One-pot mechanochemical hydrogenation and acetylation of 4-nitrophenol to 4-aminophenol and paracetamol

被引:4
|
作者
Park, Jimin [1 ,2 ,5 ]
Maier, Jacob S. [1 ]
Evans, Caria [2 ,3 ,5 ]
Hatzell, Marta [1 ,4 ]
France, Stefan [2 ,3 ,5 ]
Sievers, Carsten [1 ,2 ,5 ]
Bommarius, Andreas S. [1 ,2 ,5 ]
机构
[1] Georgia Inst Technol, Sch Chem & Biomol Engn, 311 Ferst Dr NW, Atlanta, GA 30332 USA
[2] Georgia Inst Technol, Renewable Bioprod Inst, 500 10th St NW, Atlanta, GA 30332 USA
[3] Georgia Inst Technol, Sch Chem & Biochem, 901 Atlantic Dr NW, Atlanta, GA 30332 USA
[4] Georgia Inst Technol, George W Woodruff Sch Mech Engn, 801 Ferst Dr, Atlanta, GA 30332 USA
[5] Ctr Renewables Based Econ WOOD ReWOOD, 500 10th St NW, Atlanta, GA 30332 USA
关键词
CATALYTIC-HYDROGENATION; P-AMINOPHENOL; DEPOLYMERIZATION; OXIDATION; PHENOL;
D O I
10.1039/d3gc04281b
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
The mechanochemical hydrogenation of 4-nitrophenol was examined in a ball mill reactor. Hydrogen gas flows through the reactor at ambient temperature and pressure in the presence of Pd/C catalyst and acetic anhydride. Under optimized conditions, simultaneous hydrogenation and acetylation in one pot increased paracetamol selectivity by avoiding undesirable side reactions of 4-aminophenol. Side product formation was further reduced through a novel bubbler configuration allowing for the delivery of acetic anhydride vapor to the reaction vessel. Ball mill results were compared to traditional stirred tank hydrogenations in a Parr reactor and shown to have superior yield and process mass intensity. The mechanochemical hydrogenation of 4-nitrophenol was examined in a ball mill reactor.
引用
收藏
页码:4079 / 4091
页数:13
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