Reaction mechanism and kinetics for the liquid-phase catalytic oxidation of meta-xylene to meta-phthalic acid

被引:21
作者
Wang, Qinbo [1 ,2 ]
Zhang, Yongzhao [3 ]
Cheng, Youwei [2 ]
Li, Xi [2 ]
机构
[1] Hunan Univ, Coll Chem & Chem Engn, Changsha 418002, Hunan, Peoples R China
[2] Zhejiang Univ, Dept Chem Engn, Hangzhou 310027, Zhejiang, Peoples R China
[3] Hangzhou Vocat & Tech Coll, Dept Chem Engn, Hangzhou 310027, Zhejiang, Peoples R China
关键词
catalytic oxidation; radical chain elementary reaction mechanism; kinetics; meta-xylene; meta-phthalic acid;
D O I
10.1002/aic.11574
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A detailed radical chain elementary reaction mechanism for the liquid-phase catalytic oxidation of meta-xylene to meta-phthalic acid catalyzed by cobalt acetate and manganese acetate and promoted by hydrogen bromide was proposed. Using several reasonable assumptions a simple fractional-like kinetic model was derived from the assumed reaction mechanism. Several batch oxidation experiments were carried out to study the oxidation kinetics. The experiments included three values of the initial concentration of meta-xylene and four values of reaction temperature. The developed model parameters were determined in a nonlinear optimization, minimizing the difference between the simulated and experimental time evolutions of the product compostions obtained in a batch oxidation reactor, where the gas and liquid phases were well mixed. The experimental results cannot be interpreted by the empirical n-th order kinetics, but can be interpreted by the kinetic model proposed in this work. It means the kinetic model proposed in this work reveals the reaction mechanism. (C) 2008 American Institute of Chemical Engineers.
引用
收藏
页码:2674 / 2688
页数:15
相关论文
共 40 条
[1]  
[Anonymous], 1986, MODELLING OXIDATION
[2]   A lumped kinetic model for liquid-phase catalytic oxidation of p-xylene to terephthalic acid [J].
Cao, Giacomo ;
Pisu, Massimo ;
Morbidelli, Massimo .
CHEMICAL ENGINEERING SCIENCE, 1994, 49 (24B) :5775-5788
[3]   KINETICS OF P-XYLENE LIQUID-PHASE CATALYTIC-OXIDATION [J].
CAO, GM ;
SERVIDA, A ;
PISU, M ;
MORBIDELLI, M .
AICHE JOURNAL, 1994, 40 (07) :1156-1166
[4]  
Cheng Y. W., 2004, THESIS ZHEJIANG U HA
[5]  
[成有为 Cheng Youwei], 2003, [化学反应工程与工艺, Chemical Reaction Engineering and Technology], V19, P182
[6]   Kinetics and related engineering aspects of catalytic liquid-phase oxidation of p-xylene to terephthalic acid [J].
Cincotti, A ;
Orrù, R ;
Cao, G .
CATALYSIS TODAY, 1999, 52 (2-3) :331-347
[7]   Effect of catalyst concentration and simulation of precipitation processes on liquid phase catalytic oxidation of p-xylene to terephthalic acid [J].
Cincotti, A ;
Orru, R ;
Broi, A ;
Cao, G .
CHEMICAL ENGINEERING SCIENCE, 1997, 52 (21-22) :4205-4213
[8]  
GEORGE WP, 1992, HOMOGENEOUS CATALYSI
[9]   KINETICS AND MECHANISM OF COBALT BROMIDE CATALYZED OXIDATION OF PARA-XYLENE IN THE PRESENCE OF PHASE-TRANSFER CATALYSTS [J].
HARUSTIAK, M ;
HRONEC, M ;
ILAVSKY, J .
JOURNAL OF MOLECULAR CATALYSIS, 1989, 53 (02) :209-217
[10]   KINETICS AND MECHANISM OF PHASE-TRANSFER CATALYZED OXIDATION OF PARA-XYLENE BY MOLECULAR-OXYGEN [J].
HARUSTIAK, M ;
HRONEC, M ;
ILAVSKY, J .
JOURNAL OF MOLECULAR CATALYSIS, 1988, 48 (2-3) :335-342