EXPERIMENTAL-STUDY OF GAS AND PARTICLE BEHAVIOR IN THE GRID ZONE OF A JETTING FLUIDIZED-BED COLD MODEL

被引:26
作者
KIMURA, T
HORIUCHI, K
WATANABE, T
MATSUKATA, M
KOJIMA, T
机构
[1] Department of Industrial Chemistry, Seikei University, Musashino-shi, Tokyo, 180
关键词
FLUIDIZED BED; GRID ZONE; MODEL; OPTICAL FIBER SENSOR; PARTICLE VELOCITY; JET HEIGHT; GAS CONCENTRATION PROFILE;
D O I
10.1016/0032-5910(94)02913-9
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The local behavior of gas and solids in a grid zone was investigated using a jetting fluidized bed cold model. Spherical alumina particles (440 mum, 1500 kg/m3) were used as bed material. A pair of optical fiber sensors, an A/D converter and a personal computer were used to measure particle velocity in the jet, jet diameter and jet height. Tracer gas introduced from a center nozzle was sampled from various points in the grid zone and its concentration was measured by gas chromatography to investigate gas interchange between the jet and the annulus, and the gas dispersion in the annulus region. The effects of operational conditions, i.e., the shape of the gas distributor, nozzle diameter and gas flow rates, on the gas and particle behavior are discussed. It was considered that many more particles entered into the jet when a cone-shaped distributor rather than a flat distributor was employed. Employment of a narrower nozzle caused an increase in particle velocity at the bottom of the bed.
引用
收藏
页码:135 / 143
页数:9
相关论文
共 28 条
[1]   GRID REGION IN A FLUIDIZED-BED REACTOR [J].
BEHIE, LA ;
KEHOE, P .
AICHE JOURNAL, 1973, 19 (05) :1070-1072
[2]   SOLID FLOW IN THE ANNULAR REGION OF A SPOUTED BED [J].
BENKRID, A ;
CARAM, HS .
AICHE JOURNAL, 1989, 35 (08) :1328-1336
[3]  
DAVIDSON JF, 1985, FLUIDIZATION, P144
[4]   HYDRODYNAMICS OF FLUIDIZATION IN A SEMICIRCULAR BED WITH A JET [J].
ETTEHADIEH, B ;
GIDASPOW, D ;
LYCZKOWSKI, RW .
AICHE JOURNAL, 1984, 30 (04) :529-536
[5]   GAS TRANSFER BETWEEN A CENTRAL JET AND A LARGE TWO-DIMENSIONAL GAS-FLUIDIZED BED [J].
GBORDZOE, EAM ;
FREYCHET, N ;
BERGOUGNOU, MA ;
LARGE, JF .
POWDER TECHNOLOGY, 1988, 55 (03) :207-222
[6]   FLUIDIZATION IN TWO-DIMENSIONAL BEDS WITH A JET .2. HYDRODYNAMIC MODELING [J].
GIDASPOW, D ;
ETTEHADIEH, B .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1983, 22 (02) :193-201
[7]   PARTICLE MOVEMENT ON A PERFORATED PLATE DISTRIBUTOR OF FLUIDIZED-BED [J].
HORIO, M ;
KIYOTA, H ;
MUCHI, I .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1980, 13 (02) :137-142
[8]   VISUALIZATION OF GAS VOIDS BEHAVIOR ABOVE THE DISTRIBUTOR IN A 3-DIMENSIONAL GAS-FLUIDIZED BED [J].
KHATTAB, IAH ;
ISHIDA, M .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1986, 19 (05) :367-374
[9]  
KIMURA T, UNPUB J CHEM ENG JPN
[10]   DEVELOPMENT OF NUMERICAL-MODEL FOR REACTIONS IN FLUIDIZED-BED GRID ZONE - APPLICATION TO CHEMICAL VAPOR-DEPOSITION OF POLYCRYSTALLINE SILICON BY MONOSILANE PYROLYSIS [J].
KOJIMA, T ;
KIMURA, T ;
MATSUKATA, M .
CHEMICAL ENGINEERING SCIENCE, 1990, 45 (08) :2527-2534