Pressure distribution and particle concentration in bubbling fluidized beds
Paper i proceeding, 1989

The expansion of and particle concentration in large-particle (>0.5 mm) bubbling beds, fluidized at high gas velocities (U-Umf>1 m/s) have been studied in a boiler with 10 m2 hot bed and in a cold two-dimensional bed. The significantly different behaviour of a freely bubbling versus a tube-filled bed at high gas velocity is demonstrated.

Författare

Filip Johnsson

Institutionen för energiomvandling

Bengt-Åke Andersson

Institutionen för energiomvandling

Bo G Leckner

Institutionen för energiomvandling

Proc of the 6th International Conference on Fluidization

Vol. 6 419-426

Ämneskategorier

Energiteknik

Styrkeområden

Energi

Infrastruktur

Chalmers kraftcentral

ISBN

0-8169-0459-6