Catalytic hydrogenation of N-4-nitrophenyl nicotinamide in a micro-packed bed reactor

被引:69
作者
Yang, Cuixian [1 ]
Teixeira, Andrew R. [1 ]
Shi, Yanxiang [1 ]
Born, Stephen C. [1 ]
Lin, Hongkun [1 ]
Song, Yunfei Li [2 ]
Martin, Benjamin [3 ]
Schenkel, Berthold [3 ]
Lachegurabi, Maryam Peer [1 ]
Jensen, Klavs F. [1 ]
机构
[1] MIT, Dept Chem Engn, Cambridge, MA 02139 USA
[2] Univ Cambridge, Dept Chem Engn & Biotechnol, Cambridge, England
[3] Novartis Pharma AG, Chem & Analyt Dev, CH-4002 Basel, Switzerland
关键词
MASS-TRANSFER; NITRO-COMPOUNDS; REDUCTION; DESIGN;
D O I
10.1039/c7gc03469e
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Recent advancements in micro-flow technologies and a drive toward more efficient, greener and safer processes have led to a renaissance in flow-chemistry for pharmaceutical production. In this work, we demonstrate the use of a stabilized Pd nanoparticle-organic-silica catalyst to selectively catalyze the hydrogenation of N-4-nitrophenyl nicotinamide, a functionalized active pharmaceutical ingredient (API) surrogate. Extensive catalyst and reactor characterization is provided to establish an in-depth understanding of the unique multiphase dynamics within the micro-packed bed reactor, including the identification of a large liquid holdup (74-84%), rapid multiphase mass transfer (k(m)a > 1 s(-1)), and liquid residence time distributions. A kinetic analysis has revealed that the surface catalyzed hydrogenation progresses through a condensation mechanism whereby an azo dimer intermediate is formed and rapidly consumed. Finally, a parametric study was performed at various pressures, temperatures, residence times and flow regimes to achieve quantitative chemoselective conversion of the nitroarene to the corresponding primary amine.
引用
收藏
页码:886 / 893
页数:8
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