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One-pot mechanochemical hydrogenation and acetylation of 4-nitrophenol to 4-aminophenol and paracetamol
被引:1
|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.
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页码:4079 / 4091
页数:13
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