Qingyu Zhang, Leming Cheng, Kun Li, 等. Experimental study on secondary air mixing along the bed height in a circulating fluidized bed with a multitracer-gas method[J]. 中国化学工程学报(英文版), 2024,70(6):54-62.
Qingyu Zhang, Leming Cheng, Kun Li, Qixun Kang, Qiang Guo, Chaogang Wu. Experimental study on secondary air mixing along the bed height in a circulating fluidized bed with a multitracer-gas method[J]. Chinese Journal of Chemical Engineering, 2024, 70(6): 54-62.
Qingyu Zhang, Leming Cheng, Kun Li, 等. Experimental study on secondary air mixing along the bed height in a circulating fluidized bed with a multitracer-gas method[J]. 中国化学工程学报(英文版), 2024,70(6):54-62.DOI: 10.1016/j.cjche.2024.03.003.
Qingyu Zhang, Leming Cheng, Kun Li, Qixun Kang, Qiang Guo, Chaogang Wu. Experimental study on secondary air mixing along the bed height in a circulating fluidized bed with a multitracer-gas method[J]. Chinese Journal of Chemical Engineering, 2024, 70(6): 54-62.DOI: 10.1016/j.cjche.2024.03.003.
Experimental study on secondary air mixing along the bed height in a circulating fluidized bed with a multitracer-gas method
A multitracer-gas method was proposed to study the secondary air (SA) mixing along the bed height in a circulating fluidized bed (CFB) using carbon monoxide (CO)
oxygen (O
2
)
and carbon dioxide (CO
2
) as tracer gases. Experiments were carried out on a cold CFB test rig with a cross-section of 0.42 m×0.73 m and a height of 5.50 m. The effects of superficial velocity
SA ratio
bed inventory
and particle diameter on the SA mixing were investigated. The results indicate that there are some differences in the measurement results obtained using different tracer gases
wherein the deviation between CO and CO
2
ranges from 42% to 66% and that between O
2
and CO
2
ranges from 45% to 71% in the lower part of the fluidized bed. However
these differences became less pronounced as the bed height increased. Besides
the high solid concentration and fine particle diameter in the CFB may weaken the difference. The measurement results of different tracer gases show the same trends under the variation of operating parameters. Increasing superficial velocity and SA ratio and decreasing particle diameter result in better mixing of the SA. The effect of bed inventory on SA mixing is not monotonic.
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