摘要
Phenol hydroxylation with aqueous H2O2 was known as one of the most effective manufactures in the world. With Fe-Cu or Fe-Cu/Al2O3 metallic acid salts as catalyst and in gradientless reactor, phenol hydroxylation reaction kinetics process was investigated by changing the factors of reaction temperature, phenol/H2O2 molar ratio and phenol initial mass fraction. It was shown that under the same value of M/FA0(M-the mass of catalyst; FA0-the mass flow rate of critical component A of reactant at the inlet of reactor), phenol conversion was increased but dihydroxybenzene total selectivity went down with the temperature rise, H2O2/phenol molar ratio and phenol initial mass fraction increasing. Therefore, the reaction mechanism of phenol/H2O2 hydroxylation over Fe-Cu or Fe-Cu/Al2O3 was purposed, its reaction kinetics equation and the relative kinetics parameters were also calculated.
源语言 | 英语 |
---|---|
页(从-至) | 87-92 |
页数 | 6 |
期刊 | Shiyou Xuebao, Shiyou Jiagong/Acta Petrolei Sinica (Petroleum Processing Section) |
卷 | 22 |
期 | 2 |
出版状态 | 已出版 - 4月 2006 |