Ozone decomposition in a 0.254 m diameter circulating fluidized bed reactor
- 31 January 1993
- journal article
- Published by Elsevier BV in Powder Technology
- Vol. 74 (1), 73-78
- https://doi.org/10.1016/0032-5910(93)80010-8
Abstract
No abstract availableKeywords
This publication has 4 references indexed in Scilit:
- The effect of particle size distribution on the performance of a catalytic fluidized bed reactorChemical Engineering Science, 1990
- Flow characterization in high-velocity fluidized beds using pressure fluctuationsChemical Engineering Science, 1988
- Bed expansion in high velocity fluidizationPowder Technology, 1982
- A Homogeneous Model for Reactant Conversions in a Vertical Pneumatic Transport Reactor for Catalytic ReactionsThe Chemical Engineering Journal, 1981