Operational range of a Gas-Solid Vortex Unit

被引:7
作者
Friedle, Maximilian [1 ]
Marin, Guy B. [1 ]
Heynderickx, Geraldine J. [1 ]
机构
[1] Univ Ghent, Lab Chem Technol, Technol Pk 914, B-9052 Ghent, Belgium
关键词
Gas-Solid Vortex Unit; Dimensional analysis; Maximum capacity; Multiphase flow; ROTATING FLUIDIZED-BEDS; FLOW; CHAMBERS;
D O I
10.1016/j.powtec.2018.07.062
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The Gas-Solid Vortex Unit is an advancing fluidization technology with the potential to overcome the limitations of conventional fluidized beds. The conditions for stable fluidization are investigated, that are the upper and lower limit, i.e. minimum and maximum capacity (W-s,W-min and W-s.max) Based on dimensional analysis three non-dimensional groups are identified, governing the fluidization phenomena: the superficial radial particle Reynolds number Re-p,Re- p, the swirl ratio S and the unit loading lambda. Data from different authors is gathered for minimum (42 datasets, 3 geometries) and maximum (251 datasets, 8 geometries) capacity and used in regression analysis. Parameters are estimated for different proposed functional dependencies of the identified dimensionless groups. The model equations describing the minimum and maximum unit loading best, including their 95% confidence intervals, are: lambda(max) = (4.0 +/- 0.4) 10(-3) (Rep,RS(0.454 +/- 0.018))-S-(0.43 +/- 0.011) lambda(min) = (1.15 +/- 0.05) 10(-4) Re-p,Re-R The two equations describe the limits of the operational range of a GSVU for which stable fluidization is possible. The applicability of the model equations is verified against a wide range of data taken from different publications. (C) 2018 Published by Elsevier B.V.
引用
收藏
页码:702 / 715
页数:14
相关论文
共 36 条
[1]  
Abdollahi M., 2010, 13 INT C FLUID NEW P
[2]   Vortex apparatus for drying fibre-forming polymers [J].
Akulich, AV ;
Sazhin, BS .
FIBRE CHEMISTRY, 1999, 31 (02) :128-131
[3]   2-COMPONENT VORTEX FLOW STUDIES OF COLLOID CORE NUCLEAR ROCKET [J].
ANDERSON, LA ;
HASINGER, SH ;
TURMAN, BN .
JOURNAL OF SPACECRAFT AND ROCKETS, 1972, 9 (05) :311-&
[4]  
[Anonymous], 1969, CHEM PET ENG, DOI DOI 10.1007/BF01146998
[5]  
[Anonymous], 1969, CHEM-US, DOI DOI 10.1007/BF01136999
[6]   Modeling fast biomass pyrolysis in a gas-solid vortex reactor [J].
Ashcraft, Robert W. ;
Heynderickx, Geraldine J. ;
Marin, Guy B. .
CHEMICAL ENGINEERING JOURNAL, 2012, 207 :195-208
[7]   Rotating fluidized beds in a static geometry: Experimental proof of concept [J].
De Wilde, Juray ;
de Broqueville, Axel .
AICHE JOURNAL, 2007, 53 (04) :793-810
[8]   Combustion in vortex chambers with a fluidized particle bed [J].
Dvornikov, N. A. .
COMBUSTION EXPLOSION AND SHOCK WAVES, 2015, 51 (06) :631-640
[9]   Experimental investigation of a gas-solid rotating bed reactor with static geometry [J].
Ekatpure, Rahul P. ;
Suryawanshi, Vaishali U. ;
Heynderickx, Geraldine J. ;
de Broqueville, Axel ;
Marin, Guy B. .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2011, 50 (01) :77-84
[10]   Modeling and simulation of biomass drying in vortex chambers [J].
Eliaers, Philippe ;
Pati, Jnyana Ranjan ;
Dutta, Subhajit ;
De Wilde, Juray .
CHEMICAL ENGINEERING SCIENCE, 2015, 123 :648-664