BEHAVIOR OF AN ADIABATIC FIXED-BED REACTOR FOR THE OXIDATION OF CARBON-MONOXIDE .2. EFFECT OF PERTURBATIONS

被引：46

作者：

SHARMA, CS

HUGHES, R

机构：

[1] Department of Chemical Engineering, University of Salford, Salford

来源：

CHEMICAL ENGINEERING SCIENCE | 1979年 / 34卷 / 05期

关键词：

D O I：

10.1016/0009-2509(79)85107-6

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

The effect of perturbations on the performance of an adiabatic reactor used for processing the exothermic catalytic oxidation of carbon monoxide has been investigated. Perturbations studied included, step changes in concentration and temperature, pulse changes in concentration, hysteresis effects and addition of CO2 to the feed stream. Intraparticle temperatures were measured for some of these perturbations. The heterogeneous dispersion model was suitable for steady-state predictions but was not adequate for transient behaviour. © 1979.

引用

收藏

页码：625 / 634

页数：10

相关论文

共 12 条

[1] ON UNIQUENESS OF STEADY STATE OF A CATALYST PELLET INVOLVING BOTH INTRAPHASE AND INTERPHASE TRANSPORT [J].

CRESSWELL, DL .

CHEMICAL ENGINEERING SCIENCE, 1970, 25 (02) :267-+

[2]

HLAVACEK V, 1974, ADV CHEM SER, V133, P545

[3] EXPERIMENTAL EVALUATION OF DYNAMIC MODELS FOR A FIXED-BED CATALYTIC REACTOR [J].

HOIBERG, JA ;

LYCHE, BC ;

FOSS, AS .

AICHE JOURNAL, 1971, 17 (06) :1434-&

[4] MAXIMUM TEMPERATURE RISE INSIDE CATALYTIC PELLETS [J].

LEE, JCM ;

LUSS, D .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1969, 8 (03) :596-&

[5] RESPONSE OF A TUBULAR HETEROGENEOUS CATALYTIC REACTOR TO A STEP INCREASE IN FLOW RATE [J].

LEHR, CG ;

YURCHAK, S ;

KABEL, RL .

AICHE JOURNAL, 1968, 14 (04) :627-&

[6]

LUSS D, 1978, 4TH P INT 6TH EUR S, P280

[7] REDUCED DYNAMIC-MODEL OF A FIXED-BED REACTOR [J].

MCGREAVY, C ;

NAIM, HM .

CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1977, 55 (03) :326-332

[8] MODELING OF NONCATALYTIC GAS-SOLID REACTIONS .2. TRANSIENT SIMULATION OF A PACKED-BED REACTOR [J].

SAMPATH, BS ;

RAMACHANDRAN, PA ;

HUGHES, R .

CHEMICAL ENGINEERING SCIENCE, 1975, 30 (01) :135-143

[9] BEHAVIOR OF AN ADIABATIC FIXED-BED REACTOR FOR THE OXIDATION OF CARBON-MONOXIDE .1. GENERAL PARAMETRIC STUDIES [J].

SHARMA, CS ;

HUGHES, R .

CHEMICAL ENGINEERING SCIENCE, 1979, 34 (05) :613-624

[10] KINETICS OF CATALYTIC-OXIDATION OF CARBON-MONOXIDE OVER OXIDE CATALYSTS [J].

SHARMA, CS ;

RAMACHANDRAN, PA ;

HUGHES, R .

JOURNAL OF APPLIED CHEMISTRY AND BIOTECHNOLOGY, 1976, 26 (05) :231-238