Non-uniform distribution of gas-solid flow through six parallel cyclones in a CFB system: An experimental study

Abstract In large-scale circulating fluidized bed (CFB) boilers, it is common to use multiple cyclones in parallel for the capture of solids, assuming that gas–solid flow to be the same in the cyclones. This article presents a study investigating gas–solid flow through six parallel cyclones in a CFB cold test rig. The six cyclones were located asymmetrically on the left and right walls of the riser. Solid volume fraction and particle velocity profiles at the riser outlets and in the horizontal ducts were measured using a fiber optical probe. Cyclone pressure drop and solid circulating rate were measured for each individual cyclone. Measurements showed good agreement as to the non-uniform distribution of the gas–solid flow, which occurred mainly across the three cyclones on one side: the middle cyclones on both sides had higher particle velocities. Conversely, the solid volume fractions, solid fluxes and solid circulating rates of the middle cyclones were lower than those of the other four cyclones. The apparent reason for the flow non-uniformity among the cyclones is the significant flow non-uniformity at the riser outlets. Under typical operating conditions, the solid volume fractions at the riser outlets had a deviation of up to 26% whereas the solid circulating rates at the stand pipes, 7%. These results are consistent with most other studies in the literature.

[1]  Joachim Werther,et al.  Measurement techniques in fluidized beds , 1999 .

[2]  Leon R. Glicksman,et al.  Simplified scaling relationships for fluidized beds , 1993 .

[3]  Jinghai Li,et al.  3D CFD simulation of hydrodynamics of a 150 MWe circulating fluidized bed boiler , 2010 .

[4]  Arto Hotta,et al.  Foster Wheeler’s Solutions for Large Scale CFB Boiler Technology: Features and Operational Performance of Łagisza 460 MWe CFB Boiler , 2009 .

[5]  John R. Grace,et al.  Non‐Uniform Distribution of Two‐Phase Flows through Parallel Identical Paths , 2008 .

[6]  J. Makansi,et al.  Can fluid-bed take on p-c units in the 250- to 400-MW range , 1993 .

[7]  Investigation of nonuniformity in a liquid–solid fluidized bed with identical parallel channels , 2009 .

[8]  Reverse‐flow centrifugal separators in parallel: Performance and flow pattern , 2007 .

[9]  Jürgen Stumper,et al.  Gas–liquid two-phase flow distributions in parallel channels for fuel cells , 2009 .

[10]  John R. Grace,et al.  Wear of water walls in a commercial circulating fluidized bed combustor with two gas exits , 2007 .

[11]  John R. Grace,et al.  Distribution of multi-phase gas–solid flow across identical parallel cyclones: Modeling and experimental study , 2010 .

[12]  Yao Ben-rong Design of 600 MW Supercritical Circulating Fluidized Bed Boiler , 2008 .

[13]  Guang-bo Zhao,et al.  Experimental investigation on flow asymmetry in solid entrance region of a square circulating fluidized bed , 2009 .