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Expansion of a freely bubbling fluidized bed

Filip Johnsson (Institutionen för energiomvandling) ; Sven Andersson (Institutionen för energiomvandling) ; Bo Leckner (Institutionen för energiomvandling)
Powder Technology (0032-5910). Vol. 68 (1991), 2, p. 117-123.
[Artikel, refereegranskad vetenskaplig]

The expansion of a freely bubbling fluidized bed is studied over a range of particle properties and gas velocities that applies to fluidized bed boilers. A bed expansion model is derived from a modified two-phase flow model. The results from the model are compared with measurements in both a cold two-dimensional bed and a 16 MW,, fluidized bed boiler, as well as with data found in the literature. The model represents experimental results for sand particles of a diameter ranging from 0.15 mm to 4.0 mm and with gas velocities up to 3 m s-‘.

Nyckelord: Fluidized bed; Combustion; Boiler; Fluid dynamicsl

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Denna post skapades 2016-06-23. Senast ändrad 2016-08-15.
CPL Pubid: 238151


Institutioner (Chalmers)

Institutionen för energiomvandling (1900-2003)


Termisk energiteknik

Chalmers infrastruktur

Chalmers Kraftcentral (CK)