Patrycja Roszkowska, Abbie M. Scholes, James L. Walsh, Timothy L. Easun and Anna G. Slater
Macrocycles are candidates for wide-ranging applications, yet their synthesis can be low-yielding, poorly reproducible, and resource-intensive, limiting their use. Here, we explore the use of Non-Thermal Plasma (NTP) as an efficient method for the synthesis of imine macrocycles at the gram scale. NTP-mediated macrocyclisations consistently achieved high yields of up to 97% in reduced reaction times compared to the standard non-plasma method, and were successfully carried out with a range of different aldehyde substrates. Control experiments were performed to explore the origin of the observed improvements. The results indicate that NTP methods could be advantageous for macrocycle synthesis, particularly for substrates that are sensitive to elevated temperature, and other materials formed via imine condensation.
{"title":"High-efficiency non-thermal plasma synthesis of imine macrocycles†","authors":"Patrycja Roszkowska, Abbie M. Scholes, James L. Walsh, Timothy L. Easun and Anna G. Slater","doi":"10.1039/D4RE00061G","DOIUrl":"10.1039/D4RE00061G","url":null,"abstract":"<p >Macrocycles are candidates for wide-ranging applications, yet their synthesis can be low-yielding, poorly reproducible, and resource-intensive, limiting their use. Here, we explore the use of Non-Thermal Plasma (NTP) as an efficient method for the synthesis of imine macrocycles at the gram scale. NTP-mediated macrocyclisations consistently achieved high yields of up to 97% in reduced reaction times compared to the standard non-plasma method, and were successfully carried out with a range of different aldehyde substrates. Control experiments were performed to explore the origin of the observed improvements. The results indicate that NTP methods could be advantageous for macrocycle synthesis, particularly for substrates that are sensitive to elevated temperature, and other materials formed <em>via</em> imine condensation.</p>","PeriodicalId":101,"journal":{"name":"Reaction Chemistry & Engineering","volume":null,"pages":null},"PeriodicalIF":3.4,"publicationDate":"2024-04-08","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.rsc.org/en/content/articlepdf/2024/re/d4re00061g?page=search","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"140579739","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Huifen Kang, Xintong Guo, Mei An, Conghua Ma, Guozhang Chang, Qingjie Guo and Jingjing Ma
The effects of Ca and Fe of a bimetallic Ca–Fe catalyst when applied to pine sawdust pyrolysis were investigated by thermogravimetry-mass spectrometry. Trials were also performed using heterotopic Ca–Fe and HZSM-5 to catalyse the degradation of pine sawdust to produce aromatic hydrocarbons, employing a fixed bed reactor and gas chromatography-mass spectrometry. The presence of CaO was found to promote deoxygenation while Fe enhanced in situ hydrogen supply, whereas the Ca–Fe catalyst combined these effects. This material promoted the formation of low-oxygen compounds to generate precursors that were transformed into aromatics via HZSM-5. Up to 90.47% aromatic proportion and a 31.02 mg g−1 benzene/toluene/ethylbenzene/xylene yield were obtained at 600 °C using a 1 : 1 mass ratio of Ca–Fe to HZSM-5 and a 2 : 1 mass ratio of catalysts to pine sawdust. This combination of catalysts is evidently an effective means of strengthening the pyrolysis of pine sawdust to produce aromatic hydrocarbons.
通过热重-质谱法研究了双金属 Ca-Fe 催化剂的 Ca 和 Fe 对松木锯屑热解的影响。此外,还采用固定床反应器和气相色谱-质谱法,对异位 Ca-Fe 和 HZSM-5 催化松木锯屑降解生成芳香烃进行了试验。研究发现,CaO 的存在促进了脱氧,而 Fe 则增强了原位供氢,而 Ca-Fe 催化剂则综合了这些作用。这种材料可促进低氧化合物的形成,从而生成前体,并通过 HZSM-5 转化为芳烃。在 600 °C 温度下,使用 1 . 1 质量比的 Ca-Fe 与 HZSM-5 催化剂,可获得高达 90.47% 的芳烃比例和 31.02 mg g-1 的苯/甲苯/乙苯/二甲苯产量:在 600 °C 条件下,使用 Ca-Fe 与 HZSM-5 的质量比为 1 : 1,催化剂与松木的质量比为 2 :催化剂与松木锯屑的质量比为 2:1。这种催化剂组合显然是加强松木锯屑热解生成芳香烃的有效方法。
{"title":"Catalytic degradation of pine sawdust over heterotopic Ca–Fe and HZSM-5 to produce aromatic hydrocarbons†","authors":"Huifen Kang, Xintong Guo, Mei An, Conghua Ma, Guozhang Chang, Qingjie Guo and Jingjing Ma","doi":"10.1039/D3RE00572K","DOIUrl":"10.1039/D3RE00572K","url":null,"abstract":"<p >The effects of Ca and Fe of a bimetallic Ca–Fe catalyst when applied to pine sawdust pyrolysis were investigated by thermogravimetry-mass spectrometry. Trials were also performed using heterotopic Ca–Fe and HZSM-5 to catalyse the degradation of pine sawdust to produce aromatic hydrocarbons, employing a fixed bed reactor and gas chromatography-mass spectrometry. The presence of CaO was found to promote deoxygenation while Fe enhanced <em>in situ</em> hydrogen supply, whereas the Ca–Fe catalyst combined these effects. This material promoted the formation of low-oxygen compounds to generate precursors that were transformed into aromatics <em>via</em> HZSM-5. Up to 90.47% aromatic proportion and a 31.02 mg g<small><sup>−1</sup></small> benzene/toluene/ethylbenzene/xylene yield were obtained at 600 °C using a 1 : 1 mass ratio of Ca–Fe to HZSM-5 and a 2 : 1 mass ratio of catalysts to pine sawdust. This combination of catalysts is evidently an effective means of strengthening the pyrolysis of pine sawdust to produce aromatic hydrocarbons.</p>","PeriodicalId":101,"journal":{"name":"Reaction Chemistry & Engineering","volume":null,"pages":null},"PeriodicalIF":3.4,"publicationDate":"2024-04-08","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"140579684","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Soritz S., Sommitsch A., Irndorfer S., Brouczek D., Schwentenwein M., Priestley I. J. G., Iosub A. V., Krieger J. P. and Gruber-Woelfler H.
Measuring the thermokinetic data of chemical reactions is an important part for chemical process development. However, some reactions are very sensitive to the presence of metals, limiting the use of standard materials for calorimeters. In this work we present a flow calorimeter employing a 3D printed ceramic reactor plate for the measurement of metal-sensitive reactions. The calorimeter was characterized by residence time measurements aided by mixing simulations, and was validated via a standard neutralization reaction, an aggressive nitration reaction, and a binary solvent system for mixing enthalpy, before being used for a nitrosylation reaction featuring a metal sensitive product.
测量化学反应的热动力学数据是化学工艺开发的重要组成部分。然而,有些反应对金属的存在非常敏感,从而限制了热量计标准材料的使用。在这项工作中,我们介绍了一种采用 3D 打印陶瓷反应板的流动量热计,用于测量对金属敏感的反应。该量热计通过混合模拟辅助的停留时间测量进行表征,并通过标准中和反应、强硝化反应和二元溶剂系统的混合焓进行验证,然后用于以金属敏感产物为特征的亚硝化反应。
{"title":"Thermokinetic analyses of metal-sensitive reactions in a ceramic flow calorimeter","authors":"Soritz S., Sommitsch A., Irndorfer S., Brouczek D., Schwentenwein M., Priestley I. J. G., Iosub A. V., Krieger J. P. and Gruber-Woelfler H.","doi":"10.1039/D4RE00014E","DOIUrl":"10.1039/D4RE00014E","url":null,"abstract":"<p >Measuring the thermokinetic data of chemical reactions is an important part for chemical process development. However, some reactions are very sensitive to the presence of metals, limiting the use of standard materials for calorimeters. In this work we present a flow calorimeter employing a 3D printed ceramic reactor plate for the measurement of metal-sensitive reactions. The calorimeter was characterized by residence time measurements aided by mixing simulations, and was validated <em>via</em> a standard neutralization reaction, an aggressive nitration reaction, and a binary solvent system for mixing enthalpy, before being used for a nitrosylation reaction featuring a metal sensitive product.</p>","PeriodicalId":101,"journal":{"name":"Reaction Chemistry & Engineering","volume":null,"pages":null},"PeriodicalIF":3.4,"publicationDate":"2024-04-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.rsc.org/en/content/articlepdf/2024/re/d4re00014e?page=search","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"140579690","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Teta Fathya Widawati, Muhammad Fuad Refki, Rochmadi, Joko Wintoko and Arief Budiman
Indonesia, renowned for its tropical marine environments, boasts a rich diversity of macroalgae, with Sargassum being a major contributor. Currently, the primary application of Sargassum revolves around alginate extraction, prompting a systematic exploration of alternative end-products for optimal utilization. Thermochemical conversion of Sargassum into bio-oil, biochar, and gas, particularly through microwave-assisted pyrolysis (MAP), emerges as a promising avenue. MAP, distinguished by its energy-efficient process and high heating rate, stands as a viable alternative to conventional pyrolysis. A thorough feasibility analysis of MAP, incorporating kinetic studies and bio-oil characterization, revealed that particle sizes of 40–70 mesh exhibited the highest reaction rates. Sensitivity tests validated the reliability of kinetic parameters (A and Ea) obtained from MATLAB 2016b, confirming their suitability for scaling-up purposes. These findings underscore the potential of MAP compared to conventional pyrolysis, driven by its rapid heating rates. The resulting bio-oil, with a pH of 8, comprised carboxylic acids and aliphatic, cyclic aliphatic, and aromatic compounds, along with sterols and polyaromatic derivatives that can be further utilized particularly as building blocks and end-products in chemical industries. However, it is crucial to note that the bio-oil poses challenges in the upgrading process to transform it into fuel.
{"title":"Comprehensive study of lumped kinetic models and bio-oil characterization in microwave-assisted pyrolysis of Sargassum sp.†","authors":"Teta Fathya Widawati, Muhammad Fuad Refki, Rochmadi, Joko Wintoko and Arief Budiman","doi":"10.1039/D3RE00674C","DOIUrl":"10.1039/D3RE00674C","url":null,"abstract":"<p >Indonesia, renowned for its tropical marine environments, boasts a rich diversity of macroalgae, with <em>Sargassum</em> being a major contributor. Currently, the primary application of <em>Sargassum</em> revolves around alginate extraction, prompting a systematic exploration of alternative end-products for optimal utilization. Thermochemical conversion of <em>Sargassum</em> into bio-oil, biochar, and gas, particularly through microwave-assisted pyrolysis (MAP), emerges as a promising avenue. MAP, distinguished by its energy-efficient process and high heating rate, stands as a viable alternative to conventional pyrolysis. A thorough feasibility analysis of MAP, incorporating kinetic studies and bio-oil characterization, revealed that particle sizes of 40–70 mesh exhibited the highest reaction rates. Sensitivity tests validated the reliability of kinetic parameters (<em>A</em> and <em>E</em><small><sub>a</sub></small>) obtained from MATLAB 2016b, confirming their suitability for scaling-up purposes. These findings underscore the potential of MAP compared to conventional pyrolysis, driven by its rapid heating rates. The resulting bio-oil, with a pH of 8, comprised carboxylic acids and aliphatic, cyclic aliphatic, and aromatic compounds, along with sterols and polyaromatic derivatives that can be further utilized particularly as building blocks and end-products in chemical industries. However, it is crucial to note that the bio-oil poses challenges in the upgrading process to transform it into fuel.</p>","PeriodicalId":101,"journal":{"name":"Reaction Chemistry & Engineering","volume":null,"pages":null},"PeriodicalIF":3.4,"publicationDate":"2024-04-04","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"140579860","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Egor N. Boronin, Milena M. Svetlakova, Ilya I. Vorobyov, Yulia B. Malysheva, Yuri V. Polushtaytsev, Sergey N. Mensov, Andrey V. Vorotyntsev, Alexey Yu. Fedorov, Timothy Noël and Alexander V. Nyuchev
C–N bond formation plays a crucial role in various chemical synthesis processes in both the chemical industry and nature. While numerous methods have been developed for the formation of C–N bonds, only a few meet the criteria of “green chemistry”. In this study, we present a continuous-flow procedure for the decyanative N-heteroarylation of anilines and secondary alicyclic amines using a photoorganocatalytic reaction. Through the synergistic combination of photochemistry, organocatalysis, and continuous-flow technology, we were able to achieve high and close to quantitative yields, while significantly reducing the reaction time from 12 hours in batch procedures to just 1 hour in continuous-flow conditions.
{"title":"Photochemical organocatalytic heteroarylation of anilines and secondary alicyclic amines in continuous-flow†","authors":"Egor N. Boronin, Milena M. Svetlakova, Ilya I. Vorobyov, Yulia B. Malysheva, Yuri V. Polushtaytsev, Sergey N. Mensov, Andrey V. Vorotyntsev, Alexey Yu. Fedorov, Timothy Noël and Alexander V. Nyuchev","doi":"10.1039/D4RE00130C","DOIUrl":"10.1039/D4RE00130C","url":null,"abstract":"<p >C–N bond formation plays a crucial role in various chemical synthesis processes in both the chemical industry and nature. While numerous methods have been developed for the formation of C–N bonds, only a few meet the criteria of “green chemistry”. In this study, we present a continuous-flow procedure for the decyanative <em>N</em>-heteroarylation of anilines and secondary alicyclic amines using a photoorganocatalytic reaction. Through the synergistic combination of photochemistry, organocatalysis, and continuous-flow technology, we were able to achieve high and close to quantitative yields, while significantly reducing the reaction time from 12 hours in batch procedures to just 1 hour in continuous-flow conditions.</p>","PeriodicalId":101,"journal":{"name":"Reaction Chemistry & Engineering","volume":null,"pages":null},"PeriodicalIF":3.4,"publicationDate":"2024-04-03","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"140579859","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Zhihui Wang, Wenbo Li, Xinyao Fu, Chen Zhang, Wei Zhang, Long Huang and Cuiqing Li
The conversion of biomass-derived furfuryl alcohol into 1,2-pentanediol, a high-value fine chemical with wide applications, is of high research and commercial value. In this study, Ce-doped CuCeMgAl mixed metal oxide catalysts were synthesized using layered double hydroxides as the precursor. Characterization techniques including BET, XRD, XPS, TPR and TPD were used to study the structure and physiochemical properties of synthesized catalysts. In furfuryl alcohol hydrogenolysis, CuCeMgAl catalysts showed higher furfuryl alcohol conversion and higher 1,2-pentanediol yield than the CuMgAl sample, likely due to more metal active sites and higher concentration of basic sites. Furthermore, reduction temperature, an important parameter for MMO-type catalysts, was studied for its effect on catalyst activity. It is found that basic site concentration is affected by reduction temperatures, leading to distinct activity for CuCeMgAl catalysts. With lower reduction temperatures, the activity of CuCeMgAl catalysts could be further increased, demonstrating the importance of reduction parameters for Cu-based mixed metal oxide catalysts.
{"title":"Hydrogenolysis of furfuryl alcohol over CuCeMgAl mixed metal oxide catalysts derived from layered double hydroxides†","authors":"Zhihui Wang, Wenbo Li, Xinyao Fu, Chen Zhang, Wei Zhang, Long Huang and Cuiqing Li","doi":"10.1039/D4RE00070F","DOIUrl":"10.1039/D4RE00070F","url":null,"abstract":"<p >The conversion of biomass-derived furfuryl alcohol into 1,2-pentanediol, a high-value fine chemical with wide applications, is of high research and commercial value. In this study, Ce-doped CuCeMgAl mixed metal oxide catalysts were synthesized using layered double hydroxides as the precursor. Characterization techniques including BET, XRD, XPS, TPR and TPD were used to study the structure and physiochemical properties of synthesized catalysts. In furfuryl alcohol hydrogenolysis, CuCeMgAl catalysts showed higher furfuryl alcohol conversion and higher 1,2-pentanediol yield than the CuMgAl sample, likely due to more metal active sites and higher concentration of basic sites. Furthermore, reduction temperature, an important parameter for MMO-type catalysts, was studied for its effect on catalyst activity. It is found that basic site concentration is affected by reduction temperatures, leading to distinct activity for CuCeMgAl catalysts. With lower reduction temperatures, the activity of CuCeMgAl catalysts could be further increased, demonstrating the importance of reduction parameters for Cu-based mixed metal oxide catalysts.</p>","PeriodicalId":101,"journal":{"name":"Reaction Chemistry & Engineering","volume":null,"pages":null},"PeriodicalIF":3.4,"publicationDate":"2024-04-02","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"140579698","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Christian Mark Salvador, Jason M. Richards, Shannon M. Mahurin, Meng-Dawn Cheng and Joshua A. Hubbard
The reaction pathway of hydrolysis of UF6 to form UO2F2 particles is an essential insight in nuclear fuel processing; however, it is still limited to theoretical calculations. Herein, we present the identification of the intermediates and products using various gas precursor concentrations and molecular beam mass spectrometer (MBMS). Compounds containing different uranium atom counts were identified by exposing 300 and 2323 ppm water to 200 ppm UF6. Non-uranium compounds (e.g., (HF)3(H2O)H, (HF)4H, and (H2O)2(HF)3) dominate the mass spectra in terms of absolute signal intensity. These compounds were dependent on the initial concentration of UF6 based on the linear relationship observed between products and gas reactant. Uranium compounds were characterized by UF6, UO3, and UO2F2 core molecules, with each species existing predominantly in a certain water concentration. Monomeric compounds (e.g., UF6(HF)2(H2O)7, UO2F2(HF)7H, and UO2F2(HF)5(H2O)3) or species with one uranium atom had high fluorine to uranium ratio (F/U) due to several HF units bonded with the uranium core. Dimeric (e.g. (UO2F2)2(H2O) and (UF6)2(H2O)4(HF)3H) and trimeric (e.g., (UO3)(UO2F2)2(HF)(H2O)3 and (UO2F2)2UF6H2F) compounds persisted in high masses with low F/U and H/U ratios. Moreover, ramping of UF6 concentration (50–231 ppm) at fixed water content (1.3% Rh or 300 ppm) showed different trends among 949 ions, with some following consistently with molecular identification (e.g., (UO3)3(HF)2(H2O)H). Overall, this study provided important information regarding the formation pathway of UO2F2
{"title":"Determination of intermediates and products of the uranyl aerosol formation in UF6 hydrolysis in the gas phase†","authors":"Christian Mark Salvador, Jason M. Richards, Shannon M. Mahurin, Meng-Dawn Cheng and Joshua A. Hubbard","doi":"10.1039/D3RE00665D","DOIUrl":"10.1039/D3RE00665D","url":null,"abstract":"<p >The reaction pathway of hydrolysis of UF<small><sub>6</sub></small> to form UO<small><sub>2</sub></small>F<small><sub>2</sub></small> particles is an essential insight in nuclear fuel processing; however, it is still limited to theoretical calculations. Herein, we present the identification of the intermediates and products using various gas precursor concentrations and molecular beam mass spectrometer (MBMS). Compounds containing different uranium atom counts were identified by exposing 300 and 2323 ppm water to 200 ppm UF<small><sub>6</sub></small>. Non-uranium compounds (<em>e.g.</em>, (HF)<small><sub>3</sub></small>(H<small><sub>2</sub></small>O)H, (HF)<small><sub>4</sub></small>H, and (H<small><sub>2</sub></small>O)<small><sub>2</sub></small>(HF)<small><sub>3</sub></small>) dominate the mass spectra in terms of absolute signal intensity. These compounds were dependent on the initial concentration of UF<small><sub>6</sub></small> based on the linear relationship observed between products and gas reactant. Uranium compounds were characterized by UF<small><sub>6</sub></small>, UO<small><sub>3</sub></small>, and UO<small><sub>2</sub></small>F<small><sub>2</sub></small> core molecules, with each species existing predominantly in a certain water concentration. Monomeric compounds (<em>e.g.</em>, UF<small><sub>6</sub></small>(HF)<small><sub>2</sub></small>(H<small><sub>2</sub></small>O)<small><sub>7</sub></small>, UO<small><sub>2</sub></small>F<small><sub>2</sub></small>(HF)<small><sub>7</sub></small>H, and UO<small><sub>2</sub></small>F<small><sub>2</sub></small>(HF)<small><sub>5</sub></small>(H<small><sub>2</sub></small>O)<small><sub>3</sub></small>) or species with one uranium atom had high fluorine to uranium ratio (F/U) due to several HF units bonded with the uranium core. Dimeric (<em>e.g.</em> (UO<small><sub>2</sub></small>F<small><sub>2</sub></small>)<small><sub>2</sub></small>(H<small><sub>2</sub></small>O) and (UF<small><sub>6</sub></small>)<small><sub>2</sub></small>(H<small><sub>2</sub></small>O)4(HF)<small><sub>3</sub></small>H) and trimeric (<em>e.g.</em>, (UO<small><sub>3</sub></small>)(UO<small><sub>2</sub></small>F<small><sub>2</sub></small>)<small><sub>2</sub></small>(HF)(H<small><sub>2</sub></small>O)<small><sub>3</sub></small> and (UO<small><sub>2</sub></small>F<small><sub>2</sub></small>)<small><sub>2</sub></small>UF<small><sub>6</sub></small>H<small><sub>2</sub></small>F) compounds persisted in high masses with low F/U and H/U ratios. Moreover, ramping of UF<small><sub>6</sub></small> concentration (50–231 ppm) at fixed water content (1.3% Rh or 300 ppm) showed different trends among 949 ions, with some following consistently with molecular identification (<em>e.g.</em>, (UO<small><sub>3</sub></small>)<small><sub>3</sub></small>(HF)<small><sub>2</sub></small>(H<small><sub>2</sub></small>O)H). Overall, this study provided important information regarding the formation pathway of UO<small><sub>2</sub></small>F<small><sub>2</s","PeriodicalId":101,"journal":{"name":"Reaction Chemistry & Engineering","volume":null,"pages":null},"PeriodicalIF":3.4,"publicationDate":"2024-04-02","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.rsc.org/en/content/articlepdf/2024/re/d3re00665d?page=search","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"140579689","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Florian Gaulhofer, Markus Metzger, Alexander Peschl and Dirk Ziegenbalg
The importance of mixing in photoreactors along the direction of light propagation for competitive photochemical reactions is experimentally demonstrated in the MISCOP mini-plant photoreactor. The installation of customized static mixers improved the photonic efficiency of the photochemical ring-opening isomerization of 1,3,3-trimethylindolino-6′-nitrobenzopyrylospirane by a factor of 2.4, which could be related to the improved mass transport. This knowledge enables future scaling of photoreactions in multi-lamp reactors.
{"title":"Enhancing mass transport to accelerate photoreactions and enable scale-up†","authors":"Florian Gaulhofer, Markus Metzger, Alexander Peschl and Dirk Ziegenbalg","doi":"10.1039/D3RE00689A","DOIUrl":"10.1039/D3RE00689A","url":null,"abstract":"<p >The importance of mixing in photoreactors along the direction of light propagation for competitive photochemical reactions is experimentally demonstrated in the MISCOP mini-plant photoreactor. The installation of customized static mixers improved the photonic efficiency of the photochemical ring-opening isomerization of 1,3,3-trimethylindolino-6′-nitrobenzopyrylospirane by a factor of 2.4, which could be related to the improved mass transport. This knowledge enables future scaling of photoreactions in multi-lamp reactors.</p>","PeriodicalId":101,"journal":{"name":"Reaction Chemistry & Engineering","volume":null,"pages":null},"PeriodicalIF":3.4,"publicationDate":"2024-03-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.rsc.org/en/content/articlepdf/2024/re/d3re00689a?page=search","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"140325261","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Emmanuel Agunloye, Panagiotis Petsagkourakis, Muhammad Yusuf, Ricardo Labes, Thomas Chamberlain, Frans L. Muller, Richard A. Bourne and Federico Galvanin
Industry 4.0 has birthed a new era for the chemical manufacturing sector, transforming reactor design and integrating digital twin into process control. To bridge the gap between autonomous chemistry development, on-demand manufacturing and real-time optimization, we developed a cloud-based platform driven by model-based design of experiment (MBDoE) algorithms integrated in a simulation software for model identification (SimBot) to remotely coordinate a smart flow reactor, also known as the LabBot, sited in a different location. With real-time data and setpoints synchronization, MBDoE was able to identify kinetic models using a limited number of experimental runs. Within this platform, two pharmaceutically relevant syntheses were investigated as case studies: amide formation and nucleophilic aromatic substitution. A new kinetic model providing statistically adequate data description within the whole investigated experimental design space was identified for the amide formation reaction. The model for the nucleophilic aromatic substitution with a well-known but complex mechanism was accurately identified ensuring a statistically precise estimation of kinetic parameters.
{"title":"Automated kinetic model identification via cloud services using model-based design of experiments†","authors":"Emmanuel Agunloye, Panagiotis Petsagkourakis, Muhammad Yusuf, Ricardo Labes, Thomas Chamberlain, Frans L. Muller, Richard A. Bourne and Federico Galvanin","doi":"10.1039/D4RE00047A","DOIUrl":"10.1039/D4RE00047A","url":null,"abstract":"<p >Industry 4.0 has birthed a new era for the chemical manufacturing sector, transforming reactor design and integrating digital twin into process control. To bridge the gap between autonomous chemistry development, on-demand manufacturing and real-time optimization, we developed a cloud-based platform driven by model-based design of experiment (MBDoE) algorithms integrated in a simulation software for model identification (SimBot) to remotely coordinate a smart flow reactor, also known as the LabBot, sited in a different location. With real-time data and setpoints synchronization, MBDoE was able to identify kinetic models using a limited number of experimental runs. Within this platform, two pharmaceutically relevant syntheses were investigated as case studies: amide formation and nucleophilic aromatic substitution. A new kinetic model providing statistically adequate data description within the whole investigated experimental design space was identified for the amide formation reaction. The model for the nucleophilic aromatic substitution with a well-known but complex mechanism was accurately identified ensuring a statistically precise estimation of kinetic parameters.</p>","PeriodicalId":101,"journal":{"name":"Reaction Chemistry & Engineering","volume":null,"pages":null},"PeriodicalIF":3.4,"publicationDate":"2024-03-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.rsc.org/en/content/articlepdf/2024/re/d4re00047a?page=search","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"140314018","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
An additive manufacturing method (digital light procession) is proposed to fabricate carbon-based monolithic catalysts and is applied to nitrobenzene (NB) hydrogenation in a packed-bed micro-reactor. The geometric model of the integrated catalyst is gyroid, a triply periodic minimal surface structure without a dead zone and a large surface area. Compared with particle catalysts, monolithic catalysts have higher porosity and regular pore structure, which can achieve better conversion and selectivity in hydrogenation reactions at high flow rates. The flow characteristics of the monolithic catalyst in the packed-bed micro-reactor were compared between gas–liquid upward and gas–liquid downward flow. It was found that, in the reactor with an inner diameter of 12 mm, the downward gas–liquid process exhibits Taylor flow characteristics, while the upward process for gas–liquid shows bubble flow. Both modes exhibit higher activity in the NB hydrogenation reaction compared with that reported in the literature. Under room temperature and pressure, the gas flow rate was 0.6 mL min−1 and the liquid flow rate was 15 mL min−1, and the gas–liquid downward residence time was 0.83 min. The conversion reached 99% and the selectivity was 98.2%. The three-dimensional printed carbon-based monolithic catalyst has a hierarchical porous structure and a large specific surface area, which can effectively enhance organic hydrogenation reactions.
{"title":"Novel TPMS carbon-based monolithic catalysts by three-dimensional printing for enhancement of nitrobenzene hydrogenation reaction","authors":"Haoyang Wang, Haoran Tian, Qi Zhang and Li Zhang","doi":"10.1039/D4RE00049H","DOIUrl":"10.1039/D4RE00049H","url":null,"abstract":"<p >An additive manufacturing method (digital light procession) is proposed to fabricate carbon-based monolithic catalysts and is applied to nitrobenzene (NB) hydrogenation in a packed-bed micro-reactor. The geometric model of the integrated catalyst is gyroid, a triply periodic minimal surface structure without a dead zone and a large surface area. Compared with particle catalysts, monolithic catalysts have higher porosity and regular pore structure, which can achieve better conversion and selectivity in hydrogenation reactions at high flow rates. The flow characteristics of the monolithic catalyst in the packed-bed micro-reactor were compared between gas–liquid upward and gas–liquid downward flow. It was found that, in the reactor with an inner diameter of 12 mm, the downward gas–liquid process exhibits Taylor flow characteristics, while the upward process for gas–liquid shows bubble flow. Both modes exhibit higher activity in the NB hydrogenation reaction compared with that reported in the literature. Under room temperature and pressure, the gas flow rate was 0.6 mL min<small><sup>−1</sup></small> and the liquid flow rate was 15 mL min<small><sup>−1</sup></small>, and the gas–liquid downward residence time was 0.83 min. The conversion reached 99% and the selectivity was 98.2%. The three-dimensional printed carbon-based monolithic catalyst has a hierarchical porous structure and a large specific surface area, which can effectively enhance organic hydrogenation reactions.</p>","PeriodicalId":101,"journal":{"name":"Reaction Chemistry & Engineering","volume":null,"pages":null},"PeriodicalIF":3.4,"publicationDate":"2024-03-27","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"140313622","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}