| dc.contributor | Universitat Ramon Llull. IQS | |
| dc.contributor.author | Barozzi, Marco | |
| dc.contributor.author | FERNANDEZ, JAVIER | |
| dc.contributor.author | Berzosa, Xavier | |
| dc.contributor.author | Sempere, Julián | |
| dc.contributor.author | Di Tomaso, Saverio | |
| dc.contributor.author | Copelli, Sabrina | |
| dc.date.accessioned | 2025-12-04T15:08:56Z | |
| dc.date.available | 2025-12-04T15:08:56Z | |
| dc.date.issued | 2025-11 | |
| dc.identifier.issn | 2666-8211 | ca |
| dc.identifier.uri | http://hdl.handle.net/20.500.14342/5665 | |
| dc.description.abstract | The synthesis of active pharmaceutical ingredients (APIs) traditionally relies on batch reactors, which often exhibit challenges in terms of both selectivity and heat transfer control. This study investigated the Aza-Michael addition between methylamine and 2-vinylpyridine to synthetize betahistine, an analogue of histamine, converting a traditional batch process into a continuous flow reaction. The aim of the study was to define an intensification protocol capable of identifying optimized operating conditions to maximise betahistine production. A dedicated experimental setup was developed using a custom-built PTFE-based tubular microreactor which allowed for an optimal control of pressure, temperature, residence time, and reactants molar ratio. Analytical characterization was performed using both UHPLC and H-NMR. Process intensification was achieved using two different approaches: a traditional one, based on deterministic mathematical models to simulate the chemical reactions involved, and a modern approach based on Feedforward Neural Networks. The highest selectivity experimentally observed was approximately 82% at a 2:1 methylamine to 2-vinylpyridine ratio and 150°C, with a residence time of 4 minutes. Both optimizing approaches lead to the same results, confirming the advantages of using suitable intensification protocols for shifting to continuous flow batch processes, especially in pharmaceutical synthesis. | ca |
| dc.format.extent | p.17 | ca |
| dc.language.iso | eng | ca |
| dc.publisher | Elsevier | ca |
| dc.relation.ispartof | Chemical Engineering Journal Advances 2025, 24 | ca |
| dc.rights | © L'autor/a | ca |
| dc.rights | Attribution-NonCommercial-NoDerivatives 4.0 International | ca |
| dc.rights.uri | http://creativecommons.org/licenses/by-nc-nd/4.0/ | * |
| dc.subject.other | Flow chemistry | ca |
| dc.subject.other | Aza-Michael addition | ca |
| dc.subject.other | Betahistine | ca |
| dc.subject.other | Continuous flow processing | ca |
| dc.subject.other | Runaway reactions | ca |
| dc.subject.other | AI-driven intensification | ca |
| dc.subject.other | Pharmaceutical synthesis | ca |
| dc.subject.other | Química | ca |
| dc.subject.other | Reaccions d'addició | ca |
| dc.title | A simple AI-driven process intensification protocol for active pharmaceutical ingredients synthesis | ca |
| dc.type | info:eu-repo/semantics/article | ca |
| dc.rights.accessLevel | info:eu-repo/semantics/openAccess | |
| dc.embargo.terms | cap | ca |
| dc.subject.udc | 54 | ca |
| dc.identifier.doi | https://doi.org/10.1016/j.ceja.2025.100905 | ca |
| dc.description.version | info:eu-repo/semantics/publishedVersion | ca |