DISCRIMINATION OF 3 APPROACHES TO EVALUATE HEAT FLUXES FOR WALL-COOLED FIXED-BED CHEMICAL REACTORS

被引:70
作者
VORTMEYER, D
HAIDEGGER, E
机构
[1] Fakultät für Maschinenwesen, Technische Universität München, 8000 München 2
关键词
D O I
10.1016/0009-2509(91)80058-7
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Temperature and concentration profiles were measured in the presence of an exothermic chemical reaction along the axis and the wall of a wall-cooled packed bed reactor. The data allowed the discrimination of three approaches to evaluate wall heat fluxes in solving the equations of the quasi-homogeneous model. All model coefficients were obtained from literature data. At Reynolds numbers of 25 and 32 (related to inlet temperatures around 600 K) the wall heat conduction model turned out to be the superior one.
引用
收藏
页码:2651 / 2660
页数:10
相关论文
共 35 条
[1]   TUBULAR REACTOR DESIGN .1. 2 DIMENSIONAL MODEL [J].
AHMED, M ;
FAHIEN, RW .
CHEMICAL ENGINEERING SCIENCE, 1980, 35 (04) :889-895
[2]  
BADDOUR RF, 1961, CHEM ENG PROGR S SER, V57, P35
[3]   THEORETICAL-MODEL OF HEAT-TRANSFER TO A PACKED OR QUIESCENT FLUIDIZED-BED [J].
BOTTERILL, JSM ;
DENLOYE, AOO .
CHEMICAL ENGINEERING SCIENCE, 1978, 33 (04) :509-515
[4]  
BROTZ W, 1951, CHEM-ING-TECH, V23, P408
[5]   EFFECTIVE THERMAL CONDUCTIVITIES IN GAS-SOLID SYSTEMS [J].
BUNNELL, DG ;
IRVIN, HB ;
OLSON, RW ;
SMITH, JM .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1949, 41 (09) :1977-1981
[6]   TRANSVERSE THERMAL DISPERSION AND WALL CHANNELING IN A PACKED-BED WITH FORCED CONVECTIVE FLOW [J].
CHENG, P ;
VORTMEYER, D .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (09) :2523-2532
[8]  
COBERLY CA, 1951, CHEM ENG PROG, V47, P141
[9]   ANALYSIS OF ANNULAR BED REACTOR FOR METHANATION OF CARBON-MONOXIDE [J].
DAVIS, ME ;
YAMANIS, J .
AICHE JOURNAL, 1982, 28 (02) :266-273
[10]   A SIMULATION-MODEL ACCOUNTING FOR STRUCTURAL RADIAL NONUNIFORMITIES IN FIXED-BED REACTORS [J].
DELMAS, H ;
FROMENT, GF .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (08) :2281-2287