Skip to main content
U.S. Department of Energy
Office of Scientific and Technical Information

Minimum liquid fluidization velocity in gas-liquid-solid fluidized beds

Journal Article · · AIChE Journal
; ; ;  [1]
  1. Univ. of Western Ontario, London, Ontario (Canada). Dept. of Chemical and Biochemical Engineering
Accurate detection of minimum liquid fluidization is essential to the successful operation of gas-liquid-solid fluidized beds, especially when particle or liquid properties evolve. A gas-liquid-solid system of 3-mm glass beads exhibits three distinct flow regimes as the liquid velocity is increased: compacted, agitated and fluidized-bed regimes. Measurements showed that the bed is not fluidized in the agitated bed regime. Pressure gradient and bed height measurements do not provide the minimum liquid fluidization velocity; instead, they offer the velocity between the compacted and agitated bed regimes. Time-averaged signals are not reliable for determining the minimum liquid fluidization velocity. It can be obtained from the standard deviation, the average frequency, the Hurst exponent and the V statistic of the cross-sectional average conductivity, which can be measured under many industrial conditions. Examples of applications of gas-liquid-solid fluidized bed reactors include coal liquefaction and petroleum hydrotreating.
Sponsoring Organization:
Natural Sciences and Engineering Research Council of Canada, Ottawa, ON (Canada)
OSTI ID:
506007
Journal Information:
AIChE Journal, Journal Name: AIChE Journal Journal Issue: 5 Vol. 43; ISSN 0001-1541; ISSN AICEAC
Country of Publication:
United States
Language:
English

Similar Records

Hydrodynamics and interfacial gas-liquid mass transfer of gas-liquid-solid fluidized beds
Thesis/Dissertation · Sat Dec 31 23:00:00 EST 1988 · OSTI ID:6859458

Evaluation of minimum-fluidizing velocity correlations for bed particles used in fluidized-bed calcination processes
Technical Report · Mon Oct 31 23:00:00 EST 1988 · OSTI ID:6110111

Fractal analysis of fluidized particle behavior in liquid-solid fluidized beds
Journal Article · Sun Feb 28 23:00:00 EST 1993 · AIChE Journal (American Institute of Chemical Engineers); (United States) · OSTI ID:6431095