{"title":"通过微流控系统提高吡非尼酮的产量:新颖而全面的化学动力学研究","authors":"","doi":"10.1016/j.cep.2024.109928","DOIUrl":null,"url":null,"abstract":"<div><p>Batch and continuous systems were fabricated to synthesize Pirfenidone (PFD). Effects of parameters on reaction yield including; microreactors, micromixer, solvents, temperature, reaction time, and catalysts were understudied. Moreover, FTIR, NMR and HPLC analyses used to evaluate the prepared PFD. Its yield in microfluidic (30.5 %) was higher than that of batch (17.1 %) reactor. Besides, reaction yield in the presence of DMSO was higher than DMF in both reactors. It was shown that, adding a micromixer enhanced reaction time. leading to a higher PFD yield. Nonetheless, the yield was reduced by enhancing the temperature when DMF was utilized. Additionally, the traditional synthesis method of PFD in a batch system, which reached a yield of 53.7 % after 19 h, now reached 30.5 % in a microreactor under similar conditions within 40 min. Utilizing the Design Expert Software, the results revealed a maximum overall reaction yield of 31 % achieved at reactant ratio of K<sub>2</sub>CO<sub>3</sub> to 2‑hydroxy-5-methylpyridine of 7, Temperature of 160 °C and reaction time of 60 min completely matching the experimental results. Ultimately, kinetics of PFD was understudied incorporating a Molecular Dynamic Software where a new 3-steps mechanism was proposed. Moreover, a power law model revealed an empirical reaction order of 1.45.</p></div>","PeriodicalId":9929,"journal":{"name":"Chemical Engineering and Processing - Process Intensification","volume":null,"pages":null},"PeriodicalIF":3.8000,"publicationDate":"2024-08-04","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Enhanced production of Pirfenidone through a microfluidic system: A novel and thorough chemical kinetics investigation\",\"authors\":\"\",\"doi\":\"10.1016/j.cep.2024.109928\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>Batch and continuous systems were fabricated to synthesize Pirfenidone (PFD). Effects of parameters on reaction yield including; microreactors, micromixer, solvents, temperature, reaction time, and catalysts were understudied. Moreover, FTIR, NMR and HPLC analyses used to evaluate the prepared PFD. Its yield in microfluidic (30.5 %) was higher than that of batch (17.1 %) reactor. Besides, reaction yield in the presence of DMSO was higher than DMF in both reactors. It was shown that, adding a micromixer enhanced reaction time. leading to a higher PFD yield. Nonetheless, the yield was reduced by enhancing the temperature when DMF was utilized. Additionally, the traditional synthesis method of PFD in a batch system, which reached a yield of 53.7 % after 19 h, now reached 30.5 % in a microreactor under similar conditions within 40 min. Utilizing the Design Expert Software, the results revealed a maximum overall reaction yield of 31 % achieved at reactant ratio of K<sub>2</sub>CO<sub>3</sub> to 2‑hydroxy-5-methylpyridine of 7, Temperature of 160 °C and reaction time of 60 min completely matching the experimental results. Ultimately, kinetics of PFD was understudied incorporating a Molecular Dynamic Software where a new 3-steps mechanism was proposed. Moreover, a power law model revealed an empirical reaction order of 1.45.</p></div>\",\"PeriodicalId\":9929,\"journal\":{\"name\":\"Chemical Engineering and Processing - Process Intensification\",\"volume\":null,\"pages\":null},\"PeriodicalIF\":3.8000,\"publicationDate\":\"2024-08-04\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Chemical Engineering and Processing - Process Intensification\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S0255270124002666\",\"RegionNum\":3,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q3\",\"JCRName\":\"ENERGY & FUELS\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemical Engineering and Processing - Process Intensification","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0255270124002666","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"ENERGY & FUELS","Score":null,"Total":0}
Enhanced production of Pirfenidone through a microfluidic system: A novel and thorough chemical kinetics investigation
Batch and continuous systems were fabricated to synthesize Pirfenidone (PFD). Effects of parameters on reaction yield including; microreactors, micromixer, solvents, temperature, reaction time, and catalysts were understudied. Moreover, FTIR, NMR and HPLC analyses used to evaluate the prepared PFD. Its yield in microfluidic (30.5 %) was higher than that of batch (17.1 %) reactor. Besides, reaction yield in the presence of DMSO was higher than DMF in both reactors. It was shown that, adding a micromixer enhanced reaction time. leading to a higher PFD yield. Nonetheless, the yield was reduced by enhancing the temperature when DMF was utilized. Additionally, the traditional synthesis method of PFD in a batch system, which reached a yield of 53.7 % after 19 h, now reached 30.5 % in a microreactor under similar conditions within 40 min. Utilizing the Design Expert Software, the results revealed a maximum overall reaction yield of 31 % achieved at reactant ratio of K2CO3 to 2‑hydroxy-5-methylpyridine of 7, Temperature of 160 °C and reaction time of 60 min completely matching the experimental results. Ultimately, kinetics of PFD was understudied incorporating a Molecular Dynamic Software where a new 3-steps mechanism was proposed. Moreover, a power law model revealed an empirical reaction order of 1.45.
期刊介绍:
Chemical Engineering and Processing: Process Intensification is intended for practicing researchers in industry and academia, working in the field of Process Engineering and related to the subject of Process Intensification.Articles published in the Journal demonstrate how novel discoveries, developments and theories in the field of Process Engineering and in particular Process Intensification may be used for analysis and design of innovative equipment and processing methods with substantially improved sustainability, efficiency and environmental performance.