## AbstrW -An experimental study is described of Ihe behaviour of Synclyst particles (do, = 48pm) fluidised by air in a 0.05 m i.d. column; pressures in the range 1-22 bar were used. The expansion of the dense phase during bubbling is compared with maximum bed expansion before bubbling. The data a
Drag force on the particles at the upstream end of a packed bed and the stability of the roof of bubbles in fluidised beds
β Scribed by J.B.L.M. Campos; J.R.F. Guedes de Carvalho
- Publisher
- Elsevier Science
- Year
- 1992
- Tongue
- English
- Weight
- 539 KB
- Volume
- 47
- Category
- Article
- ISSN
- 0009-2509
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β¦ Synopsis
A study is reported on the "bed support experiment" in which measurements of the minimum supporting velocity are performed for a wide range of conditions. Values of the drag coefficient for the particles at the upstream end of a packed bed are then calculated, and the data are seen to be well represented by C* = 650/Re + 16.9.
The analysis of drag forces is applied to a study of the stability of the roof of bubbles in fluid&d beds. It is concluded that gas throughflow is sufficient to hold up the particles on the roof of spherical bubbles in 3Dbeds, bat that it is insufficient to prevent particles from raining down across cylindrical bubbles in 2D-beds.
π SIMILAR VOLUMES
When dlffuslon mslde the sohd particles which are dried m a fluldlsed bed can not be neglected this Internal ddTuslon can be accounted for by two mechanisms (a) the long term response which describes the gradual build up of a concentrahon profile inside the solid particles as function of the total d
## Abstract The atmospheric pressure catalytic oxidative coupling of methane was studied in detail by axial gas concentration probing experiments in a 60 mm OD bubbling fluidisedβbed reactor system. Experimental data demonstrated a very fast reaction which occurred within the vicinity of the distri