Dynamic experiments in flow accelerate reaction network definition in a complex hydrogenation using catalytic static mixers

被引:7
|
作者
Martinuzzi, Stefano [1 ,2 ]
Tranninger, Markus [3 ]
Sagmeister, Peter [1 ,2 ]
Horn, Martin [3 ]
Williams, Jason D. [1 ,2 ]
Kappe, C. Oliver [1 ,2 ]
机构
[1] Res Ctr Pharmaceut Engn GmbH RCPE, Ctr Continuous Flow Synth & Proc CCFLOW, Inffeldgasse 13, A-8010 Graz, Austria
[2] Karl Franzens Univ Graz, Inst Chem, NAWI Graz, Heinrichstr 28, A-8010 Graz, Austria
[3] Graz Univ Technol, Inst Automat & Control, Inffeldgasse 21b, A-8010 Graz, Austria
关键词
OPTIMIZATION; DESIGN; SCALE;
D O I
10.1039/d3re00451a
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Kinetic screening, when conducted in batch or under steady state flow conditions, is time consuming. In this work we leverage transient flow experiments to investigate the hydrogenation of an aryl ketone in a gas-liquid flow reactor, catalyzed by catalytic static mixers and monitored using process analytical technologies. Ramping reactor parameters over time allowed the exploration of different residence times and temperatures in a single experiment, allowing rapid definition of the reaction network. Data analysis using a batch approximation approach and a plug flow reactor approach allowed parameterization of predictive reaction models. A Pd/Al2O3 catalyst performed ketone reduction, followed by dehydration to the ethylbenzene derivative. Conversely, Pt/Al2O3 and Ru/Al2O3 showed aromatic ring hydrogenation as the main reaction pathway, following ketone reduction. The developed workflow is likely to be highly applicable to other chemical systems and reaction types. The combination of transient flow experiments with process analytical technology (PAT) enables the rapid characterization and kinetic modelling of a complex ketone hydrogenation, catalyzed by catalytic static mixers (CSMs).
引用
收藏
页码:132 / 138
页数:7
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