MODELING AND SIMULATION OF THE REVERSED FLOW OPERATION OF A FIXED-BED REACTOR FOR METHANOL SYNTHESIS

被引:65
作者
VANDENBUSSCHE, KM [1 ]
NEOPHYTIDES, SN [1 ]
ZOLOTARSKII, IA [1 ]
FROMENT, GF [1 ]
机构
[1] STATE UNIV GHENT,PETROCHEM TECH LAB,KRIJGSLAAN 281,B-9000 GHENT,BELGIUM
关键词
D O I
10.1016/0009-2509(93)80150-O
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The proposed simulation of the reversed flow operation of a fixed-bed reactor for methanol synthesis is based upon a heterogeneous one-dimensional model. Different levels of transient modelling are compared. By using the most sophisticated model, the influence of a number of operating parameters is assessed. Considerable insight into the reactor behaviour is obtained.
引用
收藏
页码:3335 / 3345
页数:11
相关论文
共 32 条
[1]   TRANSIENT PROCESSES IN CATALYTIC COMBUSTION OF WASTE GASES [J].
BALMER, J ;
GILLES, ED .
CHEMIE INGENIEUR TECHNIK, 1989, 61 (08) :632-635
[2]  
BORESKOV GK, 1983, Patent No. 994400
[3]   ORTHOGONAL COLLOCATION ON FINITE-ELEMENTS [J].
CAREY, GF ;
FINLAYSON, BA .
CHEMICAL ENGINEERING SCIENCE, 1975, 30 (5-6) :587-596
[4]   CATALYTIC COMBUSTION WITH PERIODIC-FLOW REVERSAL [J].
EIGENBERGER, G ;
NIEKEN, U .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (08) :2109-2115
[5]  
ERGUN S, 1952, CHEM ENG PROG, V48, P89
[6]  
FROMENT GF, 1990, UNSTEADY STATE PROCE
[7]   DYNAMIC PROPERTIES OF THE ADIABATIC TUBULAR REACTOR WITH SWITCH FLOW [J].
GAWDZIK, A ;
RAKOWSKI, L .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (11) :3023-3030
[8]  
GOSIEWSKI K, 1990, UNSTEADY STATE PROCE, P629
[9]   CHEMICAL-EQUILIBRIA IN METHANOL SYNTHESIS [J].
GRAAF, GH ;
SIJTSEMA, PJJM ;
STAMHUIS, EJ ;
JOOSTEN, GEH .
CHEMICAL ENGINEERING SCIENCE, 1986, 41 (11) :2883-2890
[10]   KINETICS OF LOW-PRESSURE METHANOL SYNTHESIS [J].
GRAAF, GH ;
STAMHUIS, EJ ;
BEENACKERS, AACM .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (12) :3185-3195