Bottom Zone Flow Properties of a Square Circulating Fluidized Bed with Air Staging

Author(s):  
Zhengyang Wang ◽  
Shaozeng Sun ◽  
Xiangbin Qin ◽  
Qigang Deng ◽  
Shaohua Wu
Author(s):  
Shaozeng Sun ◽  
Zhengyang Wang ◽  
Hao Chen ◽  
Dong Li ◽  
Qigang Deng ◽  
...  

Effects of secondary air (SA) injection or air-staging on the gas-solids flow properties in the riser of a circulating fluidized bed (CFB) were investigated. The experiments were carried out in a CFB cold model with a square cross-section of 0.25m×0.25m and a height of 6.07m. The axial pressure drop profile along the riser was reported. And the local solids holdup profile at the centerline and the diagonal line of some cross sections which influenced by the SA injection was measured with an optical fiber probe. Two SA arrangement modes, i.e. four SA nozzles located on four walls (Wall SA) and four corners (Corner SA) were conducted. Air-staging results in a denser bottom bed for both two SA modes. The Wall SA case has a higher solids holdup than the Corner SA case in most regions of lower bed except the corner region but was leaner in the vicinity of SA injection level. W-shaped solids concentration profile was found in the region immediately above the SA injection level for Wall SA case but not obvious for Corner SA case. Fractal dimension was analyzed for pressure drop fluctuations and local solids concentration signal. Air-staging led to smaller fractal dimension value than the case without SA injection. The SA jets affected the local gas-solids distribution and fluctuation in the region close to the SA injection. Radial and axial solids transfer should be considered for the fractal analysis.


2001 ◽  
Vol 120 (1-2) ◽  
pp. 21-33 ◽  
Author(s):  
Philipp Schlichthaerle ◽  
Joachim Werther

Author(s):  
Hong-Shun Li ◽  
Yi-Jun Wang ◽  
Shi-Ping Jin

Solids flow pattern in the bottom zone of a rectangular cross-section CFB was investigated by using hot particles as the tracer. The experiments were carried out in a cold model circulating fluidized bed. The riser has an inner cross-section of 0.3 m by 0.5 m and a height of 5.8 m. The solids were returned into the riser at a height of 0.75 m above the air distributor within an angle of about 40 degree. Quartz sand was used as the bed material. The hot particles were also quartz sand but with a little smaller size. Specially designed miniature electrically heating devices were installed flush with the inner bed wall or inside the bed. At each run, about 10–15 cm3 hot particles were slowly pulled into the bed. The temperature response around the device was measured with four copper-constantan thermocouples. Based on the experimental results, a 3-D core-annulus model describing the solids flow pattern in the bottom zone of the CFB riser is proposed.


2004 ◽  
Vol 145 (1) ◽  
pp. 25-33 ◽  
Author(s):  
L.E Ersoy ◽  
M.R Golriz ◽  
M Koksal ◽  
F Hamdullahpur

Fuel ◽  
2018 ◽  
Vol 234 ◽  
pp. 904-913 ◽  
Author(s):  
Yukui Zhang ◽  
Qiangqiang Ren ◽  
Hongxiang Deng ◽  
Qinggang Lyu

Sign in / Sign up

Export Citation Format

Share Document