Measurement of solids circulation rate in a high-temperature dual fluidized bed pilot plant

被引:21
|
作者
Rahman, M. Hafizur [1 ]
Bi, Xiaotao T. [1 ]
Grace, John R. [1 ]
Lim, C. Jim [1 ]
机构
[1] Univ British Columbia, Fluidizat Res Ctr, Dept Chem & Biol Engn, 2360 East Mall, Vancouver, BC V6T 1Z3, Canada
关键词
Solid circulation rate; Thermal-tracing technique; Pilot plant gasifier; Dual fluidized bed; BIOMASS;
D O I
10.1016/j.powtec.2017.01.073
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A number of fluidized bed reactor processes operating at high temperature require that solid particles be circulated back and forth between two reactor vessels. Since the circulation rate strongly affects mass and energy balances, and therefore greatly influences hydrodynamics and performance of the system, a reliable technique for its accurate measurement would be helpful in monitoring and modeling the process. However, there are no reported techniques suitable for measuring solid circulation rates at elevated temperatures typical of gasification systems. A novel thermal-tracing technique was developed for measuring the solids circulation rate between two reactors. Particles at room temperatures (cold particles) are injected into a downward-moving packed bed of solids at elevated temperature (hot particles), creating reduced-temperature zones inside the moving bed. The transit time of the cold-particle-clusters between pairs of thermocouples is determined by cross correlation allowing the flux to be estimated. The technique was shown to provide sensitive and reproducible data for a cold model unit with injection of dry ice. The technique was then applied to determine the solids circulation rate between the bubbling bed gasifier and the riser combustor of a pilot scale dual fluidized bed gasification system. A number of conditions are imposed on the data to eliminate unsatisfactory data at high temperatures. Data which satisfy the discrimination criteria are shown to lead to measured solids circulation fluxes up to 133 kg/m(2)-s at temperatures up to 856 degrees C in the gasifier test section. The technique provides high-temperature solids circulation rate information beyond the capability of other techniques. (C) 2017 Elsevier B.V. All rights reserved.
引用
收藏
页码:658 / 669
页数:12
相关论文
共 50 条
  • [21] HIGH-TEMPERATURE CORROSION IN FLUIDIZED-BED COMBUSTORS
    STRINGER, J
    EHRLICH, S
    MECHANICAL ENGINEERING, 1977, 99 (05) : 91 - 91
  • [22] Solid circulation rate in recirculating fluidized bed
    Alappat, BJ
    Rane, VC
    JOURNAL OF ENERGY ENGINEERING-ASCE, 2001, 127 (02): : 51 - 68
  • [23] Application of the magnetic tracer-tracking system in solids circulation measurement in a fluidized bed standpipe
    Zhou, Chunguang
    Jonasson, Christian
    Gullberg, Marcus
    Ahrentorp, Fredrik
    Johansson, Christer
    CHEMICAL ENGINEERING JOURNAL, 2024, 498
  • [24] EFFECT OF CHEMISORBED WATER ON BED VOIDAGE OF HIGH-TEMPERATURE FLUIDIZED-BED
    YAMAZAKI, R
    HAN, NS
    SUN, ZF
    JIMBO, G
    POWDER TECHNOLOGY, 1995, 84 (01) : 15 - 22
  • [25] Fluidized Bed Apparatus for High-Temperature Sorption of Carbon Dioxide
    Staf, Marek
    Miklova, Barbora
    CHEMICKE LISTY, 2021, 115 (08): : 441 - 446
  • [26] HIGH-TEMPERATURE CORROSION IN FLUIDIZED-BED COMBUSTION SYSTEMS
    STRINGER, J
    MINCHINER, AJ
    JOURNAL OF METALS, 1984, 36 (07): : 20 - 21
  • [27] DOLOMITE DECOMPOSITION IN A HIGH-TEMPERATURE FLUIDIZED-BED REACTOR
    HEHL, M
    HELMRICH, H
    SCHUGERL, K
    JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY A-CHEMICAL TECHNOLOGY, 1983, 33 (01): : 12 - 24
  • [28] FLOW CHARACTERISTICS OF SLUGGING IN FLUIDIZED-BED AT HIGH-TEMPERATURE
    HONG, GH
    YAMAZAKI, R
    JIMBO, G
    KAGAKU KOGAKU RONBUNSHU, 1981, 7 (02) : 109 - 114
  • [29] OXIDATION OF STEEL HEATED IN A HIGH-TEMPERATURE FLUIDIZED-BED
    BASKAKOV, AP
    BERG, BV
    SADILOV, PV
    ZAVAROV, AS
    RUSSIAN METALLURGY-METALLY-USSR, 1971, 1972 (02): : 73 - &
  • [30] Investigation of solids circulation in a cold model of a circulating fluidized bed
    Lim, Mook Tzeng
    Pang, Shusheng
    Nijdam, Justin
    POWDER TECHNOLOGY, 2012, 226 : 57 - 67