposition process. This approach addresses a previously unexplored area in CFD application, proposing a model that fine-tunes the decomposition efficiency of propylene oxide by considering the interplay of key parameters such as inlet mixture temperature, activation energy, flow rate, and the resulting thermal profile. The primary goal is to advance the development of more efficient and environmentally friendly chemical processing techniques in the propylene oxide industry. The study highlights the critical relationship between activation energy (74–76 kJ/mol), process temperature (29–37 °C), and cooling efficiency in optimizing the decomposition process. Significant findings indicate that higher inlet temperatures (37 °C) and lower activation energies (74 kJ/mol) lead to superior conversion rates. The study presents a clear correlation between temperature elevation, reduced activation energy, and enhanced conversion rates, demonstrating that optimizing these parameters can lead to significantly improved conversion efficiencies, potentially approaching 100 % under ideal conditions.

Case Studies in Thermal EngineeringVol. 61
Northwest African American Museum (US), Thi Qar University (IQ), University of Ha'il (SA), Biruni University (TR), Kuwait College of Science and Technology (KW), King Khalid University (SA)
King Khalid University
Affordable and clean energy
Openalex Percentile: Top 68%
Catalysis and Oxidation Reactions
0.11
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