MODELING OF THE LIQUID-PHASE NORMAL-OCTANE OXIDATION CATALYZED BY COBALT

被引:13
作者
GARCIAOCHOA, F
QUEROL, J
ROMERO, A
机构
[1] Departamento de Ingenieria Quimica, Facultad de CC Quimicas, Universidad Complutense
关键词
D O I
10.1021/ie00106a002
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
n-Octane liquid-phase oxidation with oxygen-nitrogen mixtures homogeneously catalyzed by cobalt palmitate has been studied. Molecular schemes of four and five reactions with two possibilities of kinetic equations used for lumping compounds are tested. Apparent rate constants are calculated by a multiresponse linear method, and discrimination among kinetic models is carried out by applying both statistical and physical criteria. Relationships of the apparent rate constants with temperature, oxygen partial pressure, and catalyst concentration are established, and parameters are optimized by nonlinear regression. The selected models are the same for catalytic and noncatalytic oxidation and describe in a suitable way the influence of temperature, oxygen partial pressure, and catalyst concentration on conversion and product selectivity. Finally, a discussion about lumping of different products based on experimental data is included. © 1990, American Chemical Society. All rights reserved.
引用
收藏
页码:1989 / 1994
页数:6
相关论文
共 11 条
[1]  
CHEN Z, 1985, INT CHEM ENG, V25, P738
[2]  
D'oro P. C., 1980, OXID COMMUN, V1, P153
[3]  
EMANUEL NM, 1965, OXIDATION HYDROCARBO
[4]   A COMPARISON OF KINETIC DATA INTERPRETATION METHODS - THERMAL-OXIDATION OF NORMAL-OCTANE IN LIQUID-PHASE [J].
GARCIAOCHOA, F ;
QUEROL, J ;
ROMERO, A .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1988, 39 (01) :47-54
[5]   NORMAL-OCTANE LIQUID-PHASE OXIDATION CATALYZED BY COBALT SALTS - OVERALL KINETIC AND PRODUCT DISTRIBUTION [J].
GARCIAOCHOA, F ;
ROMERO, A ;
QUEROL, J .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1990, 43 (01) :33-40
[6]   MODELING OF THE THERMAL NORMAL-OCTANE OXIDATION IN THE LIQUID-PHASE [J].
GARCIAOCHOA, F ;
ROMERO, A ;
QUEROL, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1989, 28 (01) :43-48
[7]   DETERMINATION OF RATE CONSTANTS FOR COMPLEX KINETICS MODELS [J].
HIMMELBLAU, DM ;
JONES, CR ;
BISCHOFF, KB .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1967, 6 (04) :539-+
[8]   KINETICS AND MECHANISM OF COBALT-CATALYZED OXIDATION OF PARA-XYLENE IN THE PRESENCE OF WATER [J].
HRONEC, M ;
CVENGROSOVA, Z ;
ILAVSKY, J .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1985, 24 (03) :787-794
[9]   AN ALGORITHM FOR LEAST-SQUARES ESTIMATION OF NONLINEAR PARAMETERS [J].
MARQUARDT, DW .
JOURNAL OF THE SOCIETY FOR INDUSTRIAL AND APPLIED MATHEMATICS, 1963, 11 (02) :431-441
[10]  
SAUNBY JB, 1976, HYDROCARB PROCESS, V55, P247