화학공학소재연구정보센터
Chinese Journal of Chemical Engineering, Vol.9, No.3, 291-296, 2001
Hydrodynamics and lateral gas dispersion in a high-density circulating fluidized bed reactor with bluff internals
Effect of bluff internals on the hydrodynamics and lateral gas mixing was studied in a 0.186 m ID high-density riser. With the bluff internals, the extremely non-uniform radial profiles of solid fraction and particle velocity become flat and the dense downflow layer near the wall disappears, indicating the significant enhancement of solid turbulence introduced by the internals. The fluctuation velocity and solid fraction transient signal analysis indicates a significant increase in fluctuation intensity near the wall region. The length influenced by the internals on the flow structure is about 1 meter. The lateral gas dispersion coefficient increases significantly as the bluff internals exist in the riser.