A generalized spherical multi-particle model for particulate systems: fixed and fluidized beds
β Scribed by M.R. Panigrahi; J.S. Murty
- Publisher
- Elsevier Science
- Year
- 1991
- Tongue
- English
- Weight
- 455 KB
- Volume
- 46
- Category
- Article
- ISSN
- 0009-2509
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β¦ Synopsis
REFERENCES
de Bruijn, I. Naka and Sonnemans, J. W. M., 1981, Effect of the noncylindrical shape of extrudates on the hydrodesulfurization of oil fractions. Ind. Engng Chem. Process Des. Dev. 20, 4CL45. Mears, D. E., 1971, The role of axial dispersion in trickleflow laboratory reactors.
π SIMILAR VOLUMES
AMract-A model is derived for a fluidised bed that enables its steady state particulate expansion to be predicted as a function of superficial velocity from the initial backed bed) condition to the final fully expanded (single suspended particle) state. These predictions are in good agreement with t
## Abstract In the present investigation minimum fluidization velocity, __U__~mf~, in a twoβphase inverse fluidized bed reactor is determined using lowβdensity polyethylene and polypropylene particles of different diameters (4,6 and 8 mm) by measuring pressure drop. In a glycerol system __U__~mf~ d