Phenol hydroxylation with nitrous oxide

被引:0
作者
Ivanov, D.P. [1 ]
Pirutko, L.V. [1 ]
机构
[1] Boreskov Institute of Catalysis, Siberian Branch, Russian Academy of Sciences, Novosibirsk
基金
俄罗斯基础研究基金会;
关键词
Dihydroxybenzenes; Nitrous oxide; Phenol hydroxylation; Zeolite catalysts;
D O I
10.1134/S207005041203004X
中图分类号
学科分类号
摘要
Phenol hydroxylation with nitrous oxide opens up a new, promising way to the gas-phase synthesis of dihydroxybenzenes, which are among the most important semiproducts of contemporary organic chemis-try. A process based on this reaction could provide an alternative to the existing liquid-phase processes employing hydrogen peroxide as the oxidizer. Here, we report phenol oxidation with nitrous oxide over zeo-lite MFI at 450-500°C and a residence time of 1.70-3.4 s. The dihydrobenzenes production rate per unit weight of the catalyst is 2.3 mmol/(g h). The process involving nitrous oxide is superior to the other technol-ogies in terms of oxidizer consumption efficiency and dihydroxybenzene isomer proportions. Specifically, the nitrous oxide conversion into dihydroxybenzenes is 74% and hydroquinone-to-catechol ratio in the reaction product is 1.2-1.4. © Pleiades Publishing, Ltd., 2012.
引用
收藏
页码:168 / 173
页数:5
相关论文
共 18 条
[1]  
Khimicheskaya Entsiklopediya (Encyclopedia of Chem-Istry), 1, (1998)
[2]  
Notari B., Stud. Surf. Sci. Catal, 37, (1988)
[3]  
Panov G.I., Kharitonov A.S., Sobolev V.I., Appl. Catal. A, 98, (1993)
[4]  
Motz J.I., Heinichen H., Holderich W.F., J. Mol. Catal, 136, (1998)
[5]  
Kustov L.M., Tarasov A.L., Bogdan V.I., Tyrlov A.A., Fulmer J.W., Catal. Today, 61, (2000)
[6]  
Ribera A., Arends I.W.C.E., De Vries S., Perez-Ramires J., Sheldon R.A., J. Catal, 195, (2000)
[7]  
Uriarte A.K., Rodkin M.A., Gross M.J., Khari-Tonov A.S., Panov G.I., Stud. Surf. Sci. Catal, 110, (1997)
[8]  
Panov G.I., CATTECH, 4, (2000)
[9]  
Jia J., Pillay K.S., Sachtler W.M.H., J. Catal, 221, (2004)
[10]  
Hensen E., Zhu Q., Liu P.-H., Chao K.-J., Santen V.R., J. Catal, 226, (2004)