期刊论文详细信息
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN
Downward Gas–Solids Flow Characteristics in a High-Density Downer Reactor
Chihiro Fushimi3  Guoqing Guan2  Atsushi Tsutsumi4  Masanori Ishizuka4  Yoshizo Suzuki1 
[1] Clean Gas Group, Energy Technology Research Institute, National Institute of Advanced Industrial Science and Technology;North Japan Research Institute for Sustainable Energy (NJRISE), Hirosaki University;Department of Chemical Engineering, Tokyo University of Agriculture and Technology;Collaborative Research Center for Energy Engineering, Department of Mechanical and Biofunctional Systems, Institute of Industrial Science, The University of Tokyo
关键词: High Density Downer Reactor;    Solids Hold-Up;    Solids Mass Flux;    Gasification;    Pyrolysis;   
DOI  :  10.1252/jcej.12we125
来源: Maruzen Company Ltd
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【 摘 要 】

References(34)A specially designed high-density downward gas–solids flow fluidized bed, consisting of a solids reservoir tank, a solid distributor, an acrylic downer (3.0 m high), a gas–solid separator and a solid receiver tank, has been developed to study the fundamentals of high-density downward gas–solids flow characteristics in the downer reactor. Experiments have been carried out using two types of sand particles (ρp=2600 kg/m3, dp=80 and 320 µm) as bed materials with superficial downward gas velocities (Ugd) ranging from 0 to 5 m/s. Particle diameter has a great effect on the solids mass flux (Gs) and solids hold-up (εs) in the downer. It is found that Gs in a 50 mm diameter downer reached up to 1876 and 815 kg/m2·s, with average εs up to 0.16 and 0.07 in the developed region, for 80 and 320 µm sand, respectively. The solids hold-up decreased with increasing Ugd at a fixed solids mass flux in the developed region. By considering the effects of downer diameters, operating conditions, and solids properties, a correlation for the prediction of dense solids hold-up (εs*>0.07) in the developed region of the downer is proposed based on experimental data from the literature and this study.

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