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Solvent‐Free Hydrogenation of Squalene Using Parts per Million Levels of Palladium Supported on Carbon Nanotubes: Shift from Batch Reactor to Continuous‐Flow System
The transition from batch catalytic processes to continuous flow processes requires highly active and stable catalysts that still need to be developed. The preparation and characterization of catalysts where palladium single atoms and nanoparticles are simultaneously present on carbon nanotubes were...
Autores principales: | , , , , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
John Wiley and Sons Inc.
2022
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9804222/ https://www.ncbi.nlm.nih.gov/pubmed/35880580 http://dx.doi.org/10.1002/cssc.202200916 |
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author | Guicheret, Boris Vanoye, Laurent Rivera‐Cárcamo, Camila de Bellefon, Claude Serp, Philippe Philippe, Régis Favre‐Réguillon, Alain |
author_facet | Guicheret, Boris Vanoye, Laurent Rivera‐Cárcamo, Camila de Bellefon, Claude Serp, Philippe Philippe, Régis Favre‐Réguillon, Alain |
author_sort | Guicheret, Boris |
collection | PubMed |
description | The transition from batch catalytic processes to continuous flow processes requires highly active and stable catalysts that still need to be developed. The preparation and characterization of catalysts where palladium single atoms and nanoparticles are simultaneously present on carbon nanotubes were recently reported by us. These catalysts are considerably more active than commercial or previously described catalysts for the liquid phase hydrogenation of terpenes. Herein is shown that under solvent‐free conditions, squalene (SQE) could be converted into squalane (SQA,>98 %) using only 300 ppm of Pd in less than 1.4 h at 20 bar H(2) and 120 °C. Catalyst stability was assessed in a lab‐scale flow reactor, and long‐term experiments led to turnover number (TON) higher than 300000 without any detectable loss in the activity. Then, the implementation of this catalyst in a commercial intensified continuous‐flow milli‐reactor pilot was achieved. High purity SQA (>98 %) could be obtained by continuous hydrogenation of solvent‐free SQE at 180 °C and 30 bar H(2) with a contact time below 15 min. A production capacity of 3.6 kg per day of SQA could be obtained with an effective reactor volume (V (R)) of 43.2 mL for this complex 3 phase reaction. Large‐scale production can now be foreseen thanks to seamless scale‐up provided by the continuous flow pilot supplier. |
format | Online Article Text |
id | pubmed-9804222 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2022 |
publisher | John Wiley and Sons Inc. |
record_format | MEDLINE/PubMed |
spelling | pubmed-98042222023-01-03 Solvent‐Free Hydrogenation of Squalene Using Parts per Million Levels of Palladium Supported on Carbon Nanotubes: Shift from Batch Reactor to Continuous‐Flow System Guicheret, Boris Vanoye, Laurent Rivera‐Cárcamo, Camila de Bellefon, Claude Serp, Philippe Philippe, Régis Favre‐Réguillon, Alain ChemSusChem Research Articles The transition from batch catalytic processes to continuous flow processes requires highly active and stable catalysts that still need to be developed. The preparation and characterization of catalysts where palladium single atoms and nanoparticles are simultaneously present on carbon nanotubes were recently reported by us. These catalysts are considerably more active than commercial or previously described catalysts for the liquid phase hydrogenation of terpenes. Herein is shown that under solvent‐free conditions, squalene (SQE) could be converted into squalane (SQA,>98 %) using only 300 ppm of Pd in less than 1.4 h at 20 bar H(2) and 120 °C. Catalyst stability was assessed in a lab‐scale flow reactor, and long‐term experiments led to turnover number (TON) higher than 300000 without any detectable loss in the activity. Then, the implementation of this catalyst in a commercial intensified continuous‐flow milli‐reactor pilot was achieved. High purity SQA (>98 %) could be obtained by continuous hydrogenation of solvent‐free SQE at 180 °C and 30 bar H(2) with a contact time below 15 min. A production capacity of 3.6 kg per day of SQA could be obtained with an effective reactor volume (V (R)) of 43.2 mL for this complex 3 phase reaction. Large‐scale production can now be foreseen thanks to seamless scale‐up provided by the continuous flow pilot supplier. John Wiley and Sons Inc. 2022-08-25 2022-10-10 /pmc/articles/PMC9804222/ /pubmed/35880580 http://dx.doi.org/10.1002/cssc.202200916 Text en © 2022 The Authors. ChemSusChem published by Wiley-VCH GmbH https://creativecommons.org/licenses/by-nc-nd/4.0/This is an open access article under the terms of the http://creativecommons.org/licenses/by-nc-nd/4.0/ (https://creativecommons.org/licenses/by-nc-nd/4.0/) License, which permits use and distribution in any medium, provided the original work is properly cited, the use is non‐commercial and no modifications or adaptations are made. |
spellingShingle | Research Articles Guicheret, Boris Vanoye, Laurent Rivera‐Cárcamo, Camila de Bellefon, Claude Serp, Philippe Philippe, Régis Favre‐Réguillon, Alain Solvent‐Free Hydrogenation of Squalene Using Parts per Million Levels of Palladium Supported on Carbon Nanotubes: Shift from Batch Reactor to Continuous‐Flow System |
title | Solvent‐Free Hydrogenation of Squalene Using Parts per Million Levels of Palladium Supported on Carbon Nanotubes: Shift from Batch Reactor to Continuous‐Flow System |
title_full | Solvent‐Free Hydrogenation of Squalene Using Parts per Million Levels of Palladium Supported on Carbon Nanotubes: Shift from Batch Reactor to Continuous‐Flow System |
title_fullStr | Solvent‐Free Hydrogenation of Squalene Using Parts per Million Levels of Palladium Supported on Carbon Nanotubes: Shift from Batch Reactor to Continuous‐Flow System |
title_full_unstemmed | Solvent‐Free Hydrogenation of Squalene Using Parts per Million Levels of Palladium Supported on Carbon Nanotubes: Shift from Batch Reactor to Continuous‐Flow System |
title_short | Solvent‐Free Hydrogenation of Squalene Using Parts per Million Levels of Palladium Supported on Carbon Nanotubes: Shift from Batch Reactor to Continuous‐Flow System |
title_sort | solvent‐free hydrogenation of squalene using parts per million levels of palladium supported on carbon nanotubes: shift from batch reactor to continuous‐flow system |
topic | Research Articles |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9804222/ https://www.ncbi.nlm.nih.gov/pubmed/35880580 http://dx.doi.org/10.1002/cssc.202200916 |
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