Development of a multi-zone adiabatic reactor optimization framework for oxidative coupling of methane

• Introduced a new optimization framework for staged adiabatic reactors using OCM. • Distributed O 2 feeding with interstage cooling improves reactor safety and control. • C 2 yield enhanced 8 times higher with staged reactor zoning and cooling. • Framework can be extended for other highly exothermic catalytic systems. Managing heat is a major challenge for oxidative coupling of methane (OCM) because of its high exothermicity. While recent innovations have mainly focused on reactor design, most studies assume isothermal operation, which is often impractical for scale-up. Adiabatic operation better reflects industrial conditions but remains underexplored. Additionally, little attention has been given to distributing O 2 along the reactor or using interstage cooling to smooth temperature variations inside the OCM reactor and improve performance. In this work, we address those gaps by optimizing a multi-zone reactor design with distribution feeding of O 2 . Using Simulated Annealing, we model up to 30 reactor zones, each treated as a fixed-bed, one-dimensional and pseudo-homogeneous system. Our results show that distributing oxygen across multiple zones with interstage cooling increases the C 2 yield by almost 8 times, from 5.7% in a single zone to 46.5 % across 30 zones, achieving smoother temperature profiles without changing the catalyst.

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Publication Details

Journal
Chemical Engineering Science
Published
2025-11-21
DOI
https://doi.org/10.1016/j.ces.2025.123040
Primary Topic
Catalysis and Oxidation Reactions
Type
article
Field-Weighted Citation Impact
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article

Development of a multi-zone adiabatic reactor optimization framework for oxidative coupling of methane

Chemical Engineering Science
Catalysis and Oxidation Reactions
article

Development of a multi-zone adiabatic reactor optimization framework for oxidative coupling of methane

article en

Abstract

• Introduced a new optimization framework for staged adiabatic reactors using OCM. • Distributed O 2 feeding with interstage cooling improves reactor safety and control. • C 2 yield enhanced 8 times higher with staged reactor zoning and cooling. • Framework can be extended for other highly exothermic catalytic systems. Managing heat is a major challenge for oxidative coupling of methane (OCM) because of its high exothermicity. While recent innovations have mainly focused on reactor design, most studies assume isothermal operation, which is often impractical for scale-up. Adiabatic operation better reflects industrial conditions but remains underexplored. Additionally, little attention has been given to distributing O 2 along the reactor or using interstage cooling to smooth temperature variations inside the OCM reactor and improve performance. In this work, we address those gaps by optimizing a multi-zone reactor design with distribution feeding of O 2 . Using Simulated Annealing, we model up to 30 reactor zones, each treated as a fixed-bed, one-dimensional and pseudo-homogeneous system. Our results show that distributing oxygen across multiple zones with interstage cooling increases the C 2 yield by almost 8 times, from 5.7% in a single zone to 46.5 % across 30 zones, achieving smoother temperature profiles without changing the catalyst.

Chemical Engineering ScienceVol. 322
Hamad bin Khalifa University (QA), Texas A&M University at Qatar (QA), Texas A&M University (US)
Affordable and clean energy
Openalex Percentile: Top 65%
Catalysis and Oxidation Reactions
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