The oxidation of 2-ethylhexanol (2-EHA) to produce 2-ethylhexanoic acid (2-EHAD) suffers from low efficiency and high energy consumption caused by industrial batch production process. To tackle this challenge, we proposed an AI-assisted design methodology for continuous reactor and process of 2-EHA oxidation to 2-EHAD to enhance problem-solving efficiency. Specifically, a precise reactor surrogate model is developed to accelerate the optimization of reactor internals and enhance the utility of experimental data, thereby overcoming the challenge of scarce continuous oxidation experimental data caused by long operating cycles and oxygen safety concerns. Based on optimal reaction parameters, an economic profit growth of 30% to 40% and carbon emissions reduction of 10% to 50% can be attained compared to traditional batch processes and butyraldehyde processes at the same production level. Our work not only propels continuous process design of alcohol oxidation production processes but also lays the groundwork for their widespread industrial application.
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Univ Paris Cite, CNRS, INSERM, UTCBS Chem & Biol Technol Hlth Grp, F-75006 Paris, France
Novo Nord A S, Novo Nord Pk 1, DK-2760 Malov, DenmarkUniv Paris Cite, CNRS, INSERM, UTCBS Chem & Biol Technol Hlth Grp, F-75006 Paris, France
Rebollo, Rene
Oyoun, Feras
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Univ Paris Cite, CNRS, INSERM, UTCBS Chem & Biol Technol Hlth Grp, F-75006 Paris, FranceUniv Paris Cite, CNRS, INSERM, UTCBS Chem & Biol Technol Hlth Grp, F-75006 Paris, France
Oyoun, Feras
Corvis, Yohann
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Univ Paris Cite, CNRS, INSERM, UTCBS Chem & Biol Technol Hlth Grp, F-75006 Paris, FranceUniv Paris Cite, CNRS, INSERM, UTCBS Chem & Biol Technol Hlth Grp, F-75006 Paris, France
Corvis, Yohann
El-Hammadi, Mazen M.
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Univ Seville, Fac Pharm, Dept Pharm & Pharmaceut Technol, Seville 41012, SpainUniv Paris Cite, CNRS, INSERM, UTCBS Chem & Biol Technol Hlth Grp, F-75006 Paris, France